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NGNP-CTF MTECH-TDRM-017 December 2008 Revision 0
NGNP and Hydrogen Production
Conceptual Design Study
NGNP Technology Development Road
Mapping Report
Section 17: Integrated Schedule and Cost
Estimate
APPROVALS
Function Printed Name and Signature Date Author
Name: Louisa Venter Company: M-Tech Industrial
December 2, 2008
Author
Name: Werner Koekemoer Company: M-Tech Industrial
December 2, 2008
Reviewer
Name: Scott Penfield Company: Technology Insights
December 2, 2008
Reviewer
Name: Dan Allen Company: Technology Insights
December 2, 2008
Reviewer
Name: Michael Correia Company: Pebble Bed Modular Reactor
December 2, 2008
Approval
Name: Jan van Ravenswaay Company: M-Tech Industrial
December 2, 2008
Westinghouse Electric Company LLC Nuclear Power Plants Post Office Box 355
Pittsburgh, PA 15230-0355
�2008 Westinghouse Electric Company LLC All Rights Reserved
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LIST OF CONTRIBUTORS
Name and Company Date
Johan Markgraaff (M-Tech Industrial (Pty) Ltd.) December 2008
Phil Rittenhouse (Technology Insights) December 2008
George Hayner (Technology Insights) December 2008
Scott Penfield (Technology Insights) December 2008
Dan Allen (Technology Insights) December 2008
Jan van Ravenswaay (M-Tech Industrial (Pty) Ltd.) December 2008
BACKGROUND INTELLECTUAL PROPERTY CONTENT
Section Title Description
N/A
REVISION HISTORY
RECORD OF CHANGES
Revision No. Revision Made by Description Date
A Louisa Venter Werner Koekemoer
Initial Review November 18, 2008
B Louisa Venter Werner Koekemoer
Formal Review November 20, 2008
C Louisa Venter Werner Koekemoer
Document for approval December 3, 2008
0 Louisa Venter Werner Koekemoer
Document for release to WEC December 4, 2008
DOCUMENT TRACEABILITY
Created to Support the Following
Document(s) Document Number Revision
N/A
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TABLE OF CONTENTS
Section Title Page
17.1 INTEGRATED TEST SCHEDULE........................................................................... 10
17.1.1 INTRODUCTION.................................................................................................... 10 17.1.2 INTEGRATED TEST SCHEDULE WITH ORIGINAL TDRM SCHEDULE ................. 10 17.1.3 MODIFIED TDRM SCHEDULE ............................................................................ 16 17.1.4 MODIFIED CTF SCHEDULE................................................................................. 23 17.1.5 CONCLUSION ....................................................................................................... 26
17.2 COST ESTIMATE ....................................................................................................... 27
17.2.1 INTRODUCTION.................................................................................................... 27 17.2.2 ASSUMPTIONS AND BASES OF COST ESTIMATIONS ............................................. 27 17.1.2.1 APPLICABILITY TO SCHEDULE............................................................................ 27 17.1.2.2 TRL ADVANCEMENTS......................................................................................... 28 17.1.2.3 CONTINGENCIES AND UNCERTAINTIES .............................................................. 28 17.1.2.4 GENERAL ............................................................................................................. 29 17.2.3 SUMMARY COST: ORIGINAL TDRMS ................................................................ 30 17.2.4 ORIGINAL TDRM COST ESTIMATE (FACILITIES DESCRIPTION AND TOTAL
COST INCLUDED).................................................................................................. 32 17.1.6 CONCLUSION – COST ESTIMATES....................................................................... 42 17.2.5 APPENDIX A: DETAILED COST ESTIMATION SHEETS ....................................... 43 17.2.6 APPENDIX B: REFERENCES ................................................................................ 88
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LIST OF TABLES
Table 17-1: The number of loops required in the CTF.................................................................. 26 Table 17-2: Cost ratios for metallic IHX A to IHX B .................................................................... 28 Table 17-3: Summary Cost: Original TDRM................................................................................ 31 Table 17-4: Original TDRM Cost Estimates (Facilities description and total cost included) ......... 33
LIST OF FIGURES
Figure 17-1: Integrated Schedule with original TDRMs ................................................................ 11 Figure 17-2: Modified TDRM Schedule ......................................................................................... 17 Figure 17-3: Modified CTF Schedule - 950°C case......................................................................... 24 Figure 17-4: Modified CTF Schedule - 750°C case......................................................................... 25
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ACRONYMS
Acronym Definition
AI Inner Annulus (active cooling piping) AMS Activity Measurement System ANL Argonne National Laboratory AO Outer Annulus (active cooling piping) AOO Anticipated Operational Occurrence AS Automation System ASME American Society of Mechanical Engineers AVR Arbeitsgemeinschaft Versuchs-Reaktor BNL Brookhaven National Laboratory BOP Balance of Plant BUMS Burn-up Measurement System CB Core Barrel CCS Core Conditioning System CEA Commissariat à l'Énergie Atomique CFD Computational Fluid Dynamics CHE Compact Heat Exchanger CIP Core Inlet Pipe CO2 Carbon Dioxide COC Core Outlet Connection COP Core Outlet Pipe COTS Commercial Off The Shelf CRADA Co-operative Research and Development Agreement CRD Control Rod Drive CSC Core Structure Ceramics CSIR Council for Scientific Industrial Research CTF Component Test Facility CTF Component Test Facility CUD Core Unloading Devices DAU Data Acquisition Unit DBA Design Base Accident DBE Design Base Event DDN Design Data Need DFC Depressurized Forced Cooling DLOFC De-pressurized Loss of Forced Cooling DOE Department of Energy DPP Demonstration Power Plant DRL Design Readiness Level DWS Demineralized Water System ELE Elecrolyser System EM Evaluation Model EMB Electomagnetic Bearing EOFY End of Fiscal Year EPCC Equipment Protection Cooling Circuit
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Acronym Definition
EPCT Equipment Protection Cooling Tower F&OR Functional and Operational Requirements FHS Fuel Handling System FHSS Fuel Handling and Storage System FIMA Fissions per Initial Metal Atoms FMECA Failure Modes, Effects and Criticality Analysis FS Fuel Spheres FTA Fault Tree Analysis FUS Feed and Utility System H2 Hydrogen H2SO4 Sulfuric Acid HC Helium Circulator He Helium HETP Height Equivalent of the theoretical Plate HGD Hot Gas Duct HI Hydro-Iodic HLW High Level Waste HPB Helium Pressure Boundary HPC High Pressure Compressor HPS Helium Purification System HPS Hydrogen Production System HPT High Pressure Turbine HPU Hydrogen Production Unit HRS Heat Removal System HTF Helium Test Facility HTGR High Temperature Gas-Cooled Reactor HTR High Temperature Reactor HTS Heat Transport System HTSE High Temperature Steam Electrolysis HTTR High Temperature Test Reactor HVAC Heating Ventilation and Air Conditioning HX Heat Exchanger HyS Hybrid Sulfur I&C Instrumentation and Control I2 Iodine ID Inner Diameter IHX Intermediate Heat Exchanger ILS Integrated Laboratory Scale I-NERI International Nuclear Energy Research Initiative INL Idaho National Laboratory INL Idaho National Laboratory IPT Intermediate Pressure Turbine ISR Inner Side Reflector K-T Kepner-Tregoe
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Acronym Definition
KTA German nuclear technical committee LANL Los Alamos National Laboratory LEU Low Enriched Uranium LOFC Loss of Forced Cooling LPT Low Pressure Turbine MES Membrane-electrode assembly MTR Material Test Reactor NAA Neutron Activation Analysis NCS Nuclear Control System NGNP Next Generation Nuclear Plant NHI Nuclear Hydrogen Initiative NHS Nuclear Heat Supply NHSS Nuclear Heat Supply System NNR National Nuclear Regulator NRG Nuclear Research and consultancy Group NRV Non-Return Valve O2 Oxygen OD Outer Diameter ORNL Oak Ridge National Laboratory PBMR Pebble Bed Modular Reactor PCC Power Conversion System PCDR Pre-Conceptual Design Report PCHE Printed Circuit Heat Exchanger PCHX Process Coupling Heat Exchanger PCS Power Conversion System PFHE Plate Fin Heat Exchanger PHTS Primary Heat Transport System PIE Post-irradiation Examination PLOFC Pressurized Loss of Forced Cooling POC Power Conversion System PPM Parts per million PPU Product Purification Unit PPWC Primary Pressurized Water Cooler QA Quality Assurance RAMI Reliability, Availability, Maintainability and Inspectability RC Reactor Cavity RCCS Reactor Cavity Cooling System RCS Reactivity Control System RCSS Reactivity Control and Shutdown System RDM Rod Drive Mechanism RIM Reliability and Integrity Management RIT Reactor Inlet Temperature RM Road Map ROT Reactor Outlet Temperature RPS Reactor Protection System
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Acronym Definition
RPT Report RPV Reactor Pressure Vessel RS Reactor System RSS Reserve Shutdown System RUS Reactor Unit System SAD Acid Decomposition System SAR Safety Analysis Report SAS Small Absorber Spheres SG Steam Generator SHTS Secondary Heat Transport System S-I Sulfur Iodine SiC Silicon Carbide SNL Sandia National Laboratory SO2 Sulfur Dioxide SOE Sulfuric Oxide Electrolyzers SOEC Sulfuric Oxide Electrolyzers Cells SR Side Reflector SSC System Structure Component SSCs Systems, Structures and Components SSE Safe Shutdown Earthquake SUD Software Under Development TBC To Be Confirmed TBD To Be Determined TDL Technology Development Loop (As incorporated in Concept 1) TDRM Technology Development Road Map TER Test Execution Report THTR Thorium High Temperature Reactor TRISO Triple Coated Isotropic TRL Technology Readiness Level TRM Technology Road Map UCO Uranium Oxycarbide UO2 Uranium Dioxide USA. United States of America V&V Verification and Validation V&Ved Verified and Validated VLE Vapor-Liquid Equilibrium WBS Work Breakdown Structure WEC Westinghouse Electric Company
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SUMMARY AND CONCLUSIONS
In this section, the integrated Technology Development Road Maps (TDRMs) schedule is
provided for the WEC NGNP Critical SSCs, together with cost estimates for certain critical Systems, Structures and Components (SSC’s).
The cost and schedule of the NGNP evolves continuously as the project progresses due to
high uncertainties associated with technology advancements, evolving test plans and schedules, timely availability of resources, etc. Therefore this document presents detailed schedules which include the following:
• Integrated Test Schedule with original TDRM Schedule – Inclusive of the overall NGNP schedule, the original TDRM schedules for critical SSC’s as well as the CTF high level schedule.
• Modified TDRM Schedule - The main purpose of the modified TDRM schedule is to move back non-critical tasks in order to relieve pressure on the front end of the schedule. This was done without jeopardizing CTF and NGNP start up dates. Also shown in this schedule is the total estimated cost per specification with possible testing facilities identified.
• Modified CTF Schedule – Schedules of CTF specific tasks were outlined for the 950°C Reactor Outlet Temperature (ROT) case (inclusive of Small Scale Development Tests (SSDT), Technology Development Loops (TDL), Component Qualification Loops (CQL) and Circulator Test Loop (CTL)) as well as for the 750°C ROT case. Results and conclusions for the above mentioned scenarios are given in Section 17.1.5.
Cost estimates are provided for certain critical SSCs (notably IHX A (metallic as well as ceramic), IHX B and HTS Piping). Estimates have only been provided only up to a TRL rating of 5. Estimates for higher TRL advancements can only be provided when additional design information (preliminary or final) pertaining to the NGNP and its components becomes available. For some of the SSCs, more design information is required in order to develop reliable cost estimates (notably PHTS Circulator, SHTS Mixing Chamber and Steam Generator). Trade studies (or various trade studies) need to be done to verify and determine the specific combinations of sub-components that will be used in the aforementioned SSCs. There is enough time in the modified schedule to perform the trade studies before the advancement of the TRLs and before possible testing in the CTF will be performed. Costing input relating to the HPS, as noted in the Hydrogen Plant Alternatives Study (HPAS), has also been incorporated into this document.
The bases for all estimates given are noted in Appendix A of this document.
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17.1 INTEGRATED TEST SCHEDULE
17.1.1 Introduction
In this section, the integrated schedule for the Technology Development Road Maps (TDRMs) addressing the WEC NGNP Critical SSCs is provided. This schedule, Figure 17-1, is bounded by the CTF schedule [17-2] showing a CTF operational date of 2014 and the WEC Next Generation Nuclear Plant (NGNP) Demonstration Plant schedule [17-1] showing a NGNP start up date of 2021.
The schedule was prepared in Microsoft Project to get an overall impression of the
anticipated schedules for the Test Specifications provided in the Technology Development Road Maps.
All of the Test Specifications and their original dates, as stated in Sections 3 to 16, are
indicated in the TDRM Schedule Section of the Integrated Test Schedule. This schedule was then modified to accommodate the Small Scale Development Tests (SSDT), an assumed CTF Initial Operational Date of March 2014 (when the first TDL can be assumed to be finished) and the NGNP Initial Operational Date of FY 2021. The resulting modified schedule is given in Figure 17-2.
The CTF schedule with the above mentioned modified Test Specification Schedule
incorporated can be seen in Figure 17-3. The following Critical SSCs are included in the TDRM schedule:
• PHTS Circulator (including the SHTS Circulator and Valve) • IHX A – Metallic and Ceramic • IHX B • HTS Piping • SHTS Flow Mixing Chamber • Hydrogen Production System • Power Conversion system Steam Generator • Fuel Elements • Core Structure Ceramics • Reserve Shutdown System • Reactivity Control System • Core Conditioning System • Reactor Cavity Cooling System
17.1.2 Integrated Test Schedule with Original TDRM Schedule The integrated Test Schedule given in Figure 17-1 includes the NGNP Schedule, the original TDRM Schedules, as in Section 3 – Section 16 in the previous report sections, and the CTF High Level Schedule.
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e en
viro
nmen
t
99W
EC
-TS
-IH
XA
-025
Man
ufac
turin
g T
echn
olog
ies
for
Cer
amic
Hea
t Exc
hang
ers
100
TR
L 4
- T
RL
5
101
Orig
inal
Sch
edul
e in
TD
RM
102
WE
C-T
S-I
HX
A-0
26C
eram
ic M
ater
ials
Cod
es a
nd S
tand
ards
103
WE
C-T
S-I
HX
A-0
27M
etho
ds fo
r T
herm
al/F
luid
and
Str
ess/
Str
ain
Mod
elin
g
104
WE
C-T
S-I
HX
A-0
28S
truc
tura
l Int
egrit
y C
riter
ia fo
r C
eram
ic H
eat E
xcha
nger
s
105
WE
C-T
S-I
HX
A-0
29P
erfo
rman
ce M
odel
ing
of C
eram
ic H
eat E
xcha
nger
s
106
WE
C-T
S-I
HX
A-0
30T
estin
g of
uni
t cel
l of C
ompa
ct H
eat E
xcha
nger
107
TR
L 5
- T
RL
6
108
Orig
inal
Sch
edul
e in
TD
RM
109
WE
C-T
S-I
HX
A-0
31S
peci
ficat
ions
of t
estin
g of
uni
t cel
ls o
f com
pact
Hea
t Exc
hang
er M
odul
e (1
.2M
W)
110
WE
C-T
S-I
HX
A-0
32A
SM
E C
ode
Cas
e fo
r C
eram
ic C
ompa
ct H
eat E
xcha
nger
Des
ign
111
TR
L 6
- T
RL
7
112
Orig
inal
Sch
edul
e in
TD
RM
113
WE
C-T
S-I
HX
A-0
33S
hell-
side
Flo
w D
istr
ibut
ion
and
Byp
ass
Leak
age
Tes
ting
114
WE
C-T
S-I
HX
A-0
34M
ulti-
mod
e H
eat T
rans
fer
Tes
ting
115
TR
L 7
- T
RL
8
116
Orig
inal
Sch
edul
e in
TD
RM
117
WE
C-T
S-I
HX
A-0
35S
peci
ficat
ions
of t
estin
g of
a fu
ll sc
ale
com
pact
Hea
t Exc
hang
er
118
IHX
B11
9T
RL
3 -
TR
L 4
: A
lloy
800
H M
ater
ial S
pec
ific
atio
n a
nd
Pro
cure
men
t
2006
2007
2008
2009
2010
2011
2012
2013
2014
2015
2016
2017
2018
2019
2020
2021
2022
2023
2024
2025
2026
2027
2028
Tas
k
Spl
it
Pro
gres
s
Mile
ston
e
Sum
mar
y
Pro
ject
Sum
mar
y
Ext
erna
l Tas
ks
Ext
erna
l Mile
ston
e
Dea
dlin
e
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng
TD
RM
-017
_6.m
pp
Fig
ure
17-
1: I
nte
gra
ted
Sch
edu
leF
ri 08
/12/
05
Pro
ject
: Pro
ject
1D
ate:
Fri
08/1
2/05
IDN
otes
Tas
k N
ame
120
Orig
inal
Sch
edul
e in
TD
RM
121
WE
C-T
S-I
HX
B-0
01A
lloy
800H
Mat
eria
l Spe
cific
atio
n an
d P
rocu
rem
ent
122
WE
C-T
S-I
HX
B-0
02D
atab
ase
for
Bra
zed
and
Diff
usio
n B
onde
d A
lloy
800H
123
WE
C-T
S-I
HX
B-0
03A
lloy
800H
Hig
h T
empe
ratu
re M
ater
ial P
rope
rtie
s
124
WE
C-T
S-I
HX
B-0
04E
ffect
s of
The
rmal
Agi
ng a
nd E
nviro
nmen
t on
Allo
y 80
0H P
rope
rtie
s
125
WE
C-T
S-I
HX
B-0
05E
ffect
s of
Env
ironm
enta
l Exp
osur
e on
Allo
y 80
0H B
raze
and
Diff
usio
n B
onde
d Jo
ints
126
WE
C-T
S-I
HX
B-0
06E
ffect
s of
Gra
in S
ize
and
Sec
tion
Thi
ckne
ss o
n A
lloy
800H
Pro
pert
ies
127
WE
C-T
S-I
HX
B-0
07C
orro
sion
Allo
wan
ces
for
Allo
y 80
0H
128
WE
C-T
S-I
HX
B-0
08T
herm
al/F
luid
Mod
elin
g M
etho
ds fo
r IH
X B
129
WE
C-T
S-I
HX
B-0
09M
etho
ds fo
r S
tres
s/S
trai
n M
odlin
g of
IHX
B
130
WE
C-T
S-I
HX
B-0
10C
riter
ia fo
r S
truc
tura
l Int
ergr
ity o
f IH
X B
131
WE
C-T
S-I
HX
B-0
11P
erfo
rman
ce M
odel
ing
Met
hods
for
IHX
B
132
TR
L 4
- T
RL
5:
Dat
abas
e fo
r B
raze
d a
nd
Dif
fusi
on
Bo
nd
ed A
lloy
800H
133
Orig
inal
Sch
edul
e in
TD
RM
134
WE
C-T
S-I
HX
B-0
12T
estin
g of
Uni
t Cel
l of C
ompa
ct H
eat E
xcha
nger
135
TR
L 5
- T
RL
6
136
Orig
inal
Sch
edul
e in
TD
RM
137
WE
C-T
S-I
HX
B-0
13T
estin
g of
inte
grat
ed c
ompa
ct H
eat E
xcha
nger
138
WE
C-T
S-I
HX
B-0
14A
SM
E II
I Cod
e C
ase
for
Mea
tllic
Com
pact
Hea
t Exc
hang
er D
esig
n
139
TR
L 6
- T
RL
7
140
Orig
inal
Sch
edul
e in
TD
RM
141
WE
C-T
S-I
HX
B-0
15S
hell-
side
Flo
w D
istr
ibut
ion
and
Byp
ass
Leak
age
Tes
ting
142
WE
C-T
S-I
HX
B-0
16M
ulti-
mod
e H
eat T
rans
fer
Tes
ting
143
TR
L 7
- T
RL
8
144
Orig
inal
Sch
edul
e in
TD
RM
145
WE
C-T
S-I
HX
B-0
17T
estin
g of
full
size
Com
pact
Hea
t Exc
hang
er
146
Pip
ing
147
TR
L 4
- T
RL
5
148
Orig
inal
Sch
edul
e in
TD
RM
149
WE
C-T
S-P
IP-0
01P
HT
S h
igh-
tem
pera
ture
[760
°C a
nd 9
50°C
] pip
ing
cool
ing,
line
r an
d in
sula
tion
optio
ns tr
ade
stud
y
150
WE
C-T
S-P
IP-0
02P
HT
S lo
w-t
empe
ratu
re [3
50°C
] pip
ing
liner
and
insu
latio
n op
tions
trad
e st
udy
151
WE
C-T
S-P
IP-0
03S
HT
S h
igh-
tem
pera
ture
[840
°C a
nd 9
00°C
] pip
ing
liner
and
insu
latio
n st
udy
152
WE
C-T
S-P
IP-0
04S
HT
S m
ediu
m-t
empe
ratu
re [6
59°C
and
700
°C] p
ipin
g lin
er a
nd in
sula
tion
trad
e st
udy
153
WE
C-T
S-P
IP-0
05S
HT
S lo
w-t
empe
ratu
re [<
300°
C] p
ipin
g lin
er a
nd in
sula
tion
trad
e st
udy
154
TR
L 5
- T
RL
6
155
Orig
inal
Sch
edul
e in
TD
RM
156
WE
C-T
S-P
IP-0
06E
ffect
s of
He
infil
trat
ion
on th
erm
al c
ondu
ctiv
ity o
f ins
ulat
ion
mat
eria
l
157
WE
C-T
S-P
IP-0
07T
he e
ffect
of f
luid
impu
ritie
s on
insu
latio
n pr
oper
ties
158
WE
C-T
S-P
IP-0
08R
e-ev
alua
tion
of n
eede
d m
atur
atio
n ta
sks
base
d on
Tra
de s
tudi
es
159
TR
L 6
- T
RL
7
160
Orig
inal
Sch
edul
e in
TD
RM
161
WE
C-T
S-P
IP-0
09P
erfo
rman
ce a
nd e
nviro
nmen
tal t
estin
g of
pro
toty
pica
l hig
h-te
mpe
ratu
re a
nd lo
w-t
empe
ratu
re p
ipin
g/in
sula
162
TR
L 7
- T
RL
8
163
Orig
inal
Sch
edul
e in
TD
RM
164
WE
C-T
S-P
IP-0
10T
estin
g of
full
size
PH
TS
pip
ing
in N
GN
P
165
Mix
ing
Ch
amb
er16
6T
RL
6 -
TR
L 7
167
Orig
inal
Sch
edul
e in
TD
RM
168
WE
C-T
S-M
C-0
01E
nhan
ced
Mix
ing
Dev
ices
Tes
t Spe
cific
atio
n
169
WE
C-T
S-M
C-0
02V
ibra
tion
Dam
ping
Dev
ices
Tes
t Spe
cific
atio
n
170
WE
C-T
S-M
C-0
03P
artia
l or
Ful
l Sca
le F
low
Mix
ing
Cha
mbe
r M
odel
Tes
t Spe
cific
atio
n
171
TR
L 7
- T
RL
8
172
Orig
inal
Sch
edul
e in
TD
RM
173
WE
C-T
S-M
C-0
04P
roto
type
Flo
w M
ixin
g C
ham
ber
Tes
t Spe
cific
atio
n
174
Ste
am G
ener
ato
r17
5T
RL
6 -
TR
L 7
176
Orig
inal
Sch
edul
e in
TD
RM
177
WE
C-T
S-S
G-0
01P
erfo
rm a
dow
n se
lect
ion
trad
e st
udy
to d
eter
min
e th
e pr
efer
red
conc
eptu
al a
rran
gem
ent o
f the
SG
178
WE
C-T
S-S
G-0
02D
efin
e re
quire
men
ts a
nd d
esig
n de
tails
for
the
SG
in th
e P
CS
sys
tem
con
text
179
WE
C-T
S-S
G-0
03P
erfo
rm c
onfig
urat
ion
deve
lopm
ent t
ests
to s
ubst
antia
te th
e de
sign
TB
D
2006
2007
2008
2009
2010
2011
2012
2013
2014
2015
2016
2017
2018
2019
2020
2021
2022
2023
2024
2025
2026
2027
2028
Tas
k
Spl
it
Pro
gres
s
Mile
ston
e
Sum
mar
y
Pro
ject
Sum
mar
y
Ext
erna
l Tas
ks
Ext
erna
l Mile
ston
e
Dea
dlin
e
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng
TD
RM
-017
_6.m
pp
Fig
ure
17-
1: I
nte
gra
ted
Sch
edu
leF
ri 08
/12/
05
Pro
ject
: Pro
ject
1D
ate:
Fri
08/1
2/05
IDN
otes
Tas
k N
ame
180
WE
C-T
S-S
G-0
04D
esig
n an
d su
pply
a s
cale
pro
toty
pe fo
r th
e te
stin
g in
the
CT
F
181
WE
C-T
S-S
G-0
05P
erfo
rman
ce te
stin
g in
CT
F
182
TR
L 7
- T
RL
8
183
Orig
inal
Sch
edul
e in
TD
RM
184
WE
C-T
S-S
G-0
06C
ompl
ete
final
des
ign
of th
e pr
otot
ype
SG
for
the
NG
NP
185
WE
C-T
S-S
G-0
07F
abric
ate
and
deliv
er to
NG
NP
to th
e S
ite
186
WE
C-T
S-S
G-0
08In
stal
l and
ope
rate
187
Hyd
rog
en P
rod
uct
ion
Sys
tem
188
Su
lfu
ric
Aci
d D
eco
mp
osi
tio
n
189
Up
to c
ompl
etio
n of
S-I
ILS
190
Com
plet
e an
alys
is, s
uppo
rtin
g da
ta, m
ater
ials
test
ing
and
cata
lyst
cho
ice
& te
sts
191
Pilo
t tes
t of D
ecom
pose
r
192
Eng
inee
ring
test
of D
ecom
pose
r
193
Pro
toty
pe te
st o
f Dec
ompo
ser
194
Su
lfu
r D
ioxi
de
Ele
ctro
lysi
s T
ech
no
log
y A
rea
195
Up
to c
ompl
etio
n of
cel
l dem
onst
ratio
n at
tem
pera
ture
and
pre
ssur
e
196
HyS
ILS
and
opt
imiz
ed c
ell d
emon
stra
tion
197
Sca
le-u
p ce
lls to
400
cm
2 ,
and
Ele
ctro
lyze
r P
ilot T
est –
mod
ule
198
Sca
le-u
p ce
lls to
100
0 cm
2 an
d E
ngin
eerin
g te
st o
f Ele
ctro
lyze
r
199
Sca
le-u
p ce
lls to
1 m
2 an
d P
roto
type
test
of E
lect
roly
zer
200
Bu
nse
n R
eact
ion
an
d H
I Dec
om
po
sist
ion
Tec
hn
olo
gy
Are
a
201
Up
to c
ompl
etio
n of
S-I
ILS
–B
unse
n: T
RL
202
HI S
ectio
n E
xper
imen
tal T
est
– H
I
203
Bun
sen
and
HI S
yste
ms
Pilo
t Tes
t
204
Bun
sen
and
HI S
yste
ms
Eng
inee
ring
Tes
t
205
Pro
toty
pe H
PS
Tes
t: S
ulfu
ric A
cid,
Bun
sen
& H
I Sec
tions
206
Hig
h T
emp
erat
ure
Ste
am E
lect
roly
sis
Tec
hn
olo
gy
Are
a
207
Up
to c
ompl
etio
n of
ILS
208
Ful
l-sca
le s
tack
dem
onst
ratio
n
209
Pilo
t Tes
t
210
Pro
toty
pe H
PS
Tes
t
211
Sul
furic
Aci
d D
ecom
posi
tion
212
Sul
fur
Dio
xide
Ele
ctor
lysi
s
213
Bun
sen
Rea
ctio
n an
d H
I dec
ompo
sitio
n
214
Hig
h T
empe
ratu
re S
team
Ele
ctro
lysi
s
215
Fu
el E
lem
ents
216
TR
L 6
- T
RL
7
217
WE
C-T
S-F
UE
L-0
01P
rod
uct
ion
Fu
el Ir
rad
iati
on
Tes
ts f
or
No
rmal
Op
erat
ion
al C
on
dit
ion
s
218
Irra
diat
ion
plan
ning
& P
repa
ratio
n
219
Irra
diat
ion
of P
re-P
rodu
ctio
n F
uel
220
PIE
and
Ana
lysi
s
221
WE
C-T
S-F
UE
L-0
02P
rod
uct
ion
Fu
el H
eat-
up
Tes
ts a
t 16
00°C
an
d 1
800°
C.
222
Phy
sica
l Hea
ting
Tes
t
223
PIE
and
ana
lysi
s of
Hea
ted
Sph
eres
224
WE
C-T
S-F
UE
L-0
03F
uel
Mat
rix
Gra
ph
ite
Irra
dia
tio
n t
ests
an
d P
IE
225
Irra
diat
ion
Pla
nnin
g &
Pre
para
tion
226
Irra
diat
ion
and
PIE
227
WE
C-T
S-F
UE
L-0
04M
ach
ined
Gra
ph
ite
Irra
dia
tio
n t
ests
an
d P
IE
228
Irra
diat
ion
Pla
nnin
g &
Pre
para
tion
229
Irra
diat
ion
and
PIE
230
TR
L 7
- T
RL
8
231
WE
C-T
S-F
UE
L-0
02P
rod
uct
ion
Fu
el Ir
rad
iati
on
Tes
ts f
or
NG
NP
No
rmal
Op
erat
ion
al C
on
dit
ion
s
232
Irra
diat
ion
plan
ning
& P
repa
ratio
n
233
Irra
diat
ion
of P
re-P
rodu
ctio
n F
uel
234
PIE
and
Ana
lysi
s
235
WE
C-T
S-F
UE
L-0
03P
rod
uct
ion
Fu
el H
eat-
up
Tes
ts a
t 17
00°C
an
d 1
900°
C.
236
Phy
sica
l Hea
ting
Tes
t
237
PIE
and
ana
lysi
s of
Hea
ted
Sph
eres
238
WE
C-T
S-F
UE
L-0
04F
uel
Mat
rix
Gra
ph
ite
Irra
dia
tio
n t
ests
an
d P
IE
239
Irra
diat
ion
Pla
nnin
g &
Pre
para
tion
2006
2007
2008
2009
2010
2011
2012
2013
2014
2015
2016
2017
2018
2019
2020
2021
2022
2023
2024
2025
2026
2027
2028
Tas
k
Spl
it
Pro
gres
s
Mile
ston
e
Sum
mar
y
Pro
ject
Sum
mar
y
Ext
erna
l Tas
ks
Ext
erna
l Mile
ston
e
Dea
dlin
e
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng
TD
RM
-017
_6.m
pp
Fig
ure
17-
1: I
nte
gra
ted
Sch
edu
leF
ri 08
/12/
05
Pro
ject
: Pro
ject
1D
ate:
Fri
08/1
2/05
IDN
otes
Tas
k N
ame
240
Irra
diat
ion
and
PIE
241
Co
re S
tru
ctu
re C
eram
ics
242
TR
L 6
- T
RL
7
243
WE
C-T
S-C
SC
-001
PB
MR
Rel
evan
t
244
WE
C-T
S-C
SC
-002
Ext
ende
d P
rope
rtie
s of
Irra
diat
ed G
raph
ite a
t Low
Tem
pera
ture
s
245
WE
C-T
S-C
SC
-003
Ext
ende
d P
rope
rtie
s of
Irra
diat
ed G
raph
ite a
t Hig
h T
empe
ratu
res
246
WE
C-T
S-C
SC
-004
Cha
ract
eriz
e R
ace
Tra
ck S
trap
and
Tie
Rod
Mat
eria
l
247
WE
C-T
S-C
SC
-005
Insu
latio
n M
ater
ial (
Uni
rrad
iate
d D
ata
Nee
ded)
248
Res
erve
Sh
utd
ow
n S
yste
m24
9A
ntic
ipat
ed S
ched
ule
250
TR
L 6
- T
RL
7
251
TR
L 7
- T
RL
8
252
Rea
ctiv
ity
Co
ntr
ol S
yste
m25
3A
ntic
ipat
ed S
ched
ule
254
TR
L 6
- T
RL
7
255
TR
L 7
- T
RL
8
256
Co
re C
on
dit
ion
ing
Sys
tem
257
TR
L 6
- T
RL
7
258
WE
C-T
S-C
CS
-001
Val
ves
deve
lopm
ent T
est S
peci
ficat
ion
259
WE
C-T
S-C
CS
-002
Blo
wer
dev
elop
men
t Tes
t Spe
cific
atio
n
260
TR
L 7
- T
R8
261
WE
C-T
S-C
CS
-003
CC
S D
evel
opm
ent T
est S
peci
ficat
ion
262
Rea
cto
r C
avit
y C
oo
ling
Sys
tem
263
TR
L 6
- T
RL
7
264
No
test
s de
fined
yet
. Adv
ance
men
t to
the
next
TR
L on
ly a
chie
ved
thro
ugh
softw
are
anal
ysis
.
265
TR
L 7
- T
RL
8
266
Orig
inal
Sch
edul
e in
TD
RM
267
WE
C-T
S-R
CC
S-0
01V
erify
the
func
tioni
ng o
f the
RC
CS
with
res
pect
to m
aint
aini
ng R
eact
or C
avity
con
cret
e be
low
cod
e lim
its
268
WE
C-T
S-R
CC
S-0
02C
onfir
m o
pera
tion
of R
CC
S ta
nk a
utom
atic
wat
er r
eple
nish
men
t fun
ctio
n
269
WE
C-T
S-R
CC
S-0
03V
alid
ate
anal
ysis
of D
WS
sup
ply
and
heat
sin
k pe
rfor
man
ces
270
WE
C-T
S-R
CC
S-0
04V
alid
ate
theo
retic
al a
naly
sis
of p
ump
trip
effe
ct o
n R
CC
S p
ress
ure
271
272
C:
HT
GR
Co
mp
on
ent
Tes
t F
acili
ty27
3In
dust
ry C
TF
Rec
omm
enda
tion
Stu
dies
274
Pre
-Con
cept
ual D
esig
n
275
CT
F P
CD
R
276
Stu
dy #
1, T
DR
M a
nd T
est P
lans
for
Hig
h T
empe
ratu
re S
SC
s
277
50%
ICD
Rev
iew
278
Pre
pare
CT
F P
CD
R
279
Pre
pare
CT
F P
re-C
once
ptua
l Tes
t Loo
p D
esig
n
280
PC
D 9
0% R
evie
w
281
Pre
-Con
cept
ual T
DR
M &
Tes
t Loo
p D
esig
n
282
PC
D 9
0% R
evie
w
283
DO
E o
r P
PP
Issu
es E
PC
SO
W &
RF
P
284
Sta
rt E
PC
Con
tact
285
CT
F P
relim
inar
y D
esig
n
286
Pre
limin
ary
90%
Des
ign
Rev
iew
287
CT
F F
inal
Des
ign
288
Fin
al D
esig
n 90
% R
evie
w
289
Issu
e C
onst
ruct
ion
Doc
umen
ts
290
Tes
t & T
urno
ver
291
CT
F c
onst
ruct
ion
com
plet
ion
292
CT
F B
egin
Com
pone
nt In
stal
latio
n &
Tes
ting
293
Pro
ject
Tra
nsfe
r
2006
2007
2008
2009
2010
2011
2012
2013
2014
2015
2016
2017
2018
2019
2020
2021
2022
2023
2024
2025
2026
2027
2028
Tas
k
Spl
it
Pro
gres
s
Mile
ston
e
Sum
mar
y
Pro
ject
Sum
mar
y
Ext
erna
l Tas
ks
Ext
erna
l Mile
ston
e
Dea
dlin
e
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng
TD
RM
-017
_6.m
pp
Fig
ure
17-
1: I
nte
gra
ted
Sch
edu
leF
ri 08
/12/
05
Pro
ject
: Pro
ject
1D
ate:
Fri
08/1
2/05
NGNP-CTF MTECH-TDRM-017 NGNP Technology Development Road Mapping Section 17 : Integrated Schedule and Cost Estimate
NGNP-CTF MTECH-TDRM-017_Rev0.doc 10/27/2008
16 of 89
17.1.3 Modified TDRM Schedule
The original integrated TDRM Schedule (Figure 17-1) made the assumption that all work would start in October 2008 (FY2009). In the modified schedule, Figure 17-2, this was changed to relieve the initial pressure on the schedule by moving some of the less critical SSCs to a later starting date, but still within the constraints of the CTF- and NGNP start-up dates noted in the assumptions that follow:
• Small Scale Development Test will start in (October 2011-TBC as part of Phase II). • CTF Initial Operating Date is March 2014 • NGNP Initial Operation Date is October 2021 • The designs of modules and unit cells are finished and they are fabricated just prior to the
start of a test.
