sump pipe nps 12 sch 100

Table of Contents

Cover Sheet...........................................................................................................................................................2

Title Page..............................................................................................................................................................4

Warnings and Errors :....................................................................................................................................6

Input Echo :.........................................................................................................................................................7

XY Coordinate Calculations :.................................................................................................................18

Internal Pressure Calculations :........................................................................................................19

Element and Detail Weights :.................................................................................................................26

Nozzle Flange MAWP :....................................................................................................................................29

Center of Gravity Calculation :..........................................................................................................30

Nozzle Calcs. : N9A 2 in. LLC...............................................................................................................31

Nozzle Calcs. : DRAIN PIPE 1.................................................................................................................38



Nozzle Calcs. : N8A......................................................................................................................................53

Nozzle Calcs. : N8B......................................................................................................................................58

Nozzle Calcs. : N12 B(2 in.).................................................................................................................63

Nozzle Calcs. : N12 A(2 in.).................................................................................................................69

Nozzle Calcs. : N7A......................................................................................................................................75

Nozzle Calcs. : N7 B....................................................................................................................................80

Nozzle Calcs. : N6A......................................................................................................................................85

Nozzle Calcs. : N6B......................................................................................................................................90

Nozzle Calcs. : N9A 2 in. LLC...............................................................................................................95

Nozzle Schedule :.........................................................................................................................................102

Nozzle Summary :...........................................................................................................................................105

MDMT Summary :................................................................................................................................................107

Vessel Design Summary :...........................................................................................................................109

Cover Page

DESIGN CALCULATION

In Accordance with ASME Section VIII Division 1

ASME Code Version : 2013

Analysis Performed by : SPLM Licensed User

Job File : E:\FREE LANCING\DDFC\SSGC\VERTICAL SCUBBER\MODEL

Date of Analysis : Oct 2,2015 6:21pm

2

Cover Page

PV Elite 2015 SP2, May 2015

3

Title Page

Note: PV Elite performs all calculations internally in Imperial Units

to remain compliant with the ASME Code and any built in assumptions

in the ASME Code formulas. The finalized results are reflected to show

the users set of selected units.

5

PV Elite 2015 SP2 Licensee: SPLM Licensed UserFileName : Sump pipe NPS 12 SCH 100 Warnings and Errors : Step: 0 6:21pm Oct 2,2015

Class From To : Basic Element Checks.

==========================================================================

Class From To: Check of Additional Element Data

==========================================================================

There were no geometry errors or warnings.

PV Elite is a trademark of Intergraph CADWorx & Analysis Solutions, Inc. 2015

6

PV Elite 2015 SP2 Licensee: SPLM Licensed UserFileName : Sump pipe NPS 12 SCH 100 Input Echo : Step: 1 6:21pm Oct 2,2015

PV Elite Vessel Analysis Program: Input Data

Design Internal Pressure (for Hydrotest) 1440.0 psig

Design Internal Temperature 170 °F

Type of Hydrotest User Entered Pressure

Hydrotest Position Horizontal

Projection of Nozzle from Vessel Top 0.0000 mm

Projection of Nozzle from Vessel Bottom 0.0000 mm

Minimum Design Metal Temperature 32 °F

Type of Construction Welded

Special Service None

Degree of Radiography RT 1

Use Higher Longitudinal Stresses (Flag) Y

Select t for Internal Pressure (Flag) N

Select t for External Pressure (Flag) N

Select t for Axial Stress (Flag) N

Select Location for Stiff. Rings (Flag) N

Consider Vortex Shedding N

Perform a Corroded Hydrotest N

Is this a Heat Exchanger No

User Defined Hydro. Press. (Used if > 0) 2160.0 psig

User defined MAWP 1440.0 psig

User defined MAPnc 0.0000 psig

Load Case 1 NP+EW+WI+FW+BW

Load Case 2 NP+EW+EE+FS+BS

Load Case 3 NP+OW+WI+FW+BW

Load Case 4 NP+OW+EQ+FS+BS

Load Case 5 NP+HW+HI

Load Case 6 NP+HW+HE

Load Case 7 IP+OW+WI+FW+BW

Load Case 8 IP+OW+EQ+FS+BS

Load Case 9 EP+OW+WI+FW+BW

7


Load Case 10 EP+OW+EQ+FS+BS

Load Case 11 HP+HW+HI

Load Case 12 HP+HW+HE

Load Case 13 IP+WE+EW

Load Case 14 IP+WF+CW

Load Case 15 IP+VO+OW

Load Case 16 IP+VE+EW

Load Case 17 NP+VO+OW

Load Case 18 FS+BS+IP+OW

Load Case 19 FS+BS+EP+OW

Wind Design Code ASCE-7 93

Basic Wind Speed [V] 112.65 km/hr

Surface Roughness Category C: Open Terrain

Importance Factor 1.0

Type of Surface Moderately Smooth

Base Elevation 0.0000 mm

Percent Wind for Hydrotest 33.0

Using User defined Wind Press. Vs Elev. N

Damping Factor (Beta) for Wind (Ope) 0.0100

Damping Factor (Beta) for Wind (Empty) 0.0000

Damping Factor (Beta) for Wind (Filled) 0.0000

Seismic Design Code UBC 94

UBC Seismic Zone (1=1,2=2a,3=2b,4=3,5=4) 0.000

UBC Importance Factor 1.000

UBC Soil Type S1

UBC Horizontal Force Factor 3.000

UBC Percent Seismic for Hydrotest 0.000

Design Nozzle for Des. Press. + St. Head Y

Consider MAP New and Cold in Noz. Design N

Consider External Loads for Nozzle Des. Y

Use ASME VIII-1 Appendix 1-9 N

8


Material Database Year Current w/Addenda or Code Year

Configuration Directives:

Do not use Nozzle MDMT Interpretation VIII-1 01-37 No

Use Table G instead of exact equation for "A" Yes

Shell Head Joints are Tapered Yes

Compute "K" in corroded condition Yes

Use Code Case 2286 No

Use the MAWP to compute the MDMT Yes

Using Metric Material Databases, ASME II D No

Complete Listing of Vessel Elements and Details:

Element From Node 10

Element To Node 20

Element Type Elliptical

Description PIPE CAP 12 " SCH 80

Distance "FROM" to "TO" 88.000 mm

Inside Diameter 288.89 mm

Element Thickness 17.480 mm

Internal Corrosion Allowance 3.0000 mm

Nominal Thickness 17.480 mm

External Corrosion Allowance 0.0000 mm

Design Internal Pressure 1440.0 psig

Design Temperature Internal Pressure 170 °F

Design External Pressure 0.0000 psig

Design Temperature External Pressure 0 °F

Effective Diameter Multiplier 1.2

Material Name SA-234 WPB

Allowable Stress, Ambient 117.90 N/mm²

Allowable Stress, Operating 117.90 N/mm²

Allowable Stress, Hydrotest 217.19 N/mm²

Material Density 7750.4 kg/m³

P Number Thickness 30.988 mm

9


Yield Stress, Operating 224.64 N/mm²

UCS-66 Chart Curve Designation B

External Pressure Chart Name CS-2

UNS Number K03006

Product Form Smls. & wld. fittings

Efficiency, Longitudinal Seam 1.0

Efficiency, Circumferential Seam 1.0

Elliptical Head Factor 2.0


Detail Type Liquid

Detail ID Liquid 10

Dist. from "FROM" Node / Offset dist 0.0000 mm

Height/Length of Liquid 288.89 mm

Liquid Density 999.54 kg/m³


Detail Type Nozzle

Detail ID N9A 2" LLC


Nozzle Diameter 3.625 in.