SSC specific comments contributing to the starting/end date modification can be seen in Figure 17-2.
IDN
otes
Tas
k N
ame
Cha
nge
to O
rigin
alP
ossi
ble
test
ing
faci
lity
loca
tions
1T
est
Sp
ecN
um
ber
Mo
dif
ied
TD
RM
Sch
edu
leC
om
men
ts
2C
ircu
lato
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L 6
- T
RL
7
4O
rigin
al S
ched
ule
in T
DR
M
5T
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Stu
dies
Sup
plie
r / D
esig
n A
utho
rity
6W
EC
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-CIR
C-0
01E
MB
s, c
atch
er b
earin
gs T
est S
peci
ficat
ion
Sta
rt d
ate
mov
ed: S
mal
l Sca
leD
evel
opm
ent T
est
EM
Bs
Sup
plie
r T
est F
acili
ty
7W
EC
-TS
-CIR
C-0
02H
eliu
m R
otat
ing
seal
s T
est S
peci
ficat
ion
Sta
rt d
ate
mov
ed: S
mal
l Sca
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evel
opm
ent T
est
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atin
g S
eal S
uppl
ier
Tes
t Fac
ility
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Ful
l sca
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ircul
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Mod
el T
est S
peci
ficat
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Sta
rt d
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mov
ed to
coi
ncid
e w
ithC
TF
Sta
rtin
g da
te:
CT
LC
TF
/Sup
plie
r S
ite
9TR
L 7
- T
RL
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10O
rigin
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in T
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11W
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C-0
04P
roto
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ficat
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rt d
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ed to
coi
ncid
e w
ithN
GN
P In
itial
Ope
ratin
g da
teN
GN
P S
ite
12IH
X A
(M
etal
lic)
13TR
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RL
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14O
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in T
DR
M
15W
EC
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Allo
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7 M
ater
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peci
ficat
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and
proc
urem
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INL,
OR
NL
16W
EC
-TS
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Allo
y 61
7 Jo
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d R
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Pro
pert
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Sta
rtin
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mov
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mor
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alis
tic a
nd a
chie
vabl
e da
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INL,
OR
NL,
AN
L, C
ompa
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eat
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r de
sign
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man
ufac
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17W
EC
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The
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/phy
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l and
mec
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cal p
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date
s m
oved
to m
ore
real
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and
ach
ieva
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date
sIN
L, O
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NL,
LA
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18W
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Effe
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mov
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mor
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INL,
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NL
19W
EC
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Effe
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Sta
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AN
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20W
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Cor
rosi
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acla
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21TR
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- T
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4
22O
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23W
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AS
ME
sec
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ode
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vabl
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sign
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man
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24W
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-TS
-IH
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The
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/Flu
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Met
hods
for
Met
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IHX
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tart
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to m
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real
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and
ach
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sC
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uppl
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26W
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-TS
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Crit
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tegr
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f IH
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desi
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-IH
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Mod
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rigin
al S
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Spe
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f com
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Hea
t Exc
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man
ufac
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and
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of c
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tart
ing
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mov
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34W
EC
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Des
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tart
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Au
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ng
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Test
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$ 0.
00
NG
NP
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0.00
INL
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NL
$
105,
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, OR
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, AN
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pac
t h
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, AN
L, L
AN
L, S
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L, C
SIR
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1,25
7.70
INL
, OR
NL
$ 4,
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176.
80
INL
, OR
NL
, AN
L, L
AN
L, S
NL
, BN
L, C
SIR
$ 83
3,70
7.60
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, OR
NL
, FZ
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1,90
4,40
8.00
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, OR
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ner
s/m
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fact
ure
rs$
760,
650.
00
CH
E s
up
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r/d
esig
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ori
ty, I
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, OR
NL
, AN
L, L
AN
L$
140,
250.
00
CH
E s
up
plie
r/d
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uth
ori
ty, I
NL
, OR
NL
, AN
L, L
AN
L$
140,
250.
00
CH
E s
up
plie
r/d
esig
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ori
ty, I
NL
, OR
NL
, AN
L, L
AN
L$
140,
250.
00
CH
E s
up
plie
r/d
esig
n a
uth
ori
ty, I
NL
, OR
NL
, AN
L, L
AN
L$
140,
250.
00
CH
E d
esig
ner
/man
ufa
ctu
rer
(Hea
tric
, Bra
yto
n E
ner
gy)
$ 20
0,00
0.00
CTF
$ 0.
00
CH
E s
up
plie
r/d
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n a
uth
ori
ty, I
NL
, OR
NL
, AN
L, L
AN
L$
0.00 CTF
$ 0.
00
NG
NP
Initi
al O
pera
ting
CT
F In
itial
Ope
ratin
g
2007
2008
2009
2010
2011
2012
2013
2014
2015
2016
2017
2018
2019
2020
2021
2022
2023
2024
2025
2026
Tas
k
Spl
it
Pro
gres
s
Mile
ston
e
Sum
mar
y
Pro
ject
Sum
mar
y
Ext
erna
l Tas
ks
Ext
erna
l Mile
ston
e
Dea
dlin
e
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng
TD
RM
-017
_7.m
pp
Fig
ure
17-
2: M
od
ifie
d T
DR
M S
ched
ule
Fri
08/1
2/05
Pro
ject
: TD
RM
Sch
edul
e_te
rugg
etre
k D
ate:
Fri
08/1
2/05
IDN
otes
Tas
k N
ame
Cha
nge
to O
rigin
alP
ossi
ble
test
ing
faci
lity
loca
tions
38W
EC
-TS
-IH
XA
-016
Mul
ti-m
odul
e H
eat T
rans
fer
Tes
ting
Sta
rtin
g da
te m
oved
to c
oinc
ide
with
CT
F S
tart
ing
date
: TD
LC
TF
39TR
L 7
- T
RL
8
40O
rigin
al S
ched
ule
in T
DR
M
41W
EC
-TS
-IH
XA
-017
Spe
cific
atio
n of
test
ing
of a
full
scal
e co
mpa
ct H
eat E
xcha
nger
sS
tart
dat
e m
oved
to c
oinc
ide
with
NG
NP
Initi
al O
pera
ting
date
NG
NP
42IH
X A
(C
eram
ic)
43TR
L 2
- T
RL
3
44O
rigin
al S
ched
ule
in T
DR
M
45W
EC
-TS
-IH
XA
-018
Tra
de s
tudy
on
Can
dida
te C
eram
ic M
ater
ial f
or IH
X A
Orig
inal
Dat
eS
uppl
ier
/ Des
ign
Aut
horit
y
46W
EC
-TS
-IH
XA
-019
Tra
de s
tudy
on
Can
dida
te C
eram
ic D
esig
ns fo
r IH
X A
Orig
inal
Dat
eS
uppl
ier
/ Des
ign
Aut
horit
y
47TR
L 3
- T
RL
4
48O
rigin
al S
ched
ule
in T
DR
M
49W
EC
-TS
-IH
XA
-020
Cer
amic
Det
aile
d D
esig
n D
ata
Nee
ds (
DD
Ns)
Sta
rtin
g da
tes
mov
ed to
mor
ere
alis
tic a
nd a
chie
vabl
e da
tes
Des
ign
Aut
horit
y
50W
EC
-TS
-IH
XA
-021
Cer
amic
Mat
eria
ls S
peci
ficat
ions
and
Pro
cure
men
tS
tart
ing
date
s m
oved
to m
ore
real
istic
and
ach
ieva
ble
date
sIN
L, O
RN
L
51W
EC
-TS
-IH
XA
-022
The
rmal
Phy
sica
l Pro
pert
ies
of C
eram
ics
Sta
rtin
g da
tes
mov
ed to
mor
ere
alis
tic a
nd a
chie
vabl
e da
tes
INL,
OR
NL,
AN
L, L
AN
L, S
NL,
BN
L,C
SIR
52W
EC
-TS
-IH
XA
-023
Mec
hani
cal P
rope
rtie
s of
Cer
amic
sS
tart
ing
date
s m
oved
to m
ore
real
istic
and
ach
ieva
ble
date
sIN
L, O
RN
L, A
NL,
LA
NL,
SN
L, B
NL,
CS
IR
53W
EC
-TS
-IH
XA
-024
Com
patib
ility
of C
eram
ic M
ater
ials
to N
GN
P H
e en
viro
nmen
tS
tart
ing
date
s m
oved
to m
ore
real
istic
and
ach
ieva
ble
date
sIN
L, O
RN
L
54W
EC
-TS
-IH
XA
-025
Man
ufac
turin
g T
echn
olog
ies
for
Cer
amic
Hea
t Exc
hang
ers
Sta
rtin
g da
tes
mov
ed to
mor
ere
alis
tic a
nd a
chie
vabl
e da
tes
CH
E d
esig
ner/
man
ufac
ture
r
55TR
L 4
- T
RL
5
56O
rigin
al S
ched
ule
in T
DR
MA
ssum
ing
unit
cell
is d
esig
ned
and
Fab
ricat
ed
57W
EC
-TS
-IH
XA
-026
Cer
amic
Mat
eria
ls C
odes
and
Sta
ndar
dsS
tart
ing
date
s m
oved
to m
ore
real
istic
and
ach
ieva
ble
date
sC
HE
sup
plie
r/de
sign
aut
horit
y, IN
L,O
RN
L, A
NL,
LA
NL
58W
EC
-TS
-IH
XA
-027
Met
hods
for
The
rmal
/Flu
id a
nd S
tres
s/S
trai
n M
odel
ing
Sta
rtin
g da
tes
mov
ed to
mor
ere
alis
tic a
nd a
chie
vabl
e da
tes
CH
E s
uppl
ier/
desi
gn a
utho
rity,
INL,
OR
NL,
AN
L, L
AN
L
59W
EC
-TS
-IH
XA
-028
Str
uctu
ral I
nteg
rity
Crit
eria
for
Cer
amic
Hea
t Exc
hang
ers
Sta
rtin
g da
tes
mov
ed to
mor
ere
alis
tic a
nd a
chie
vabl
e da
tes
CH
E s
uppl
ier/
desi
gn a
utho
rity,
INL,
OR
NL,
AN
L, L
AN
L
60W
EC
-TS
-IH
XA
-029
Per
form
ance
Mod
elin
g of
Cer
amic
Hea
t Exc
hang
ers
Sta
rtin
g da
tes
mov
ed to
mor
ere
alis
tic a
nd a
chie
vabl
e da
tes
CH
E s
uppl
ier/
desi
gn a
utho
rity,
INL,
OR
NL,
AN
L, L
AN
L
61W
EC
-TS
-IH
XA
-030
Tes
ting
of u
nit c
ell o
f Com
pact
Hea
t Exc
hang
erS
tart
dat
e m
oved
bac
k: S
mal
lS
cale
Dev
elop
men
t Tes
tC
HE
des
igne
r/m
anuf
actu
rer
(Hea
tric
,B
rayt
on E
nerg
y)
62TR
L 5
- T
RL
6
63O
rigin
al S
ched
ule
in T
DR
MA
ssum
ing
1.2M
W M
odul
e is
desi
gned
and
Fab
ricat
ed
64W
EC
-TS
-IH
XA
-031
Spe
cific
atio
n of
test
ing
of c
ompa
ct h
eat e
xcha
nger
mod
ule
(1.2
Mw
)S
tart
ing
date
mov
ed to
coi
ncid
ew
ith C
TF
Sta
rtin
g da
te: T
DL
CT
F
65W
EC
-TS
-IH
XA
-032
AS
ME
Cod
e C
ase
for
Cer
amic
Com
pact
Hea
t Exc
hang
er D
esig
nS
tart
ing
date
s m
oved
to m
ore
real
istic
and
ach
ieva
ble
date
sC
HE
sup
plie
r/de
sign
aut
horit
y, IN
L,O
RN
L, A
NL,
LA
NL
66TR
L 6
- T
RL
7
67O
rigin
al S
ched
ule
in T
DR
M
68W
EC
-TS
-IH
XA
-033
She
ll-si
de F
low
Dis
trib
utio
n an
d B
ypas
s Le
akag
e T
estin
gS
tart
ing
date
mov
ed to
coi
ncid
ew
ith C
TF
Sta
rtin
g da
te: T
DL
CT
F
69W
EC
-TS
-IH
XA
-034
Mul
ti-m
ode
Hea
t Tra
nsfe
r T
estin
gS
tart
ing
date
mov
ed to
coi
ncid
ew
ith C
TF
Sta
rtin
g da
te: T
DL
CT
F
70TR
L 7
- T
RL
8
71O
rigin
al S
ched
ule
in T
DR
M
72W
EC
-TS
-IH
XA
-035
Spe
cific
atio
ns o
f tes
ting
of a
full
scal
e co
mpa
ct H
eat E
xcha
nger
Sta
rt d
ate
mov
ed to
coi
ncid
e w
ithN
GN
P In
itial
Ope
ratin
g da
teN
GN
P
73IH
X B
74TR
L 3
- T
RL
4
CTF
$ 0.
00
NG
NP
$ 0.
00
Su
pp
lier
/ Des
ign
Au
tho
rity
$ 21
1,20
0.00
Su
pp
lier
/ Des
ign
Au
tho
rity
$ 21
1,20
0.00
Des
ign
Au
tho
rity
$ 17
6,00
0.00
INL
, OR
NL
$ 10
5,60
0.00
INL
, OR
NL
, AN
L, L
AN
L, S
NL
, BN
L, C
SIR
$ 33
8,62
4.00
INL
, OR
NL
, AN
L, L
AN
L, S
NL
, BN
L, C
SIR
$ 6,
350,
142.
00
INL
, OR
NL
$ 1,
199,
000.
00
CH
E d
esig
ner
/man
ufa
ctu
rer
$ 5,
275,
512.
00
CH
E s
up
plie
r/d
esig
n a
uth
ori
ty, I
NL
, OR
NL
, AN
L, L
AN
L$
1,52
1,30
0.00
CH
E s
up
plie
r/d
esig
n a
uth
ori
ty, I
NL
, OR
NL
, AN
L, L
AN
L$
415,
800.
00
CH
E s
up
plie
r/d
esig
n a
uth
ori
ty, I
NL
, OR
NL
, AN
L, L
AN
L$
280,
500.
00
CH
E s
up
plie
r/d
esig
n a
uth
ori
ty, I
NL
, OR
NL
, AN
L, L
AN
L$
280,
500.
00
CH
E d
esig
ner
/man
ufa
ctu
rer
(Hea
tric
, Bra
yto
n E
ner
gy)
$ 40
0,00
0.00
CTF
$ 0.
00
CH
E s
up
plie
r/d
esig
n a
uth
ori
ty, I
NL
, OR
NL
, AN
L, L
AN
L$
0.00
CTF
$ 0.
00
CTF
$ 0.
00
NG
NP
$ 0.
00
2007
2008
2009
2010
2011
2012
2013
2014
2015
2016
2017
2018
2019
2020
2021
2022
2023
2024
2025
2026
Tas
k
Spl
it
Pro
gres
s
Mile
ston
e
Sum
mar
y
Pro
ject
Sum
mar
y
Ext
erna
l Tas
ks
Ext
erna
l Mile
ston
e
Dea
dlin
e
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng
TD
RM
-017
_7.m
pp
Fig
ure
17-
2: M
od
ifie
d T
DR
M S
ched
ule
Fri
08/1
2/05
Pro
ject
: TD
RM
Sch
edul
e_te
rugg
etre
k D
ate:
Fri
08/1
2/05
IDN
otes
Tas
k N
ame
Cha
nge
to O
rigin
alP
ossi
ble
test
ing
faci
lity
loca
tions
75O
rigin
al S
ched
ule
in T
DR
M
76W
EC
-TS
-IH
XB
-001
Allo
y 80
0H M
ater
ial S
peci
ficat
ion
and
Pro
cure
men
tS
tart
ing
date
s m
oved
to m
ore
real
istic
and
ach
ieva
ble
date
sIN
L, O
RN
L
77W
EC
-TS
-IH
XB
-002
Dat
abas
e fo
r B
raze
d an
d D
iffus
ion
Bon
ded
Allo
y 80
0HS
tart
ing
date
s m
oved
to m
ore
real
istic
and
ach
ieva
ble
date
sIN
L, O
RN
L, A
NL,
CH
Ede
sign
ers/
man
ufac
ture
rs
78W
EC
-TS
-IH
XB
-003
Allo
y 80
0H H
igh
Tem
pera
ture
Mat
eria
l Pro
pert
ies
Sta
rtin
g da
tes
mov
ed to
mor
ere
alis
tic a
nd a
chie
vabl
e da
tes
INL,
OR
NL,
CS
IR
79W
EC
-TS
-IH
XB
-004
Effe
cts
of T
herm
al A
ging
and
Env
ironm
ent o
n A
lloy
800H
Pro
pert
ies
Sta
rtin
g da
tes
mov
ed to
mor
ere
alis
tic a
nd a
chie
vabl
e da
tes
INL,
OR
NL
80W
EC
-TS
-IH
XB
-005
Effe
cts
of E
nviro
nmen
tal E
xpos
ure
on A
lloy
800H
Bra
ze a
ndD
iffus
ion
Bon
ded
Join
tsS
tart
ing
date
s m
oved
to m
ore
real
istic
and
ach
ieva
ble
date
sIN
L, O
RN
L
81W
EC
-TS
-IH
XB
-006
Effe
cts
of G
rain
Siz
e an
d S
ectio
n T
hick
ness
on
Allo
y 80
0HP
rope
rtie
sS
tart
ing
date
s m
oved
to m
ore
real
istic
and
ach
ieva
ble
date
sIN
L, O
RN
L, A
NL,
LA
NL,
SN
L, B
NL,
CS
IR
82W
EC
-TS
-IH
XB
-007
Cor
rosi
on A
llow
ance
s fo
r A
lloy
800H
Sta
rtin
g da
tes
mov
ed to
mor
ere
alis
tic a
nd a
chie
vabl
e da
tes
INL,
OR
NL,
FZ
J, S
acla
y
83W
EC
-TS
-IH
XB
-008
The
rmal
/Flu
id M
odel
ing
Met
hods
for
IHX
BC
HE
des
igne
r/su
pplie
r, IN
L, O
RN
L,A
NL
84W
EC
-TS
-IH
XB
-009
Met
hods
for
Str
ess/
Str
ain
Mod
ling
of IH
X B
Sta
rtin
g da
tes
mov
ed to
mor
ere
alis
tic a
nd a
chie
vabl
e da
tes
CH
E d
esig
ner/
supp
lier,
INL,
OR
NL,
AN
L
85W
EC
-TS
-IH
XB
-010
Crit
eria
for
Str
uctu
ral I
nter
grity
of I
HX
BS
tart
ing
date
s m
oved
to m
ore
real
istic
and
ach
ieva
ble
date
sC
HE
des
igne
r/su
pplie
r, IN
L, O
RN
L,A
NL
86W
EC
-TS
-IH
XB
-011
Per
form
ance
Mod
elin
g M
etho
ds fo
r IH
X B
Sta
rtin
g da
tes
mov
ed to
mor
ere
alis
tic a
nd a
chie
vabl
e da
tes
CH
E d
esig
ner/
supp
lier,
INL,
OR
NL,
AN
L
87TR
L 4
- T
RL
5
88O
rigin
al S
ched
ule
in T
DR
MA
ssum
ing
unit
cell
is d
esig
ned
and
Fab
ricat
ed
89W
EC
-TS
-IH
XB
-012
Tes
ting
of U
nit C
ell o
f Com
pact
Hea
t Exc
hang
erS
tart
dat
e m
oved
bac
k: S
mal
lS
cale
Dev
elop
men
t Tes
tC
HE
des
igne
r/m
anuf
actu
rer
(Hea
tric
,B
rayt
on E
nerg
y)
90TR
L 5
- T
RL
6
91O
rigin
al S
ched
ule
in T
DR
M
92W
EC
-TS
-IH
XB
-013
Tes
ting
of in
tegr
ated
com
pact
Hea
t Exc
hang
erS
tart
ing
date
mov
ed to
coi
ncid
ew
ith C
TF
Sta
rtin
g da
te: T
DL
CT
F
93W
EC
-TS
-IH
XB
-014
AS
ME
III C
ode
Cas
e fo
r M
eatll
ic C
ompa
ct H
eat E
xcha
nger
Des
ign
Sta
rtin
g da
tes
mov
ed to
mor
ere
alis
tic a
nd a
chie
vabl
e da
tes
CH
E s
uppl
ier/
desi
gn a
utho
rity,
INL,
OR
NL,
AN
L, L
AN
L
94TR
L 6
- T
RL
7
95O
rigin
al S
ched
ule
in T
DR
M
96W
EC
-TS
-IH
XB
-015
She
ll-si
de F
low
Dis
trib
utio
n an
d B
ypas
s Le
akag
e T
estin
gS
tart
ing
date
mov
ed to
coi
ncid
ew
ith C
TF
Sta
rtin
g da
te: T
DL
CT
F
97W
EC
-TS
-IH
XB
-016
Mul
ti-m
odul
e H
eat T
rans
fer
Tes
ting
Sta
rtin
g da
te m
oved
to c
oinc
ide
with
CT
F S
tart
ing
date
: TD
LC
TF
98TR
L 7
- T
RL
8
99O
rigin
al S
ched
ule
in T
DR
M
100
WE
C-T
S-I
HX
B-0
17T
estin
g of
full
size
Com
pact
Hea
t Exc
hang
erS
tart
dat
e m
oved
to c
oinc
ide
with
NG
NP
Initi
al O
pera
ting
date
NG
NP
101
Pip
ing
102
TRL
4 -
TR
L5
103
Orig
inal
Sch
edul
e in
TD
RM
104
WE
C-T
S-P
IP-0
01P
HT
S h
igh-
tem
pera
ture
[760
°C a
nd 9
50°C
] pip
ing
cool
ing,
line
r&in
sula
tion
optio
ns tr
ade
stud
yO
rigin
al D
ate
Pip
ing
Sys
tem
Des
igne
r
105
WE
C-T
S-P
IP-0
02P
HT
S lo
w-t
empe
ratu
re [3
50°C
] pip
ing
liner
and
insu
latio
n op
tions
trad
e st
udy
Orig
inal
Dat
eP
ipin
g S
yste
m D
esig
ner
106
WE
C-T
S-P
IP-0
03S
HT
S h
igh-
tem
pera
ture
[840
°C a
nd 9
00°C
] pip
ing
liner
and
insu
altio
n st
udy
Orig
inal
Dat
eP
ipin
g S
yste
m D
esig
ner
107
WE
C-T
S-P
IP-0
04S
HT
S m
ediu
m-t
empe
ratu
re [6
59°C
and
700
°C] p
ipin
g lin
er a
ndin
sula
tion
trad
e st
udy
Orig
inal
Dat
eP
ipin
g S
yste
m D
esig
ner
108
WE
C-T
S-P
IP-0
05S
HT
S lo
w-t
empe
ratu
re [<
300°
C] p
ipin
g lin
er a
nd in
sula
tion
trad
est
udy
Orig
inal
Dat
eP
ipin
g S
yste
m D
esig
ner
109
TRL
5 -
TR
L 6
110
Orig
inal
Sch
edul
e in
TD
RM
111
WE
C-T
S-P
IP-0
06E
ffect
s of
He
infil
trat
ion
on th
erm
al c
ondu
ctiv
ity o
f ins
ulat
ion
mat
eria
lS
tart
dat
e m
oved
forw
ard:
Sm
all
Sca
le D
evel
opm
ent T
est
Insu
latio
n M
anuf
actu
rers
, IN
L, O
RN
L,A
NL
INL
, OR
NL
$ 70
,400
.00
INL
, OR
NL
, AN
L, C
HE
des
ign
ers/
man
ufa
ctu
rers
$ 3,
730,
875.
50
INL
, OR
NL
, CS
IR$
80,9
72.3
2 INL
, OR
NL
$ 10
4,50
9.02
INL
, OR
NL
$ 36
7,61
6.37
INL
, OR
NL
, AN
L, L
AN
L, S
NL
, BN
L, C
SIR
$ 83
2,45
6.90
INL
, OR
NL
, FZ
J, S
acla
y$
1,90
1,07
5.00
CH
E d
esig
ner
/su
pp
lier,
INL
, OR
NL
, AN
L$
140,
250.
00
CH
E d
esig
ner
/su
pp
lier,
INL
, OR
NL
, AN
L$
140,
250.
00
CH
E d
esig
ner
/su
pp
lier,
INL
, OR
NL
, AN
L$
140,
250.
00
CH
E d
esig
ner
/su
pp
lier,
INL
, OR
NL
, AN
L$
140,
250.
00
CH
E d
esig
ner
/man
ufa
ctu
rer
(Hea
tric
, Bra
yto
n E
ner
gy)
$ 20
0,00
0.00
CTF
$ 0.
00
CH
E s
up
plie
r/d
esig
n a
uth
ori
ty, I
NL
, OR
NL
, AN
L, L
AN
L$
0.00
CTF
$ 0.
00
CTF
$ 0.
00
NG
NP
$ 0.
00
Pip
ing
Sys
tem
Des
ign
er$
211,
200.
00 Pip
ing
Sys
tem
Des
ign
er$
140,
800.
00 Pip
ing
Sys
tem
Des
ign
er$
211,
200.
00 Pip
ing
Sys
tem
Des
ign
er$
140,
800.
00 Pip
ing
Sys
tem
Des
ign
er$
105,
600.
00
Insu
lati
on
Man
ufa
ctu
rers
, IN
L, O
RN
L, A
NL
$ 40
0,00
0.00
2007
2008
2009
2010
2011
2012
2013
2014
2015
2016
2017
2018
2019
2020
2021
2022
2023
2024
2025
2026
Tas
k
Spl
it
Pro
gres
s
Mile
ston
e
Sum
mar
y
Pro
ject
Sum
mar
y
Ext
erna
l Tas
ks
Ext
erna
l Mile
ston
e
Dea
dlin
e
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng
TD
RM
-017
_7.m
pp
Fig
ure
17-
2: M
od
ifie
d T
DR
M S
ched
ule
Fri
08/1
2/05
Pro
ject
: TD
RM
Sch
edul
e_te
rugg
etre
k D
ate:
Fri
08/1
2/05
IDN
otes
Tas
k N
ame
Cha
nge
to O
rigin
alP
ossi
ble
test
ing
faci
lity
loca
tions
112
WE
C-T
S-P
IP-0
07T
he e
ffect
of f
luid
impu
ritie
s on
insu
latio
n pr
oper
ties
Sta
rt d
ate
mov
ed fo
rwar
d: S
mal
lS
cale
Dev
elop
men
t Tes
tIn
sula
tion
Man
ufac
ture
rs, I
NL,
OR
NL,
AN
L
113
WE
C-T
S-P
IP-0
08R
e-ev
alua
tion
of n
eede
d m
atur
atio
n ta
sks
base
d on
Tra
de s
tudi
esS
tart
ing
date
s m
oved
to m
ore
real
istic
and
ach
ieva
ble
date
sP
ipin
g S
yste
m D
esig
ner
114
TRL
6 -
TR
L 7
115
Orig
inal
Sch
edul
e in
TD
RM
116
WE
C-T
S-P
IP-0
09P
erfo
rman
ce&
envi
ronm
enta
l tes
ting:
prot
otyp
ical
hig
h-&
low
-tem
ppi
ping
/insu
latio
n sy
stem
Sta
rtin
g da
te m
oved
to c
oinc
ide
with
CT
F: T
DL/
CT
LC
TF
117
TRL
7 -
TR
L 8
118
Orig
inal
Sch
edul
e in
TD
RM
119
WE
C-T
S-P
IP-0
10T
estin
g of
full
sie
PH
TS
pip
ing
in N
GN
PS
tart
dat
e m
oved
to c
oinc
ide
with
NG
NP
Initi
al O
pera
ting
date
NG
NP
120
Mix
ing
Ch
amb
er
121
TRL
6 -
TR
L 7
122
Orig
inal
Sch
edul
e in
TD
RM
123
WE
C-T
S-M
C-0
01E
nhan
ced
Mix
ing
Dev
ices
Tes
t Spe
cific
atio
nO
rigin
al D
ate
Sup
plie
r / D
esig
n A
utho
rity
124
WE
C-T
S-M
C-0
02V
ibra
tion
Dam
ping
Dev
ices
Tes
t Spe
cific
atio
nO
rigin
al D
ate
supp
lier
site
125
WE
C-T
S-M
C-0
03P
artia
l or
Ful
l Sca
le F
low
Mix
ing
Cha
mbe
r M
odel
Tes
t Spe
cific
atio
nS
tart
ing
date
mov
ed to
coi
ncid
ew
ith C
TF
Sta
rtin
g da
te: C
TL
supp
lier
site
126
TRL
7 -
TR
L 8
127
Orig
inal
Sch
edul
e in
TD
RM
128
WE
C-T
S-M
C-0
04P
roto
type
Flo
w M
ixin
g C
ham
ber
Tes
t Spe
cific
atio
nS
tart
dat
e m
oved
to c
oinc
ide
with
NG
NP
Initi
al O
pera
ting
date
CT
F /
Sup
plie
r si
te
129
Ste
am G
ener
ato
r
130
TRL
6 -
TR
L 7
131
Orig
inal
Sch
edul
e in
TD
RM
132
Tra
de S
tudi
esn/
a
133
WE
C-T
S-S
G-0
01D
own
sele
ctio
n tr
ade
stud
y:de
term
ine
the
pref
erre
d co
ncep
tual
arra
ngem
ent o
f the
SG
Orig
inal
Dat
en/
a
134
WE
C-T
S-S
G-0
02D
efin
e re
quire
men
ts a
nd d
esig
n de
tails
for
the
SG
in th
e P
CS
syst
em c
onte
xtT
o be
per
form
ed a
fter
Tra
de S
tudy
n/a
135
WE
C-T
S-S
G-0
03P
erfo
rm c
onfig
urat
ion
deve
lopm
ent t
ests
to s
ubst
antia
te th
e de
sign
To
be p
erfo
rmed
afte
r T
rade
Stu
dyn/
a
136
WE
C-T
S-S
G-0
04D
esig
n an
d su
pply
a s
cale
pro
toty
pe fo
r th
e te
stin
g in
the
CT
FM
oved
to b
e fin
ishe
d be
fore
test
ing
in C
TF
CT
F
137
WE
C-T
S-S
G-0
05P
erfo
rman
ce te
stin
g in
CT
FS
tart
ing
date
mov
ed to
coi
ncid
ew
ith C
TF
Sta
rtin
g da
te: C
TL
138
TRL
7 -
TR
L 8
139
Orig
inal
Sch
edul
e in
TD
RM
140
WE
C-T
S-S
G-0
06C
ompl
ete
final
des
ign
of th
e pr
otot
ype
SG
for
the
NG
NP
Sta
rtin
g da
tes
mov
ed to
mor
ere
alis
tic a
nd a
chie
vabl
e da
tes
n/a
141
WE
C-T
S-S
G-0
07F
abric
ate
and
deliv
er to
NG
NP
Site
Mov
ed to
be
finis
hed
befo
re te
stin
gin
CT
Fn/
a
142
WE
C-T
S-S
G-0
08In
stal
l and
ope
rate
Sta
rt d
ate
mov
ed to
coi
ncid
e w
ithN
GN
P In
itial
Ope
ratin
g da
teN
GN
P
143
Hyd
rog
en P
rod
uct
ion
Sys
tem
144
Su
lfu
ric
Aci
d D
eco
mp
osi
tio
nO
rig
inal
Dat
en
/a
145
Up
to c
ompl
etio
n of
S-I
ILS
146
Com
plet
e an
alys
is, s
uppo
rtin
g da
ta, m
ater
ials
test
ing
and
cata
lyst
choi
ce &
test
s
147
Pilo
t tes
t of D
ecom
pose
r
148
Eng
inee
ring
test
of D
ecom
pose
r
Insu
lati
on
Man
ufa
ctu
rers
, IN
L, O
RN
L, A
NL
$ 45
0,00
0.00
Pip
ing
Sys
tem
Des
ign
er$
105,
600.
00
CTF
$ 0.
00
NG
NP
$ 0.
00
Su
pp
lier
/ Des
ign
Au
tho
rity
$ 25
0,00
0.00 su
pp
lier
site
$ 0.
00
sup
plie
r si
te$
0.00
CTF
/ S
up
plie
r si
te$
0.00
n/a
$ 0.
00
n/a
$ 0.
00
n/a
$ 0.
00
n/a
$ 0.
00
CTF
$ 0.
00
$ 0.
00
n/a
$ 0.
00
n/a
$ 0.
00
NG
NP
$ 0.
00
$ 0.
00
$ 1,
500,
000.
00
$ 10
,300
,000
.00
$ 22
,000
,000
.00
2007
2008
2009
2010
2011
2012
2013
2014
2015
2016
2017
2018
2019
2020
2021
2022
2023
2024
2025
2026
Tas
k
Spl
it
Pro
gres
s
Mile
ston
e
Sum
mar
y
Pro
ject
Sum
mar
y
Ext
erna
l Tas
ks
Ext
erna
l Mile
ston
e
Dea
dlin
e
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng
TD
RM
-017
_7.m
pp
Fig
ure
17-
2: M
od
ifie
d T
DR
M S
ched
ule
Fri
08/1
2/05
Pro
ject
: TD
RM
Sch
edul
e_te
rugg
etre
k D
ate:
Fri
08/1
2/05
IDN
otes
Tas
k N
ame
Cha
nge
to O
rigin
alP
ossi
ble
test
ing
faci
lity
loca
tions
149
Pro
toty
pe te
st o
f Dec
ompo
ser
150
Su
lfu
r D
ioxi
de
Ele
ctro
lysi
s Te
chn
olo
gy
Are
a
151
Up
to c
ompl
etio
n of
cel
l dem
onst
ratio
n at
tem
pera
ture
and
pre
ssur
e
152
HyS
ILS
and
opt
imiz
ed c
ell d
emon
stra
tion
153
Sca
le-u
p ce
lls to
400
cm
2 ,
and
Ele
ctro
lyze
r P
ilot T
est –
mod
ule
154
Sca
le-u
p ce
lls to
100
0 cm
2 an
d E
ngin
eerin
g te
st o
f Ele
ctro
lyze
r
155
Sca
le-u
p ce
lls to
1 m
2 an
d P
roto
type
test
of E
lect
roly
zer
156
Bu
nse
n R
eact
ion
an
d H
I Dec
om
po
sist
ion
Tec
hn
olo
gy
Are
a
157
Up
to c
ompl
etio
n of
S-I
ILS
–B
unse
n: T
RL
158
HI S
ectio
n E
xper
imen
tal T
est
– H
I
159
Bun
sen
and
HI S
yste
ms
Pilo
t Tes
t
160
Bun
sen
and
HI S
yste
ms
Eng
inee
ring
Tes
t
161
Pro
toty
pe H
PS
Tes
t: S
ulfu
ric A
cid,
Bun
sen
& H
I Sec
tions
162
Hig
h T
emp
erat
ure
Ste
am E
lect
roly
sis
Tech
no
log
y A
rea
163
Up
to c
ompl
etio
n of
ILS
164
Ful
l-sca
le s
tack
dem
onst
ratio
n
165
Pilo
t Tes
t
166
Pro
toty
pe H
PS
Tes
t
167
Fu
el E
lem
ents
168
TRL
6 -
TR
L 7
169
WE
C-T
S-F
UE
L-0
01P
rod
uct
ion
Fu
el Ir
rad
iati
on
Tes
ts f
or
No
rmal
Op
erat
ion
alC
on
dit
ion
sIN
M F
acili
ty
170
Irra
diat
ion
plan
ning
& P
repa
ratio
nO
rigin
al D
ate
171
Irra
diat
ion
of P
re-P
rodu
ctio
n F
uel
Orig
inal
Dat
e
172
PIE
and
Ana
lysi
sO
rigin
al D
ate
173
WE
C-T
S-F
UE
L-0
02P
rod
uct
ion
Fu
el H
eat-
up
Tes
ts a
t 16
00°C
an
d 1
800°
C.