Nozzle Schedule None

Nozzle Class None

Layout Angle 0.0

Blind Flange (Y/N) N

Weight of Nozzle ( Used if > 0 ) 0.01971 kN

Grade of Attached Flange None

Nozzle Matl SA-105

--------------------------------------------------------------------


Element To Node 30

Element Type Cylinder

Description SUMP PIPE 12" SCH 100

10













Material Name SA-106 B









UNS Number K03006

Product Form Smls. pipe




Detail Type Liquid

Detail ID WATER





Detail Type Nozzle

Detail ID DRAIN PIPE 1

11




Nozzle Schedule 160

Nozzle Class None

Layout Angle 0.0




Nozzle Matl SA-106 B


Detail Type Nozzle




Nozzle Schedule 160

Nozzle Class None

Layout Angle 0.0






Detail Type Nozzle




Nozzle Schedule 160

Nozzle Class None

Layout Angle 0.0





12



Detail Type Nozzle

Detail ID N8A




Nozzle Class None

Layout Angle 0.0




Nozzle Matl SA-105


Detail Type Nozzle

Detail ID N8B




Nozzle Class None

Layout Angle 180.0




Nozzle Matl SA-105


Detail Type Nozzle

Detail ID N12 B(2")



Nozzle Schedule XXS

Nozzle Class 900

Layout Angle 180.0

13




Grade of Attached Flange GR 1.1

Nozzle Matl SA-105


Detail Type Nozzle

Detail ID N12 A(2")



Nozzle Schedule XXS

Nozzle Class 900

Layout Angle 180.0



Grade of Attached Flange GR 1.1

Nozzle Matl SA-105


Detail Type Nozzle

Detail ID N7A




Nozzle Class None

Layout Angle 0.0




Nozzle Matl SA-105


Detail Type Nozzle

Detail ID N7 B


14




Nozzle Class None

Layout Angle 180.0




Nozzle Matl SA-105


Detail Type Nozzle

Detail ID N6A




Nozzle Class None

Layout Angle 270.0




Nozzle Matl SA-105


Detail Type Nozzle

Detail ID N6B




Nozzle Class None

Layout Angle 270.0




Nozzle Matl SA-105

15


--------------------------------------------------------------------


Element To Node 40

Element Type Elliptical

Description PIPE CAP 12" SCH 80












Material Name SA-234 WPB









UNS Number K03006

Product Form Smls. & wld. fittings



Elliptical Head Factor 2.0


Detail Type Liquid

Detail ID Liquid 30

16






Detail Type Nozzle

Detail ID N9A 2" LLC




Nozzle Class None

Layout Angle 0.0




Nozzle Matl SA-105


17

PV Elite 2015 SP2 Licensee: SPLM Licensed UserFileName : Sump pipe NPS 12 SCH 100 XY Coordinate Calculations : Step: 2 6:21pm Oct 2,2015

XY Coordinate Calculations

| | | | | |

From| To | X (Horiz.)| Y (Vert.) |DX (Horiz.)| DY (Vert.) |

| | mm | mm | mm | mm |

--------------------------------------------------------------

PIPE CAP 1| 88.0000 | ... | 88.0000 | ... |

SUMP PIPE| 2526.00 | ... | 2438.00 | ... |

PIPE CAP 1| 2614.00 | ... | 88.0000 | ... |


18

PV Elite 2015 SP2 Licensee: SPLM Licensed UserFileName : Sump pipe NPS 12 SCH 100 Internal Pressure Calculations : Step: 3 6:21pm Oct 2,2015

Element Thickness, Pressure, Diameter and Allowable Stress :

| | Int. Press | Nominal | Total Corr| Element | Allowable |

From| To | + Liq. Hd | Thickness | Allowance | Diameter | Stress(SE)|

| | psig | mm | mm | mm | N/mm² |

---------------------------------------------------------------------------

PIPE CAP 1| 1440.4 | 17.480 | 3.0000 | 288.89 | 117.90 |

SUMP PIPE| 1440.4 | 21.440 | 3.0000 | 288.89 | 117.90 |

PIPE CAP 1| 1440.4 | 17.480 | 3.0000 | 288.89 | 117.90 |

Element Required Thickness and MAWP :

| | Design | M.A.W.P. | M.A.P. | Minimum | Required |

From| To | Pressure | Corroded | New & Cold | Thickness | Thickness |

| | psig | psig | psig | mm | mm |

----------------------------------------------------------------------------

PIPE CAP 1| 1440.00 | 1585.46 | 2044.61 | 17.4800 | 15.1958 |

SUMP PIPE| 1440.00 | 1728.11 | 2071.17 | 18.8672 | 16.0817 |

PIPE CAP 1| 1440.00 | 1585.46 | 2044.61 | 17.4800 | 15.1958 |

Minimum 1440.000 2044.611

MAWP: 1440.000 psig, limited by: DESIGN (user specified)

Internal Pressure Calculation Results :

ASME Code, Section VIII, Division 1, 2013

Elliptical Head From 10 To 20 SA-234 WPB , UCS-66 Crv. B at 170 °F

PIPE CAP 12 " SCH 80

Material UNS Number: K03006

Required Thickness due to Internal Pressure [tr]:

19


= (P*D*Kcor)/(2*S*E-0.2*P) Appendix 1-4(c)

= (1440.415*294.8900*0.974)/(2*117.90*1.00-0.2*1440.415)

= 12.1958 + 3.0000 = 15.1958 mm

Max. Allowable Working Pressure at given Thickness, corroded [MAWP]:

Less Operating Hydrostatic Head Pressure of 0.415 psig

= (2*S*E*t)/(Kcor*D+0.2*t) per Appendix 1-4 (c)

= (2*117.90*1.00*14.4800)/(0.974*294.8900+0.2*14.4800)

= 1707.502 - 0.415 = 1707.087 psig

Maximum Allowable Pressure, New and Cold [MAPNC]:

= (2*S*E*t)/(K*D+0.2*t) per Appendix 1-4 (c)

= (2*117.90*1.00*17.4800)/(1.000*288.8900+0.2*17.4800)

= 2044.612 psig

Actual stress at given pressure and thickness, corroded [Sact]:

= (P*(Kcor*D+0.2*t))/(2*E*t)

= (1440.415*(0.974*294.8900+0.2*14.4800))/(2*1.00*14.4800)

= 99.462 N/mm²

Straight Flange Required Thickness:

= (P*R)/(S*E-0.6*P) + c per UG-27 (c)(1)

= (1440.415*147.4450)/(117.90*1.00-0.6*1440.415)+3.000

= 16.081 mm

Straight Flange Maximum Allowable Working Pressure:


= (S*E*t)/(R+0.6*t) per UG-27 (c)(1)

= (117.90 * 1.00 * 14.4800 )/(147.4450 + 0.6 * 14.4800 )

= 1585.879 - 0.415 = 1585.464 psig

Factor K, corroded condition [Kcor]:

= ( 2 + ( Inside Diameter/( 2 * Inside Head Depth ))2)/6

= ( 2 + ( 294.890/( 2 * 75.222 ))2)/6

= 0.973677

20


MDMT Calculations in the Knuckle Portion:

Govrn. thk, tg = 17.480 , tr = 12.196 , c = 3.0000 mm , E* = 1.00

Stress Ratio = tr * (E*)/(tg - c) = 0.842 , Temp. Reduction = 16 °F

Min Metal Temp. w/o impact per UCS-66, Curve B 11 °F

Min Metal Temp. at Required thickness (UCS 66.1) -4 °F

MDMT Calculations in the Head Straight Flange:




Min Metal Temp. at Required thickness (UCS 66.1) 2 °F

Cylindrical Shell From 20 To 30 SA-106 B , UCS-66 Crv. B at 170 °F

SUMP PIPE 12" SCH 100



= (P*R)/(S*E-0.6*P) per UG-27 (c)(1)

= (1440.415*147.4450)/(117.90*1.00-0.6*1440.415)

= 13.0817 + 3.0000 = 16.0817 mm



= (S*E*t)/(R+0.6*t) per UG-27 (c)(1)

= (117.90*1.00*15.8672)/(147.4450+0.6*15.8672)

= 1728.527 - 0.415 = 1728.112 psig


21


= (S*E*t)/(R+0.6*t) per UG-27 (c)(1)

= (117.90*1.00*18.8672)/(144.4450+0.6*18.8672)

= 2071.172 psig


= (P*(R+0.6*t))/(E*t)

= (1440.415*(147.4450+0.6*15.8672))/(1.00*15.8672)

= 98.248 N/mm²

Minimum Design Metal Temperature Results:





Elliptical Head From 30 To 40 SA-234 WPB , UCS-66 Crv. B at 170 °F

PIPE CAP 12" SCH 80



= (P*D*Kcor)/(2*S*E-0.2*P) Appendix 1-4(c)

= (1440.415*294.8900*0.974)/(2*117.90*1.00-0.2*1440.415)

= 12.1958 + 3.0000 = 15.1958 mm



= (2*S*E*t)/(Kcor*D+0.2*t) per Appendix 1-4 (c)

= (2*117.90*1.00*14.4800)/(0.974*294.8900+0.2*14.4800)

= 1707.502 - 0.415 = 1707.087 psig


22


= (2*S*E*t)/(K*D+0.2*t) per Appendix 1-4 (c)

= (2*117.90*1.00*17.4800)/(1.000*288.8900+0.2*17.4800)

= 2044.612 psig


= (P*(Kcor*D+0.2*t))/(2*E*t)

= (1440.415*(0.974*294.8900+0.2*14.4800))/(2*1.00*14.4800)

= 99.462 N/mm²

Straight Flange Required Thickness:

= (P*R)/(S*E-0.6*P) + c per UG-27 (c)(1)

= (1440.415*147.4450)/(117.90*1.00-0.6*1440.415)+3.000

= 16.081 mm

Straight Flange Maximum Allowable Working Pressure:


= (S*E*t)/(R+0.6*t) per UG-27 (c)(1)

= (117.90 * 1.00 * 14.4800 )/(147.4450 + 0.6 * 14.4800 )

= 1585.879 - 0.415 = 1585.464 psig

Factor K, corroded condition [Kcor]:

= ( 2 + ( Inside Diameter/( 2 * Inside Head Depth ))2)/6

= ( 2 + ( 294.890/( 2 * 75.222 ))2)/6

= 0.973677

MDMT Calculations in the Knuckle Portion:





MDMT Calculations in the Head Straight Flange:

23





Min Metal Temp. at Required thickness (UCS 66.1) 2 °F

Hydrostatic Test Pressure Results:

Pressure per UG99b = 1.3 * M.A.W.P. * Sa/S 1872.000 psig

Pressure per UG99b[36] = 1.3 * Design Pres * Sa/S 1872.000 psig

Pressure per UG99c = 1.3 * M.A.P. - Head(Hyd) 2657.584 psig

Pressure per UG100 = 1.1 * M.A.W.P. * Sa/S 1584.000 psig

Pressure per PED = 1.43 * MAWP 2059.200 psig

User Defined Hydrostatic Test Pressure at High Point 2160.000 psig

Horizontal Test performed per: User Hydro Pressure

Please note that Nozzle, Shell, Head, Flange, etc MAWPs are all considered

when determining the hydrotest pressure for those test types that are based

on the MAWP of the vessel.