INM
Fac
ility
174
Phy
sica
l Hea
ting
Tes
tO
rigin
al D
ate
175
PIE
and
ana
lysi
s of
Hea
ted
Sph
eres
Orig
inal
Dat
e
176
WE
C-T
S-F
UE
L-0
03F
uel
Mat
rix
Gra
ph
ite
Irra
dia
tio
n t
ests
an
d P
IEIV
V-2
M R
uss
ian
Rea
cto
r
177
Irra
diat
ion
Pla
nnin
g &
Pre
para
tion
Orig
inal
Dat
e
178
Irra
diat
ion
and
PIE
Orig
inal
Dat
e
179
WE
C-T
S-F
UE
L-0
04M
ach
ined
Gra
ph
ite
Irra
dia
tio
n t
ests
an
d P
IEIV
V-2
M R
uss
ian
Rea
cto
r
180
Irra
diat
ion
Pla
nnin
g &
Pre
para
tion
Orig
inal
Dat
e
181
Irra
diat
ion
and
PIE
Orig
inal
Dat
e
182
TRL
7 -
TR
L 8
183
WE
C-T
S-F
UE
L-0
05P
rod
uct
ion
Fu
el Ir
rad
iati
on
Tes
ts f
or
NG
NP
No
rmal
Op
erat
ion
al C
on
dit
ion
sS
uit
able
Tes
t R
eact
or
- A
TR
184
Irra
diat
ion
plan
ning
& P
repa
ratio
nO
rigin
al D
ate
185
Irra
diat
ion
of P
re-P
rodu
ctio
n F
uel
Orig
inal
Dat
e
$ 27
,000
,000
.00
$ 3,
000,
000.
00
$ 4.
80
$ 36
.50
$ 59
,000
,000
.00
$ 22
,000
,000
.00
$ 0.
00 $ 3,
000,
000.
00
$ 43
,000
,000
.00
$ 58
,000
,000
.00
$ 0.
00
$ 0.
00
$ 35
,000
,000
.00
$ 30
,000
,000
.00
$ 50
,000
,000
.00
$ 0.
00
$ 0.
00
$ 0.
00
$ 0.
00
$ 0.
00
$ 0.
00
$ 0.
00
$ 0.
00
$ 0.
00
$ 0.
00
$ 0.
00
2007
2008
2009
2010
2011
2012
2013
2014
2015
2016
2017
2018
2019
2020
2021
2022
2023
2024
2025
2026
Tas
k
Spl
it
Pro
gres
s
Mile
ston
e
Sum
mar
y
Pro
ject
Sum
mar
y
Ext
erna
l Tas
ks
Ext
erna
l Mile
ston
e
Dea
dlin
e
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng
TD
RM
-017
_7.m
pp
Fig
ure
17-
2: M
od
ifie
d T
DR
M S
ched
ule
Fri
08/1
2/05
Pro
ject
: TD
RM
Sch
edul
e_te
rugg
etre
k D
ate:
Fri
08/1
2/05
IDN
otes
Tas
k N
ame
Cha
nge
to O
rigin
alP
ossi
ble
test
ing
faci
lity
loca
tions
186
PIE
and
Ana
lysi
sO
rigin
al D
ate
187
WE
C-T
S-F
UE
L-0
06P
rod
uct
ion
Fu
el H
eat-
up
Tes
ts a
t 17
00°C
an
d 1
900°
C.
Su
itab
le T
est
Rea
cto
r -
ATR
188
Phy
sica
l Hea
ting
Tes
tO
rigin
al D
ate
189
PIE
and
ana
lysi
s of
Hea
ted
Sph
eres
Orig
inal
Dat
e
190
WE
C-T
S-F
UE
L-0
07F
uel
Mat
rix
Gra
ph
ite
Irra
dia
tio
n t
ests
an
d P
IES
uit
able
Tes
t R
eact
or
- A
TR
191
Irra
diat
ion
Pla
nnin
g &
Pre
para
tion
Orig
inal
Dat
e
192
Irra
diat
ion
and
PIE
Orig
inal
Dat
e
193
Co
re S
tru
ctu
re C
eram
ics
194
TRL
6 -
TR
L 7
195
WE
C-T
S-C
SC
-001
PB
MR
Rel
evan
tO
rigin
al D
ate
196
WE
C-T
S-C
SC
-002
Ext
ende
d P
rope
rtie
s of
Irra
diat
ed G
raph
ite a
t Low
Tem
pera
ture
sO
rigin
al D
ate
Nat
iona
l Lab
orat
ory
/ Uni
vers
ity
197
WE
C-T
S-C
SC
-003
Ext
ende
d P
rope
rtie
s of
Irra
diat
ed G
raph
ite a
t Hig
h T
empe
ratu
res
Orig
inal
Dat
eN
atio
nal L
abor
ator
y / U
nive
rsity
198
WE
C-T
S-C
SC
-004
Cha
ract
eriz
e R
ace
Tra
ck S
trap
and
Tie
Rod
Mat
eria
lO
rigin
al D
ate
Nat
iona
l Lab
orat
ory
/ Uni
vers
ity
199
WE
C-T
S-C
SC
-005
Insu
latio
n M
ater
ial (
Uni
rrad
iate
d D
ata
Nee
ded)
Orig
inal
Dat
eN
atio
nal L
abor
ator
y / U
nive
rsity
200
Res
erve
Sh
utd
ow
n S
yste
m
201
Orig
inal
Sch
edul
e in
TD
RM
202
TR
L 6
- T
RL
7O
rigin
al D
ate
n/a
203
TR
L 7
- T
RL
8O
rigin
al D
ate
n/a
204
Rea
ctiv
ity
Co
ntr
ol S
yste
m
205
Orig
inal
Sch
edul
e in
TD
RM
206
TR
L 6
- T
RL
7O
rigin
al D
ate
n/a
207
TR
L 7
- T
RL
8O
rigin
al D
ate
n/a
208
Co
re C
on
dit
ion
ing
Sys
tem
209
TRL
6 -
TR
L 7
210
WE
C-T
S-C
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-001
Val
ves
deve
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ent T
est S
peci
ficat
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Orig
inal
Dat
en/
a
211
WE
C-T
S-C
CS
-002
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wer
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elop
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t Tes
t Spe
cific
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ate
n/a
212
TRL
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213
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214
Rea
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.Adv
ance
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217
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218
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TD
RM
219
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inal
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en/
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222
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alid
ate
theo
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al a
naly
sis
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ump
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ct o
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CC
S p
ress
ure
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inal
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en/
a
$ 0.
00
$ 0.
00
$ 0.
00 $ 0.
00
$ 0.
00
$ 0.
00
Nat
ion
al L
abo
rato
ry /
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iver
sity
$ 0.
00
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ion
al L
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n/a
$ 0.
00
n/a
$ 0.
00
n/a
$ 0.
00
n/a
$ 0.
00
2007
2008
2009
2010
2011
2012
2013
2014
2015
2016
2017
2018
2019
2020
2021
2022
2023
2024
2025
2026
Tas
k
Spl
it
Pro
gres
s
Mile
ston
e
Sum
mar
y
Pro
ject
Sum
mar
y
Ext
erna
l Tas
ks
Ext
erna
l Mile
ston
e
Dea
dlin
e
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng
TD
RM
-017
_7.m
pp
Fig
ure
17-
2: M
od
ifie
d T
DR
M S
ched
ule
Fri
08/1
2/05
Pro
ject
: TD
RM
Sch
edul
e_te
rugg
etre
k D
ate:
Fri
08/1
2/05
NGNP-CTF MTECH-TDRM-017 NGNP Technology Development Road Mapping Section 17 : Integrated Schedule and Cost Estimate
NGNP-CTF MTECH-TDRM-017_Rev0.doc 10/27/2008
23 of 89
17.1.4 Modified CTF Schedule
Figure 17-3 shows the test specifications relevant to the CTF only and especially for the 950ºC Reactor Outlet (ROT) Temperature related SSCs. These include Small Scale Development Tests (SSDTs), Technology development Loops (TDLs), Component Qualification Loops and the envisaged Circulator Test Loop (CTL).
The SSDTs are envisaged to incorporate separate and multiple effects tests which are
more sophisticated than normal university of laboratory testing. The TDLs are envisaged to be loops with mass flows in the order of 3.6 kg/s at temperature of 950ºC and pressures up to 9 MPa. The CQLs are earmarked for larger component testing and consists of a combination of TDLs linked together to provide higher mass flows and more heating capacity.
For the case in which the NGNP ROT is lowered to 750°C, the test specifications that
will still be relevant can be seen in Figure 17-4. This CTF test schedule is an input to the Test Loop(s) Preconceptual Design and will be
updated as the Test Loop(s) Preconceptual Design develops.
IDN
otes
Task
Nam
e1
Test
Spe
c N
umbe
rM
odifi
ed C
TF O
nly
950°
C2
Circ
ulat
or3
TRL
6 - T
RL
7
4W
EC
-TS
-CIR
C-0
01E
MB
s, c
atch
er b
earin
gs T
est S
peci
ficat
ion
5W
EC
-TS
-CIR
C-0
02H
eliu
m R
otat
ing
seal
s Te
st S
peci
ficat
ion
6W
EC
-TS
-CIR
C-0
03P
artia
l or F
ull s
cale
circ
ulat
or M
odel
Tes
t Spe
cific
atio
n
7IH
X A
(Met
allic
)8
TRL
4 - T
RL
5
9W
EC
-TS
-IHX
A-1
2S
peci
ficat
ion
of te
stin
g of
uni
t cel
l of c
ompa
ct H
eat E
xcha
nger
s
10TR
L 5
- TR
L 6
11W
EC
-TS
-IHX
A-0
13S
peci
ficat
ion
of te
stin
g of
com
pact
hea
t exc
hang
er m
odul
e (1
.2M
W)
12TR
L 6
- TR
L 7
13W
EC
-TS
-IHX
A-0
15S
hell
Sid
e Fl
ow D
istri
butio
n an
d B
ypas
s Le
akag
e Te
stin
g
14W
EC
-TS
-IHX
A-0
16M
ulti-
mod
ule
Hea
t Tra
nsfe
r Tes
ting
15IH
X A
(Cer
amic
)16
TRL
4 - T
RL
5
17W
EC
-TS
-IHX
A-0
30Te
stin
g of
uni
t cel
l of C
ompa
ct H
eat E
xcha
nger
18TR
L 5
- TR
L 6
19W
EC
-TS
-IHX
A-0
31S
peci
ficat
ion
of te
stin
g of
com
pact
hea
t exc
hang
er m
odul
e (1
.2M
w)
20TR
L 6
- TR
L 7
21W
EC
-TS
-IHX
A-0
33S
hell-
side
Flo
w D
istri
butio
n an
d B
ypas
s Le
akag
e Te
stin
g
22W
EC
-TS
-IHX
A-0
34M
ulti-
mod
ule
Hea
t Tra
nsfe
r Tes
ting
23IH
X B
24TR
L 4
- TR
L 5
25W
EC
-TS
-IHX
B-0
12Te
stin
g of
Uni
t Cel
l of C
ompa
ct H
eat E
xcha
nger
26TR
L 5
- TR
L 6
27W
EC
-TS
-IHX
B-0
13Te
stin
g of
inte
grat
ed c
ompa
ct H
eat E
xcha
nger
28TR
L 6
- TR
L 7
29W
EC
-TS
-IHX
B-0
15S
hell-
side
Flo
w D
istri
butio
n an
d B
ypas
s Le
akag
e Te
stin
g
30W
EC
-TS
-IHX
B-0
16M
ulti-
mod
e H
eat T
rans
fer T
estin
g
31Pi
ping
32TR
L 5
- TR
L 6
33W
EC
-TS
-PIP
-006
Effe
cts
of H
e in
filtra
tion
on th
erm
al c
ondu
ctiv
ity o
f ins
ulat
ion
mat
eria
l
34W
EC
-TS
-PIP
-007
The
effe
ct o
f flu
id im
purit
ies
( C) o
n in
sula
tion
prop
ertie
s
35W
EC
-TS
-PIP
-008
Re-
eval
uatio
n of
nee
ded
mat
urat
ion
task
s ba
sed
on T
rade
stu
dies
36TR
L 6
- TR
L 7
37W
EC
-TS
-PIP
-009
Per
form
ance
&en
viro
nmen
tal t
estin
g:pr
otot
ypic
al h
igh-
& lo
w-te
mp
pipi
ng/in
sula
tion
syst
em
38M
ixin
g C
ham
ber
39TR
L 6
- TR
L 7
40W
EC
-TS
-MC
-003
Par
tial o
r Ful
l Sca
le F
low
Mix
ing
Cha
mbe
r Mod
el T
est S
peci
ficat
ion
41St
eam
Gen
erat
or42
TRL
6 - T
RL
7
43W
EC
-TS
-SG
-005
Per
form
ance
test
ing
in C
TF
CTF
Initi
al O
pera
ting
Dat
e
Sm
all S
cale
Dev
elop
men
t Tes
ts
Tech
nolo
gy D
evel
opm
ent L
oop
Circ
ulat
or T
est L
oop
2008
2009
2010
2011
2012
2013
2014
2015
2016
2017
2018
2019
2020
2021
2022
Task
Spl
it
Pro
gres
s
Mile
ston
e
Sum
mar
y
Pro
ject
Sum
mar
y
Ext
erna
l Tas
ks
Ext
erna
l Mile
ston
e
Dea
dlin
e
NG
NP
-CTF
MTE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng
CTF
Sch
edul
e 95
0.m
pp
Figu
re 1
7-3:
Mod
ified
CTF
Sch
edul
e - 9
50°C
Thu
08/1
2/04
Pro
ject
: CTF
Sch
edul
e 95
0D
ate:
Thu
08/
12/0
4
IDN
otes
Task
Nam
e1
Test
Spe
c N
umbe
rM
odifi
ed C
TF O
nly
750°
C
2C
ircul
ator
3TR
L 6
- TR
L 7
4W
EC
-TS
-CIR
C-0
01E
MB
s, c
atch
er b
earin
gs T
est S
peci
ficat
ion
5W
EC
-TS
-CIR
C-0
02H
eliu
m R
otat
ing
seal
s Te
st S
peci
ficat
ion
6W
EC
-TS
-CIR
C-0
03P
artia
l or F
ull s
cale
circ
ulat
or M
odel
Tes
t Spe
cific
atio
n
7IH
X B
8TR
L 4
- TR
L 5
9W
EC
-TS
-IHX
B-0
12Te
stin
g of
Uni
t Cel
l of C
ompa
ct H
eat E
xcha
nger
10TR
L 5
- TR
L 6
11W
EC
-TS
-IHX
B-0
13Te
stin
g of
inte
grat
ed c
ompa
ct H
eat E
xcha
nger
12TR
L 6
- TR
L 7
13W
EC
-TS
-IHX
B-0
15S
hell-
side
Flo
w D
istri
butio
n an
d B
ypas
s Le
akag
e Te
stin
g
14W
EC
-TS
-IHX
B-0
16M
ulti-
mod
ule
Hea
t Tra
nsfe
r Tes
ting
15Pi
ping
16TR
L 5
- TR
L 6
17W
EC
-TS
-PIP
-006
Effe
cts
of H
e in
filtra
tion
on th
erm
al c
ondu
ctiv
ity o
f ins
ulat
ion
mat
eria
l
18W
EC
-TS
-PIP
-007
The
effe
ct o
f flu
id im
purit
ies
( C) o
n in
sula
tion
prop
ertie
s
19W
EC
-TS
-PIP
-008
Re-
eval
uatio
n of
nee
ded
mat
urat
ion
task
s ba
sed
on T
rade
stu
dies
20TR
L 6
- TR
L 7
21W
EC
-TS
-PIP
-009
Per
form
ance
&en
viro
nmen
tal t
estin
g:pr
otot
ypic
al h
igh-
& lo
w-te
mp
pipi
ng/in
sula
tion
syst
em
22M
ixin
g C
ham
ber
23TR
L 6
- TR
L 7
24W
EC
-TS
-MC
-003
Par
tial o
r Ful
l Sca
le F
low
Mix
ing
Cha
mbe
r Mod
el T
est S
peci
ficat
ion
25St
eam
Gen
erat
or
26TR
L 6
- TR
L 7
27W
EC
-TS
-SG
-005
Per
form
ance
test
ing
in C
TF
CTF
Initi
al O
pera
ting
Dat
e
Sm
all S
cale
Dev
elop
men
t Tes
ts
Tech
nolo
gy D
evel
opm
ent L
oop
Circ
ulat
or T
est L
oop
2008
2009
2010
2011
2012
2013
2014
2015
2016
2017
2018
2019
2020
2021
2022
Task
Spl
it
Pro
gres
s
Mile
ston
e
Sum
mar
y
Pro
ject
Sum
mar
y
Ext
erna
l Tas
ks
Ext
erna
l Mile
ston
e
Dea
dlin
e
NG
NP
-CTF
MTE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng
CTF
Sch
edul
e 75
0.m
pp
Figu
re 1
7-4:
CTF
Sch
edul
e 75
0°C
Thu
08/1
2/04
Pro
ject
: CTF
Sch
edul
e 75
0.m
ppD
ate:
Thu
08/
12/0
4
NGNP-CTF MTECH-TDRM-017 NGNP Technology Development Road Mapping Section 17 : Integrated Schedule and Cost Estimate
NGNP-CTF MTECH-TDRM-017_Rev0.doc 10/27/2008
26 of 89
17.1.5 Conclusion
Pending further schedule enhancements and optimization, the number of loops required in the CTF is forecasted in Table 17.1. (This will be confirmed as part of the Test Loop(s) Preconceptual Design)
Table 17-1: The number of loops required in the CTF
Number of: 950ºC ROT Related SSCs
750ºC ROT Related SSCs
Technology Development Loops 5-6 2-3 Circulator Test Loops 1 1 CQL-1 1 1
For the 950ºC ROT it is forecasted that five to six TDLs are required, This can be
optimized (and will be as part of the Test Loop(s) Preconceptual Design). For instance if the IHX A (Ceramic) tests are conducted after the IHX A (Metallic) testing is completed), two TDLs will fall away. As the methods and software used in the design matures some of the scheduled testing could also be reduced as risks will be mitigated though code verification and validation.
For the 750ºC ROT it is forecasted that two TDLs are required for testing of IHX B. It is
forecasted that a CTL will be required to test the circulator as well as some of the piping sections and the mixing chamber.
The Component Qualification Loops (CQL-1) are envisaged for testing of larger
components that might be required as the NGNP design progresses and are configured using TDLs.
The number of Small Scale Development Tests will be determined as part of the Test
Loop(s) Preconceptual Design.
At the completion of the CTF Preconceptual Design, where the optimum construction and commissioning schedule for the CTF will be determined, the TDRM Schedules will be updated accordingly.
NGNP-CTF MTECH-TDRM-017 NGNP Technology Development Road Mapping Section 17 : Integrated Schedule and Cost Estimate
NGNP-CTF MTECH-TDRM-017_Rev0.doc 10/27/2008
27 of 89
17.2 COST ESTIMATE
17.2.1 Introduction
Cost estimates are provided for certain critical Systems, Structures and Components (SSCs) in this document. These SSCs entail inter alia the metallic IHX A, ceramic IHX A and IHX B, as well as the HTS Piping systems. For the purpose of this document, estimates have been provided only up to a TRL rating of 5, due to the high uncertainty that exists in estimating the costs for higher TRL advancements. Estimates for higher TRL advancements can only be provided when additional design information (preliminary or final) of the NGNP and components are available. For some of the SSCs, more design information is required in order to develop reliable cost estimates. These include the PHTS Circulator, SHTS Mixing Chamber and Steam Generator. Trade studies need to be done to progress the designs and to verify and determine the specific combinations of sub-components that will be used. There is enough time as per the modified schedule to perform the trade study before the advancement of the TRL and before possible testing in the CTF will be performed.
The Hydrogen production system cost estimate has been developed as part of the
Hydrogen Production Alternatives Study [17-3] and is presented in this document (see Tables 17-3 and 17-4). Estimates for the HPS shown in Table 17-3 (summary cost of original TDRMs) only incorporate total estimates for (i) sulfuric acid decomposition and (ii) sulfur dioxide electrolysis technologies, the respective technologies needed for the Hybrid Sulfur (HyS) hydrogen production system. Although a reference design has not been down selected for the HPS, the HyS process has been selected as the basis for the estimates shown.
Where cost information was not available, the WEC NGNP PCDR costs were used as the
basis, i.e., Fuel Elements, Core Structures Ceramics, etc [17-4]. The bulk of estimated costs provided are based on input received/readily available from
contributors/institutions conducting similar work in industry. Table 17-4 of this document captures the estimates made for the identified SSCs as well as possible test locations/facilities that were identified and are involved with similar testing programs. The compositions of the estimates made for each test specification are captured in individual specification estimates in Appendix A. The bases used in these sheets will be elaborated upon here after.
17.2.2 Assumptions and Bases of Cost Estimates The following assumptions and bases are applicable to the estimates shown in Appendix
A.
17.1.2.1 Applicability to Schedule The cost estimates stated in Table 17.4 are based on November 2008 dollar values. No
escalation for future years has been incorporated.
NGNP-CTF MTECH-TDRM-017 NGNP Technology Development Road Mapping Section 17 : Integrated Schedule and Cost Estimate
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17.1.2.2 TRL Advancements For the purpose of this document, estimates have only been provided up to a TRL rating
of 5 due to the high uncertainty that exists in estimating the costs for higher TRL advancements. Estimates for higher TRL advancements can only be provided when additional design information (preliminary or final) is available and the initial technology development has progressed to a more mature point.
17.1.2.3 Contingencies and Uncertainties
Contingencies for the proposed estimates given involve a 10 percent adjustment on resource, testing, materials and other applicable costs stated. This is separate from the adjustment factors applicable to the ceramic IHX A as well as IHX B. The adjustment factors applicable to IHX B are based on IHX A and are shown in Table 17.2. These factors have been used as the basis for the IHX B estimates due to time constraints. The adjustment factors for the ceramic IHX A have been based on a factor of 2 due to various uncertainties that still exist in the estimate process. These factors involve intricacies that exist relating to sample preparation, sample machining as well as the ceramic material that still needs to be identified through relevant trade studies.
Table 17-2: Cost Ratios for Metallic IHX A to IHX B
# IHX A Test
Specification IHX B Test
Specification Comments IHX A to IHX B Cost Ratio
1 617 Material Specification and Procure
800H Material Specification and
Procure
Adopt existing 800H specification, procure 1 to 2 heats vs. 3 for 617
>2
2 617 Joining Technology and Result Properties
Database for Braze & Diffusion Bond
800H
Equivalent work for both 1
3 Thermal/Physical/ Mech. Prop of 617
800H High Temp Material Properties
Adopt existing 800H database
>10
4
Effects of Thermal Ageing and Environment on 617 Properties
Effects of Thermal Ageing and
Environment on 800H
Adopt existing 800H database
>10
5 Covered in rows 2 and 4 above.
Effects of Environment
Exposure on 800H Braze & Diff
Bonds
Equivalent work for 617 and 800H
1
6 Effects of GS and Section Thickness on 617 Properties
Effects of GS and Section Thickness
on 800H Properties
Equivalent work for 617 and 800H
1
7 Corrosion Allowance for 617
Corrosion Allowance for
800H
Equivalent work for 617 and 800H but time and cost may be reduced by
working in parallel
1
8 ASME Sect III CC for 617
Existing ASME Section III Code
No or minimal cost for IHX B
>100
NGNP-CTF MTECH-TDRM-017 NGNP Technology Development Road Mapping Section 17 : Integrated Schedule and Cost Estimate
NGNP-CTF MTECH-TDRM-017_Rev0.doc 10/27/2008
29 of 89
# IHX A Test
Specification IHX B Test
Specification Comments IHX A to IHX B Cost Ratio
Case
9 Thermal/Fluid Modeling Methods
Thermal/Fluid Modeling Methods
Probably a shared task but with higher
temperatures to be considered for IHX A
1
10 Methods for Stress/Strain Modeling
Methods for Stress/Strain
Modeling
Probably a shared task but with higher
temperatures to be considered for IHX A
1.25
11 Structural Integrity Criteria
Structural Integrity Criteria
Probably a shared task but with higher
temperatures to be considered for IHX A
1.25
12 Performance Modeling Methods
Performance Modeling Methods
Probably a shared task but with higher
temperatures to be considered for IHX A
1
13 Unit Cell Tests Unit Cell Tests Separate and equivalent
in cost 1
At a ROT of 950°C, it is important to note that development of both IHX A (metallic or
ceramic) and IHX B will be required. At a ROT of 750°C, only the development of an IHX B will be applicable.
The confidence level of the cost estimates at present is +120%/-:60%, which corresponds
to an accuracy level of Class 4 as noted in [17-5].
17.1.2.4 General
Other bases for the estimates relating to resources used, testing estimates as well as materials are stated in Appendix A. Aspects lacking an estimate basis will only be updated when additional plant design information is available (preliminary or final). Until this information is readily available, only an allowance for certain identified tasks without a basis can be given.
NGNP-CTF MTECH-TDRM-017 NGNP Technology Development Road Mapping Section 17 : Integrated Schedule and Cost Estimate
NGNP-CTF MTECH-TDRM-017_Rev0.doc 10/27/2008
30 of 89
17.2.3 Summary Cost: Original TDRMs Table 17.3 shows the sum of cost estimates distributed along a timeline starting in
FY2009 and ending in FY2021. The starts and durations of the tasks corresponds to those noted in the original TDRMs. Comments and assumptions applicable to the values shown are given below Table 17.3.
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t R
oad
Map
ping
Rep
ort
Sec
tion
17: I
nteg
rate
d S
ched
ule
and
Cos
t E
stim
ate
Tab
le 1
7-3:
Sum
mar
y C
ost:
Ori
gina
l TD
RM
Su
mm
ary
cost
s: O
rig
inal
TD
RM
sS
SC
[1],
[2]
FY
2009
FY
2010
FY
2011
FY
2012
FY
2013
FY
2014
FY
201
5F
Y 2
016
FY
201
7F
Y 2
018
FY
201
9F
Y 2
020
FY
202
1T
ota
l
Circ
ulat
or [3
]$4
50,0
00$0
$0$0
$0$0
$0$0
$0$0
$0$0
$0$4
50,0
00IH
X A
(M
etal
lic)
$4,2
05,0
30$4
,464
,905
$3,3
00,9
71$1
,007
,072
$225
,225
$100
,000
$100
,000
$0$0
$0$0
$0$0
$13,
403,
203
IHX
A (
Cer
amic
)$5
,482
,274
$4,4
88,6
66$3
,896
,338
$0$0
$0$0
$0$7
05,9
25$7
05,9
25$7
05,9
25$3
80,3
25$4
00,0
00$1
6,76
5,37
8IH
X B
$3,1
07,6
90$2
,851
,809
$1,6
89,4
06$0
$0$1
00,0
00$1
00,0
00$0
$0$0
$0$0
$0$7
,848
,905
Pip
ing
$1,4
81,8
67$2
83,3
33$0
$0$0
$0$0
$0$0
$0$0
$0$0
$1,7
65,2
00M
ixin
g C
ham
ber
[3]
$0$0
$1,1
24,0
00$1
,124
,000
$0$0
$0$0
$0$0
$0$0
$0$2
,248
,000
Ste
am G
ener
ator
$0$4
,092
,000
$7,2
74,0
00$7
,741
,000
$2,8
14,0
00$0
$0$0
$0$0
$0$0
$0$2
1,92
1,00
0H
PS
[4]
$3,5
00,0
00$5
,300
,000
$12,
670,
000
$15,
610,
000
$15,
610,
000
$23,
110,
000
$30,
670,
000
$30,
670,
000
$24,
500,
000
$24,
500,
000
$7,8
00,0
00$0
$0$1
93,9
40,0
00F
uel
$4,5
00,0
00$6
,500
,000
$6,5
00,0
00$6
,500
,000
$5,5
00,0
00$3
,500
,000
$3,5
00,0
00$3
,500
,000
$4,5
00,0
00$0
$0$0
$0$4
4,50
0,00
0C
SC
$500
,000
$600
,000
$800
,000
$800
,000
$700
,000
$900
,000
$700
,000
$0$0
$0$0
$0$0
$5,0
00,0
00R
SS
n/a
n/a
n/a
n/a
n/a
n/a
n/a
n/a
n/a
n/a
n/a
n/a
n/a
n/a
RC
Sn/
an/
an/
an/
an/
an/
an/
an/
an/
an/
an/
an/
an/
an
/aC
CS
n/a
n/a
n/a
n/a
n/a
n/a
n/a
n/a
n/a
n/a
n/a
n/a
n/a
n/a
RC
CS
n/a
n/a
n/a
n/a
n/a
n/a
n/a
n/a
n/a
n/a
n/a
n/a
n/a
n/a
TO
TA
L (
$)$2
3,22
6,86
1$2
8,58
0,71
4$3
7,25
4,71
4$3
2,78
2,07
2$2
4,84
9,22
5$2
7,71
0,00
0$3
5,07
0,00
0$3
4,17
0,00
0$2
9,70
5,92
5$2
5,20
5,92
5$8
,505
,925
$380
,325
$400
,000
$113
,901
,686
[1]
E
stim
ates
not
ed fo
r so
me
SS
C's
are
thos
e gi
ven
in N
GN
P-1
6-R
PT
-001
(no
tabl
y M
ixin
g C
ham
ber,
Ste
am G
ener
ator
, Fue
l, C
SC
) du
e to
lim
ited
desi
gn
.
in
form
atio
n[2
]
Cos
ting
of R
SS
, RC
S, C
CS
and
RC
CS
mak
e pa
rt o
f PB
MR
DP
P a
nd a
re n
ot in
clud
ed[3
]
For
the
Circ
ulat
or, M
ixin
g C
ham
ber
as w
ell a
s th
e S
team
Gen
erat
or, c
once
pt d
esig
n ne
eds
to b
e pr
ogre
ssed
furt
her
befo
re s
ensi
ble
estim
atio
ns c
an b
e
.
mad
e[4
]
Sum
tota
l of H
PS
ref
lect
s to
tals
of s
ulfu
ric a
cid
deco
mpo
sitio
n te
chno
logy
dev
elop
men
t as
wel
l as
sulfu
r di
oxid
e el
ectr
olys
is te
chno
logy
dev
elop
men
t [N
GN
P-
.
CT
F M
TE
CH
-TD
RM
-008
]. F
or th
e pu
rpos
es o
f thi
s es
timat
ion,
est
imat
ions
ref
lect
cos
ts n
eede
d to
eta
blis
h H
ybrid
Sul
phur
hyd
roge
n pr
oduc
tion
syst
em (
even
.
th
ough
the
refe
renc
e de
sign
stil
l has
to b
e se
lect
ed).
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NGNP-CTF MTECH-TDRM-017 NGNP Technology Development Road Mapping Section 17 : Integrated Schedule and Cost Estimate
NGNP-CTF MTECH-TDRM-017_Rev0.doc 10/27/2008
32 of 89
17.2.4 Original TDRM Cost Estimate (Facilities Description and Total Cost Included)
Table 17.4 shows the original TDRM cost estimate for each test specification with
associated details regarding possible facilities that have the capabilities of conducting the relevant testing. Costing assumptions have also been listed at the end of the table. Detailed bases for each of the individual test specifications estimates are given in Specification cost estimate sheets shown in Appendix A.
Due to the large number of possible facilities that can conduct similar work to that stated
in the test specifications (notably materials qualification actions), only the facility capability is noted in Table 17.4 and not the facility availability. Facilities have been identified in the following areas:
1. Laboratories – These facilities are most common and widely available. Work associated with these facilities involves aspects relating to material qualification actions.
2. Small Scale Testing – Specialized testing on scaled units is required here and can in general be conducted by the relevant supplier or in a small scale development test loop (CTF capability)
3. CTF Testing – Testing of partial or full scaled units at relevant temperatures and pressures.
NG
NP
-CT
F-M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
SS
CT
est
Sp
ecif
icat
ion
Tes
t S
pec
ific
atio
n N
um
ber
Fac
ility
/Su
pp
ort
ing
Org
aniz
atio
ns
Du
rati
on
Fis
cal
Yea
r/s
To
tal (
$)
$450
,000
TR
L 6
- T
RL
7T
rade
stu
dies
to s
elec
t ref
eren
ce d
esig
nn/
aS
uppl
ier
/ Des
ign
Aut
horit
y12
Mon
ths
FY
201
0 -
FY
20
13$4
50,0
00
EM
Bs,
Cat
cher
bea
rings
Tes
t Spe
cific
atio
nW
EC
-TS
-CIR
C-0
01E
MB
s S
uppl
ier
Tes
t Fac
ility
12 M
onth
sF
Y 2
010
- F
Y
2013
[-]
Hel
ium
Rot
atin
g se
als
Tes
t Spe
cific
atio
nW
EC
-TS
-CIR
C-0
02R
otat
ing
Sea
l Sup
plie
r T
est F
acili
ty12
Mon
ths
FY
201
0 -
FY
20
13[-
]
Par
tial o
r F
ull s
cale
circ
ulat
or M
odel
Tes
t Spe
cific
atio
nW
EC
-TS
-CIR
C-0
03C
TF
/Sup
plie
r S
ite18
Mon
ths
FY
201
0 -
FY
20
13[-
]
TR
L 7
- T
RL
8P
roto
type
circ
ulat
or T
est S
peci
ficat
ion
WE
C-T
S-C
IRC
-004
NG
NP
Site
3 -
12 M
onth
sF
Y 2
016
- F
Y
2018
[-]
$13,
403,
203
TR
L 2
- T
RL
3A
lloy
617
Mat
eria
l Spe
cific
atio
n an
d pr
ocur
emen
tW
EC
-TS
-IH
XA
-001
INL,
OR
NL
12 M
onth
sF
Y 2
009
- F
Y
2012
$105
,600
Allo
y 61
7 Jo
inin
g T
echn
olog
y an
d R
esul
tant
Pro
pert
ies
WE
C-T
S-I
HX
A-0
02IN
L, O
RN
L, A
NL,
Com
pact
hea
t exc
hang
er
desi
gner
s/m
anuf
actu
rers
30 M
onth
sF
Y 2
009
- F
Y
2012
$3,7
35,4
03
The
rmal
/phy
sica
l and
mec
hani
cal p
rope
rtie
s of
Allo
y 61
7W
EC
-TS
-IH
XA
-003
INL,
OR
NL,
AN
L, L
AN
L, S
NL,
BN
L, C
SIR
36 M
onth
sF
Y 2
009
- F
Y
2012
$811
,258
Effe
cts
of th
erm
al A
ging
and
env
ironm
ent o
n A
lloy
617
WE
C-T
S-I
HX
A-0
04IN
L, O
RN
L42
Mon
ths
FY
200
9 -
FY
20
12$4
,491
,177
Effe
cts
of G
rain
siz
e an
d se
lect
ion
thic
knes
s on
Allo
y 61
7 pr
oper
ties
WE
C-T
S-I
HX
A-0
05IN
L, O
RN
L, A
NL,
LA
NL,
SN
L, B
NL,
CS
IR24
Mon
ths
FY
200
9 -
FY
20
12$8
33,7
08
Cor
rosi
on A
llow
ance
s fo
r A
lloy
617
WE
C-T
S-I
HX
A-0
06IN
L, O
RN
L, F
ZJ,
Sac
lay
36 M
onth
sF
Y 2
009
- F
Y
2012
$1,9
04,4
08
Tab
le 1
7-4:
Ori
gina
l TD
RM
Cos
t E
stim
ates
(F
acili
ty D
escr
ipti
on a
nd T
otal
Cos
t In
clud
ed)
Cir
cula
tor
[1]
IHX
A (
Met
allic
) [2
]
NG
NP
-CTF
MTE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F-M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
SS
CT
est
Sp
ecif
icat
ion
Tes
t S
pec
ific
atio
n N
um
ber
Fac
ility
/Su
pp
ort
ing
Org
aniz
atio
ns
Du
rati
on
Fis
cal
Yea
r/s
To
tal (
$)
Tab
le 1
7-4:
Ori
gina
l TD
RM
Cos
t E
stim
ates
(F
acili
ty D
escr
ipti
on a
nd T
otal
Cos
t In
clud
ed)
TR
L 3
- T
RL
4A
SM
E s
elec
tion
III C
ode
Cas
e fo
r A
lloy
617
WE
C-T
S-I
HX
A-0
07IN
L, O
RN
L, C
HE
des
igne
rs/m
anuf
actu
rers
48 M
onth
sF
Y 2
010
- F
Y
2015
$760
,650
The
rmal
/Flu
id M
odel
ing
Met
hods
for
Met
allic
IHX
AW
EC
-TS
-IH
XA
-008
CH
E s
uppl
ier/
desi
gn a
utho
rity,
INL,
OR
NL,
AN
L, L
AN
L36
Mon
ths
FY
201
0 -
FY
20
15$1
40,2
50
Met
hods
for
stre
ss/s
trai
n m
odel
ing
of m
etal
lic IH
X A
WE
C-T
S-I
HX
A-0
09C
HE
sup
plie
r/de
sign
aut
horit
y, IN
L, O
RN
L, A
NL,
LA
NL
36 M
onth
sF
Y 2
010
- F
Y
2015
$140
,250
Crit
eria
for
stru
ctur
al in
tegr
ity o
f IH
X A
WE
C-T
S-I
HX
A-0
10C
HE
sup
plie
r/de
sign
aut
horit
y, IN
L, O
RN
L, A
NL,
LA
NL
36 M
onth
sF
Y 2
010
- F
Y
2015
$140
,250
Per
form
ance
Mod
elin
g M
etho
ds fo
r IH
X A
WE
C-T
S-I
HX
A-0
11C
HE
sup
plie
r/de
sign
aut
horit
y, IN
L, O
RN
L, A
NL,
LA
NL
48 M
onth
sF
Y 2
010
- F
Y
2015
$140
,250
TR
L 4
- T
RL
5S
peci
ficat
ion
of te
stin
g of
uni
t cel
l of c
ompa
ct H
eat
Exc
hang
ers
[3]
WE
C-T
S-I
HX
A-0
12C
HE
des
igne
r/m
anuf
actu
rer
(Hea
tric
, Bra
yton
Ene
rgy)
24 M
onth
sF
Y 2
014
- F
Y
2016
$200
,000
TR
L 5
- T
RL
6T
estin
g of
inte
grat
ed c
ompa
ct h
eat e
xcha
nger
mod
ule
(~1.
2MW
) W
EC
-TS
-IH
XA
-013
CT
F24
Mon
ths
FY
201
7 -
FY
20
19[-
]
AS
ME
III C
ode
Cas
e fo
r C
ompa
ct H
eat E
xcha
nger
D
esig
ns
WE
C-T
S-I
HX
A-0
14C
HE
sup
plie
r/de
sign
aut
horit
y, IN
L, O
RN
L, A
NL,
LA
NL
48 M
onth
sF
Y 2
017
- F
Y
2019
[-]
TR
L 6
- T
RL
7 S
hell-
side
flow
dis
trib
utio
n an
d by
pass
leak
age
test
ing
WE
C-T
S-I
HX
A-0
15C
TF
FY
201
8 -
FY
20
20[-
]
Mul
ti-m
odul
e he
at tr
ansf
er te
stin
g W
EC
-TS
-IH
XA
-016
CT
FF
Y 2
018
- F
Y
2020
[-]
TR
L 7
- T
RL
8T
estin
g of
full
size
com
pact
hea
t exc
hang
er (
Ful
l sca
le
NG
NP
IHX
A)
WE
C-T
S-I
HX
A-0
17N
GN
P48
Mon
ths
FY
201
9 -
FY
20
20[-
]
$16,
765,
378
TR
L 2
- T
RL
3T
rade
stu
dy o
n C
andi
date
Cer
amic
Mat
eria
l for
IHX
AW
EC
-TS
-IH
XA
-018
Sup
plie
r / D
esig
n A
utho
rity
12 M
onth
sF
Y 2
009
- F
Y
2010
$211
,200
IHX
A (
Cer
amic
) [4
]
NG
NP
-CTF
MTE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F-M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
SS
CT
est
Sp
ecif
icat
ion
Tes
t S
pec
ific
atio
n N
um
ber
Fac
ility
/Su
pp
ort
ing
Org
aniz
atio
ns
Du
rati
on
Fis
cal
Yea
r/s
To
tal (
$)
Tab
le 1
7-4:
Ori
gina
l TD
RM
Cos
t E
stim
ates
(F
acili
ty D
escr
ipti
on a
nd T
otal
Cos
t In
clud
ed)
Tra
de s
tudy
on
Can
dida
te C
eram
ic D
esig
ns fo
r IH
X A
WE
C-T
S-I
HX
A-0
19S
uppl
ier
/ Des
ign
Aut
horit
y12
Mon
ths
FY
200
9 -
FY
20
10$2
11,2
00
TR
L 3
- T
RL
4C
aram
ic H
X D
etai
led
Des
ign
Dat
a N
eeds
(D
DN
s)W
EC
-TS
-IH
XA
-020
Des
ign
Aut
horit
y18
Mon
ths
FY
201
1 -
FY
20
16$1
76,0
00
Cer
amic
Mat
eria
ls S
peci
ficat
ions
and
Pro
cure
men
tW
EC
-TS
-IH
XA
-021
INL,
OR
NL
30 M
onth
sF
Y 2
009
- F
Y
2011
$105
,600
The
rmal
Phy
sica
l Pro
pert
ies
of C
eram
ics
WE
C-T
S-I
HX
A-0
22IN
L, O
RN
L, A
NL,
LA
NL,
SN
L, B
NL,
CS
IR18
Mon
ths
FY
200
9 -
FY
20
11$3
38,6
24
Mec
hani
cal P
rope
rtie
s of
Cer
amic
sW
EC
-TS
-IH
XA
-023
INL,
OR
NL,
AN
L, L
AN
L, S
NL,
BN
L, C
SIR
36 M
onth
sF
Y 2
009
- F
Y
2011
$6,3
50,1
42
Com
patib
ility
of C
eram
ic M
ater
ials
to N
GN
P H
e E
nviro
nmen
tW
EC
-TS
-IH
XA
-024
INL,
OR
NL
18 M
onth
sF
Y 2
009
- F
Y
2011
$1,1
99,0
00
Man
ufac
turin
g T
echn
olog
ies
for
Cer
amic
Hea
t E
xcha
nger
sW
EC
-TS
-IH
XA
-025
CH
E d
esig
ner/
man
ufac
ture
r36
Mon
ths
FY
200
9 -
FY
20
11$5
,275
,512
TR
L 4
- T
RL
5C
eram
ic M
ater
ials
Cod
es a
nd S
tand
ards
WE
C-T
S-I
HX
A-0
26C
HE
sup
plie
r/de
sign
aut
horit
y, IN
L, O
RN
L, A
NL,
LA
NL
48 M
onth
sF
Y 2
017
- F
Y
2020
$1,5
21,3
00
Met
hods
for
The
rmal
/Flu
id a
nd S
tres
s/S
trai
n M
odel
ing
WE
C-T
S-I
HX
A-0
27C
HE
sup
plie
r/de
sign
aut
horit
y, IN
L, O
RN
L, A
NL,
LA
NL
48 M
onth
sF
Y 2
017
- F
Y
2020
$415
,800
Str
uctu
ral I
nteg
rity
Crit
eria
for
Cer
amic
Hea
t E
xcha
nger
sW
EC
-TS
-IH
XA
-028
CH
E s
uppl
ier/
desi
gn a
utho
rity,
INL,
OR
NL,
AN
L, L
AN
L48
Mon
ths
FY
201
7 -
FY
20
20$2
80,5
00
Per
form
ance
Mod
elin
g of
Cer
amic
Hea
t Exc
hang
ers
WE
C-T
S-I
HX
A-0
29C
HE
sup
plie
r/de
sign
aut
horit
y, IN
L, O
RN
L, A
NL,
LA
NL
48 M
onth
sF
Y 2
017
- F
Y
2020
$280
,500
Tes
ting
of u
nit c
ell o
f com
pact
hea
t exc
hang
er [
3]W
EC
-TS
-IH
XA
-030
CH
E d
esig
ner/
man
ufac
ture
r (H
eatr
ic, B
rayt
on E
nerg
y)12
Mon
ths
FY
201
7 -
FY
20
20$4
00,0
00
TR
L 5
- T
RL
6S
peci
ficat
ions
of t
estin
g of
com
pact
hea
t exc
hang
er
mod
ule
(~1
.2M
W)
WE
C-T
S-I
HX
A-0
31C
TF
12 M
onth
sF
Y 2
020
- F
Y
2022
[-]
NG
NP
-CTF
MTE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F-M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
SS
CT
est
Sp
ecif
icat
ion
Tes
t S
pec
ific
atio
n N
um
ber
Fac
ility
/Su
pp
ort
ing
Org
aniz
atio
ns
Du
rati
on
Fis
cal
Yea
r/s
To
tal (
$)
Tab
le 1
7-4:
Ori
gina
l TD
RM
Cos
t E
stim
ates
(F
acili
ty D
escr
ipti
on a
nd T
otal
Cos
t In
clud
ed)
AS
ME
III C
ode
Cas
e fo
r C
eram
ic C
ompa
ct H
eat
Exc
hang
er D
esig
nsW
EC
-TS
-IH
XA
-032
CH
E s
uppl
ier/
desi
gn a
utho
rity,
INL,
OR
NL,
AN
L, L
AN
L48
Mon
ths
FY
202
0 -
FY
20
22[-
]
TR
L 6
- T
RL
7S
hell-
side
flow
dis
trib
utio
n an
d by
pass
leak
age
test
s.W
EC
-TS
-IH
XA
-033
CT
FF
Y 2
022
- F
Y
2024
[-]
Mul
ti-m
odul
e he
at tr
ansf
er te
stin
gW
EC
-TS
-IH
XA
-034
CT
FF
Y 2
022
- F
Y
2024
[-]
TR
L 7
- T
RL
8T
estin
g of
full
size
com
pact
hea
t exc
hang
er (
Ful
l sca
le
NG
NP
IHX
A)
WE
C-T
S-I
HX
A-0
35N
GN
PF
Y 2
024
- F
Y
2027
[-]
$7,8
48,9
05
TR
L 3
- T
RL
4A
lloy
800H
Mat
eria
l Spe
cific
atio
n an
d P
rocu
rem
ent
WE
C-T
S-I
HX
B-0
01IN
L, O
RN
L12
Mon
ths
FY
200
9 -
FY
20
15$7
0,40
0
Dat
abas
e fo
r B
raze
d an
d D
iffus
ion
Bon
ded
Allo
y 80
0HW
EC
-TS
-IH
XB
-002
INL,
OR
NL,
AN
L, C
HE
des
igne
rs/m
anuf
actu
rers
30 M
onth
sF
Y 2
009
- F
Y
2015
$3,7
30,8
76
Allo
y 80
0H H
igh
Tem
pera
ture
Mat
eria
l Pro
pert
ies
WE
C-T
S-I
HX
B-0
03IN
L, O
RN
L, C
SIR
3 M
onth
sF
Y 2
009
- F
Y
2015
$80,
972
Effe
cts
of T
herm
al A
ging
and
Env
ironm
ent o
n A
lloy
800H
Pro
pert
ies
WE
C-T
S-I
HX
B-0
04IN
L, O
RN
L6
Mot
nhs
FY
200
9 -
FY
20
15$1
04,5
09
Effe
cts
of E
nviro
nmen
tal E
xpos
ure
on A
lloy
800H
B
raze
and
Diff
usio
n B
onde
d Jo
ints
WE
C-T
S-I
HX
B-0
05IN
L, O
RN
L36
Mon
ths
FY
200
9 -
FY
20
15$3
67,6
16
Effe
cts
of G
rain
Siz
e an
d S
ectio
n T
hick
ness
on
Allo
y 80
0H P
rope
rtie
sW
EC
-TS
-IH
XB
-006
INL,
OR
NL,
AN
L, L
AN
L, S
NL,
BN
L, C
SIR
24 M
onth
sF
Y 2
009
- F
Y
2015
$832
,457
Cor
rosi
on A
llow
ance
s fo
r A
lloy
800H
WE
C-T
S-I
HX
B-0
07IN
L, O
RN
L, F
ZJ,
Sac
lay
36 M
onth
sF
Y 2
009
- F
Y
2015
$1,9
01,0
75
The
rmal
/Flu
id M
odel
ing
Met
hods
for
IHX
BW
EC
-TS
-IH
XB
-008
CH
E d
esig
ner/
supp
lier,
INL,
OR
NL,
AN
L36
Mon
ths
FY
200
9 -
FY
20
15$1
40,2
50
IHX
B [
5]
NG
NP
-CTF
MTE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F-M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
SS
CT
est
Sp
ecif
icat
ion
Tes
t S
pec
ific
atio
n N
um
ber
Fac
ility
/Su
pp
ort
ing
Org
aniz
atio
ns
Du
rati
on
Fis
cal
Yea
r/s
To
tal (
$)
Tab
le 1
7-4:
Ori
gina
l TD
RM
Cos
t E
stim
ates
(F
acili
ty D
escr
ipti
on a
nd T
otal
Cos
t In
clud
ed)
Met
hods
for
Str
ess/
Str
ain
Mod
ling
of IH
X B
WE
C-T
S-I
HX
B-0
09C
HE
des
igne
r/su
pplie
r, IN
L, O
RN
L, A
NL
36 M
onth
sF
Y 2
009
- F
Y
2015
$140
,250
Crit
eria
for
Str
uctu
ral I
nter
grity
of I
HX
BW
EC
-TS
-IH
XB
-010
CH
E d
esig
ner/
supp
lier,
INL,
OR
NL,
AN
L36
Mon
ths
FY
200
9 -
FY
20
15$1
40,2
50
Per
form
ance
Mod
elin
g M
etho
ds fo
r IH
X B
WE
C-T
S-I
HX
B-0
11C
HE
des
igne
r/su
pplie
r, IN
L, O
RN
L, A
NL
48 M
onth
sF
Y 2
009
- F
Y
2015
$140
,250
TR
L 4
- T
RL
5S
peci
ficat
ion
of te
stin
g of
Uni
t Cel
l of C
ompa
ct H
eat
Exc
hang
er [
3]W
EC
-TS
-IH
XB
-012
CH
E d
esig
ner/
man
ufac
ture
r (H
eatr
ic, B
rayt
on E
nerg
y)24
Mon
ths
FY
201
4 -
FY
2016
$200
,000
TR
L 5
- T
RL
6S
peci
ficat
ion
of te
stin
g of
com
pact
hea
t exc
hang
er
mod
ule
(~1
.2M
W)
WE
C-T
S-I
HX
B-0
13C
TF
24 M
onth
sF
Y 2
017
- F
Y
2019
[-]
AS
ME
Sec
tion
III C
ode
Cas
e fo
r C
ompa
ct H
eat
Exc
hang
er D
esig
nsW
EC
-TS
-IH
XB
-014
CH
E s
uppl
ier/
desi
gn a
utho
rity,
INL,
OR
NL,
AN
L, L
AN
L48
Mon
ths
FY
201
7 -
FY
20
19[-
]
TR
L 6
- T
RL
7S
hell-
side
Flo
w D
istr
ibut
ion
and
Byp
ass
Leak
age
Tes
ting
WE
C-T
S-I
HX
B-0
15C
TF
FY
201
8 -
FY
20
20[-
]
Mul
ti-m
odul
e H
eat T
rans
fer
Tes
ting
WE
C-T
S-I
HX
B-0
16C
TF
FY
201
8 -
FY
20
20[-
]
TR
L 7
- T
RL
8S
peci
ficat
ion
of te
stin
g of
a fu
ll sc
ale
com
pact
hea
t ex
chan
ger
WE
C-T
S-I
HX
B-0
17N
GN
P24
Mon
ths
FY
202
0 -
FY
20
22[-
]
$1,7
65,2
00
TR
L 4
- T
RL
5 P
HT
S h
igh-
tem
pera
ture
[760
°C a
nd 9
50°C
] pip
ing
cool
ing,
line
r an
d in
sula
tion
optio
ns tr
ade
stud
yW
EC
-TS
-PIP
-001
Pip
ing
Sys
tem
Des
igne
r6
Mon
ths
FY
200
9 -
FY
20
12$2
11,2
00
PH
TS
low
-tem
pera
ture
[350
°C] p
ipin
g lin
er a
nd
insu
latio
n op
tions
trad
e st
udy
WE
C-T
S-P
IP-0
02P
ipin
g S
yste
m D
esig
ner
6 M
onth
sF
Y 2
009
- F
Y
2012
$140
,800
SH
TS
hig
h-te
mpe
ratu
re[8
40°C
and
900
°C] p
ipin
g lin
er
and
insu
altio
n st
udy
WE
C-T
S-P
IP-0
03P
ipin
g S
yste
m D
esig
ner
6 M
onth
sF
Y 2
009
- F
Y
2012
$211
,200
SH
TS
med
ium
-tem
pera
ture
[659
°C a
nd 7
00°C
] pip
ing
liner
and
insu
latio
n tr
ade
stud
y W
EC
-TS
-PIP
-004
Pip
ing
Sys
tem
Des
igne
r6
Mon
ths
FY
200
9 -
FY
20
12$1
40,8
00
HT
S P
ipin
g
NG
NP
-CTF
MTE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F-M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
SS
CT
est
Sp
ecif
icat
ion
Tes
t S
pec
ific
atio
n N
um
ber
Fac
ility
/Su
pp
ort
ing
Org
aniz
atio
ns
Du
rati
on
Fis
cal
Yea
r/s
To
tal (
$)
Tab
le 1
7-4:
Ori
gina
l TD
RM
Cos
t E
stim
ates
(F
acili
ty D
escr
ipti
on a
nd T
otal
Cos
t In
clud
ed)
SH
TS
low
-tem
pera
ture
[<30
0°C
] pip
ing
liner
and
in
sula
tion
trad
e st
udy
WE
C-T
S-P
IP-0
05P
ipin
g S
yste
m D
esig
ner
6 M
onth
sF
Y 2
009
- F
Y
2012
$105
,600
TR
L 5
- T
RL
6E
ffect
s of
He
infil
trat
ion
on th
erm
al c
ondu
ctiv
ity o
f in
sula
tion
mat
eria
l [6]
WE
C-T
S-P
IP-0
06In
sula
tion
Man
ufac
ture
rs, I
NL,
OR
NL,
AN
L18
Mon
ths
FY
200
9 -
FY
20
12$4
00,0
00
The
effe
ct o
f flu
id im
purit
ies
on in
sula
tion
prop
ertie
s [7
]W
EC
-TS
-PIP
-007
Insu
latio
n M
anuf
actu
rers
, IN
L, O
RN
L, A
NL
18 M
onth
sF
Y 2
009
- F
Y
2012
$450
,000
Re-
eval
uatio
n of
nee
ded
mat
urat
ion
task
s ba
sed
on
Tra
de s
tudi
esW
EC
-TS
-PIP
-008
Pip
ing
Sys
tem
Des
igne
r3
Mon
ths
FY
200
9 -
FY
20
12$1
05,6
00
TR
L 6
- T
RL
7P
erfo
rman
ce a
nd e
nviro
nmen
tal t
estin
g of
pro
toty
pica
l he
gh-t
empe
ratu
re a
nd lo
w-t
empe
ratu
re
pipi
ng/in
sula
tion
syst
emW
EC
-TS
-PIP
-009
CT
F24
Mon
ths
FY
201
1 -
FY
20
13[-
]
TR
L 7
- T
RL
8T
estin
g of
full
sie
PH
TS
pip
ing
in N
GN
PW
EC
-TS
-PIP
-010
NG
NP
24 M
onth
sF
Y 2
019
- F
Y
2020
[-]
$2,4
98,0
00
TR
L 6
- T
RL
7T
rade
stu
dies
to s
elec
t ref
eren
ce d
esig
nn/
aS
uppl
ier
/ Des
ign
Aut
horit
y12
Mon
ths
FY
201
0 -
FY
20
13$2
50,0
00
Spe
cific
atio
n 1:
Enh
ance
d M
ixin
g D
evic
es T
est
Spe
cific
atio
nW
EC
-TS
-MC
-001
supp
lier
site
6 M
onth
sF
Y 2
009
- F
Y
2012
[-]
Spe
cific
atio
n 2:
Vib
ratio
n D
ampi
ng D
evic
es T
est
Spe
cific
atio
nW
EC
-TS
-MC
-002
supp
lier
site
6 M
onth
sF
Y 2
009
- F
Y
2012
[-]
Par
tial o
r F
ull S
cale
Flo
w M
ixin
g C
ham
ber
Mod
el T
est
Spe
cific
atio
nW
EC
-TS
-MC
-003
CT
F /
Sup
plie
r si
te12
Mon
ths
FY
200
9 -
FY
20
12[-
]
TR
L 7
- T
RL
8P
roto
type
Flo
w M
ixin
g C
ham
ber
Tes
t Spe
cific
atio
nW
EC
-TS
-MC
-004
NG
NP
Site
12 M
onth
sF
Y 2
016
- F
Y20
18[-
]
$22,
500,
000
Ste
am G
ener
ato
r [9
]
Mix
ing
Ch
amb
er [
8]
NG
NP
-CTF
MTE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F-M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
SS
CT
est
Sp
ecif
icat
ion
Tes
t S
pec
ific
atio
n N
um
ber
Fac
ility
/Su
pp
ort
ing
Org
aniz
atio
ns
Du
rati
on
Fis
cal
Yea
r/s
To
tal (
$)
Tab
le 1
7-4:
Ori
gina
l TD
RM
Cos
t E
stim
ates
(F
acili
ty D
escr
ipti
on a
nd T
otal
Cos
t In
clud
ed)
TR
L 6
- T
RL
7P
erfo
rm a
dow
n se
lect
ion
trad
e st
udy
to d
eter
min
e th
e pr
efer
red
conc
eptu
al a
rran
gem
ent o
f the
SG
WE
C-T
S-S
G-0
01n/
a48
Mon
ths
FY
200
9 -
FY
2012
[-]
Def
ine
requ
irem
ents
and
des
ign
deta
ils fo
r th
e S
G in
th
e P
CS
sys
tem
con
text
WE
C-T
S-S
G-0
02n/
a48
Mon
ths
FY
200
9 -
FY
2012
[-]
Per
form
con
figur
atio
n de
velo
pmen
t tes
ts to
su
bsta
ntia
te th
e de
sign
WE
C-T
S-S
G-0
03n/
a48
Mon
ths
FY
200
9 -
FY
2012
[-]
Des
ign
and
supp
ly a
sca
le p
roto
type
for
the
test
ing
in
the
CT
FW
EC
-TS
-SG
-004
n/a
48 M
onth
sF
Y 2
009
- F
Y20
12[-
]
Per
form
ance
test
ing
in C
TF
WE
C-T
S-S
G-0
05C
TF
48 M
onth
sF
Y 2
009
- F
Y20
12[-
]
TR
L 7
- T
RL
8C
ompl
ete
final
des
ign
of th
e pr
otot
ype
SG
for
the
NG
NP
WE
C-T
S-S
G-0
06n/
a40
- 5
0 m
onth
sF
Y 2
011
- F
Y20
14[-
]
Fab
ricat
e an
d de
liver
to N
GN
P to
the
Site
WE
C-T
S-S
G-0
07n/
a40
- 5
0 m
onth
sF
Y 2
011
- F
Y20
14[-
]
Inst
all a
nd o
pera
teW
EC
-TS
-SG
-008
NG
NP
40 -
50
mon
ths
FY
201
1 -
FY
2014
[-]
$45,
000,
000
TR
L 6
- T
RL
7P
rodu
ctio
n F
uel I
rrad
iatio
n T
ests
for
Nor
mal
O
pera
tiona
l Con
ditio
nsW
EC
-TS
-FU
EL-
001
INM
Fac
ility
FY
201
2 -
2015
[-]
Pro
duct
ion
Fue
l Hea
t-up
Tes
tsW
EC
-TS
-FU
EL-
002
INM
Fac
ility
FY
201
2 -
2015
[-]
Fue
l Mat
rix G
raph
ite Ir
radi
atio
n te
sts
and
PIE
WE
C-T
S-F
UE
L-00
3IV
V-2
M R
ussi
an R
eact
orF
Y 2
012
- 20
15[-
]
Mac
hine
d G
raph
ite Ir
radi
atio
n te
sts
and
PIE
WE
C-T
S-F
UE
L-00
4IV
V-2
M R
ussi
an R
eact
orF
Y 2
012
- 20
15[-
]
Fu
el [
10]
NG
NP
-CTF
MTE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F-M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
SS
CT
est
Sp
ecif
icat
ion
Tes
t S
pec
ific
atio
n N
um
ber
Fac
ility
/Su
pp
ort
ing
Org
aniz
atio
ns
Du
rati
on
Fis
cal
Yea
r/s
To
tal (
$)
Tab
le 1
7-4:
Ori
gina
l TD
RM
Cos
t E
stim
ates
(F
acili
ty D
escr
ipti
on a
nd T
otal
Cos
t In
clud
ed)
TR
L 7
- T
RL
8A
dditi
onal
Pro
duct
ion
Fue
l Irr
adia
tion
Tes
ts fo
r N
orm
al
Ope
ratio
nal C
ondi
tions
WE
C-T
S-F
UE
L-00
5S
uita
ble
Tes
t Rea
ctor
- A
TR
FY
201
2 -
2015
[-]
Pro
duct
ion
Fue
l Hea
t-up
Tes
tsW
EC
-TS
-FU
EL-
006
Sui
tabl
e T
est R
eact
or -
AT
RF
Y 2
012
- 20
15[-
]
Fue
l Mat
rix G
raph
ite Ir
radi
atio
n te
sts
and
PIE
WE
C-T
S-F
UE
L-00
7S
uita
ble
Tes
t Rea
ctor
- A
TR
FY
201
2 -
2015
[-]
CS
C [
11]
$5,0
00,0
00
TR
L 6
- T
RL
7P
BM
R R
elev
ant
WE
C-T
S-C
SC
-001
FY
200
9 -
FY
20
13[-
]
Ext
ende
d P
rope
rtie
s of
Irra
diat
ed G
raph
ite a
t Low
T
empe
ratu
res
WE
C-T
S-C
SC
-002
Nat
iona
l Lab
orat
ory
/ Uni
vers
ityF
Y 2
009
- F
Y
2013
[-]
Ext
ende
d P
rope
rtie
s of
Irra
diat
ed G
raph
ite a
t Hig
h T
empe
ratu
res
WE
C-T
S-C
SC
-003
Nat
iona
l Lab
orat
ory
/ Uni
vers
ityF
Y 2
009
- F
Y
2013
[-]
Cha
ract
eriz
e R
ace
Tra
ck S
trap
and
Tie
Rod
Mat
eria
lW
EC
-TS
-CS
C-0
04N
atio
nal L
abor
ator
y / U
nive
rsity
FY
200
9 -
FY
20
13[-
]
Insu
latio
n M
ater
ial (
Uni
rrad
iate
d D
ata
Nee
ded)
WE
C-T
S-C
SC
-005
Nat
iona
l Lab
orat
ory
/ Uni
vers
ityF
Y 2
009
- F
Y
2013
[-]
HP
S [
12]
$193
,900
,000
Sul
furi
c A
cid
D
eco
mp
osi
tio
nn/
an/
an/
an/
a$6
5,70
0,00
0
Sul
fur
Dio
xid
e E
lect
orl
ysis
n/a
n/a
n/a
n/a
$128
,200
,000
Bun
sen
Rea
ctio
n an
d H
I d
eco
mp
osi
tio
nn/
an/
an/
an/
a$2
52,1
00,0
00
NG
NP
-CTF
MTE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F-M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
SS
CT
est
Sp
ecif
icat
ion
Tes
t S
pec
ific
atio
n N
um
ber
Fac
ility
/Su
pp
ort
ing
Org
aniz
atio
ns
Du
rati
on
Fis
cal
Yea
r/s
To
tal (
$)
Tab
le 1
7-4:
Ori
gina
l TD
RM
Cos
t E
stim
ates
(F
acili
ty D
escr
ipti
on a
nd T
otal
Cos
t In
clud
ed)
Hig
h T
emp
erat
ure
Ste
am E
lect
roly
sis
n/a
n/a
n/a
n/a
$128
,800
,000
[1]
Add
ition
al d
esig
n in
form
atio
n is
req
uire
d to
con
duct
sen
sibl
e co
st e
stim
ates
. Tra
de s
tudi
es s
till h
ave
to b
e co
mpl
eted
for
the
Circ
ulat
or to
ver
ify a
nd d
eter
min
e th
e sp
ecifi
c co
mbi
natio
ns o
f sub
-com
pone
nts
that
will
be
used
.[2
]F
or IH
X A
, est
imat
es h
ave
been
con
duct
ed fo
r th
ree
heat
s. E
stim
ates
exc
lude
TR
L 5
to T
RL
8 ad
vanc
emen
ts d
ue to
unc
erta
intie
s th
at a
re s
till p
rese
nt fo
r la
ter
TR
L ad
vanc
emen
ts[3
]T
otal
bas
ed o
n di
scus
sion
s w
ith S
cott
Pen
field
. Fur
ther
det
ail f
or c
ost b
reak
dow
n st
ill r
equi
red
[4]
Equ
ival
ent w
ork
rela
ting
to m
etal
lic IH
X A
hav
e be
en a
djus
ted
by a
fact
or o
f 2 d
ue to
var
ious
unc
erta
intie
s ex
istin
g w
ith r
egar
ds to
cer
amic
s (s
ampl
e pr
epar
atio
n, m
ater
ials
cos
t, et
c.).
Est
imat
es e
xclu
de T
RL
5 to
TR
L 8
adva
ncem
ents
due
to u
ncer
tain
ties
that
are
stil
l pre
sent
for
late
r T
RL
adva
ncem
ents
[5]
Equ
ival
ent w
ork
rela
ting
to m
etal
lic IH
X A
hav
e be
en a
djus
ted
by fa
ctor
s sh
own
in T
able
18.
1 in
Sec
tion
1: In
tegr
ated
Sch
edul
e an
d C
ost E
stim
ate
(with
Fac
ility
Info
rmat
ion)
. Est
imat
es e
xclu
de T
RL
5 to
TR
L 8
adva
ncem
ents
due
to u
ncer
tain
ties
that
are
stil
l pre
sent
for
late
r T
RL
adva
ncem
ents
[6]
Tot
al b
ased
on
disc
ussi
ons
with
Phi
l Ritt
enho
use.
Fur
ther
det
ail f
or c
ost b
reak
dow
n st
ill r
equi
red
[7]
Tot
al b
ased
on
disc
ussi
ons
with
Phi
l Ritt
enho
use.
Fur
ther
det
ail f
or c
ost b
reak
dow
n st
ill r
equi
red
[8]
NG
NP
PC
DR
Rep
ort -
Sec
tion
16 e
stim
ate
give
n -
Con
cept
des
ign
of p
lant
nee
ds to
be
prog
ress
ed b
efor
e se
nsib
le c
ost e
stim
ates
can
be
give
n.
[9]
NG
NP
PC
DR
Rep
ort -
Sec
tion
16 e
stim
ate
give
n -
Con
cept
des
ign
of p
lant
nee
ds to
be
prog
ress
ed b
efor
e se
nsib
le c
ost e
stim
ates
can
be
give
n.
[10]
NG
NP
PC
DR
Rep
ort -
Sec
tion
16 e
stim
ate
give
n[1
1]N
GN
P P
CD
R R
epor
t - S
ectio
n 16
est
imat
e gi
ven
[12]
Est
imat
es fo
r va
rious
pro
cess
HP
S te
chno
logi
es n
oted
in N
GN
P-C
TF
MT
EC
H-T
DR
M-0
08. S
um to
tal r
efle
cts
tota
ls o
f sul
furic
aci
d de
com
posi
tion
tech
nolo
gy d
evel
opm
ent a
s w
ell a
s su
lfur
diox
ide
elec
trol
ysis
tech
nolo
gy d
evel
opm
ent.
For
the
purp
oses
of t
his
estim
atio
n, e
stim
atio
ns r
efle
ct c
osts
nee
ded
to e
tabl
ish
Hyb
rid S
ulph
ur h
ydro
gen
prod
uctio
n sy
stem
(ev
en th
ough
the
refe
renc
e de
sign
stil
l has
to b
e se
lect
ed).
INL
-
Idah
o N
atio
nal L
abo
rato
ryO
RN
L
-
Oak
Rid
ge
Nat
iona
l Lab
ora
tory
AN
L
- A
rgo
nne
Nat
iona
l Lab
ora
tory
LA
NL
-
Lo
s A
lam
os
Nat
iona
l Lab
ora
tory
SN
L
-S
and
ia N
atio
nal L
abo
rato
ryB
NL
-
Bro
okh
aven
Nat
iona
l Lab
ora
tory
CS
IR
-
C
oun
cil f
or
Sci
enti
fic
Ind
ustr
ial R
esea
rch
NG
NP
-CTF
MTE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NGNP-CTF MTECH-TDRM-017 NGNP Technology Development Road Mapping Section 17 : Integrated Schedule and Cost Estimate
NGNP-CTF MTECH-TDRM-017_Rev0.doc 10/27/2008
42 of 89
17.1.6 Conclusion – Cost Estimates
Cost estimates have been provided for certain critical SSCs (notably IHX A (metallic as well as ceramic), IHX B and HTS Piping). Estimates have only been provided up to a TRL rating of 5. Estimates for higher TRL advancements can only be provided when additional design information (preliminary or final) of the NGNP and components are available.
For some of the SSCs, more design information is required in order to develop reliable
cost estimates (notably PHTS Circulator, SHTS Mixing Chamber and Steam Generator). Trade studies (or various trade studies) need to be done to verify and determine the specific combinations of sub-components that will be used in the aforementioned SSC’s. There is enough time in the modified schedule to perform the trade studies before the advancement of the TRLs and before possible testing in the CTF will be performed. Costing input relating to the HPS as noted in the Hydrogen Plant Alternatives Study (HPAS) has also been incorporated into this document.
The bases for the estimates given (with the exception of the HPS) have also been noted in
Appendix A of this document.
NGNP-CTF MTECH-TDRM-017 NGNP Technology Development Road Mapping Section 17 : Integrated Schedule and Cost Estimate
NGNP-CTF MTECH-TDRM-017_Rev0.doc 10/27/2008
43 of 89
17.2.5 Appendix A: Detailed Cost Estimation Sheets
NGNP-CTF MTECH-TDRM-017 NGNP Technology Development Road Mapping Report Section 17: Integrated Schedule and Cost Estimate
Basis motivations for cost estimations
1) General- Guidelines for minimum required number of samples shown in 'sample' sheet
2) Bases for estimations- Discussions with institutions/available information from institutions conducting similar work (notably ORNL and CSIR) serves partly as basis for these estimations- Information stipulated in technology maturation plans with an element of engineering judgment also serve as part basis for cost estimations.- Basis of cost estimation of test equipment costs noted is based on available information for similar work conducted at ORNL- 10 percent contingency has been built into estimates of individual test specifications- Material costs have been based on the following:
a) Alloy 617 - $40/kg, as well as typical sample size needed for relevant testingb) Alloy 800H - $35/kg, as well as typical sample size needed for relevant testingc) Ceramic - $40/kg (please note that this is subject to change since the down selection still has to be done)
- Other additional bases for testing requirements that are needed are stated in estimate sheets
NGNP-CTF MTECH-TDRM-017-Rev0 12/03/2008
NG
NP-
CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17:
Int
egra
ted
Sche
dule
and
Cos
t Est
imat
e
Cri
t S
SC
Sp
ecifi
catio
n n
um
ber
Sp
ecifi
catio
nD
escr
iptio
nC
om
men
ts
IHX
AW
EC
-TS
-IH
XA
-001
Allo
y 61
7 M
ater
ial
Spe
cific
atio
ns a
nd
Pro
cure
men
t
Fin
aliz
e m
ater
ial
spec
ifica
tions
, dev
elop
pr
ocur
emen
t req
uire
men
ts,
proc
ure
3 he
ats
of A
lloy
617
N/A
Tas
ks r
equ
ired
Act
ion
to
be
per
form
ed b
yT
ariff
($)
Tim
e n
eed
edT
ota
l ($)
Ass
um
ptio
ns/
Bas
es
Ho
ur
Act
ion
Ho
urs
Day
sW
eeks
Mo
nth
s
Com
pile
Allo
y 61
7 pr
ocur
emen
t spe
cific
atio
nE
ngin
eer
200
N/A
85
43
9600
01)
Bas
ed o
n tim
e ne
eded
to c
ompi
le p
rocu
rem
ent s
peci
ficat
ion,
insp
ectio
n du
ring
proc
urem
ent p
rodu
ctio
n (p
rodu
ctio
n/
rolli
ng/s
ampl
ing)
as
wel
l as
com
pilin
g re
port
.