Stresses on Elements due to Test Pressure:

From To Stress Allowable Ratio Pressure

----------------------------------------------------------------------

PIPE CAP 12 " SCH 80 124.6 217.2 0.574 2160.41

SUMP PIPE 12" SCH 10 123.0 217.2 0.566 2160.41

PIPE CAP 12" SCH 80 124.6 217.2 0.574 2160.41

----------------------------------------------------------------------

Stress ratios for Nozzle and Pad Materials:

Description Pad/Nozzle Ambient Operating ratio

----------------------------------------------------------------------

N9A 2" LLC Nozzle 137.90 137.90 1.000

24


DRAIN PIPE 1 Nozzle 117.90 117.90 1.000



N8A Nozzle 137.90 137.90 1.000

N8B Nozzle 137.90 137.90 1.000

N12 B(2") Nozzle 137.90 137.90 1.000

N12 B(2") Pad 117.90 117.90 1.000

N12 A(2") Nozzle 137.90 137.90 1.000

N12 A(2") Pad 117.90 117.90 1.000

N7A Nozzle 137.90 137.90 1.000

N7 B Nozzle 137.90 137.90 1.000

N6A Nozzle 137.90 137.90 1.000

N6B Nozzle 137.90 137.90 1.000

N9A 2" LLC Nozzle 137.90 137.90 1.000

----------------------------------------------------------------------

Minimum 1.000

Stress ratios for Vessel Elements:

Description Ambient Operating ratio

----------------------------------------------------------------------

PIPE CAP 12 " SCH 80 117.90 117.90 1.000

SUMP PIPE 12" SCH 10 117.90 117.90 1.000

PIPE CAP 12" SCH 80 117.90 117.90 1.000

----------------------------------------------------------------------

Minimum 1.000

Elements Suitable for Internal Pressure.


25

PV Elite 2015 SP2 Licensee: SPLM Licensed UserFileName : Sump pipe NPS 12 SCH 100 Element and Detail Weights : Step: 5 6:21pm Oct 2,2015

Element and Detail Weights

| | Element | Element | Corroded | Corroded | Extra due |

From| To | Metal Wgt. | ID Volume |Metal Wgt. | ID Volume | Misc % |

| | kgm | m³ | kgm | m³ | kgm |

---------------------------------------------------------------------------

10| 20| 26.6946 | 0.0089258 | 22.1131 | 0.0093687 | ... |

20| 30| 394.968 | 0.15983 | 342.986 | 0.16654 | ... |

30| 40| 26.6946 | 0.0089258 | 22.1131 | 0.0093687 | ... |

---------------------------------------------------------------------------

Total 448 0.18 387 0.19 0

Weight of Details

| | Weight of | X Offset, | Y Offset, |

From|Type| Detail | Dtl. Cent. |Dtl. Cent. | Description

| | kgm | mm | mm |

-------------------------------------------------

10|Liqd| 8.92031 | -24.0742 | ... | Liquid 10

10|Nozl| 2.01011 | -72.2225 | ... | N9A 2" LLC

20|Liqd| 159.736 | 1219.00 | ... | WATER

20|Nozl| 3.94095 | 648.000 | 165.870 | DRAIN PIPE 1

20|Nozl| 10.9753 | 1147.00 | 165.870 | DRAIN PIPE 2

20|Nozl| 10.9753 | 1719.00 | 165.870 | DRAIN PIPE 3

20|Nozl| 0.39103 | 543.000 | 166.670 | N8A

20|Nozl| 0.39103 | 543.000 | 166.670 | N8B

20|Nozl| 16.7236 | 871.000 | 174.607 | N12 B(2")

20|Nozl| 16.7236 | 1434.00 | 174.607 | N12 A(2")