To
tal (
$)96
000
10%
co
nti
ng
ency
($)
9600
Gra
nd
to
tal (
$)10
5600
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP-
CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
Cri
t S
SC
Spe
cifi
cati
on n
umbe
rS
peci
fica
tion
Des
crip
tion
Com
men
tsW
= W
eldi
ng
Allo
y 61
7 jo
inin
gD
emon
stra
te th
at A
lloy6
17 c
an b
e w
elde
d,
BR
= B
razi
ng
IHX
AW
EC
-TS
-IH
XA
-002
tech
nolo
gy a
ndbr
azed
, diff
usio
n bo
nded
and
that
join
tD
B =
Diff
usio
n B
ondi
ng
resu
ltant
pro
pert
ies
prop
ertie
s ar
e ap
prop
riate
for
this
use
N/A
Res
our
ces Res
ourc
e re
quir
emen
tA
ctio
n to
be
perf
orm
ed b
yT
arif
f ($
)D
urat
ion
Tot
al (
$)A
ssum
ptio
ns/B
ases
Hou
rA
ctio
nH
ours
Day
sW
eeks
Mon
ths
Yea
rsW
eld
desi
gn/C
ompi
ling
W-B
R-D
B
s pec
ific
atio
nE
ngin
eer
200
85
43
9600
0A
ssum
ing
1 m
onth
nee
ded
per
join
ing
met
hod
to c
ompi
le s
peci
ficat
ion
(W/B
R/D
B)
Wel
ding
of
join
ts (
W/B
R/D
B)
Cod
ed w
elde
r10
08
546
1840
0054
9 sa
mpl
es to
be
join
ed. D
ue to
larg
e un
cert
aint
y of
of
time
need
ed to
est
ablis
h di
ffus
ion
bond
ed
spec
imen
s, a
ssum
e th
at 1
2 sa
mpl
es/w
eek
are
to b
e jo
ined
(irr
espe
ctiv
e of
join
ing
met
hod)
.
Con
duct
ing
test
ing:
Joi
nt p
rope
rtie
sLa
bora
tory
Tec
hnic
ian
80n/
a8
561
1952
00T
estin
g w
ill r
equi
re r
esou
rces
in th
e fo
rm o
f 1
engi
neer
($2
00/h
our)
as
wel
l as
1 la
bora
tory
tech
nici
an
Ove
rsee
& M
anag
eE
ngin
eer
200
n/a
85
6148
8000
(80
$/ho
ur).
Ass
umin
g th
at 9
sam
ples
are
test
ed /w
eek
(due
to la
rge
time
unce
rtai
nty
for
fatig
ue te
stin
g).
Tot
al 1
($)
9632
00
Tes
ting
Tas
k re
quir
emen
tT
esti
ngT
otal
($)
Ass
umpt
ions
/Bas
es
Sam
ples
[1]
Pre
p (M
achi
ning
) [2
]T
est
cost
/sam
ple
Tes
ting
Cos
ts
Eq
. set
up
Pos
t te
st s
ampl
e pr
epP
ost
test
ana
lysi
sR
epor
ting
Met
allo
grap
hy (
post
wel
ding
/bon
ding
, pre
-te
stin
g) [
3]
Cut
ting,
pol
ishi
ng54
964
035
1360
3513
60T
akin
g in
to a
ccou
nt th
at la
bora
tory
tech
nici
an w
ill n
eed
8 ho
urs
for
sam
ple
prep
arat
ion
at $
80/h
our.
Est
imat
e m
ade
by s
peci
alis
ts.
Obs
erva
tion
of m
etal
lurg
y54
940
021
9600
2196
00In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eerin
g in
put a
t $20
0/ho
ur .
Est
imat
e m
ade
by s
peci
alis
ts.
Che
mis
try
prof
ile in
join
ts54
940
021
9600
2196
00In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eerin
g in
put a
t $20
0/ho
ur .
Est
imat
e m
ade
by s
peci
alis
ts.
The
rmal
Phy
sica
l Mec
hani
cal p
rope
rtie
s
of W
/BR
/DB
join
ts
Ela
stic
pro
pert
ies
[4]
1872
0035
063
00n/
an/
an/
a50
014
000
$350
-00
per
spec
imen
at 9
50°C
(+
- 30
°C).
Bas
ed o
n of
ficia
l quo
tatio
n to
con
duct
wor
k
Ten
sile
Pro
pert
ies
[5]
4518
000
350
1575
0n/
an/
an/
a50
034
250
$350
-00
per
spec
imen
at 9
50°C
(+
- 30
°C).
Bas
ed o
n of
ficia
l quo
tatio
n to
con
duct
wor
k
Fat
igue
Str
engt
h (L
CF
)13
554
000
720
9720
066
000
n/a
n/a
1000
2182
00F
atig
ue s
tren
gth
LCF
to 1
000°
C -
$72
0-00
up
to 8
0 00
0 cy
cles
+
$20-
00/h
our
ther
e af
ter
per
spec
imen
at 9
50°C
(+
- 30
°C).
Bas
ed o
n of
ficia
l quo
tatio
n to
con
duct
wor
k
Fat
igue
str
engt
h (H
CF
)13
554
000
800
1080
0066
000
n/a
n/a
1000
2290
00F
atig
ue s
tren
gth
HC
F to
100
0°C
- $
800-
00 u
p to
100
0 00
0 cy
cles
per
spec
imen
at 9
50°C
(+
- 30
°C).
Bas
ed o
n of
ficia
l quo
tatio
n to
con
duct
wor
k
Cre
ep s
tren
gth
144
5760
035
0050
4000
n/a
n/a
n/a
500
5621
00C
reep
str
engt
h to
100
0°C
for
10,
000
h -
$350
0-00
per
spe
cim
en. B
ased
on
offic
ial q
uota
tion
to c
ondu
ct w
ork
Fra
ctur
e to
ughn
ess:
CT
OD
2710
800
1000
2700
0n/
an/
an/
a50
038
300
Fra
ctur
e to
ughn
ess:
CT
OD
- $
1000
-00
at 6
50°C
per
spe
cim
en. B
ased
on
offic
ial q
uota
tion
to c
ondu
ct w
ork
Fra
ctur
e to
ughn
ess:
Kc
2710
800
560
1512
0n/
an/
an/
a50
026
420
Fra
ctur
e to
ughn
ess:
Kc
- $5
60-0
0 at
650
°C p
er s
peci
men
. Bas
ed o
n of
ficia
l quo
tatio
n to
con
duct
wor
k
The
rmal
con
duct
ivity
1872
0010
018
00n/
an/
an/
a50
095
00T
herm
al c
ondu
ctiv
ity to
100
0°C
: - $
95-0
0 pe
r sp
ecim
en. B
ased
on
offic
ial q
uota
tion
to c
ondu
ct w
ork
Met
allo
grap
hy/O
ptic
al/S
EM
(po
st-
wel
din g
,pos
t-te
stin
g) [
6]C
uttin
g, p
olis
hing
, etc
hing
sam
ple
459
640
2937
6029
3760
Tak
ing
into
acc
ount
that
labo
rato
ry te
chni
cian
will
nee
d 8
hour
s fo
r
sam
ple
prep
arat
ion
at $
80/h
our.
Est
imat
e m
ade
by s
peci
alis
ts.
Obs
erva
tion
of s
ampl
e/m
etal
lurg
y45
940
018
3600
1836
00In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eerin
g in
put a
t $20
0/ho
ur. E
stim
ate
mad
e by
spe
cial
ists
.
Tot
al 2
($)
2196
0012
5253
013
2000
00
5000
2399
690
Mat
eria
lsM
ater
ials
req
uire
men
tT
otal
($)
Ass
umpt
ions
/Bas
es
Sam
ples
Mat
.cos
t/sa
mpl
eM
ater
ial c
ost
All
oy 6
17 s
ampl
es [
7]n/
an/
a32
,931
32,9
31C
ostin
g ba
sed
on m
ater
ial p
rice
of $
40/k
g an
d ty
pica
l sam
ple
size
for
rel
evan
t tes
ting.
Thi
s do
es n
ot
allo
w f
or th
e co
st/d
evel
opm
ent f
or th
e w
eld/
braz
e al
loy.
Tot
al 3
($)
3293
1
To
tal (
$)33
9582
1
10%
co
ntin
gen
cy (
$)33
9582
.1
Gra
nd t
ota
l ($)
3735
403.
1
[1] S
ee p
refe
rred
num
ber
of s
ampl
es to
be
used
in 's
ampl
e sh
eet'
[2] B
asis
for
pre
para
tion
cost
s -
$400
/sam
ple
[3] A
ssum
ing
that
all
the
join
ed s
ampl
es to
be
chec
ked
for
join
t int
egrit
y af
ter
join
ing
[4] D
eter
min
atio
n by
way
of
mec
hani
cal t
estin
g no
t adv
ised
. Det
erm
inat
ion
shou
ld b
e ba
sed
on n
atur
al v
ibra
tiona
l met
hods
[5] T
ensi
le p
rope
rtie
s (y
ield
str
engt
h, te
nsile
str
engt
h, e
long
atio
n, a
nd R
A)
[6] O
ptic
al/S
EM
wor
k to
be
cond
ucte
d fo
r te
sile
, fat
igue
(H
CF
& L
CF
) an
d cr
eep
[7] R
efer
to 'm
ater
ial c
ost'
shee
t for
mat
eria
l cos
ting
aspe
cts
NG
NP
-CTF
MTE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
Inte
grat
ed S
ched
ule
and
Cos
t Est
imat
e (a
nd F
acili
ty I
nfor
mat
ion)
Cri
t SS
CS
pec
ifica
tion
num
ber
Sp
ecifi
catio
nD
escr
iptio
nC
om
men
ts
The
rmal
, Phy
sica
lD
emon
stra
te th
at p
rocu
red
Allo
y617
IHX
AW
EC
-TS
-IH
XA
-003
and
Mec
hani
cal
will
hav
e th
erm
al, p
hysi
cal a
nd m
echa
nica
l
prop
ertie
s of
Allo
y 61
7pr
oper
ties
appr
opria
te fo
r us
e in
CH
EN
/A
Res
ou
rces R
eso
urce
req
uire
men
tA
ctio
n to
be
per
form
ed b
yT
ariff
($)
Dur
atio
nT
ota
l ($)
Ass
ump
tions
/Bas
es
Ho
urA
ctio
nH
our
sD
ays
Wee
ksM
ont
hsY
ears
Co
nduc
ting
test
ing
Labo
rato
ry T
echn
icia
n80
n/a
85
2167
200
Tes
ting
will
req
uire
res
ourc
es in
the
form
of 1
eng
inee
r ($
200/
hour
)
Ove
rsee
& M
anag
eE
ngin
eer
200
n/a
85
2116
8000
as w
ell a
s 1
labo
rato
ry te
chni
cian
(80
$/ho
ur).
Ass
umin
g th
at 9
sam
ples
are
tes
ted
/ wee
k
(due
to la
rge
time
unce
rtai
nty
for
fatig
ue te
stin
g)
To
tal 1
($)
2352
00
Tes
tin
gT
ask
req
uire
men
tT
estin
gT
ota
l ($)
Ass
ump
tions
/Bas
es
Sam
ple
s [1
]P
rep
(Mac
hini
ng) [
2]T
est c
ost
/sam
ple
Tes
ting
Co
sts
E
q. s
etup
P
ost
test
sam
ple
pre
pP
ost
test
ana
lysi
s [3
]R
epo
rtin
g
The
rmal
Phy
sica
l Mec
hani
cal p
rop
ertie
s
Ela
stic
pro
pert
ies
[4]
624
0035
021
00n/
an/
an/
a50
050
00$3
50-0
0 pe
r sp
ecim
en a
t 950
°C (
+-
30°C
). B
ased
on
offic
ial q
uote
to c
ondu
ct w
ork.
Ten
sile
Pro
pert
ies
[5]
1560
0035
052
50n/
an/
an/
a50
011
750
$350
-00
per
spec
imen
at 9
50°C
(+
- 30
°C).
Bas
ed o
n of
ficia
l quo
te to
con
duct
wor
k.
Fat
igue
Str
engt
h (L
CF
)45
1800
072
032
400
6600
0n/
a90
0010
0012
6400
Fat
igue
str
engt
h LC
F to
100
0°C
- $
720-
00 u
p to
80
000
cycl
es +
$20-
00/h
our
ther
e af
ter
per
spec
imen
at 9
50°C
(+
- 30
°C).
Bas
ed o
n of
ficia
l quo
te to
con
duct
wor
k.
Fat
igue
str
engt
h (H
CF
)45
1800
080
036
000
6600
0n/
a90
0010
0013
0000
Fat
igue
str
engt
h H
CF
to 1
000°
C -
$80
0-00
up
to 1
000
000
cycl
es p
er
spec
imen
at 9
50°C
(+
- 30
°C).
Bas
ed o
n of
ficia
l quo
te to
con
duct
wor
k.
Cre
ep s
tren
gth
4819
200
3500
1680
00n/
an/
an/
a50
018
7700
Cre
ep s
tren
gth
to 1
000°
C fo
r 10
,000
h -
$35
00-0
0 pe
r sp
ecim
en. B
ased
on
offic
ial q
uote
to c
ondu
ct w
ork.
Fra
ctur
e to
ughn
ess:
CT
OD
936
0010
0090
00n/
an/
a18
0050
014
900
Fra
ctur
e to
ughn
ess:
CT
OD
- $
1000
-00
at 6
50°C
per
spe
cim
en. B
ased
on
offic
ial q
uote
to c
ondu
ct w
ork.
Fra
ctur
e to
ughn
ess:
Kc
936
0056
050
40n/
an/
a18
0050
010
940
Fra
ctur
e to
ughn
ess:
Kc
- $5
60-0
0 at
650
°C p
er s
peci
men
. Bas
ed o
n of
ficia
l quo
te to
con
duct
wor
k.
The
rmal
con
duct
ivity
624
0010
060
0n/
an/
a12
0050
047
00T
herm
al c
ondu
ctiv
ity to
100
0°C
: - $
95-0
0 pe
r sp
ecim
en. B
ased
on
offic
ial q
uote
to c
ondu
ct w
ork.
SE
M R
elat
ed w
ork
n/a
To
tal 2
($)
7320
025
8390
1320
000
2280
050
0049
1390
Mat
eria
lsM
ater
ials
req
uire
men
tT
ota
l ($)
Ass
ump
tions
/Bas
es
Sam
ple
sM
at.c
ost
/sam
ple
Mat
eria
l co
st
Allo
y 61
7 sa
mp
les
[6]
n/a
n/a
10,9
1710
,917
Cos
ting
base
d on
mat
eria
l pric
e of
$40
/kg
and
typi
cal s
ampl
e si
ze n
eede
d fo
r re
leva
nt te
stin
g.
To
tal 3
($)
1091
7
To
tal (
$)73
7507
10%
co
nti
ng
ency
($)
7375
0.7
Gra
nd
to
tal (
$)81
1257
.7
[1] S
ee p
refe
rred
num
ber
of s
ampl
es to
be
used
in 's
ampl
e sh
eet'
[2] B
asis
for
prep
arat
ion
cost
s -
$400
/sam
ple
[3] P
ost t
est a
naly
ses
incl
udes
pos
sibl
e op
tical
and
sca
nnin
g el
ectr
on m
icro
scop
y w
ork
and
is b
ased
eng
inee
r/sc
ient
ist t
ariff
of $
200/
hour
[4] D
eter
min
atio
n by
way
of m
echa
nica
l tes
ting
not a
dvis
ed. D
eter
min
atio
n sh
ould
be
base
d on
nat
ural
vib
ratio
nal m
etho
ds
[5] T
ensi
le p
rope
rtie
s (y
ield
str
engt
h, te
nsile
str
engt
h, e
long
atio
n, a
nd R
A)
[6] R
efer
to 'm
ater
ial c
ost'
shee
t for
mat
eria
l cos
ting
aspe
cts
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d S
ched
ule
and
Cos
t Est
imat
e
Cri
t S
SC
Sp
ecif
icat
ion
nu
mb
erS
pec
ific
atio
nD
escr
ipti
on
Co
mm
ents
Effe
cts
of th
erm
alD
emon
stra
te th
at A
lloy
617
and
join
ts c
an b
e
IHX
AW
EC
-TS
-IHX
A-0
04ag
ing
and
envi
ronm
ent
utili
zed
in N
GN
P e
nviro
nmen
t (te
mpe
ratu
re &
on A
lloy
617p
rope
rtie
sm
ediu
m)
for
long
per
iods
with
out d
egra
datio
nN
/A
Res
our
ces Res
ou
rce
req
uir
emen
tA
ctio
n t
o b
e p
erfo
rmed
by
Tar
iff
($)
Du
rati
on
To
tal (
$)A
ssu
mp
tio
ns/
Bas
es
Ho
ur
Act
ion
Ho
urs
Day
sW
eeks
Mo
nth
sY
ears
Wel
din
g o
f jo
ints
(W
/BR
/DB
)C
oded
wel
der
100
n/a
85
4618
4000
549
sam
ples
to b
e jo
ined
. Due
to la
rge
unce
rtai
nty
in ti
me
need
ed to
est
ablis
h di
ffusi
on b
onde
d s
peci
men
s,
assu
me
that
12
sam
ples
/wee
k ar
e to
be
join
ed (
irres
pect
ive
of jo
inin
g m
etho
d).
Ove
rsee
& M
anag
e: T
her
mal
exp
osu
re o
f sa
mp
les
- 10
,000
hLa
bora
tory
Tec
hnic
ian
100
n/a
100
1000
0B
asis
that
ther
mal
exp
osur
e sa
mpl
es a
re to
be
mon
itore
d by
lab
tech
nici
an e
very
100
h (1
00 in
terv
als)
.
Co
nd
uct
ing
tes
tin
g:
Allo
y/Jo
int
pro
per
ties
Labo
rato
ry T
echn
icia
n80
n/a
85
8226
2400
Tes
ting
will
req
uire
res
ourc
es in
the
form
of 1
eng
inee
r ($
200/
hour
) as
wel
l as
1 la
bora
tory
tech
nici
an (
80$/
hour
).
Ove
rsee
& M
anag
eE
ngin
eer
200
n/a
85
8265
6000
Ass
umin
g th
at 9
sam
ples
are
test
ed /
wee
k (d
ue to
larg
e tim
e un
cert
aint
y fo
r fa
tigue
test
ing)
To
tal 1
($)
1112
400
Tes
ting
Tas
k re
qu
irem
ent
Tes
tin
gT
ota
l ($)
Ass
um
pti
on
s/B
ases
Sam
ple
s [1
]P
rep
(M
ach
inin
g)
[2]
Tes
t co
st/s
amp
leT
esti
ng
Co
sts
E
q. s
etu
p
Po
st t
est
sam
ple
pre
pP
ost
tes
t an
alys
isR
epo
rtin
gM
etal
log
rap
hy
(po
st w
eld
ing
/bo
nd
ing
, pre
-te
stin
g)
[3]
Cut
ting,
pol
ishi
ng s
ampl
e54
9n/
a64
035
1360
n/a
n/a
n/a
3513
60T
akin
g in
to a
ccou
nt th
at la
bora
tory
tech
nici
an w
ill n
eed
8 ho
urs
for
sam
ple
prep
arat
ion
at $
80/h
our.
Est
imat
e m
ade
by s
peci
alis
t.
Obs
erva
tion
of m
etal
lurg
y54
9n/
a40
021
9600
n/a
n/a
500
2196
00In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eerin
g in
put a
t $20
0/ho
ur. E
stim
ate
mad
e by
spe
cial
ist.
Che
mis
try
prof
ile in
join
ts54
9n/
a40
021
9600
n/a
n/a
500
2196
00In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eerin
g in
put a
t $20
0/ho
ur. E
stim
ate
mad
e by
spe
cial
ist.
Th
erm
al P
hys
ical
Mec
han
ical
pro
per
ties
of
Allo
y 61
7 an
d W
/BR
/DB
join
ts
Ela
stic
pro
pert
ies
[4]
2496
0035
084
00n/
an/
an/
a50
018
500
$350
-00
per
spec
imen
at 9
50°C
(+
- 30
°C).
Bas
ed o
n of
ficia
l quo
tatio
n to
con
duct
wor
k.
Ten
sile
Pro
pert
ies
[5]
6024
000
350
2100
0n/
an/
an/
a50
045
500
$350
-00
per
spec
imen
at 9
50°C
(+
- 30
°C).
Bas
ed o
n of
ficia
l quo
tatio
n to
con
duct
wor
k.
Fat
igue
Str
engt
h (L
CF
)18
072
000
720
1296
0066
000
n/a
n/a
1000
2686
00F
atig
ue s
tren
gth
LCF
to 1
000°
C -
$72
0-00
up
to 8
0 00
0 cy
cles
+
$20-
00/h
our
ther
e af
ter
per
spec
imen
at 9
50°C
(+
- 30
°C).
Bas
ed o
n of
ficia
l quo
tatio
n to
con
duct
wor
k.
Fat
igue
str
engt
h (H
CF
)18
072
000
800
1440
0066
000
n/a
n/a
1000
2830
00F
atig
ue s
tren
gth
HC
F to
100
0°C
- $
800-
00 u
p to
100
0 00
0 cy
cles
per
spec
imen
at 9
50°C
(+
- 30
°C).
Bas
ed o
n of
ficia
l quo
tatio
n to
con
duct
wor
k.
Cre
ep s
tren
gth
192
7680
035
0067
2000
n/a
n/a
n/a
500
7493
00C
reep
str
engt
h to
100
0°C
for
10,0
00 h
- $
3500
-00
per
spec
imen
. Bas
ed o
n of
ficia
l quo
tatio
n to
con
duct
wor
k.
Fra
ctur
e to
ughn
ess:
CT
OD
3614
400
1000
3600
0n/
an/
an/
a50
050
900
Fra
ctur
e to
ughn
ess:
CT
OD
- $
1000
-00
at 6
50°C
per
spe
cim
en. B
ased
on
offic
ial q
uota
tion
to c
ondu
ct w
ork.
Fra
ctur
e to
ughn
ess:
Kc
3614
400
560
2016
0n/
an/
an/
a50
035
060
Fra
ctur
e to
ughn
ess:
Kc
- $5
60-0
0 at
650
°C p
er s
peci
men
. Bas
ed o
n of
ficia
l quo
tatio
n to
con
duct
wor
k.
The
rmal
con
duct
ivity
2496
0010
024
00n/
an/
an/
a50
012
500
The
rmal
con
duct
ivity
to 1
000°
C: -
$95
-00
per
spec
imen
. Bas
ed o
n of
ficia
l quo
tatio
n to
con
duct
wor
k.
Met
allo
gra
ph
y/S
EM
(p
ost
-wel
din
g, p
ost
-te
stin
g)
[6]
Cut
ting,
pol
ishi
ng, e
tchi
ng s
ampl
e61
2n/
a64
039
1680
n/a
n/a
n/a
3916
80T
akin
g in
to a
ccou
nt th
at la
bora
tory
tech
nici
an w
ill n
eed
8 ho
urs
for
sam
ple
prep
arat
ion
at $
80/h
our.
Est
imat
e m
ade
by s
peci
alis
t.
Obs
erva
tion
of s
ampl
e/m
etal
lurg
y61
2n/
a40
024
4800
n/a
n/a
500
2448
00In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eerin
g in
put a
t $20
0/ho
ur. E
stim
ate
mad
e by
spe
cial
ist.
To
tal 2
($)
2928
0024
6060
013
2000
00
6500
2890
400
Mat
eria
lsM
ater
ials
req
uir
emen
tT
ota
l ($)
Ass
um
pti
on
s/B
ases
Sam
ple
sM
at.c
ost
/sam
ple
Mat
eria
l co
st
Allo
y 61
7 sa
mp
les
[7]
n/a
n/a
43,6
6843
,668
Cos
ting
base
d on
mat
eria
l pric
e of
$40
/kg
and
typi
cal s
ampl
e si
ze fo
r re
leva
nt te
stin
g. T
his
does
not
allo
w fo
r
the
cost
/dev
elop
men
t for
the
wel
d/br
aze
allo
y.
To
tal 3
($)
4366
8
Oth
erA
dd
itio
nal
req
uir
emen
tsT
ota
l ($)
Ass
um
pti
on
s/B
ases
Un
it p
rice
($)
Qu
anti
ty
Cap
ital
co
st -
fu
rnac
es f
or
ther
mal
ag
ing
3000
390
00C
ostin
g ba
sed
on v
erba
l quo
tatio
n fo
r fu
rnac
e w
ith r
equi
red
capa
bilit
y si
zed
at 1
80m
m x
180
mm
x 2
50m
mC
on
tin
gen
cies
(p
ow
er c
on
sum
pti
on
, el
emen
t re
pla
cem
ent)
900
190
0F
urna
ce c
ontin
genc
ies
base
d on
10%
of t
otal
cap
ital c
ost f
or fu
rnac
es
Hel
ium
gas
fo
r re
gu
lati
ng
en
viro
nm
ent
120
156
18,7
2015
6 x
50kg
He
cylin
ders
to b
e ut
ilize
d. N
umbe
r ba
sed
on u
tiliz
atio
n of
one
cyl
inde
r a
wee
k fo
r ea
ch
furn
ace
for
1 ye
ar (
52 w
eeks
). H
e ga
s co
st in
clus
ive
of im
purit
y ga
ses.
Sam
plin
g g
as a
nal
yses
150
527,
800
Sam
plin
g of
furn
ace
test
ing
envi
ronm
ent d
one
once
a w
eek
by e
xter
nal
inst
itutio
n. C
olle
ctiv
e sa
mpl
ing
from
3 fu
rnac
es a
dd u
p to
$15
0/w
eek.
Bas
ed o
n pe
rson
al c
omm
unic
atio
n w
ith
rele
vant
par
ties
in M
tech
.
To
tal 4
($)
3642
0
To
tal (
$)40
8288
8
10%
co
ntin
gen
cy ($
)40
8288
.8
Gra
nd to
tal (
$)44
9117
6.8
[1] S
ee p
refe
rred
num
ber
of s
ampl
es to
be
used
in 's
ampl
e sh
eet'
[2] B
asis
for
prep
arat
ion
cost
s -
$400
/sam
ple
[3] A
ssum
ing
that
all
sam
ples
to b
e ch
ecke
d fo
r jo
int c
onsi
sten
cy a
fter
join
ing
[4] D
eter
min
atio
n by
way
of m
echa
nica
l tes
ting
not a
dvis
ed. D
eter
min
atio
n sh
ould
be
base
d on
nat
ural
vib
ratio
nal m
etho
ds
[5] T
ensi
le p
rope
rtie
s (y
ield
str
engt
h, te
nsile
str
engt
h, e
long
atio
n, a
nd R
A)
[6] O
ptic
al/S
EM
wor
k to
be
cond
ucte
d fo
r te
nsile
, fat
igue
(H
CF
, LC
F),
cre
ep
[7] R
efer
to 'm
ater
ial c
ost'
shee
t for
mat
eria
l cos
ting
aspe
cts
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d S
ched
ule
and
Cos
t Est
imat
e
Cri
t S
SC
Sp
ecif
icat
ion
num
ber
Sp
ecif
icat
ion
Des
crip
tio
nC
om
men
ts
Effe
cts
of g
rain
siz
eD
emon
stra
te th
at s
light
cha
nges
in g
rain
siz
e as
IHX
AW
EC
-TS
-IH
XA
-005
and
sect
ion
thic
knes
sw
ell a
s th
e se
ctio
n th
ickn
ess
of A
lloy
617
has
little
on A
lloy
617
effe
ct in
ove
rall
prop
ertie
s of
mat
eria
lN
/A
Res
ou
rces R
eso
urce
req
uire
men
tA
ctio
n to
be
per
form
ed b
yT
arif
f ($
)D
urat
ion
To
tal (
$)A
ssum
pti
ons
/Bas
esH
our
Act
ion
Ho
urs
Day
sW
eeks
Mo
nths
Yea
rs
Co
nduc
ting
tes
ting
: A
lloy
617
pro
per
ties
Labo
rato
ry T
echn
icia
n80
n/a
85
1651
200
Tes
ting
will
req
uire
res
ourc
es in
the
form
of 1
eng
inee
r ($
200/
hour
) as
wel
l as
1 la
bora
tory
tech
nici
an
Ove
rsee
& M
anag
eE
ngin
eer
200
n/a
85
1612
8000
(80
$/ho
ur).
Ass
umin
g th
at 9
sam
ples
/wee
k ar
e te
sted
(du
e to
larg
e tim
e un
cert
aint
y fo
r fa
tigue
test
ing)
.
To
tal 1
($)
1792
00
Test
ing
Tas
k re
qui
rem
ent
Tes
ting
To
tal (
$)A
ssum
pti
ons
/Bas
esS
amp
les
[1]
Pre
p (
Mac
hini
ng)
[2]
Tes
t co
st/s
amp
leT
esti
ng C
ost
s
Eq
. set
up
Po
st t
est
sam
ple
pre
pP
ost
tes
t an
alys
isR
epo
rtin
g
The
rmal
Phy
sica
l Mec
hani
cal p
rop
erti
es
of
Allo
y 61
7F
atig
ue S
tren
gth
(LC
F)
4518
000
720
3240
066
000
n/a
n/a
1000
1174
00F
atig
ue s
tren
gth
LCF
to 1
000°
C -
$72
0-00
up
to 8
0 00
0 cy
cles
+
$20-
00/h
our
ther
e af
ter
per
spec
imen
at 9
50°C
(+-
30°
C).
Bas
ed o
n of
ficia
l quo
tatio
n to
con
duct
wor
k.
Fat
igue
str
engt
h (H
CF
)45
1800
080
036
000
6600
0n/
an/
a10
0012
1000
Fat
igue
str
engt
h H
CF
to 1
000°
C -
$80
0-00
up
to 1
000
000
cycl
es p
er
spec
imen
at 9
50°C
(+-
30°
C).
Bas
ed o
n of
ficia
l quo
tatio
n to
con
duct
wor
k.
Cre
ep s
tren
gth
4819
200
3500
1680
00n/
an/
an/
a50
018
7700
Cre
ep s
tren
gth
to 1
000°
C fo
r 10
,000
h -
$35
00-0
0 pe
r sp
ecim
en. B
ased
on
offic
ial q
uota
tion
to c
ondu
ct w
ork.
Met
allo
gra
phy
/SE
M (
po
st-t
esti
ng)
[3]
Cut
ting,
pol
ishi
ng, e
tchi
ng s
ampl
e13
864
088
320
n/a
n/a
n/a
8832
0T
akin
g in
to a
ccou
nt th
at la
bora
tory
tech
nici
an w
ill n
eed
8 ho
urs
for
sam
ple
prep
arat
ion
at $
80/h
our.
Est
imat
e m
ade
by s
peci
alis
t.
Obs
erva
tion
of s
ampl
e/m
etal
lurg
y13
840
055
200
n/a
n/a
500
5520
0In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eerin
g in
put a
t $20
0/ho
ur. E
stim
ate
mad
e by
spe
cial
ist.
To
tal 2
($)
5520
037
9920
1320
000
030
0056
9620
Mat
eria
lsM
ater
ials
req
uire
men
tT
ota
l ($)
Ass
ump
tio
ns/B
ases
Sam
ple
sM
at.c
ost
/sam
ple
Mat
eria
l co
st
Allo
y 61
7 sa
mp
les
[4]
n/a
n/a
9,09
69,
096
Cos
ting
base
d on
mat
eria
l pric
e of
$40
/kg
and
typi
cal s
ampl
e si
ze r
elev
ant f
or te
stin
g.N
umbe
r of
sam
ples
onl
y
rele
vant
to fa
tigue
test
ing
and
cree
p te
stin
g
To
tal 3
($)
9096
Tota
l ($)
7579
16
10%
co
nti
ng
ency
($)
7579
1.6
Gra
nd
to
tal (
$)83
3707
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[1] S
ee p
refe
rred
num
ber
of s
ampl
es to
be
used
in 's
ampl
e sh
eet'
[2] B
asis
for
prep
arat
ion
cost
s -
$400
/sam
ple
[3] O
ptic
al/S
EM
wor
k to
be
cond
ucte
d fo
r fa
tigue
and
cre
ep s
ampl
es
[4] R
efer
to 'm
ater
ial c
ost'
shee
t for
mat
eria
l cos
ting
aspe
cts
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP-
CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
Cri
t S
SC
Sp
ecif
icat
ion
nu
mb
erS
pec
ific
atio
nD
escr
ipti
on
Co
mm
ents
Cor
rosi
onD
emon
stra
te s
atis
fact
ory
corr
osio
n al
low
ance
s
IHX
AW
EC
-TS
-IH
XA
-006
allo
wan
ces
for
for
Allo
y 61
7 an
d w
elde
d/bo
nded
sec
tions
Allo
y 61
7N
/A
Res
ou
rces R
eso
urc
e re
qu
irem
ent
Act
ion
to
be
per
form
ed b
yT
arif
f ($
)D
ura
tio
nT
ota
l ($)
Ass
um
pti
on
s/B
ases
Ho
ur
Act
ion
Ho
urs
Day
sW
eeks
Mo
nth
sY
ears
Wel
din
g o
f jo
ints
(W
/BR
/DB
)C
oded
wel
der
100
n/a
85
1248
000
135
sam
ples
to b
e jo
ined
. Due
to la
rge
unce
rtai
nty
of ti
me
need
ed to
est
ablis
h di
ffusi
on b
onde
d sp
ecim
ens,
ass
ume
that
12
are
to b
e jo
ined
(ir
resp
ectiv
e of
join
ing
met
hod)
.
Ove
rsee
& M
anag
e: T
her
mal
exp
osu
re o
f sa
mp
les
- 10
,000
hLa
bora
tory
Tec
hnic
ian
100
n/a
100
1000
0B
asis
that
ther
mal
exp
osur
e sa
mpl
es a
re to
be
mon
itore
d by
lab
tech
nici
an e
very
100
h (1
00 in
terv
als)
.
Ove
rsee
& M
anag
eE
ngin
eer
200
n/a
85
2016
0000
To
tal 1
($)
2180
00
Tes
tin
gT
ask
req
uir
emen
tT
esti
ng
To
tal (
$)A
ssu
mp
tio
ns/
Bas
es
Sam
ple
sP
rep
(M
ach
inin
g)
[1]
Tes
t co
st/s
amp
leT
esti
ng
Co
sts
E
q. s
etu
p
Po
st t
est
sam
ple
pre
pP
ost
tes
t an
alys
isR
epo
rtin
g
Met
allo
gra
ph
y (p
ost
wel
din
g/b
on
din
g)
[2]
Cut
ting,
pol
ishi
ng s
ampl
e13
5n/
a64
086
400
n/a
n/a
n/a
8640
0T
akin
g in
to a
ccou
nt th
at la
bora
tory
tech
nici
an w
ill n
eed
8 ho
urs
for
sam
ple
prep
arat
ion
at $
80/h
our.
Est
imat
e m
ade
by s
peci
alis
t.
Obs
erva
tion
of m
etal
lurg
y13
5n/
a40
054
000
n/a
n/a
500
5400
0In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eeri
ng in
put a
t $20
0/ho
ur. E
stim
ate
mad
e by
spe
cial
ist.