20|Nozl| 0.39103 | 1878.00 | 166.670 | N7A

20|Nozl| 0.39103 | 1878.00 | 166.670 | N7 B

20|Nozl| 0.78969 | 675.000 | 173.020 | N6A

20|Nozl| 0.78969 | 1163.00 | 173.020 | N6B

30|Liqd| 8.92031 | 112.074 | ... | Liquid 30

30|Nozl| 2.52497 | 160.223 | ... | N9A 2" LLC

26


Total Weight of Each Detail Type

Total Weight of Liquid 177.6

Total Weight of Nozzles 67.0

---------------------------------------------------------------

Sum of the Detail Weights 244.6 kgm

Weight Summation

Fabricated Shop Test Shipping Erected Empty Operating

------------------------------------------------------------------------------

448.4 515.4 448.4 515.4 448.4 515.4

... 177.6 ... ... ... 177.6

67.0 ... 67.0 ... ... ...

... ... ... ... ... ...

... ... ... ... ... ...

... ... ... ... 67.0 ...

------------------------------------------------------------------------------

515.4 693.0 515.4 515.4 515.4 693.0 kgm

Note: The shipping total has been modified because some items have

been specified as being installed in the shop.

Weight Summary

Fabricated Wt. - Bare Weight W/O Removable Internals 515.4 kgm

Shop Test Wt. - Fabricated Weight + Water ( Full ) 693.0 kgm

Shipping Wt. - Fab. Wt + Rem. Intls.+ Shipping App. 515.4 kgm

Erected Wt. - Fab. Wt + Rem. Intls.+ Insul. (etc) 515.4 kgm

Ope. Wt. no Liq - Fab. Wt + Intls. + Details + Wghts. 515.4 kgm

Operating Wt. - Empty Wt + Operating Liq. Uncorroded 693.0 kgm

Oper. Wt. + CA - Corr Wt. + Operating Liquid 631.8 kgm

27


Field Test Wt. - Empty Weight + Water (Full) 693.0 kgm

Note: The Corroded Weight and thickness are used in the Horizontal

Vessel Analysis (Ope Case) and Earthquake Load Calculations.

Outside Surface Areas of Elements

| | Surface |

From| To | Area |

| | mm² |

----------------------------

10| 20| 203219. |

20| 30| 2.541E+06 |

30| 40| 203219. |

-----------------------------

Total 2947531.500 mm²


28

PV Elite 2015 SP2 Licensee: SPLM Licensed UserFileName : Sump pipe NPS 12 SCH 100 Nozzle Flange MAWP : Step: 6 6:21pm Oct 2,2015

Nozzle Flange MAWP Results :

Nozzle ----- Flange Rating

Description Operating Ambient Temperature Class Grade|Group

psig psig °F

----------------------------------------------------------------------------

N12 B(2") 2090.5 2220.0 170 900 GR 1.1

N12 A(2") 2090.5 2220.0 170 900 GR 1.1

----------------------------------------------------------------------------

Minimum Rating 2090.500 2220.000 psig (for Core Elements)

Note: ANSI Ratings are per ANSI/ASME B16.5 2009 Edition


29

PV Elite 2015 SP2 Licensee: SPLM Licensed UserFileName : Sump pipe NPS 12 SCH 100 Center of Gravity Calculation : Step: 7 6:21pm Oct 2,2015

Shop/Field Installation Options :

Note : The CG is computed from the first Element From Node

Center of Gravity of Liquid 1307.000 mm

Center of Gravity of Nozzles 1313.654 mm

Center of Gravity of Bare Shell New and Cold 1307.000 mm

Center of Gravity of Bare Shell Corroded 1307.000 mm

Vessel CG in the Operating Condition 1307.706 mm

Vessel CG in the Fabricated (Shop/Empty) Condition 1307.865 mm


30

PV Elite 2015 SP2 Licensee: SPLM Licensed UserFileName : Sump pipe NPS 12 SCH 100 Nozzle Calcs. : N9A 2" LLC Nozl: 14 6:21pm Oct 2,2015