Che
mis
try
prof
ile in
join
ts13
5n/
a40
054
000
n/a
n/a
500
5400
0In
clus
ive
of 1
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naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eeri
ng in
put a
t $20
0/ho
ur. E
stim
ate
mad
e by
spe
cial
ist.
Th
erm
al P
hys
ical
Mec
han
ical
pro
per
ties
of
Allo
y 61
7 an
d W
/BR
/DB
join
ts
n/a
n/a
n/a
n/a
n/a
n/a
n/a
n/a
n/a
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allo
gra
ph
y/S
EM
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ost
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tin
g)
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ting,
pol
ishi
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tchi
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ampl
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n/a
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akin
g in
to a
ccou
nt th
at la
bora
tory
tech
nici
an w
ill n
eed
8 ho
urs
for
sam
ple
prep
arat
ion
at $
80/h
our.
Est
imat
e m
ade
by s
peci
alis
t.
Obs
erva
tion
of s
ampl
e/m
etal
lurg
y18
0n/
a40
072
000
n/a
n/a
500
7200
0In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eeri
ng in
put a
t $20
0/ho
ur. E
stim
ate
mad
e by
spe
cial
ist.
Dep
th o
f int
erna
l oxi
datio
n18
0n/
a40
072
000
500
7250
0In
clus
ive
of 1
) A
naly
ses
cost
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clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eeri
ng in
put a
t $20
0/ho
ur. E
stim
ate
mad
e by
spe
cial
ist.
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th o
f dep
letio
n of
allo
y el
emen
ts (
Cr)
18
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a40
072
000
500
7250
0In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eeri
ng in
put a
t $20
0/ho
ur. E
stim
ate
mad
e by
spe
cial
ist.
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th a
ffect
ed b
ycar
buri
zatio
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a40
072
000
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clus
ive
of 1
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naly
ses
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clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eeri
ng in
put a
t $20
0/ho
ur. E
stim
ate
mad
e by
spe
cial
ist.
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tal 2
($)
059
7600
00
030
0059
9100
Mat
eria
lsM
ater
ials
req
uir
emen
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ota
l ($)
Ass
um
pti
on
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ases
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ple
sM
at.c
ost
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ple
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eria
l co
st
Allo
y 61
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mp
les
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2012
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ting
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mat
eria
l pri
ce o
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cal s
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ze r
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r
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t for
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aze
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tal 3
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itio
nal
req
uir
emen
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um
pti
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ases
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it p
rice
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anti
ty
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st -
fu
rnac
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or
ther
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tatio
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r fu
rnac
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ent
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2015
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cylin
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e ut
ilize
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tiliz
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n of
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cyl
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r a
wee
k fo
r ea
ch
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ace
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ar (
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eeks
). H
e ga
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st in
clus
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puri
ty g
ases
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Sam
plin
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nal
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plin
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ace
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eek
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nal
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itutio
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olle
ctiv
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mpl
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rnac
es a
dd u
p to
$15
0/w
eek.
Bas
ed o
n pe
rson
al c
omm
unic
atio
n w
ith
rele
vant
par
ties
in M
tech
.
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tal 4
($)
3642
0
To
tal (
$) (
Pri
mar
y si
de
He
effe
cts)
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Sec
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de
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cts
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tal (
Pri
mar
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d S
eco
nd
ary
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cts)
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nti
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nd
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tal (
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8
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asis
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prep
arat
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s -
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ple
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all
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ampl
es to
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for
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sist
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inin
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[3] R
efer
to 'm
ater
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ost'
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mat
eria
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ting
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cts
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NP
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MTE
CH
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-017
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0 1
2/03
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8
NG
NP
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TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d S
ched
ule
and
Cos
t Est
imat
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Cri
t S
SC
Sp
ecif
icat
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nu
mb
erS
pec
ific
atio
nD
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ipti
on
Co
mm
ents
IHX
AW
EC
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XA
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AS
ME
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ode
case
for
Allo
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evel
op a
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lish
AS
ME
Cod
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se II
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N
/A
Tas
ks r
equ
ired
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form
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yT
arif
f ($
)T
ime
nee
ded
To
tal (
$)A
ssu
mp
tio
ns/
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es
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ur
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urs
Day
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eeks
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nth
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para
tory
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kE
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eers
150
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110
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Est
mat
ion
incl
usiv
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inte
ract
ions
with
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ME
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oval
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cess
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pro
visi
on
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dditi
onal
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SM
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fttin
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de c
ase
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ased
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ussi
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rge
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tal (
$)69
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nti
ng
ency
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nd
to
tal (
$)76
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NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
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8
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d S
ched
ule
and
Cos
t Est
imat
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Cri
t S
SC
Sp
ecif
icat
ion
nu
mb
erS
pec
ific
atio
nD
escr
ipti
on
Co
mm
ents
IHX
AW
EC
-TS
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XA
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The
rmal
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id
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ellin
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etho
ds f
or IH
X A
Dev
elop
ther
mal
mod
els
for
IHX
AN
/A
Tas
ks r
equ
ired
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ion
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form
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yT
arif
f ($
)T
ime
nee
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tal (
$)A
ssu
mp
tio
ns/
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ur
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ou
rsD
ays
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ksM
on
ths
Yea
rM
odel
gen
erat
ion
givi
ng r
esul
ts f
or
mec
hani
cal,
phys
ical
and
ther
mal
pe
rfor
man
ce p
redi
ctio
n
Gro
up o
f th
erm
al f
luid
/mod
elin
g sp
ecia
lists
42,5
003
1275
001)
Est
mat
ion
mad
e by
M-T
ech
base
d on
tech
nolo
gy m
atur
atio
n pl
an in
put-
Dur
atio
n
and
cost
is g
reat
ly d
epen
dant
on
the
data
sup
plie
d by
sup
plie
rs (
tran
sfer
coe
ffic
ient
s).
Dur
atio
n of
3 y
ears
for
wor
k
To
tal (
$)12
7500
10%
co
nti
ng
ency
($)
1275
0
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nd
to
tal (
$)14
0250
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
Cri
t S
SC
Sp
ecif
icat
ion
nu
mb
erS
pec
ific
atio
nD
escr
ipti
on
Co
mm
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IHX
AW
EC
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-IH
XA
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Met
hods
for
stre
ss-
stra
in m
odel
ling
of
IHX
A
Dev
elop
str
uctu
ral m
odel
ling
met
hods
for
pred
ictiv
e o p
erat
ion
for
IHX
AN
/A
Tas
ks r
equ
ired
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ion
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form
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yT
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f ($
)T
ime
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To
tal (
$)A
ssu
mp
tio
ns/
Bas
es
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ur
Yea
rH
ou
rsD
ays
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ksM
on
ths
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rS
truc
tura
l mod
el g
ener
atio
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ving
res
ults
for
pred
ictiv
e op
erat
ion
for
IHX
BG
roup
of m
odel
ing
spec
ialis
ts42
,500
312
7500
1) E
stm
atio
n m
ade
by M
-Tec
h ba
sed
on te
chno
logy
mat
urat
ion
plan
inpu
t.
Dur
atio
n of
3 y
ears
for
wor
k
To
tal (
$)12
7500
10%
co
nti
ng
ency
($)
1275
0
Gra
nd
to
tal (
$)14
0250
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
Cri
t S
SC
Sp
ecif
icat
ion
nu
mb
erS
pec
ific
atio
nD
escr
ipti
on
Co
mm
ents
IHX
AW
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XA
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Crit
eria
for
stru
ctur
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tegr
ityE
stab
lish
crite
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r st
ruct
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in
tegr
ity o
f CH
E's
N/A
Tas
ks r
equ
ired
Act
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per
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yT
arif
f ($
)T
ime
nee
ded
To
tal (
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ssu
mp
tio
ns/
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es
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ur
Yea
rH
ou
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ays
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ksM
on
ths
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r
Str
uctu
ral i
nteg
rity
mod
els
of C
HE
'sG
roup
of m
odel
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spec
ialis
ts42
,500
312
7500
1) E
stm
atio
n m
ade
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sed
on te
chno
logy
mat
urat
ion
plan
inpu
t.
Dur
atio
n an
d co
st is
gre
atly
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enda
nt o
n th
e da
ta s
uppl
ied
by s
uppl
iers
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ansf
er c
oeff
icie
nts)
. Dur
atio
n of
3 y
ears
for
wor
k
To
tal (
$)12
7500
10%
co
nti
ng
ency
($)
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0
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nd
to
tal (
$)14
0250
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
Cri
t S
SC
Sp
ecif
icat
ion
nu
mb
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pec
ific
atio
nD
escr
ipti
on
Co
mm
ents
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AW
EC
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XA
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Per
form
ance
m
odel
ling
met
hods
fo
r IH
X A
Dev
elop
per
form
ance
mod
els
for
pred
ictiv
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erat
ion
for
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A
N/A
Tas
ks r
equ
ired
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be
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form
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yT
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f ($
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ime
nee
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tal (
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ssu
mp
tio
ns/
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es
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Yea
rH
ou
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ays
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ksM
on
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r
Per
form
ance
mod
els
for
IHX
Gro
up o
f mod
elin
g sp
ecia
lists
42,5
003
1275
001)
Est
mat
ion
mad
e by
M-T
ech
base
d on
tech
nolo
gy m
atur
atio
n pl
an in
put.
Dur
atio
n of
3 y
ears
for
wor
k
To
tal (
$)12
7500
10%
co
nti
ng
ency
($)
1275
0
Gra
nd
to
tal (
$)14
0250
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17:
Int
egra
ted
Sch
edul
e an
d C
ost E
stim
ate
Mat
eria
l co
st d
etai
ls b
ased
on
pre
ferr
ed n
um
ber
of
sam
ple
s to
be
test
ed -
Allo
y 61
7 (@
$40
/kg
)
Sam
ple
am
ou
nt
Per
sam
ple
co
st -
617
549
IHX
A.2
183
IHX
A.3
732
IHX
A.4
138
IHX
A.5
180
IHX
A.6
Mat
.co
stC
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($)
sam
ple
s($
)sa
mp
les
($)
($)
($)
($)
Ela
stic
Pro
pert
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118
186
624
240
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le P
rope
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4545
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6060
00
00
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i gue
str
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CF
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013
513
500
4545
0018
018
000
4545
0060
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Fat
i gue
str
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CF
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013
513
500
4545
0018
018
000
4545
0060
6000
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e p s
tren
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214
428
848
9619
238
448
9660
120
Fra
ctur
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ess:
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100
2727
009
900
3636
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ract
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c10
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2700
990
036
3600
00
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The
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duct
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1018
180
660
2424
00
00
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ota
l ($)
414
3293
110
917
4366
890
9612
120
NG
NP
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F M
TE
CH
-TD
RM
-017
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0 1
2/03
/200
8
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
Cri
t S
SC
Sp
ecif
icat
ion
nu
mb
erS
pec
ific
atio
nD
escr
ipti
on
Co
mm
ents
IHX
AW
EC
-TS
-IH
XA
-018
Tra
de s
tudi
es o
n ca
ndid
ate
cera
mic
m
ater
ials
Eva
luat
e ce
ram
ic m
ater
ials
fo
r us
e in
cer
amic
CH
E's
N/A
Tas
ks r
equ
ired
Act
ion
to
be
per
form
ed b
yT
arif
f ($
)T
ime
nee
ded
To
tal (
$)A
ssu
mp
tio
ns/
Bas
es
Ho
ur
Act
ion
Ho
urs
Day
sW
eeks
Mo
nth
sE
valu
ate
and
iden
tify
cand
idat
e ce
ram
ic
mat
eria
ls fr
om tr
ade
stud
ies
Eng
inee
r20
0N
/A8
54
619
2000
Bas
ed o
n ne
ed o
f one
eng
inee
r fo
r du
ratio
n of
6 m
onth
s to
com
plet
e tr
ade
stud
ies.
Rep
ortin
g in
clud
ed.
To
tal (
$)19
2000
10%
co
nti
ng
ency
($)
1920
0
Gra
nd
to
tal (
$)21
1200
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
Cri
t S
SC
Sp
ecif
icat
ion
nu
mb
erS
pec
ific
atio
nD
escr
ipti
on
Co
mm
ents
IHX
AW
EC
-TS
-IH
XA
-019
Tra
de s
tudi
es o
n ca
ndid
ate
cera
mic
C
HE
des
i gns
Eva
luat
e ce
ram
ic C
HE
de
sign
s fo
r us
e in
cer
amic
IH
X A
N/A
Tas
ks r
equ
ired
Act
ion
to
be
per
form
ed b
yT
arif
f ($
)T
ime
nee
ded
To
tal (
$)A
ssu
mp
tio
ns/
Bas
es
Ho
ur
Act
ion
Ho
urs
Day
sW
eeks
Mo
nth
sE
valu
ate
and
iden
tify
cand
idat
e ce
ram
ic C
HE
de
sign
s fr
om tr
ade
stud
ies
Eng
inee
r20
0N
/A8
54
619
2000
Bas
ed o
n ne
ed o
f one
eng
inee
r fo
r du
ratio
n of
6 m
onth
s to
com
plet
e tr
ade
stud
ies.
Rep
ortin
g in
clud
ed.
To
tal (
$)19
2000
10%
co
nti
ng
ency
($)
1920
0
Gra
nd
to
tal (
$)21
1200
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
Cri
t S
SC
Sp
ecif
icat
ion
nu
mb
erS
pec
ific
atio
nD
escr
ipti
on
Co
mm
ents
IHX
AW
EC
-TS
-IH
XA
-020
Cer
amic
Hea
t E
xcha
nger
D
etai
led
DD
N's
Dev
elop
det
aile
d D
DN
's fo
r th
e ce
ram
ic IH
X A
N/A
Tas
ks r
equ
ired
Act
ion
to
be
per
form
ed b
yT
arif
f ($
)T
ime
nee
ded
To
tal (
$)A
ssu
mp
tio
ns/
Bas
es
Ho
ur
Act
ion
Ho
urs
Day
sW
eeks
Mo
nth
s
Dev
elop
ing
deta
iled
DD
N's
for
cera
mic
IHX
AE
ngin
eer
200
N/A
85
45
1600
00B
ased
on
need
of o
ne e
ngin
eer
for
dura
tion
of 6
mon
ths
to
com
pile
DD
N's
. Rep
ortin
g in
clud
ed.
To
tal (
$)16
0000
10%
co
nti
ng
ency
($)
1600
0
Gra
nd
to
tal (
$)17
6000
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
Cri
t S
SC
Sp
ecif
icat
ion
nu
mb
erS
pec
ific
atio
nD
escr
ipti
on
Co
mm
ents
IHX
AW
EC
-TS
-IH
XA
-021
Cer
amic
Mat
eria
l S
peci
ficat
ions
and
P
rocu
rem
ent
Fin
aliz
e m
ater
ial
spec
ifica
tions
, dev
elop
pr
ocur
emen
t req
uire
men
tsN
/A
Tas
ks r
equ
ired
Act
ion
to
be
per
form
ed b
yT
arif
f ($
)T
ime
nee
ded
To
tal (
$)A
ssu
mp
tio
ns/
Bas
es
Ho
ur
Act
ion
Ho
urs
Day
sW
eeks
Mo
nth
s
Cer
amic
pro
cure
men
t spe
cific
atio
nE
ngin
eer
200
N/A
85
43
9600
01)
Bas
ed o
n tim
e ne
eded
to c
ompi
le p
rocu
rem
ent s
peci
ficat
ion,
insp
ectio
n du
ring
proc
urem
ent p
rodu
ctio
n as
wel
l as
com
pilin
g re
port
.
To
tal (
$)96
000
10%
co
nti
ng
ency
($)
9600
Gra
nd
to
tal (
$)10
5600
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP-
CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
Cri
t S
SC
Sp
ecif
icat
ion
nu
mb
erS
pec
ific
atio
nD
escr
ipti
on
Co
mm
ents
The
rmal
, Phy
sica
lD
emon
stra
te th
at p
rocu
red
Cer
amic
IHX
AW
EC
-TS
-IH
XA
-022
prop
ertie
s of
Cer
amic
will
hav
e th
erm
al, p
hysi
cal
Co
st w
ill b
e h
igh
er c
om
par
ed t
o s
imila
r m
etal
lic IH
X A
sp
ecif
icat
ion
du
e to
intr
icac
y o
f sa
mp
le p
rep
arat
ion
,
prop
ertie
s ap
prop
riate
for
use
in C
HE
N/A
mac
hin
ing
an
d a
nal
yses
as
wel
l as
un
kno
wn
det
ail r
egar
din
g t
he
cera
mic
mat
eria
l to
be
use
d.
Res
ou
rces R
eso
urc
e re
qu
irem
ent
Act
ion
to
be
per
form
ed b
yTa
riff
($)
Du
rati
on
Tota
l ($)
Ass
um
pti
on
s/B
ases
Ho
ur
Act
ion
Ho
urs
Day
sW
eeks
Mo
nth
sY
ears
Co
nd
uct
ing
tes
tin
gLa
bora
tory
Tec
hnic
ian
80n/
a8
52
6400
Tes
ting
will
req
uire
res
ourc
es in
the
form
of
1 en
gine
er (
$200
/hou
r)
Ove
rsee
& M
anag
eE
ngin
eer
200
n/a
85
216
000
as w
ell a
s 1
labo
rato
ry te
chni
cian
(80
$/ho
ur).
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
.
Tota
l 1 (
$)22
400
Tes
tin
gTa
sk r
equ
irem
ent
Test
ing
Tota
l ($)
Ass
um
pti
on
s/B
ases
Sam
ple
s [1
]P
rep
(M
ach
inin
g)
[2]
Test
co
st/s
amp
leTe
stin
g C
ost
s
Eq
. set
up
P
ost
tes
t sa
mp
le p
rep
Po
st t
est
anal
ysis
Rep
ort
ing
Ther
mal
Ph
ysic
al p
rop
erti
es
The
rmal
con
duct
ivity
624
0010
060
0n/
an/
a12
0050
047
00T
herm
al c
ondu
ctiv
ity to
100
0°C
: - $
95-0
0 pe
r sp
ecim
en.
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
Coe
ffic
ient
of
ther
mal
exp
ansi
on6
2400
350
2100
n/a
n/a
n/a
500
5000
Coe
ffic
ient
of
ther
mal
exp
ansi
on te
st c
ost b
ased
on
Ten
sile
/Ela
stic
pro
pert
ies'
pric
e.
The
rmal
sho
ck r
esis
tanc
e6
2400
350
2100
n/a
n/a
1200
500
6200
The
rmal
sho
ck r
esis
tanc
e te
st c
ost b
ased
on
Ten
sile
/Ela
stic
pro
pert
ies'
pric
e.
SE
M R
elat
ed w
ork
n/a
Tota
l 2 (
$)72
0048
000
024
0015
0015
900
Mat
eria
lsM
ater
ials
req
uir
emen
tTo
tal (
$)A
ssu
mp
tio
ns/
Bas
es
Sam
ple
sM
at.c
ost
/sam
ple
Mat
eria
l co
st
Cer
amic
sam
ple
s [3
]n/
an/
a18
018
0C
ostin
g ba
sed
on m
ater
ial p
rice
of $
40/k
g. O
ther
fac
tors
bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
Tota
l 3 (
$)18
0
To
tal (
$)38
480
To
tal (
4 h
eats
at
leas
t) (
$)15
3920
10%
co
nti
ng
ency
($)
1539
2
Gra
nd
to
tal (
$)16
9312
C
ost
will
be
hig
her
co
mp
ared
to
sim
ilar
met
allic
IHX
A
Met
allic
IHX
A t
o C
eram
ic IH
X A
rat
io a
dju
stm
ent
0.5
s
pec
ific
atio
n d
ue
to in
tric
acy
of
sam
ple
pre
par
atio
n,
m
ach
inin
g a
nd
an
alys
es a
s w
ell a
s u
nkn
ow
n d
etai
l reg
ard
ing
Eq
uiv
alen
t co
sts
for
cera
mic
IHX
A s
pec
ific
atio
n33
8624
t
he
cera
mic
mat
eria
l to
be
use
d.
[1]S
ee p
refe
rred
num
ber
of s
ampl
es to
use
in 's
ampl
e' s
heet
[2] B
asis
for
pre
para
tion
cost
s -
$400
/sam
ple
[3] R
efer
to 'm
ater
ial c
ost'
shee
t for
mat
eria
l cos
ting
aspe
cts
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP-
CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
Cri
t S
SC
Sp
ecif
icat
ion
nu
mb
erS
pec
ific
atio
nD
escr
ipti
on
Co
mm
ents
Mec
hani
cal
Dem
onst
rate
that
pro
cure
d C
eram
ic
IHX
AW
EC
-TS
-IH
XA
-023
prop
ertie
s of
Cer
amic
will
hav
e th
e m
echa
nica
lC
ost
will
be
hig
her
co
mp
ared
to
sim
ilar
met
allic
IHX
A s
pec
ific
atio
n d
ue
to in
tric
acy
of
sam
ple
pre
par
atio
n,
prop
ertie
s ap
prop
riate
for
use
in C
HE
N/A
mac
hin
ing
an
d a
nal
yses
as
wel
l as
un
kno
wn
det
ail r
egar
din
g t
he
cera
mic
mat
eria
l to
be
use
d.
Res
ou
rces R
eso
urc
e re
qu
irem
ent
Act
ion
to
be
per
form
ed b
yTa
riff
($)
Du
rati
on
Tota
l ($)
Ass
um
pti
on
s/B
ases
Ho
ur
Act
ion
Ho
urs
Day
sW
eeks
Mo
nth
sY
ears
Co
nd
uct
ing
tes
tin
gLa
bora
tory
Tec
hnic
ian
80n/
a8
520
6400
0T
estin
g w
ill r
equi
re r
esou
rces
in th
e fo
rm o
f 1
engi
neer
($2
00/h
our)
Ove
rsee
& M
anag
eE
ngin
eer
200
n/a
85
2016
0000
as w
ell a
s 1
labo
rato
ry te
chni
cian
(80
$/ho
ur).
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
.
Tota
l 1 (
$)22
4000
Tes
tin
gTa
sk r
equ
irem
ent
Test
ing
Tota
l ($)
Ass
um
pti
on
s/B
ases
Sam
ple
s [1
]P
rep
(M
ach
inin
g)
[2]
Test
co
st/s
amp
leTe
stin
g C
ost
s
Eq
. set
up
P
ost
tes
t sa
mp
le p
rep
Po
st t
est
anal
ysis
[3]
Rep
ort
ing
Ther
mal
Ph
ysic
al M
ech
anic
al p
rop
erti
es
Ela
stic
pro
pert
ies
[4]
624
0035
021
00n/
an/
an/
a50
050
00$3
50-0
0 pe
r sp
ecim
en a
t 950
°C (
+-
30°C
). B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
acto
r).
Ten
sile
Pro
pert
ies
[5]
1560
0035
052
50n/
an/
an/
a50
011
750
$350
-00
per
spec
imen
at 9
50°C
(+
- 30
°C).
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
.
Fat
igue
Str
engt
h (L
CF
)45
1800
072
032
400
6600
0n/
a90
0010
0012
6400
Fat
igue
str
engt
h LC
F to
100
0°C
- $
720-
00 u
p to
80
000
cycl
es +
$20-
00/h
our
ther
e af
ter
per
spec
imen
at 9
50°C
(+
- 30
°C).
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
.
Fat
igue
str
engt
h (H
CF
)45
1800
080
036
000
6600
0n/
a90
0010
0013
0000
Fat
igue
str
engt
h H
CF
to 1
000°
C -
$80
0-00
up
to 1
000
000
cycl
es p
er
spec
imen
at 9
50°C
(+
- 30
°C).
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
.
Cre
ep s
tren
gth
4819
200
3500
1680
00n/
an/
an/
a50
018
7700
Cre
ep s
tren
gth
to 1
000°
C f
or 1
0,00
0 h
- $3
500-
00 p
er s
peci
men
. Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
Fra
ctur
e to
ughn
ess:
CT
OD
936
0010
0090
00n/
an/
a18
0050
014
900
Fra
ctur
e to
ughn
ess:
CT
OD
- $
1000
-00
at 6
50°C
per
spe
cim
en. B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
acto
Fra
ctur
e to
ughn
ess:
Kc
936
0056
050
40n/
an/
a18
0050
010
940
Fra
ctur
e to
ughn
ess:
Kc
- $5
60-0
0 at
650
°C p
er s
peci
men
. Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
.
Tota
l 2 (
$)70
800
2577
9013
2000
021
600
4500
4866
90
Mat
eria
lsM
ater
ials
req
uir
emen
tTo
tal (
$)A
ssu
mp
tio
ns/
Bas
es
Sam
ple
sM
at.c
ost
/sam
ple
Mat
eria
l co
st
Cer
amic
sam
ple
s [6
]n/
an/
a10
,917
10,9
17C
ostin
g ba
sed
on m
ater
ial p
rice
of $
40/k
g. O
ther
fac
tors
bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
.
Tota
l 3 (
$)10
917
To
tal (
$)72
1607
To
tal (
4 h
eats
at
leas
t) (
$)28
8642
810
% c
on
tin
gen
cy (
$)28
8643
Gra
nd
to
tal (
$)31
7507
1
Co
st w
ill b
e h
igh
er c
om
par
ed t
o s
imila
r m
etal
lic IH
X A
Met
allic
IHX
A t
o C
eram
ic IH
X A
rat
io a
dju
stm
ent
0.5
s
pec
ific
atio
n d
ue
to in
tric
acy
of
sam
ple
pre
par
atio
n,
m
ach
inin
g a
nd
an
alys
es a
s w
ell a
s u
nkn
ow
n d
etai
l reg
ard
ing
Eq
uiv
alen
t co
sts
for
cera
mic
IHX
A s
pec
ific
atio
n63
5014
2
th
e ce
ram
ic m
ater
ial t
o b
e u
sed
.
[1]S
ee p
refe
rred
num
ber
of s
ampl
es to
use
in 's
ampl
e' s
heet
[2] B
asis
for
pre
para
tion
cost
s -
$400
/sam
ple
[3] P
ost t
est a
naly
ses
incl
udes
pos
sibl
e op
tical
and
sca
nnin
g el
ectr
on m
icro
scop
y w
ork
and
is b
ased
on
engi
neer
/sci
entis
t tar
iff
[4] D
eter
min
atio
n by
way
of
mec
hani
cal t
estin
g no
t adv
ised
. D
eter
min
atio
n sh
ould
be
base
d on
nat
ural
vib
ratio
nal m
etho
ds
[5] T
ensi
le p
rope
rtie
s (y
ield
str
engt
h, te
nsile
str
engt
h, e
long
atio
n, a
nd R
A)
[6] R
efer
to 'm
ater
ial c
ost'
shee
t for
mat
eria
l cos
ting
aspe
cts
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
Cri
t SS
CS
pec
ifica
tion
nu
mb
erS
pec
ifica
tion
Des
crip
tion
Co
mm
ents
Com
patib
ility
ofD
emon
stra
te th
at C
eram
ic c
an b
e
IHX
AW
EC
-TS
-IHX
A-0
24ce
ram
ic m
ater
ials
tout
ilized
in N
GN
P e
nviro
nmen
t (te
mpe
ratu
re &
Co
st w
ill b
e h
igh
er c
om
par
ed t
o s
imila
r m
etal
lic IH
X A
sp
ecif
icat
ion
du
e to
intr
icac
y o
f sam
ple
pre
par
atio
n,
NG
NP
He
envi
ronm
ent
med
ium
) fo
r lo
ng p
erio
ds w
ithou
t deg
rada
tion
N/A
mac
hin
ing
an
d a
nal
yses
as
wel
l as
un
kno
wn
det
ail r
egar
din
g th
e ce
ram
ic m
ater
ial t
o b
e u
sed
.
Res
ou
rces R
eso
urc
e re
qu
irem
ent
Act
ion
to b
e p
erfo
rmed
by
Tar
iff ($
)D
ura
tion
To
tal (
$)A
ssu
mp
tion
s/B
ases
Ho
ur
Act
ion
Ho
urs
Day
sW
eeks
Mo
nth
sY
ears
Tes
ting
: T
her
mal
exp
osu
re o
f sam
ple
s -
10,0
00h
Labo
rato
ry T
echn
icia
n10
0n/
a10
010
000
Bas
is th
at th
erm
al e
xpos
ure
sam
ples
are
to b
e m
onito
red
by la
b te
chni
cian
eve
ry 1
00h
(100
inte
rval
s).
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
.
Ove
rsee
& M
anag
eE
ngin
eer
200
n/a
85
540
000
Bas
is o
f est
imat
e: R
esou
rce
requ
irem
ent i
n th
e fo
rm o
f one
eng
inee
r at
$20
0/ho
ur a
t 9 s
ampl
es/w
eek
To
tal 1
($)
5000
0 B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
acto
r).
Tes
tin
gT
ask
req
uir
emen
tT
estin
gT
ota
l ($)
Ass
um
ptio
ns/
Bas
es
Sam
ple
sP
rep
(Mac
hin
ing
) [1]
Tes
t co
st/s
amp
leT
estin
g C
ost
s
Eq
. set
up
P
ost
test
sam
ple
pre
pP
ost
test
an
alys
isR
epo
rtin
g
Met
allo
gra
ph
y/S
EM
Cut
ting,
pol
ishi
ng, e
tchi
ng s
ampl
e45
n/a
640
2880
0n/
an/
an/
a28
800
Tak
ing
into
acc
ount
that
labo
rato
ry te
chni
cian
will
need
8 h
ours
for
sam
ple
prep
arat
ion
at $
80/h
our.
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
.
Obs
erva
tion
of s
ampl
e/m
etal
lurg
y45
n/a
400
1800
0n/
an/
a50
018
000
Incl
usiv
e of
1)
Ana
lyse
s co
st (
incl
usiv
e of
ope
rato
r an
d m
achi
ne
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eerin
g in
put a
t $20
0/ho
ur.
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
.
To
tal 2
($)
046
800
00
050
046
800
Mat
eria
lsM
ater
ials
req
uir
emen
tT
ota
l ($)
Ass
um
ptio
ns/
Bas
es
Sam
ple
sM
at.c
ost
/sam
ple
Mat
eria
l co
st
Cer
amic
sam
ple
s [2
]n/
an/
a3,
030
3,03
0C
ostin
g ba
sed
on m
ater
ial p
rice
of $
40/k
g. O
ther
fact
ors
bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
.
To
tal 3
($)
3030
Oth
erA
dd
itio
nal
req
uir
emen
tsT
ota
l ($)
Ass
um
ptio
ns/
Bas
es (
Bas
ed o
n m
etal
lic IH
X A
(see
ad
just
men
t fac
tor)
.)
Un
it p
rice
($)
Qu
antit
y
Cap
ital c
ost
- fu
rnac
es fo
r th
erm
al a
gin
g30
003
9000
Cos
ting
base
d on
ver
bal q
uota
tion
for
furn
ace
with
req
uire
d ca
pabi
lity
size
d at
180
mm
x 1
80m
m x
250
mm
Co
ntin
gen
cies
(po
wer
co
nsu
mp
tion
, el
emen
t re p
lace
men
t)90
01
900
Fur
nace
con
tinge
ncie
s ba
sed
on 1
0% o
f tot
al c
apita
l cos
t for
furn
aces
Hel
ium
gas
for
reg
ula
ting
en
viro
nm
ent
120
156
18,7
2015
6 x
50kg
He
cylin
ders
to b
e ut
ilized
. Num
ber
base
d on
util
izat
ion
of o
ne c
ylin
der
a w
eek
for
each
furn
ace
for
1 ye
ar (
52 w
eeks
). H
e ga
s co
st in
clus
ive
of im
purit
y ga
ses.
Sam
plin
g g
as a
nal
yses
150
527,
800
Sam
plin
g of
furn
ace
test
ing
envi
ronm
ent d
one
once
a w
eek
by e
xter
nal
inst
itutio
n. C
olle
ctiv
e sa
mpl
ing
from
3 fu
rnac
es a
dd u
p to
$15
0/w
eek.
Bas
ed o
n pe
rson
al c
omm
unic
atio
n w
ith
rele
vant
par
ties
in M
tech
.
To
tal 4
($)
3642
0
To
tal (
$)13
6250
To
tal (
4 h
eats
at
leas
t) (
$)54
5000
10%
co
nti
ng
ency
($)
5450
0
Gra
nd
to
tal (
$)59
9500
C
ost
will
be
hig
her
co
mp
ared
to
sim
ilar
met
allic
IHX
A
s
pec
ifica
tion
du
e to
intr
icac
y o
f sam
ple
pre
par
atio
n,
Met
allic
IHX
A t
o C
eram
ic IH
X A
rat
io a
dju
stm
ent
0.5
m
ach
inin
g a
nd
an
alys
es a
s w
ell a
s u
nkn
ow
n d
etai
l reg
ard
ing
t
he
cera
mic
mat
eria
l to
be
use
d.
Eq
uiv
alen
t co
sts
for
cera
mic
IHX
A s
pec
ific
atio
n11
9900
0
[1] B
asis
for
prep
arat
ion
cost
s -
$400
/sam
ple
[2] R
efer
to 'm
ater
ial c
ost'
shee
t for
mat
eria
l cos
ting
aspe
cts
NG
NP
-CTF
MTE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17:
Int
egra
ted
Sche
dule
and
Cos
t Est
imat
e
Cri
t S
SC
Sp
ecif
icat
ion
nu
mb
erS
pec
ific
atio
nD
escr
ipti
on
Co
mm
ents
C
-C =
cer
amic
to c
eram
ic b
ond
Man
ufac
turin
g E
nsur
e th
at m
etho
ds a
nd te
chni
ques
C
-M =
cer
amic
to m
etal
licC
ost
will
be
hig
her
co
mp
ared
to
sim
ilar
met
allic
IHX
A s
pec
ific
atio
n d
ue
to in
tric
acy
of
sam
ple
pre
par
atio
n,
IHX
AW
EC
-TS
-IH
XA
-025
tech
nolo
gy f
orar
e av
aila
ble
and
effe
ctiv
e in
est
ablis
hing
C-C
com
p =
C-C
com
posi
te jo
ints
mac
hin
ing
an
d a
nal
yses
as
wel
l as
un
kno
wn
det
ail r
egar
din
g t
he
cera
mic
mat
eria
l to
be
use
d.
cera
mic
CH
E's
the
CH
EN
/A
Res
ou
rces R
eso
urc
e re
qu
irem
ent
Act
ion
to
be
per
form
ed b
yTa
riff
($)
Du
rati
on
Tota
l ($)
Ass
um
pti
on
s/B
ases
(B
ased
on
met
allic
IHX
A (
see
adju
stm
ent
fact
or)
).
Ho
ur
Act
ion
Ho
urs
Day
sW
eeks
Mo
nth
sY
ears
Join
t d
esig
n/C
om
pili
ng
C-C
/C-M
/C-C
co
mp
bo
nd
sp
ecif
icat
ion
Eng
inee
r20
08
54
396
000
Ass
umin
g 1
mon
th n
eede
d pe
r jo
inin
g m
etho
d to
com
pile
spe
cific
atio
n (c
-c/m
-c/c
-c c
omp)
Bo
nd
ing
of
join
ts (
C-C
/C-M
/C-C
co
mp
) fo
r sa
mp
les
Cod
ed w
elde
r10
08
545
1800
0013
5 sa
mpl
es to
be
join
ed. A
ssum
e 3
sam
ples
/wee
k du
e to
the
larg
e un
cert
aint
y in
tim
e ne
eded
to e
stab
lish
cer
Ove
rsee
& M
anag
eE
ngin
eer
200
n/a
85
1512
0000
Ove
rsig
ht a
nd m
anag
emen
t will
req
uire
res
ourc
es in
the
form
of
1 en
gine
er (
$200
/hou
r)
Tota
l 1 (
$)39
6000
Tes
tin
gTa
sk r
equ
irem
ent
Test
ing
Tota
l ($)
Ass
um
pti
on
s/B
ases
Sam
ple
sP
rep
(M
ach
inin
g)
[1]
Test
co
st/s
amp
leTe
stin
g C
ost
s
Eq
. set
up
P
ost
tes
t sa
mp
le p
rep
Po
st t
est
anal
ysis
Rep
ort
ing
Met
allo
gra
ph
y/S
amp
le p
rep
arat
ion
&
anal
yses
[2]
]
Sam
ple
prep
arat
ion
135
640
8640
086
400
Tak
ing
into
acc
ount
that
labo
rato
ry te
chni
cian
will
nee
d 8
hour
s fo
r
sam
ple
prep
arat
ion
at $
80/h
our.
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
Obs
erva
tion
of m
etal
lurg
y/op
tical
/SE
M13
540
054
000
5400
0In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eerin
g in
put a
t $20
0/ho
ur .
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t
Che
mis
try
prof
ile in
join
ts13
540
054
000
5400
0In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eerin
g in
put a
t $20
0/ho
ur .
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t
Tota
l 2 (
$)14
4019
4400
1944
00
Mat
eria
ls
Mat
eria
ls r
equ
irem
ent
Tota
l ($)
Ass
um
pti
on
s/B
ases
Sam
ple
sM
at.c
ost
/sam
ple
Mat
eria
l co
st
Cer
amic
sam
ple
s [3
]n/
an/
a9,
090
9,09
0C
ostin
g ba
sed
on m
ater
ial p
rice
of $
40/k
g. T
his
does
not
allo
w f
or
the
cost
/dev
elop
men
t for
the
wel
d/br
aze
allo
y. O
ther
fac
tors
bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
Tota
l 3 (
$)90
90
To
tal (
$)59
9490
To
tal (
4 h
eats
at
leas
t) (
$)23
9796
010
% c
on
tin
gen
cy (
$)23
9796
Gra
nd
to
tal (
$)26
3775
6
Co
st w
ill b
e h
igh
er c
om
par
ed t
o s
imila
r m
etal
lic IH
X A
s
pec
ific
atio
n d
ue
to in
tric
acy
of
sam
ple
pre
par
atio
n,
Met
allic
IHX
A t
o C
eram
ic IH
X A
rat
io a
dju
stm
ent
0.5
m
ach
inin
g a
nd
an
alys
es a
s w
ell a
s u
nkn
ow
n d
etai
l reg
ard
ing
t
he
cera
mic
mat
eria
l to
be
use
d.
Eq
uiv
alen
t co
sts
for
cera
mic
IHX
A s
pec
ific
atio
n52
7551
2
[1] B
asis
for
pre
para
tion
cost
s -
$400
/sam
ple
[2] A
ssum
ing
that
all
the
join
ed s
ampl
es to
be
chec
ked
for
join
t int
egrit
y af
ter
join
ing
[3] R
efer
to 'm
ater
ial c
ost'
shee
t for
mat
eria
l cos
ting
aspe
cts
NG
NP
-CTF
MTE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d S
ched
ule
and
Cos
t Est
imat
e
Cri
t S
SC
Sp
ecif
icat
ion
nu
mb
erS
pec
ific
atio
nD
escr
ipti
on
Co
mm
ents
IHX
AW
EC
-TS
-IH
XA
-026
Cer
amic
mat
eria
ls
code
s an
d st
anda
rds
Dev
elop
and
est
ablis
h A
SM
E
code
cas
e an
d A
ST
M
stan
dard
sN
/A
Tas
ks r
equ
ired
Act
ion
to
be
per
form
ed b
yT
arif
f ($
)T
ime
nee
ded
To
tal (
$)A
ssu
mp
tio
ns/
Bas
es (
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fa
cto
r)).
Ho
ur
Act
ion
Ho
urs
Day
sW
eeks
Mo
nth
s
Pre
para
tory
wor
kE
ngin
eers
150
n/a
110
1650
01)
Est
mat
ion
incl
usiv
e of
inte
ract
ions
with
AS
ME
and
AS
TM
dur
ing
appr
oval
pro
cess
and
prov
isio
n of
add
ition
al d
ata
requ
este
d D
raftt
ing
code
cas
e an
d st
anda
rds
for
cera
mic
Eng
inee
rs15
0n/
a45
0067
5000
by A
SM
E/A
ST
M. B
asis
ent
ails
dis
cuss
ions
with
Geo
rge
Hay
ner.
Tot
al 1
($)
6915
00
To
tal (
$)69
1500
10%
co
nti
ng
ency
($)
6915
0
Gra
nd
to
tal (
$)76
0650
Met
allic
IHX
A t
o C
eram
ic IH
X A
rat
io a
dju
stm
ent
0.5
Eq
uiv
alen
t co
sts
for
cera
mic
IHX
A s
pec
ific
atio
n15
2130
0
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
Cri
t S
SC
Sp
ecif
icat
ion
nu
mb
erS
pec
ific
atio
nD
escr
ipti
on
Co
mm
ents
IHX
AW
EC
-TS
-IH
XA
-027
The
rmal
/Flu
id a
nd
stre
ss-s
trai
n m
odel
ling
met
hods
fo
r ce
ram
ic IH
X A
Dev
elop
ther
mal
-flu
id a
nd
stre
ss-s
trai
n m
odel
s fo
r ce
ram
ic IH
X A
N/A
Tas
ks r
equ
ired
Act
ion
to
be
per
form
ed b
yT
arif
f ($
)T
ime
nee
ded
To
tal (
$)A
ssu
mp
tio
ns/
Bas
es (
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fa
cto
r))
Ho
ur
Yea
rH
ou
rsD
ays
Wee
ksM
on
ths
Yea
rM
odel
gen
erat
ion
com
bini
ng th
erm
al-f
luid
as
wel
l as
stre
ss-s
trai
n m
odel
s to
gui
de
cera
mic
IHX
des
i gn
Gro
up o
f mod
elin
g sp
ecia
lists
63,0
003
1890
001)
Est
mat
ion
mad
e by
M-T
ech
- D
urat
ion
and
cost
is g
reat
ly
depe
ndan
t on
the
data
sup
plie
d by
sup
plie
rs (
tran
sfer
coe
ffici
ents
).
Dur
atio
n of
3 y
ears
for
wor
k
To
tal (
$)18
9000
10%
co
nti
ng
ency
($)
1890
0
Gra
nd
to
tal (
$)20
7900
Met
allic
IHX
A t
o C
eram
ic IH
X A
rat
io a
dju
stm
ent
0.5
Eq
uiv
alen
t co
sts
for
cera
mic
IHX
A s
pec
ific
atio
n41
5800
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP-
CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17:
Int
egra
ted
Sche
dule
and
Cos
t Est
imat
e
Cri
t S
SC
Sp
ecif
icat
ion
nu
mb
erS
pec
ific
atio
nD
escr
ipti
on
Co
mm
ents
IHX
AW
EC
-TS
-IH
XA
-028
Crit
eria
for
st
ruct
ural
inte
grity
fo
r ce
ram
ic IH
X A
Est
ablis
h cr
iteria
for
str
uctu
ral
inte
grity
for
cer
amic
IHX
AN
/A
Tas
ks r
equ
ired
Act
ion
to
be
per
form
ed b
yT
arif
f ($
)T
ime
nee
ded
To
tal (
$)A
ssu
mp
tio
ns/
Bas
es (
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fa
cto
r))
Ho
ur
Yea
rH
ou
rsD
ays
Wee
ksM
on
ths
Yea
r
Str
uctu
ral i
nteg
rity
mod
els
of c
eram
ic IH
X A
Gro
up o
f m
odel
ing
spec
ialis
ts42
,500
312
7500
1) E
stm
atio
n m
ade
by M
-Tec
h -
Dur
atio
n an
d co
st is
gre
atly
depe
ndan
t on
the
data
sup
plie
d by
sup
plie
rs (
tran
sfer
coe
ffic
ient
s).
Dur
atio
n of
3 y
ears
for
wor
k
To
tal (
$)12
7500
10%
co
nti
ng
ency
($)
1275
0
Gra
nd
to
tal (
$)14
0250
Met
allic
IHX
A t
o C
eram
ic IH
X A
rat
io a
dju
stm
ent
0.5
Eq
uiv
alen
t co
sts
for
cera
mic
IHX
A s
pec
ific
atio
n28
0500
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP-
CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17:
Int
egra
ted
Sche
dule
and
Cos
t Est
imat
e
Cri
t S
SC
Sp
ecif
icat
ion
nu
mb
erS
pec
ific
atio
nD
escr
ipti
on
Co
mm
ents
IHX
AW
EC
-TS
-IH
XA
-029
Per
form
ance
m
odel
ling
met
hods
fo
r ce
ram
ic IH
X A
Dev
elop
per
form
ance
mod
els
for
pred
ictiv
e op
erat
ion
for
cera
mic
IHX
AN
/A
Tas
ks r
equ
ired
Act
ion
to
be
per
form
ed b
yT
arif
f ($
)T
ime
nee
ded
To
tal (
$)A
ssu
mp
tio
ns/
Bas
es (
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fa
cto
r))
Ho
ur
Yea
rH
ou
rsD
ays
Wee
ksM
on
ths
Yea
r
Per
form
ance
mod
els
for
cera
mic
IHX
Gro
up o
f m
odel
ing
spec
ialis
ts42
,500
312
7500
1) E
stm
atio
n m
ade
by M
-Tec
h
Dur
atio
n of
3 y
ears
for
wor
k
To
tal (
$)12
7500
10%
co
nti
ng
ency
($)
1275
0
Gra
nd
to
tal (
$)14
0250
Met
allic
IHX
A t
o C
eram
ic IH
X A
rat
io a
dju
stm
ent
0.5
Eq
uiv
alen
t co
sts
for
cera
mic
IHX
A s
pec
ific
atio
n28
0500
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
Mat
eria
l co
st d
etai
ls b
ased
on
pre
ferr
ed n
um
ber
of
sam
ple
s to
be
test
ed -
Cer
amic
[1]
(@
$40
/kg
)
Sam
ple
am
ou
nt
[2]
Per
sam
ple
co
st -
617
18IH
XA
.22
177
IHX
A.2
345
IHX
A.2
413
5IH
XA
.25
Sh
eet
nam
eM
at.c
ost
Co
st($
)sa
mp
les
($)
sam
ple
s($
)($
)($
)E
last
ic P
rope
rtie
s 1
00
66
00
00
Ten
sile
Pro
pert
ies
10
015
150
00
0F
atig
ue s
tren
gth
(LC
F)
100
00
4545
0015
1500
4545
00F
ati g
ue s
tren
gth
(HC
F)
100
00
4545
0015
1500
4545
00C
reep
str
engt
h2
00
4896
1530
4590
Fra
ctur
e to
u ghn
ess:
CT
OD
100
00
990
00
00
0F
ract
ure
toug
hnes
s: K
c10
00
09
900
00
00
The
rmal
con
duct
ivit y
1018
180
00
00
00
To
tal (
$)41
418
010
917
3030
9090
[1] D
own
sele
ctio
n of
the
cera
mic
mat
eria
l stil
l has
to b
e do
ne a
nd th
is v
alue
is s
ubje
ct to
cha
nge
[2] S
ampl
e am
ount
nee
ded
base
d on
Met
allic
IHX
A S
ampl
es r
equi
red
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d S
ched
ule
and
Cos
t Est
imat
e
Cri
t S
SC
Sp
ecif
icat
ion
nu
mb
erS
pec
ific
atio
nD
escr
ipti
on
Co
mm
ents
IHX
BW
EC
-TS
-IH
XB
-001
Allo
y 80
0H
Mat
eria
l S
peci
ficat
ions
and
P
rocu
rem
ent
Fin
aliz
e m
ater
ial
spec
ifica
tions
, dev
elop
pr
ocur
emen
t req
uire
men
ts,
proc
ure
1/2
heat
s of
Allo
y 80
0H
N/A
Tas
ks r
equ
ired
Act
ion
to
be
per
form
ed b
yT
arif
f ($
)T
ime
nee
ded
To
tal (
$)A
ssu
mp
tio
ns/
Bas
es (
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fa
cto
r)).
Ho
ur
Act
ion
Ho
urs
Day
sW
eeks
Mo
nth
s
Allo
y 80
0H p
rocu
rem
ent s
peci
ficat
ion
Eng
inee
r20
0N
/A8
58
6400
01)
Bas
ed o
n tim
e ne
eded
to c
ompi
le p
rocu
rem
ent s
peci
ficat
ion,
insp
ectio
n du
ring
proc
urem
ent p
rodu
ctio
n (p
rodu
ctio
n/ro
lling
/sam
plin
g)
as w
ell a
s co
mpi
ling
repo
rt.
To
tal (
$)64
000
10%
co
nti
ng
ency
($)
6400
Gra
nd
to
tal (
$)70
400
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP-
CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
Cri
t S
SC
Sp
ecif
icat
ion
nu
mb
erS
pec
ific
atio
nD
escr
ipti
on
Co
mm
ents
W =
Wel
ding
Allo
y 80
0H jo
inin
gD
emon
stra
te th
at A
lloy8
00H
can
be
BR
= B
razi
ng
IHX
BW
EC
-TS
-IH
XB
-002
tech
nolo
gy a
ndbr
azed
, diff
usio
n bo
nded
and
that
join
tD
B =
Diff
usio
n B
ondi
ngS
ame
equ
ival
ent
of
wo
rk n
eed
ed a
s fo
r m
etal
lic IH
X A
sp
ecif
icat
ion
resu
ltant
pro
pert
ies
prop
ertie
s ar
e ap
prop
riate
for
this
use
N/A
Res
ou
rces R
eso
urc
e re
qu
irem
ent
Act
ion
to
be
per
form
ed b
yT
arif
f ($
)D
ura
tio
nT
ota
l ($)
Ass
um
pti
on
s/B
ases
(B
ased
on
met
allic
IHX
A (
see
adju
stm
ent
fact
or)
).
Ho
ur
Act
ion
Ho
urs
Day
sW
eeks
Mo
nth
sY
ears
Wel
d d
esi g
n/C
om
pili
ng
W-B
R-D
B
s pec
ific
atio
nE
ngin
eer
200
85
43
9600
0A
ssum
ing
1 m
onth
nee
ded
per
join
ing
met
hod
to c
ompi
le s
peci
ficat
ion
(W/B
R/D
B)
Wel
din
g o
f jo
ints
(W
/BR
/DB
)C
oded
wel
der
100
85
4618
4000
549
sam
ples
to b
e jo
ined
. Due
to la
rge
unce
rtai
nty
of th
e tim
e ne
eded
to e
stab
lish
diff
usio
n bo
nded
spe
cim
ens,
ass
ume
that
12
sam
ples
/wee
k ar
e to
be
join
ed (
irres
pect
ive
of jo
inin
g m
etho
d).
Co
nd
uct
ing
tes
tin
g:
Join
t p
rop
erti
esLa
bora
tory
Tec
hnic
ian
80n/
a8
561
1952
00T
estin
g w
ill r
equi
re r
esou
rces
in th
e fo
rm o
f 1 e
ngin
eer
($20
0/ho
ur)
Ove
rsee
& M
anag
eE
ngin
eer
200
n/a
85
6148
8000
as w
ell a
s 1
labo
rato
ry te
chni
cian
(80
$/ho
ur).
Ass
umin
g th
at 9
sam
ples
/wee
k ar
e te
sted
To
tal 1
($)
9632
00(d
ue to
larg
e tim
e un
cert
aint
y fo
r fa
tigue
test
ing)
Tes
ting
Tas
k re
qu
irem
ent
Tes
tin
gT
ota
l ($)
Ass
um
pti
on
s/B
ases
(B
ased
on
met
allic
IHX
A (
see
adju
stm
ent
fact
or)
).
Sam
ple
s [1
]P
rep
(M
ach
inin
g)
[2]
Tes
t co
st/s
amp
leT
esti
ng
Co
sts
E
q. s
etu
p
Po
st t
est
sam
ple
pre
pP
ost
tes
t an
alys
isR
epo
rtin
gM
etal
log
rap
hy
(po
st w
eld
ing
/bo
nd
ing
, pre
-te
stin
g)
[3]
Cut
ting,
pol
ishi
ng54
964
035
1360
3513
60T
akin
g in
to a
ccou
nt th
at la
bora
tory
tech
nici
an w
ill n
eed
8 ho
urs
for
sam
ple
prep
arat
ion
at $
80/h
our.
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
Obs
erva
tion
of m
etal
lurg
y54
940
021
9600
2196
00In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eerin
g in
put a
t $20
0/ho
ur.
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
Che
mis
try
prof
ile in
join
ts54
940
021
9600
2196
00In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eerin
g in
put a
t $20
0/ho
ur.
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
Th
erm
al P
hys
ical
Mec
han
ical
pro
per
ties
of
W/B
R/D
B jo
ints
Ela
stic
pro
pert
ies
[4]
1872
0035
063
00n/
an/
an/
a50
014
000
$350
-00
per
spec
imen
at 9
50°C
(+-
30°
C).
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
Ten
sile
Pro
pert
ies
[5]
4518
000
350
1575
0n/
an/
an/
a50
034
250
$350
-00
per
spec
imen
at 9
50°C
(+-
30°
C).
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
Fat
igue
Str
engt
h (L
CF
)13
554
000
720
9720
066
000
n/a
n/a
1000
2182
00F
atig
ue s
tren
gth
LCF
to 1
000°
C -
$72
0-00
up
to 8
0 00
0 cy
cles
+
$20-
00/h
our
ther
e af
ter
per
spec
imen
at 9
50°C
(+-
30°
C).
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
Fat
igue
str
engt
h (H
CF
)13
554
000
800
1080
0066
000
n/a
n/a
1000
2290
00F
atig
ue s
tren
gth
HC
F to
100
0°C
- $
800-
00 u
p to
100
0 00
0 cy
cles
per
spec
imen
at 9
50°C
(+-
30°
C).
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
Cre
ep s
tren
gth
144
5760
035
0050
4000
n/a
n/a
n/a
500
5621
00C
reep
str
engt
h to
100
0°C
for
10,0
00 h
- $
3500
-00
per
spec
imen
. Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
Fra
ctur
e to
ughn
ess:
CT
OD
2710
800
1000
2700
0n/
an/
an/
a50
038
300
Fra
ctur
e to
ughn
ess:
CT
OD
- $
1000
-00
at 6
50°C
per
spe
cim
en. B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
acto
r)
Fra
ctur
e to
ughn
ess:
Kc
2710
800
560
1512
0n/
an/
an/
a50
026
420
Fra
ctur
e to
ughn
ess:
Kc
- $5
60-0
0 at
650
°C p
er s
peci
men
. Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
The
rmal
con
duct
ivity
1872
0010
018
00n/
an/
an/
a50
095
00T
herm
al c
ondu
ctiv
ity to
100
0°C
: - $
95-0
0 pe
r sp
ecim
en. B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
acto
r)
Met
allo
gra
ph
y/O
pti
cal/S
EM
(p
ost
-w
eld
ing
,po
st-t
esti
ng
) [
6]C
uttin
g, p
olis
hing
, etc
hing
sam
ple
459
640
2937
6029
3760
Tak
ing
into
acc
ount
that
labo
rato
ry te
chni
cian
will
nee
d 8
hour
s fo
r
sam
ple
prep
arat
ion
at $
80/h
our.
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
Obs
erva
tion
of s
ampl
e/m
etal
lurg
y45
940
018
3600
1836
00In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eerin
g in
put a
t $20
0/ho
ur .
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
To
tal 2
($)
2196
0012
5253
013
2000
00
5000
2399
690
Mat
eria
lsM
ater
ials
req
uir
emen
tT
ota
l ($)
Ass
um
pti
on
s/B
ases
(B
ased
on
met
allic
IHX
A (
see
adju
stm
ent
fact
or)
).
Sam
ple
sM
at.c
ost
/sam
ple
Mat
eria
l co
st
Allo
y 80
0H s
amp
les
[7]
n/a
n/a
28,8
1528
,815
Cos
ting
base
d on
mat
eria
l pric
e of
$35
/kg.
Thi
s do
es n
ot a
llow
for
the
cost
/dev
elop
men
t for
the
wel
d/br
aze
allo
y. O
ther
asp
ects
bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
To
tal 3
($)
2881
5
To
tal (
$)33
9170
5
10%
co
ntin
gen
cy ($
)33
9170
Gra
nd
tota
l ($)
3730
875
Sam
e es
tim
ates
fo
r IH
X B
rel
atin
g t
o IH
X A
IHX
A to
IHX
B r
atio
ad
just
men
t1
Sam
e eq
uiv
alen
t o
f w
ork
nee
ded
as
for
met
allic
IHX
A s
pec
ific
atio
n
Eq
uiv
alen
t co
sts
for
IHX
B s
pec
ifica
tion
3730
875
[1] S
ee p
refe
rred
num
ber
of s
ampl
es to
be
used
in 's
ampl
e' s
heet
[2] B
asis
for
prep
arat
ion
cost
s -
$400
/sam
ple
[3] A
ssum
ing
that
all
the
join
ed s
ampl
es to
be
chec
ked
for
join
t int
egrit
y af
ter
join
ing
[4] D
eter
min
atio
n by
way
of m
echa
nica
l tes
ting
not a
dvis
ed. D
eter
min
atio
n sh
ould
be
base
d on
nat
ural
vib
ratio
nal m
etho
ds
[5] T
ensi
le p
rope
rtie
s (y
ield
str
engt
h, te
nsile
str
engt
h, e
long
atio
n, a
nd R
A)
[6] O
ptic
al/S
EM
wor
k to
be
cond
ucte
d fo
r te
sile
, fat
igue
(H
CF
& L
CF
) an
d cr
eep
[7] R
efer
to 'm
ater
ial c
ost'
shee
t for
mat
eria
l cos
ting
aspe
cts
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t R
oad
Map
ping
Rep
ort
Sec
tion
17: I
nteg
rate
d S
ched
ule
and
Cos
t E
stim
ate
Cri
t S
SC
Sp
ecif
icat
ion
num
ber
Sp
ecif
icat
ion
Des
crip
tion
Co
mm
ents
The
rmal
, Phy
sica
lD
emon
stra
te th
at p
rocu
red
Allo
y800
H
IHX
BW
EC
-TS
-IH
XB
-003
and
Mec
hani
cal
will
hav
e th
erm
al, p
hysi
cal a
nd m
echa
nica
lC
ost
will
be
low
er c
om
par
ed t
o s
imila
r m
etal
lic IH
X A
sp
ecif
icat
ion
due
to
the
exi
stin
g
prop
ertie
s of
Allo
y 80
0Hpr
oper
ties
appr
opria
te fo
r us
e in
CH
EN
/AA
lloy
800H
dat
abas
e th
at c
an b
e ad
op
ted
Res
ou
rces R
eso
urce
req
uire
men
tA
ctio
n to
be
per
form
ed b
yT
arif
f ($
)D
urat
ion
To
tal (
$)A
ssum
ptio
ns/B
ases
(B
ased
on
met
allic
IHX
A (
see
adju
stm
ent
fact
or)
).H
our
Act
ion
Ho
urs
Day
sW
eeks
Mo
nths
Yea
rs
Co
nduc
ting
tes
ting
Labo
rato
ry T
echn
icia
n80
n/a
85
2167
200
Tes
ting
will
req
uire
res
ourc
es in
the
form
of 1
eng
inee
r ($
200/
hour
)
Ove
rsee
& M
anag
eE
ngin
eer
200
n/a
85
2116
8000
as w
ell a
s 1
labo
rato
ry te
chni
cian
(80
$/ho
ur).
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
To
tal 1
($)
2352
00
Tes
tin
gT
ask
req
uire
men
tT
estin
gT
ota
l ($)
Ass
ump
tions
/Bas
es (
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fa
cto
r)).
Sam
ple
s [1
]P
rep
(M
achi
ning
) [2
]T
est
cost
/sam
ple
Tes
ting
Co
sts
E
q. s
etup
P
ost
tes
t sa
mp
le p
rep
Po
st t
est
anal
ysis
[3]
Rep
ort
ing
The
rmal
Phy
sica
l Mec
hani
cal p
rop
ertie
s
Ela
stic
pro
pert
ies
[4]
624
0035
021
00n/
an/
an/
a50
050
00$3
50-0
0 pe
r sp
ecim
en a
t 950
°C (
+-
30°C
). B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
acto
r)
Ten
sile
Pro
pert
ies
[5]
1560
0035
052
50n/
an/
an/
a50
011
750
$350
-00
per
spec
imen
at 9
50°C
(+
- 30
°C).
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
Fat
igue
Str
engt
h (L
CF
)45
1800
072
032
400
6600
0n/
a90
0010
0012
6400
Fat
igue
str
engt
h LC
F to
100
0°C
- $
720-
00 u
p to
80
000
cycl
es +
$20-
00/h
our
ther
e af
ter
per
spec
imen
at 9
50°C
(+
- 30
°C).
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
Fat
igue
str
engt
h (H
CF
)45
1800
080
036
000
6600
0n/
a90
0010
0013
0000
Fat
igue
str
engt
h H
CF
to 1
000°
C -
$80
0-00
up
to 1
000
000
cycl
es p
er
spec
imen
at 9
50°C
(+
- 30
°C).
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
Cre
ep s
tren
gth
4819
200
3500
1680
00n/
an/
an/
a50
018
7700
Cre
ep s
tren
gth
to 1
000°
C fo
r 10
,000
h -
$35
00-0
0 pe
r sp
ecim
en. B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
acto
r)
Fra
ctur
e to
ughn
ess:
CT
OD
936
0010
0090
00n/
an/
a18
0050
014
900
Fra
ctur
e to
ughn
ess:
CT
OD
- $
1000
-00
at 6
50°C
per
spe
cim
en. B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
acto
r)
Fra
ctur
e to
ughn
ess:
Kc
936
0056
050
40n/
an/
a18
0050
010
940
Fra
ctur
e to
ughn
ess:
Kc
- $5
60-0
0 at
650
°C p
er s
peci
men
. Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
The
rmal
con
duct
ivity
624
0010
060
0n/
an/
a12
0050
047
00T
herm
al c
ondu
ctiv
ity to
100
0°C
: - $
95-0
0 pe
r sp
ecim
en. B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
acto
r)
SE
M R
elat
ed w
ork
n/a
To
tal 2
($)
7320
025
8390
1320
000
2280
050
0049
1390
Mat
eria
lsM
ater
ials
req
uire
men
tT
ota
l ($)
Ass
ump
tions
/Bas
es (
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fa
cto
r)).
Sam
ple
sM
at.c
ost
/sam
ple
Mat
eria
l co
st
Allo
y 80
0H s
amp
les
[6]
n/a
n/a
9,55
29,
552
Cos
ting
base
d on
mat
eria
l pric
e of
$35
/kg.
Oth
er fa
ctot
s ba
sed
on m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
To
tal 3
($)
9552
To
tal (
$)73
6142
10%
co
nti
ng
ency
($)
7361
4
Gra
nd
to
tal (
$)80
9757
IHX
A t
o IH
X B
rat
io a
dju
stm
ent
10C
ost
will
be
low
er c
om
par
ed t
o s
imila
r m
etal
lic IH
X A
sp
ecif
icat
ion
due
to
the
exi
stin
g
Allo
y 80
0H d
atab
ase
that
can
be
ado
pte
dE
qu
ival
ent
cost
s fo
r IH
X B
sp
ecif
icat
ion
8097
6
[1] S
ee p
refe
rred
num
ber
of s
ampl
es to
be
used
in 's
ampl
e' s
heet
[2] B
asis
for
prep
arat
ion
cost
s -
$400
/sam
ple
[3] P
ost t
est a
naly
ses
incl
udes
pos
sibl
e op
tical
and
sca
nnin
g el
ectr
on m
icro
scop
y w
ork
and
is b
ased
eng
inee
r/sc
ient
ist t
ariff
of $
200/
hour
[4] D
eter
min
atio
n by
way
of m
echa
nica
l tes
ting
not a
dvis
ed. D
eter
min
atio
n sh
ould
be
base
d on
nat
ural
vib
ratio
nal m
etho
ds
[5] T
ensi
le p
rope
rtie
s (y
ield
str
engt
h, te
nsile
str
engt
h, e
long
atio
n, a
nd R
A)
[6] R
efer
to 'm
ater
ial c
ost'
shee
t for
mat
eria
l cos
ting
aspe
cts
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP-
CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
Cri
t S
SC
Sp
ecif
icat
ion
nu
mb
erS
pec
ific
atio
nD
escr
ipti
on
Co
mm
ents
Effe
cts
of th
erm
alD
emon
stra
te th
at A
lloy
800H
can
be
Co
st w
ill b
e lo
wer
co
mp
ared
to
sim
ilar
met
alli
c IH
X A
sp
ecif
icat
ion
du
e to
th
e ex
isti
ng
IHX
BW
EC
-TS
-IHX
B-0
04ag
ing
and
envi
ronm
ent
utili
zed
in N
GN
P e
nviro
nmen
t (te
mpe
ratu
re &
All
oy
800H
dat
abas
e th
at c
an b
e ad
op
ted
on A
lloy
800H
prop
ertie
sm
ediu
m)
for
long
per
iods
with
out d
egra
datio
nN
/A
Res
ou
rces R
eso
urc
e re
qu
irem
ent
Act
ion
to
be
per
form
ed b
yT
arif
f ($
)D
ura
tio
nT
ota
l ($)
Ass
um
pti
on
s/B
ases
( B
ased
on
met
alli
c IH
X A
(se
e ad
just
men
t fa
cto
r)).
Ho
ur
Act
ion
Ho
urs
Day
sW
eeks
Mo
nth
sY
ears
Wel
din
g o
f jo
ints
(W
/BR
/DB
)C
oded
wel
der
n/a
n/a
n/a
n/a
n/a
0
Ove
rsee
& M
anag
e: T
her
mal
exp
osu
re o
f sa
mp
les
- 10
,000
hLa
bora
tory
Tec
hnic
ian
100
n/a
100
1000
0T
herm
al e
xpos
ure
mon
itore
d by
lab
tech
nici
an e
very
100
h (1
00 in
terv
als)
. B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
acto
r)
Co
nd
uct
ing
tes
tin
g:
All
oy
pro
per
ties
Labo
rato
ry T
echn
icia
n80
n/a
85
2167
200
Tes
ting
will
req
uire
res
ourc
es in
the
form
of 1
eng
inee
r ($
200/
hour
)
Ove
rsee
& M
anag
eE
ngin
eer
200
n/a
85
2116
8000
as w
ell a
s 1
labo
rato
ry te
chni
cian
(80
$/ho
ur).
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
To
tal 1
($)
2452
00
Tes
tin
gT
ask
req
uir
emen
tT
esti
ng
To
tal (
$)A
ssu
mp
tio
ns/
Bas
es (
Bas
ed o
n m
etal
lic
IHX
A (
see
adju
stm
ent
fact
or)
).
Sam
ple
s [1
]P
rep
(M
ach
inin
g)
[2]
Tes
t co
st/s
amp
leT
esti
ng
Co
sts
E
q. s
etu
p
Po
st t
est
sam
ple
pre
pP
ost
tes
t an
alys
isR
epo
rtin
gM
etal
log
rap
hy
(po
st w
eld
ing
/bo
nd
ing
, pre
-te
stin
g)
[3]
Cut
ting,
pol
ishi
ng s
ampl
en/
an/
a64
00
n/a
n/a
n/a
0T
akin
g in
to a
ccou
nt th
at la
bora
tory
tech
nici
an w
ill n
eed
8 ho
urs
for
sam
ple
prep
arat
ion
at $
80/h
our.
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
Obs
erva
tion
of m
etal
lurg
yn/
an/
a40
00
n/a
n/a
500
0In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eerin
g in
put a
t $20
0/ho
ur.
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
Che
mis
try
prof
ile in
join
tsn/
an/
a40
00
n/a
n/a
500
0In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eerin
g in
put a
t $20
0/ho
ur.
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
Th
erm
al P
hys
ical
Mec
han
ical
pro
per
ties
of
All
oy
800H
an
d W
/BR
/DB
join
ts
Ela
stic
pro
pert
ies
[4]
624
0035
021
00n/
an/
an/
a50
050
00$3
50-0
0 pe
r sp
ecim
en a
t 950
°C (
+- 3
0°C
). B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
acto
r)
Ten
sile
Pro
pert
ies
[5]
1560
0035
052
50n/
an/
an/
a50
011
750
$350
-00
per
spec
imen
at 9
50°C
(+-
30°
C).
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
Fat
igue
Str
engt
h (L
CF
)45
1800
072
032
400
6600
0n/
an/
a10
0011
7400
Fat
igue
str
engt
h LC
F to
100
0°C
- $
720-
00 u
p to
80
000
cycl
es +
$20-
00/h
our
ther
e af
ter
per
spec
imen
at 9
50°C
(+-
30°
C).
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
Fat
igue
str
engt
h (H
CF
)45
1800
080
036
000
6600
0n/
an/
a10
0012
1000
Fat
igue
str
engt
h H
CF
to 1
000°
C -
$80
0-00
up
to 1
000
000
cycl
es p
er
spec
imen
at 9
50°C
(+-
30°
C).
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
Cre
ep s
tren
gth
4819
200
3500
1680
00n/
an/
an/
a50
018
7700
Cre
ep s
tren
gth
to 1
000°
C fo
r 10
,000
h -
$35
00-0
0 pe
r sp
ecim
en.
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
Fra
ctur
e to
ughn
ess:
CT
OD
936
0010
0090
00n/
an/
an/
a50
013
100
Fra
ctur
e to
ughn
ess:
CT
OD
- $
1000
-00
at 6
50°C
per
spe
cim
en.
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
Fra
ctur
e to
ughn
ess:
Kc
936
0056
050
40n/
an/
an/
a50
091
40F
ract
ure
toug
hnes
s: K
c -
$560
-00
at 6
50°C
per
spe
cim
en.
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
The
rmal
con
duct
ivity
624
0010
060
0n/
an/
an/
a50
035
00T
herm
al c
ondu
ctiv
ity to
100
0°C
: - $
95-0
0 pe
r sp
ecim
en.
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
Met
allo
gra
ph
y/S
EM
(p
ost
-wel
din
g, p
ost
-te
stin
g)
[6]
Cut
ting,
pol
ishi
ng, e
tchi
ng s
ampl
e18
3n/
a64
011
7120
n/a
n/a
n/a
1171
20T
akin
g in
to a
ccou
nt th
at la
bora
tory
tech
nici
an w
ill n
eed
8 ho
urs
for
sam
ple
prep
arat
ion
at $
80/h
our.
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
Obs
erva
tion
of s
ampl
e/m
etal
lurg
y18
3n/
a40
073
200
n/a
n/a
500
7320
0In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eerin
g in
put a
t $20
0/ho
ur.
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
To
tal 2
($)
7320
044
8710
1320
000
065
0065
8910
Mat
eria
lsM
ater
ials
req
uir
emen
tT
ota
l ($)
Ass
um
pti
on
s/B
ases
Sam
ple
sM
at.c
ost
/sam
ple
Mat
eria
l co
st
All
oy
800H
sam
ple
s [7
]n/
an/
a9,
552
9,55
2C
ostin
g ba
sed
on m
ater
ial p
rice
of $
35/k
g. T
his
does
not
allo
w fo
r
the
cost
/dev
elop
men
t for
the
wel
d/br
aze
allo
y. O
ther
asp
ects
bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
To
tal 3
($)
9552
.375
Oth
erA
dd
itio
nal
req
uir
emen
tsT
ota
l ($)
Ass
um
pti
on
s/B
ases
Un
it p
rice
($)
Qu
anti
ty
Cap
ital
co
st -
fu
rnac
es f
or
ther
mal
ag
ing
3000
390
00F
urna
ce w
ith r
equi
red
capa
bilit
y si
zed
at 1
80m
m x
180
mm
x 2
50m
m.
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
Co
nti
ng
enci
es (
po
wer
co
nsu
mp
tio
n,
elem
ent
rep
lace
men
t)90
01
900
Fur
nace
con
tinge
ncie
s m
ake
up 1
0% o
f tot
al c
apita
l cos
t for
furn
aces
. B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
acto
r)
Hel
ium
gas
fo
r re
gu
lati
ng
en
viro
nm
ent
120
156
18,7
2015
6 50
kg x
He
cylin
ders
to b
e ut
ilize
d. O
ne c
ylin
der
a w
eek
for
each
furn
ace
(52
wee
ks in
tota
l). H
e ga
s co
st in
clus
ive
of im
purit
y ga
ses.
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
Sam
pli
ng
gas
an
alys
es15
052
7,80
0S
ampl
ing
of fu
rnac
e te
stin
g en
viro
nmen
t don
e on
ce a
wee
k by
ext
erna
l
inst
itutio
n. C
olle
ctiv
e sa
mpl
ing
from
3 fu
rnac
es a
dd u
p to
$15
0/w
eek.
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
To
tal 4
($)
3642
0
To
tal (
$)95
0082
.38
10%
co
nti
ng
ency
($)
9500
8.23
8
Gra
nd
to
tal (
$)10
4509
1C
ost
wil
l be
low
er c
om
par
ed t
o s
imil
ar m
etal
lic
IHX
A s
pec
ific
atio
n d
ue
to t
he
exis
tin
g
IHX
A t
o IH
X B
rat
io a
dju
stm
ent
10A
llo
y 80
0H d
atab
ase
that
can
be
ado
pte
d
Eq
uiv
alen
t co
sts
for
IHX
B s
pec
ific
atio
n10
4509
[1] S
ee p
refe
rred
num
ber
of s
ampl
es to
be
used
in 's
ampl
e' s
heet
[2] B
asis
for
prep
arat
ion
cost
s -
$400
/sam
ple
[3] A
ssum
ing
that
all
sam
ples
to b
e ch
ecke
d fo
r jo
int c
onsi
sten
cy a
fter
join
ing
[4] D
eter
min
atio
n by
way
of m
echa
nica
l tes
ting
not a
dvis
ed. D
eter
min
atio
n sh
ould
be
base
d on
nat
ural
vib
ratio
nal m
etho
ds
[5] T
ensi
le p
rope
rtie
s (y
ield
str
engt
h, te
nsile
str
engt
h, e
long
atio
n, a
nd R
A)
[6] O
ptic
al/S
EM
wor
k to
be
cond
ucte
d fo
r te
nsile
, fat
igue
(H
CF
, LC
F),
cre
ep
[7] R
efer
to 'm
ater
ial c
ost'
shee
t for
mat
eria
l cos
ting
aspe
cts
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP-
CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17:
Inte
grat
ed S
ched
ule
and
Cos
t Est
imat
e
Cri
t S
SC
Sp
ecif
icat
ion
nu
mb
erS
pec
ific
atio
nD
escr
ipti
on
Co
mm
ents
Effe
cts
ofD
emon
stra
te t
hat
Allo
y 80
0H jo
ints
can
be
IHX
BW
EC
-TS
-IH
XB
-005
envi
ronm
ent
onut
ilize
d in
NG
NP
env
ironm
ent
(tem
pera
ture
&E
xist
ing
Allo
y 80
0H d
atab
ase
can
be
uti
lized
Allo
y 80
0H jo
ints
med
ium
) fo
r lo
ng p
erio
ds w
ithou
t de
grad
atio
nN
/A
Res
ourc
es Res
ou
rce
req
uir
emen
tA
ctio
n t
o b
e p
erfo
rmed
by
Tar
iff
($)
Du
rati
on
To
tal (
$)A
ssu
mp
tio
ns/
Bas
es (
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fa
cto
r)).
Ho
ur
Act
ion
Ho
urs
Day
sW
eeks
Mo
nth
sY
ears
Wel
din
g o
f jo
ints
(W
/BR
/DB
)C
oded
wel
der
100
n/a
85
4618
4000
549
sam
ples
to
be jo
ined
. A
ssum
e 12
sam
ples
/wee
k. B
ased
on
met
allic
IH
X A
(se
e ad
just
men
t fa
ctor
).
Ove
rsee
& M
anag
e: T
her
mal
exp
osu
re o
f sa
mp
les
- 10
,000
hLa
bora
tory
Tec
hnic
ian
100
n/a
100
1000
0T
herm
al e
xpos
ure
mon
itore
d by
lab
tech
nici
an e
very
100
h (1
00 in
terv
als)
. B
ased
on
met
allic
IH
X A
(se
e ad
just
men
t fa
cC
on
du
ctin
g t
esti
ng
: A
lloy/
Join
t p
rop
erti
esLa
bora
tory
Tec
hnic
ian
80n/
a8
561
1952
00T
estin
g w
ill r
equi
re r
esou
rces
in t
he fo
rm o
f 1 e
ngin
eer
($20
0/ho
ur)
Ove
rsee
& M
anag
eE
ngin
eer
200
n/a
85
6148
8000
as w
ell a
s 1
labo
rato
ry t
echn
icia
n (8
0$/h
our)
. B
ased
on
met
allic
IH
X A
(se
e ad
just
men
t fa
ctor
).
To
tal 1
($)
8772
00
Tes
ting
Tas
k re
qu
irem
ent
Tes
tin
gT
ota
l ($)
Ass
um
pti
on
s/B
ases
(B
ased
on
met
allic
IHX
A (
see
adju
stm
ent
fact
or)
.)
Sam
ple
s [1
]P
rep
(M
ach
inin
g)
[2]
Tes
t co
st/s
amp
leT
esti
ng
Co
sts
E
q. s
etu
p
Po
st t
est
sam
ple
pre
pP
ost
tes
t an
alys
isR
epo
rtin
gM
etal
log
rap
hy
(po
st w
eld
ing
/bo
nd
ing
, pre
-te
stin
g)
[3]
Cut
ting,
pol
ishi
ng s
ampl
e54
9n/
a64
035
1360
n/a
n/a
n/a
3513
60T
akin
g in
to a
ccou
nt t
hat
labo
rato
ry t
echn
icia
n w
ill n
eed
8 ho
urs
for
sam
ple
prep
arat
ion
at $
80/h
our.
Bas
ed o
n m
etal
lic I
HX
A (
see
adju
stm
ent
fact
or).
Obs
erva
tion
of m
etal
lurg
y54
9n/
a40
021
9600
n/a
n/a
500
2196
00In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $2
00/h
our
and
2) S
cien
tist/
Eng
inee
ring
inpu
t at
$20
0/ho
ur.
Bas
ed o
n m
etal
lic I
HX
A (
see
adju
stm
ent
fact
or).
Che
mis
try
prof
ile in
join
ts54
9n/
a40
021
9600
n/a
n/a
500
2196
00In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $2
00/h
our
and
2) S
cien
tist/
Eng
inee
ring
inpu
t at
$20
0/ho
ur.
Bas
ed o
n m
etal
lic I
HX
A (
see
adju
stm
ent
fact
or).
T
her
mal
Ph
ysic
al M
ech
anic
al p
rop
erti
es
of
Allo
y 80
0H a
nd
W/B
R/D
B jo
ints
Ela
stic
pro
pert
ies
[4]
1872
0035
063
00n/
an/
an/
a50
014
000
$350
-00
per
spec
imen
at
950°
C (
+-
30°C
). B
ased
on
met
allic
IH
X A
(se
e ad
just
men
t fa
ctor
).
Ten
sile
Pro
pert
ies
[5]
4518
000
350
1575
0n/
an/
an/
a50
034
250
$350
-00
per
spec
imen
at
950°
C (
+-
30°C
). B
ased
on
met
allic
IH
X A
(se
e ad
just
men
t fa
ctor
).
Fat
igue
Str
engt
h (L
CF
)13
554
000
720
9720
066
000
n/a
n/a
1000
2182
00F
atig
ue s
tren
gth
LCF
to
1000
°C -
$72
0-00
up
to 8
0 00
0 cy
cles
+
$20-
00/h
our
ther
e af
ter
per
spec
imen
at
950°
C (
+-
30°C
). B
ased
on
met
allic
IH
X A
(se
e ad
just
men
t fa
ctor
).
Fat
igue
str
engt
h (H
CF
)13
554
000
800
1080
0066
000
n/a
n/a
1000
2290
00F
atig
ue s
tren
gth
HC
F t
o 10
00°C
- $
800-
00 u
p to
100
0 00
0 cy
cles
per
spec
imen
at
950°
C (
+-
30°C
). B
ased
on
met
allic
IH
X A
(se
e ad
just
men
t fa
ctor
).
Cre
ep s
tren
gth
144
5760
035
0050
4000
n/a
n/a
n/a
500
5621
00C
reep
str
engt
h to
100
0°C
for
10,0
00 h
- $
3500
-00
per
spec
imen
. B
ased
on
met
allic
IH
X A
(se
e ad
just
men
t fa
ctor
).
Fra
ctur
e to
ughn
ess:
CT
OD
2710
800
1000
2700
0n/
an/
an/
a50
038
300
Fra
ctur
e to
ughn
ess:
CT
OD
- $
1000
-00
at 6
50°C
per
spe
cim
en.
Bas
ed o
n m
etal
lic I
HX
A (
see
adju
stm
ent
fact
or).
Fra
ctur
e to
ughn
ess:
Kc
2710
800
560
1512
0n/
an/
an/
a50
026
420
Fra
ctur
e to
ughn
ess:
Kc
- $5
60-0
0 at
650
°C p
er s
peci
men
. B
ased
on
met
allic
IH
X A
(se
e ad
just
men
t fa
ctor
).
The
rmal
con
duct
ivity
1872
0010
018
00n/
an/
an/
a50
095
00T
herm
al c
ondu
ctiv
ity t
o 10
00°C
: -
$95-
00 p
er s
peci
men
. B
ased
on
met
allic
IH
X A
(se
e ad
just
men
t fa
ctor
).
Met
allo
gra
ph
y/S
EM
(p
ost
-wel
din
g, p
ost
-te
stin
g)
[6]
Cut
ting,
pol
ishi
ng,
etch
ing
sam
ple
459
n/a
640
2937
60n/
an/
an/
a29
3760
Tak
ing
into
acc
ount
tha
t la
bora
tory
tec
hnic
ian
will
nee
d 8
hour
s fo
r
sam
ple
prep
arat
ion
at $
80/h
our.
Bas
ed o
n m
etal
lic I
HX
A (
see
adju
stm
ent
fact
or).
Obs
erva
tion
of s
ampl
e/m
etal
lurg
y45
9n/
a40
018
3600
n/a
n/a
500
1836
00In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $2
00/h
our
and
2) S
cien
tist/
Eng
inee
ring
inpu
t at
$20
0/ho
ur.
Bas
ed o
n m
etal
lic I
HX
A (
see
adju
stm
ent
fact
or).
To
tal 2
($)
2196
0020
4309
013
2000
00
6500
2399
690
Mat
eria
lsM
ater
ials
req
uir
emen
tT
ota
l ($)
Ass
um
pti
on
s/B
ases
(B
ased
on
met
allic
IHX
A (
see
adju
stm
ent
fact
or)
.)
Sam
ple
sM
at.c
ost
/sam
ple
Mat
eria
l co
st
Allo
y 80
0H s
amp
les
[7]
n/a
n/a
28,6
5728
,657
Cos
ting
base
d on
mat
eria
l pric
e of
$35
/kg.
Thi
s do
es n
ot a
llow
for
the
cost
/dev
elop
men
t fo
r th
e w
eld/
braz
e al
loy.
Oth
er a
spec
ts b
ased
on
met
allic
IH
X A
(se
e ad
just
men
t fa
ctor
).
To
tal 3
($)
2865
7.12
5
Oth
erA
dd
itio
nal
req
uir
emen
tsT
ota
l ($)
Ass
um
pti
on
s/B
ases
(B
ased
on
met
allic
IHX
A (
see
adju
stm
ent
fact
or)
.)
Un
it p
rice
($)
Qu
anti
ty
Cap
ital
co
st -
fu
rnac
es f
or
ther
mal
ag
ing
3000
390
00F
urna
ce w
ith r
equi
red
capa
bilit
y si
zed
at 1
80m
m x
180
mm
x 2
50m
m.
Bas
ed o
n m
etal
lic I
HX
A (
see
adju
stm
ent
fact
or).
Co
nti
ng
enci
es (
po
wer
co
nsu
mp
tio
n,
elem
ent
rep
lace
men
t)90
01
900
Fur
nace
con
tinge
ncie
s m
ake
up 1
0% o
f tot
al c
apita
l cos
t fo
r fu
rnac
es.
Bas
ed o
n m
etal
lic I
HX
A (
see
adju
stm
ent
fact
or)
Hel
ium
gas
fo
r re
gu
lati
ng
en
viro
nm
ent
120
156
18,7
2015
6 x
50kg
He
cylin
ders
to
be u
tiliz
ed.
One
cyl
inde
r a
wee
k fo
r ea
ch
furn
ace.
He
gas
cost
incl
usiv
e of
impu
rity
gase
s. B
ased
on
met
allic
IH
X A
(se
e ad
just
men
t fa
ctor
).
Sam
plin
g g
as a
nal
yses
150
527,
800
Sam
plin
g of
furn
ace
test
ing
envi
ronm
ent
done
onc
e a
wee
k by
ext
erna
l
inst
itutio
n. C
olle
ctiv
e sa
mpl
ing
from
3 fu
rnac
es a
dd u
p to
$15
0/w
eek.
Bas
ed o
n m
etal
lic I
HX
A (
see
adju
stm
ent
fact
or).
To
tal 4
($)
3642
0
Tot
al (
$)33
4196
7.1
10%
con
ting
ency
($)
3341
96.7
1
Gra
nd
tot
al (
$)36
7616
4
IHX
A t
o IH
X B
rat
io a
dju
stm
ent
10E
xist
ing
Allo
y 80
0H d
atab
ase
can
be
uti
lized
Eq
uiv
alen
t co
sts
for
IHX
B s
pec
ifica
tion
3676
16
[1]
See
pre
ferr
ed n
umbe
r of
sam
ples
to
be u
sed
in 's
ampl
e' s
heet
[2]
Bas
is fo
r pr
epar
atio
n co
sts
- $4
00/s
ampl
e
[3]
Ass
umin
g th
at a
ll sa
mpl
es t
o be
che
cked
for
join
t co
nsis
tenc
y af
ter
join
ing
[4]
Det
erm
inat
ion
by w
ay o
f mec
hani
cal t
estin
g no
t ad
vise
d. D
eter
min
atio
n sh
ould
be
base
d on
nat
ural
vib
ratio
nal m
etho
ds
[5]
Ten
sile
pro
pert
ies
(yie
ld s
tren
gth,
ten
sile
str
engt
h, e
long
atio
n, a
nd R
A)
[6]
Opt
ical
/SE
M w
ork
to b
e co
nduc
ted
for
tens
ile,
fatig
ue (
HC
F,
LCF
), c
reep
[7]
Ref
er t
o 'm
ater
ial c
ost'
shee
t fo
r m
ater
ial c
ostin
g as
pect
s
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
Cri
t SS
CS
pec
ifica
tion
nu
mb
erS
pec
ifica
tion
Des
crip
tion
Co
mm
ents
Effe
cts
of g
rain
siz
eD
emon
stra
te th
at s
light
cha
nges
in g
rain
siz
e as
IHX
BW
EC
-TS
-IHX
B-0
06an
d se
ctio
n th
ickn
ess
wel
l as
the
sect
ion
thic
knes
s of
Allo
y 80
0H h
as li
ttle
Wo
rk s
tate
d is
eq
uiv
alen
t to
sim
ilar
wo
rk s
tate
d in
met
allic
IHX
A
on A
lloy
800H
effe
ct in
ove
rall
prop
ertie
s of
mat
eria
lN
/A
Res
ou
rces R
eso
urc
e re
qu
irem
ent
Act
ion
to b
e p
erfo
rmed
by
Tar
iff ($
)D
ura
tion
To
tal (
$)A
ssu
mp
tion
s/B
ases
( B
ased
on
met
allic
IHX
A (s
ee a
dju
stm
ent f
acto
r)).
Ho
ur
Act
ion
Ho
urs
Day
sW
eeks
Mo
nth
sY
ears
Co
nd
uct
ing
test
ing
: A
lloy
800H
pro
per
ties
Labo
rato
ry T
echn
icia
n80
n/a
85
1651
200
Tes
ting
will
requ
ire r
esou
rces
in th
e fo
rm o
f 1 e
ngin
eer
($20
0/ho
ur)
Ove
rsee
& M
anag
eE
ngin
eer
200
n/a
85
1612
8000
as w
ell a
s 1
labo
rato
ry te
chni
cian
(80
$/ho
ur).
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
.
To
tal 1
($)
1792
00
Tes
tin
gT
ask
req
uir
emen
tT
estin
gT
ota
l ($)
Ass
um
ptio
ns/
Bas
es (
Bas
ed o
n m
etal
lic IH
X A
(see
ad
just
men
t fac
tor)
).
Sam
ple
s [1
]P
rep
(Mac
hin
ing
) [2]
Tes
t co
st/s
amp
leT
estin
g C
ost
s
Eq
. set
up
P
ost
test
sam
ple
pre
pP
ost
test
an
alys
isR
epo
rtin
g
Th
erm
al P
hys
ical
Mec
han
ical
pro
per
ties
of A
lloy
800H
Fat
igue
Str
engt
h (L
CF
)45
1800
072
032
400
6600
0n/
an/
a10
0011
7400
Fat
igue
str
engt
h LC
F to
100
0°C
- $
720-
00 u
p to
80
000
cycl
es +
$20-
00/h
our
ther
e af
ter
per
spec
imen
at 9
50°C
(+
- 30
°C).
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
.
Fat
igue
str
engt
h (H
CF
)45
1800
080
036
000
6600
0n/
an/
a10
0012
1000
Fat
igue
str
engt
h H
CF
to 1
000°
C -
$80
0-00
up
to 1
000
000
cycl
es p
er
spec
imen
at 9
50°C
(+
- 30
°C).
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
.
Cre
ep s
tren
gth
4819
200
3500
1680
00n/
an/
an/
a50
018
7700
Cre
e p s
tren
gth
to 1
000°
C fo
r 10
,000
h -
$35
00-0
0 pe
r sp
ecim
en. B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
acto
r
Met
allo
gra
ph
y/S
EM
(po
st-t
estin
g) [
3]
Cut
ting,
pol
ishi
ng, e
tchi
ng s
ampl
e13
864
088
320
n/a
n/a
n/a
8832
0T
akin
g in
to a
ccou
nt th
at la
bora
tory
tech
nici
an w
ill ne
ed 8
hou
rs fo
r
sam
ple
prep
arat
ion
at $
80/h
our.
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
.
Obs
erva
tion
of s
ampl
e/m
etal
lurg
y13
840
055
200
n/a
n/a
500
5520
0In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eerin
g in
put a
t $20
0/ho
ur. B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
act
To
tal 2
($)
5520
037
9920
1320
000
030
0056
9620
Mat
eria
lsM
ater
ials
req
uir
emen
tT
ota
l ($)
Ass
um
ptio
ns/
Bas
es (
Bas
ed o
n m
etal
lic IH
X A
(see
ad
just
men
t fac
tor)
).
Sam
ple
sM
at.c
ost
/sam
ple
Mat
eria
l co
st
Allo
y 80
0H s
amp
les
[4]
n/a
n/a
7,95
97,
959
Cos
ting
base
d on
mat
eria
l pric
e of
$35
/kg.
Num
ber
of s
ampl
es o
nly
rele
vant
to fa
tigue
test
ing
and
cree
p te
stin
g. B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
acto
r).
To
tal 3
($)
7959
To
tal (
$)75
6779
10%
co
nti
ng
ency
($)
7567
7.9
Gra
nd
to
tal (
$)83
2456
.9S
ame
estim
ates
for
IHX
B r
elat
ing
to IH
X A
IHX
A t
o IH
X B
rat
io a
dju
stm
ent
1W
ork
sta
ted
is e
qu
ival
ent t
o s
imila
r w
ork
sta
ted
in m
etal
lic IH
X A
Eq
uiv
alen
t co
sts
for
IHX
B s
pec
ific
atio
n83
2456
.9
[1] S
ee p
refe
rred
num
ber
of s
ampl
es to
be
used
in 's
ampl
e' s
heet
[2] B
asis
for
prep
arat
ion
cost
s -
$400
/sam
ple
[3] O
ptic
al/S
EM
wor
k to
be
cond
ucte
d fo
r fa
tigue
and
cre
ep s
ampl
es
[4] R
efer
to 'm
ater
ial c
ost'
shee
t for
mat
eria
l cos
ting
aspe
cts
NG
NP
-CTF
MTE
CH
-TD
RM
-017
-Rev
0 1
2/03
/200
8
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17:
Inte
grat
ed S
ched
ule
and
Cos
t Est
imat
e
Cri
t S
SC
Sp
ecif
icat
ion
nu
mb
erS
pec
ific
atio
nD
escr
ipti
on
Co
mm
ents
Cor
rosi
onD
emon
stra
te s
atis
fact
ory
corr
osio
n al
low
ance
s
IHX
BW
EC
-TS
-IH
XB
-007
allo
wan
ces
for
for
Allo
y 80
0H a
nd w
elde
d/bo
nded
sec
tions
Wo
rk s
tate
d is
eq
uiv
alen
t to
th
at s
tate
d in
met
allic
IHX
A
Allo
y 80
0HN
/A
Res
ourc
es Res
ou
rce
req
uir
emen
tA
ctio
n t
o b
e p
erfo
rmed
by
Tar
iff
($)
Du
rati
on
To
tal (
$)A
ssu
mp
tio
ns/
Bas
es (
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fa
cto
r)).
Ho
ur
Act
ion
Ho
urs
Day
sW
eeks
Mo
nth
sY
ears
Wel
din
g o
f jo
ints
(W
/BR
/DB
)C
oded
wel
der
100
n/a
85
1248
000
135
sam
ples
to b
e jo
ined
. Ass
ume
12 s
ampl
es/w
eek.
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
.
Ove
rsee
& M
anag
e: T
her
mal
exp
osu
re o
f sa
mp
les
- 10
,000
hLa
bora
tory
Tec
hnic
ian
100
n/a
100
1000
0T
herm
al e
xpos
ure
mon
itore
d by
lab
tech
nici
an e
very
100
h (1
00 in
terv
als)
. Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
.
Ove
rsee
& M
anag
eE
ngin
eer
200
n/a
85
2016
0000
To
tal 1
($)
2180
00
Tes
ting
Tas
k re
qu
irem
ent
Tes
tin
gT
ota
l ($)
Ass
um
pti
on
s/B
ases
(B
ased
on
met
allic
IHX
A (
see
adju
stm
ent
fact
or)
).
Sam
ple
sP
rep
(M
ach
inin
g)
[1]
Tes
t co
st/s
amp
leT
esti
ng
Co
sts
E
q. s
etu
p
Po
st t
est
sam
ple
pre
pP
ost
tes
t an
alys
isR
epo
rtin
g
Met
allo
gra
ph
y (p
ost
wel
din
g/b
on
din
g)
[2]
Cut
ting,
pol
ishi
ng s
ampl
e13
5n/
a64
086
400
n/a
n/a
n/a
8640
0T
akin
g in
to a
ccou
nt th
at la
bora
tory
tech
nici
an w
ill n
eed
8 ho
urs
for
sam
ple
prep
arat
ion
at $
80/h
our.
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
.
Obs
erva
tion
of m
etal
lurg
y13
5n/
a40
054
000
n/a
n/a
500
5400
0In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eeri
ng in
put a
t $20
0/ho
ur. B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
acto
r).
Che
mis
try
prof
ile in
join
ts13
5n/
a40
054
000
n/a
n/a
500
5400
0In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eeri
ng in
put a
t $20
0/ho
ur. B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
acto
r).
Th
erm
al P
hys
ical
Mec
han
ical
pro
per
ties
of
Allo
y 80
0H a
nd
W/B
R/D
B jo
ints
n/a
n/a
n/a
n/a
n/a
n/a
n/a
n/a
n/a
Met
allo
gra
ph
y/S
EM
(p
ost
-tes
tin
g)
Cut
ting,
pol
ishi
ng, e
tchi
ng s
ampl
e18
0n/
a64
011
5200
n/a
n/a
n/a
1152
00T
akin
g in
to a
ccou
nt th
at la
bora
tory
tech
nici
an w
ill n
eed
8 ho
urs
for
sam
ple
prep
arat
ion
at $
80/h
our.
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
.
Obs
erva
tion
of s
ampl
e/m
etal
lurg
y18
0n/
a40
072
000
n/a
n/a
500
7200
0In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eeri
ng in
put a
t $20
0/ho
ur. B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
acto
r).
Dep
th o
f int
erna
l oxi
datio
n18
0n/
a40
072
000
500
7250
0In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eeri
ng in
put a
t $20
0/ho
ur. B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
acto
r).
Dep
th o
f dep
letio
n of
allo
y el
emen
ts (
Cr)
18
0n/
a40
072
000
500
7250
0In
clus
ive
of 1
) A
naly
ses
cost
(in
clus
ive
of o
pera
tor
and
mac
hine
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eeri
ng in
put a
t $20
0/ho
ur. B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
acto
r).
Dep
th a
ffect
ed b
ycar
buri
zatio
n/
deca
rbur
izat
ion
180
n/a
400
7200
050
072
500
Incl
usiv
e of
1)
Ana
lyse
s co
st (
incl
usiv
e of
ope
rato
r an
d m
achi
ne
cost
s) a
t $20
0/ho
ur a
nd 2
) S
cien
tist/E
ngin
eeri
ng in
put a
t $20
0/ho
ur. B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
acto
r).
To
tal 2
($)
059
7600
00
030
0059
9100
Mat
eria
lsM
ater
ials
req
uir
emen
tT
ota
l ($)
Ass
um
pti
on
s/B
ases
(B
ased
on
met
allic
IHX
A (
see
adju
stm
ent
fact
or)
).
Sam
ple
sM
at.c
ost
/sam
ple
Mat
eria
l co
st
Allo
y 80
0H s
amp
les
[3]
n/a
n/a
10,6
0510
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Cos
ting
base
d on
mat
eria
l pri
ce o
f $35
/kg.
Thi
s do
es n
ot a
llow
for
the
cost
/dev
elop
men
t for
the
wel
d/br
aze
allo
y. B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
acto
r).
To
tal 3
($)
1060
5
Oth
erA
dd
itio
nal
req
uir
emen
tsT
ota
l ($)
Ass
um
pti
on
s/B
ases
(B
ased
on
met
allic
IHX
A (
see
adju
stm
ent
fact
or)
).
Un
it p
rice
($)
Qu
anti
ty
Cap
ital
co
st -
fu
rnac
es f
or
ther
mal
ag
ing
3000
390
00F
urna
ce w
ith r
equi
red
capa
bilit
y si
zed
at 1
80m
m x
180
mm
x 2
50m
m. B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
acto
r).
Co
nti
ng
enci
es (
po
wer
co
nsu
mp
tio
n,
elem
ent
rep
lace
men
t)90
01
900
Fur
nace
con
tinge
ncie
s m
ake
up 1
0% o
f tot
al c
apita
l cos
t for
furn
aces
. Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
.
Hel
ium
gas
fo
r re
gu
lati
ng
en
viro
nm
ent
120
156
18,7
2015
6 x
50kg
He
cylin
ders
to b
e ut
ilize
d. O
ne c
ylin
der
a w
eek
for
each
furn
ace.
He
gas
cost
incl
usiv
e of
impu
rity
gas
es. B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
acto
r).
Sam
plin
g g
as a
nal
yses
150
527,
800
Sam
plin
g of
furn
ace
test
ing
envi
ronm
ent d
one
once
a w
eek
by e
xter
nal
inst
itutio
n. C
olle
ctiv
e sa
mpl
ing
from
3 fu
rnac
es a
dd u
p to
$15
0/w
eek.
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fac
tor)
.
To
tal 4
($)
3642
0
Tot
al (
$) (
Pri
mar
y si
de H
e ef
fect
s)86
4125
Sec
onda
ry s
ide
He
effe
cts
($)
8641
25
Tot
al (
Pri
mar
y an
d se
cond
ary
effe
cts)
($)
1728
250
10%
con
ting
ency
($)
1728
25
Gra
nd t
otal
($)
1901
075
IHX
A t
o IH
X B
rat
io a
djus
tmen
t1
Wo
rk s
tate
d is
eq
uiv
alen
t to
th
at s
tate
d in
met
allic
IHX
A
Equ
ival
ent
cost
s fo
r IH
X B
spe
cifi
cati
on19
0107
5
[1] B
asis
for
prep
arat
ion
cost
s -
$400
/sam
ple
[2] A
ssum
ing
that
all
join
ed s
ampl
es to
be
chec
ked
for
join
t con
sist
ency
afte
r jo
inin
g
[3] R
efer
to 'm
ater
ial c
ost'
shee
t for
mat
eria
l cos
ting
aspe
cts
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
-Rev
0 1
2/03
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8
NG
NP-
CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17:
Int
egra
ted
Sche
dule
and
Cos
t Est
imat
e
Cri
t S
SC
Sp
ecif
icat
ion
nu
mb
erS
pec
ific
atio
nD
escr
ipti
on
Co
mm
ents
IHX
BW
EC
-TS
-IH
XB
-008
The
rmal
/Flu
id
mod
ellin
g m
etho
ds
for
IHX
B
Dev
elop
ther
mal
mod
els
for
IHX
BN
/A
Tas
ks r
equ
ired
Act
ion
to
be
per
form
ed b
yT
arif
f ($
)T
ime
nee
ded
To
tal (
$)A
ssu
mp
tio
ns/
Bas
es (
Bas
ed o
n m
etal
lic IH
X A
(se
e ad
just
men
t fa
cto
r))
Ho
ur
Yea
rH
ou
rsD
ays
Wee
ksM
on
ths
Yea
rM
odel
gen
erat
ion
givi
ng r
esul
ts f
or
mec
hani
cal,
phys
ical
and
ther
mal
pe
rfor
man
ce p
redi
ctio
n
Gro
up o
f th
erm
al f
luid
/mod
elin
g sp
ecia
lists
42,5
003
1275
001)
Est
mat
ion
mad
e by
M-T
ech
- D
urat
ion
and
cost
is g
reat
ly
depe
ndan
t on
the
data
sup
plie
d by
sup
plie
rs (
tran
sfer
coe
ffic
ient
s).
Dur
atio
n of
3 y
ears
for
wor
k. B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
acto
r)
To
tal (
$)12
7500
10%
co
nti
ng
ency
($)
1275
0
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nd
to
tal (
$)14
0250
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
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0 1
2/03
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8
NG
NP
-CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17: I
nteg
rate
d Sc
hedu
le a
nd C
ost E
stim
ate
Cri
t S
SC
Sp
ecif
icat
ion
nu
mb
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pec
ific
atio
nD
escr
ipti
on
Co
mm
ents
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BW
EC
-TS
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XB
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Met
hods
for
stre
ss-
stra
in m
odel
ling
of
IHX
B
Dev
elop
str
uctu
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odel
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met
hods
for
pred
ictiv
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erat
ion
for
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BN
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Tas
ks r
equ
ired
Act
ion
to
be
per
form
ed b
yT
arif
f ($
)T
ime
nee
ded
To
tal (
$)A
ssu
mp
tio
ns/
Bas
es (
Bas
ed o
n m
etal
lic IH
X A
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just
men
t fa
cto
r)).
Ho
ur
Yea
rH
ou
rsD
ays
Wee
ksM
on
ths
Yea
rS
truc
tura
l mod
el g
ener
atio
n gi
ving
res
ults
fo
r pr
edic
tive
oper
atio
n fo
r IH
X B
Gro
up o
f mod
elin
g sp
ecia
lists
42,5
003
1275
001)
Est
mat
ion
mad
e by
M-T
ech
Dur
atio
n of
3 y
ears
for
wor
k. B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
acto
r)
To
tal (
$)12
7500
10%
co
nti
ng
ency
($)
1275
0
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nd
to
tal (
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0250
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NP
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F M
TE
CH
-TD
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-017
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0 1
2/03
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NP-
CT
F M
TE
CH
-TD
RM
-017
NG
NP
Tec
hnol
ogy
Dev
elop
men
t Roa
d M
appi
ng R
epor
t Sec
tion
17:
Int
egra
ted
Sche
dule
and
Cos
t Est
imat
e
Cri
t S
SC
Sp
ecif
icat
ion
nu
mb
erS
pec
ific
atio
nD
escr
ipti
on
Co
mm
ents
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BW
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-TS
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XB
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Crit
eria
for
st
ruct
ural
inte
grity
Est
ablis
h cr
iteria
for
str
uctu
ral
inte
grity
of
CH
E's
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Tas
ks r
equ
ired
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per
form
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yT
arif
f ($
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ime
nee
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tal (
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ssu
mp
tio
ns/
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es (
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e ad
just
men
t fa
cto
r)).
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ur
Yea
rH
ou
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ays
Wee
ksM
on
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Yea
r
Str
uctu
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nteg
rity
mod
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HE
'sG
roup
of
mod
elin
g sp
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42,5
003
1275
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Est
mat
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mad
e by
M-T
ech
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urat
ion
and
cost
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reat
ly
depe
ndan
t on
the
data
sup
plie
d by
sup
plie
rs (
tran
sfer
coe
ffic
ient
s).
Dur
atio
n of
3 y
ears
for
wor
k. B
ased
on
met
allic
IHX
A (
see
adju
stm
ent f
acto
r)
To
tal (
$)12
7500
10%
co
nti
ng
ency
($)
1275
0
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nd
to
tal (
$)14
0250
NG
NP
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F M
TE
CH
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-017
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0 1
2/03
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NP-
CT
F M
TE
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-017
NG
NP
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hnol
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Dev
elop
men
t Roa
d M
appi
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17:
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dule
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t Est
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t S
SC
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mb
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pec
ific
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nD
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ipti
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mm
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form
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m
odel
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met
hods
fo
r IH
X B
Dev
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per
form
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mod
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ime
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ssu
mp
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Dur
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ears
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ased
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met
allic
IHX
A (
see
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stm
ent f
acto
r)
To
tal (
$)12
7500
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co
nti
ng
ency
($)
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pre
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um
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sam
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test
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Ass
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tal (
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NGNP-CTF MTECH-TDRM-017 NGNP Technology Development Road Mapping Report Section 17: Integrated Schedule and Cost Estimate
Additional notes on preferred number of testing samples - Alloy 617 / Alloy 800H
1) General- Samples representative of the three heats to be tested for all thermal, physical and mechanical tests
2) Elastic properties- At least 2 samples for each heat should be tested assuming the vibrational methods permit testing of a single specimen at multiple temperatures
3) Tensile properties- As a minimum, testing should be conducted on 15 samples (5 temperatures for each heat)- Noted testing does not include any duplicates
4) Fatigue tests- As a minimum, LCF testing should be conducted on 45 samples [3 heats x 5 temperatures x 3 strain ranges]- As a minimum, HCF testing should be conducted on 45 samples [3 heats x 5 temperatures x 3 cycle rates]
5) Creep strength- As a minimum, testing should be conducted on 48 samples [3 heats x 4 temperatures x 4 stress levels]
6) Fracture Toughness- As a minimum, testing for fracture toughness [CTOD] should be conducted on 9 samples [3 heats x 3 temperatures]- As a minimum, testing for fracture toughness [Kc] should be conducted on 9 samples [3 heats x 3 temperatures]
7) Thermal conductivity- As a minimum, testing should be conducted on 6 samples, 2 for each heat, as the complete temperature range can be covered with a single specimen
8) Coefficient of thermal expansion- As a minimum, testing should be conducted on 6 samples, 2 for each heat, as the complete temperature range can be covered with a single specimen
9) Stress rupture- As a minimum, stress rupture testing should be conducted on 48 samples [3 heats x 4 temperatures x 4 stress levels]
NGNP-CTF MTECH-TDRM-017-Rev0 12/03/2008
NGNP-CTF MTECH-TDRM-017 NGNP Technology Development Road Mapping Section 17 : Integrated Schedule and Cost Estimate
NGNP-CTF MTECH-TDRM-017_Rev0.doc 10/27/2008
88 of 89
17.2.6 Appendix B: References
NGNP-CTF MTECH-TDRM-017 NGNP Technology Development Road Mapping Section 17 : Integrated Schedule and Cost Estimate
NGNP-CTF MTECH-TDRM-017_Rev0.doc 10/27/2008
89 of 89
[17-1] “NGNP and Hydrogen Production Pre-conceptual Design Report - SECTION 18: NGNP PROJECT SCHEDULE “,NGNP-18-RPT-001, Rev 0, May 2007
[17-2] CTF Schedule per e-mail from BEA
[17-3] HPS.000.S01 (WBS Element Code Level) - Hydrogen Plant Alternatives Study
[17-4] NGNP-16-RPT-001 – NGNP and Hydrogen Production Pre-conceptual Design Report – Technology Development
[17-5] AACE International Recommended Practice No. 17R-97 TCM Framework; 7.3-Cost Estimating and Budgeting (as supplied by BEA)