INPUT VALUES, Nozzle Description: N9A 2" LLC From : 10

Pressure for Reinforcement Calculations P 1440.205 psig

Temperature for Internal Pressure Temp 170 °F

Shell Material SA-234 WPB

Shell Allowable Stress at Temperature S 117.90 N/mm²

Shell Allowable Stress At Ambient Sa 117.90 N/mm²

Inside Diameter of Elliptical Head D 288.89 mm

Aspect Ratio of Elliptical Head Ar 2.00

Head Finished (Minimum) Thickness t 17.4800 mm

Head Internal Corrosion Allowance c 3.0000 mm

Head External Corrosion Allowance co 0.0000 mm

Distance from Head Centerline L1 0.0000 mm

User Entered Minimum Design Metal Temperature 32.00 °F

Type of Element Connected to the Shell : Nozzle

Material SA-105

Material UNS Number K03504

Material Specification/Type Forgings

Allowable Stress at Temperature Sn 137.90 N/mm²

Allowable Stress At Ambient Sna 137.90 N/mm²

Diameter Basis (for tr calc only) OD

Layout Angle 0.00 deg

Diameter 3.6250 in.

Size and Thickness Basis Actual

Actual Thickness tn 15.8750 mm

31


Corrosion Allowance can 3.0000 mm

Joint Efficiency of Shell Seam at Nozzle E1 1.00

Joint Efficiency of Nozzle Neck En 1.00

Outside Projection ho 85.7250 mm

Weld leg size between Nozzle and Pad/Shell Wo 10.0000 mm

Groove weld depth between Nozzle and Vessel Wgnv 15.8750 mm

ASME Code Weld Type per UW-16 None

The Pressure Design option was Design Pressure + static head.

Nozzle Sketch (may not represent actual weld type/configuration)

| |

| |

| |

| |

| |

|\ |

__________/|_\|

| |

| |

|______________|

Abutting/Set-on Nozzle No Pad

Reinforcement CALCULATION, Description: N9A 2" LLC

ASME Code, Section VIII, Div. 1, 2013, UG-37 to UG-45

Actual Outside Diameter Used in Calculation 3.625 in.

Actual Thickness Used in Calculation 0.625 in.

Nozzle input data check completed without errors.

32


Reqd thk per UG-37(a)of Elliptical Head, Tr [Int. Press]

= (P*K1*D))/(2*S*E-0.2*P) per UG-37(a)(3)

= (1440.21*0.883*294.8900)/(2 *117.90*1.00-0.2*1440.21)

= 11.0571 mm

Reqd thk per UG-37(a)of Nozzle Wall, Trn [Int. Press]

= (P*Ro)/(S*E+0.4*P) per Appendix 1-1 (a)(1)

= (1440.21*46.0375)/(138*1.00+0.4*1440.21)

= 3.2224 mm

UG-40, Limits of Reinforcement : [Internal Pressure]

Parallel to Vessel Wall (Diameter Limit) Dl 132.6500 mm

Parallel to Vessel Wall, opening length d 66.3250 mm

Normal to Vessel Wall (Thickness Limit), no pad Tlnp 32.1875 mm

Weld Strength Reduction Factor [fr1]:

= 1.000


= min( 1, Sn/S )

= min( 1, 137.9/117.9 )

= 1.000


= min( fr2, fr4 )

= min( 1.0 , 1.0 )

= 1.000

Results of Nozzle Reinforcement Area Calculations:

AREA AVAILABLE, A1 to A5 Design External Mapnc

Area Required Ar 733.364 NA NA mm²

Area in Shell A1 227.022 NA NA mm²

Area in Nozzle Wall A2 621.389 NA NA mm²

Area in Inward Nozzle A3 0.000 NA NA mm²

33


Area in Welds A41+A42+A43 100.000 NA NA mm²

Area in Element A5 0.000 NA NA mm²

TOTAL AREA AVAILABLE Atot 948.411 NA NA mm²

The Internal Pressure Case Governs the Analysis.

Nozzle Angle Used in Area Calculations 90.00 Degs.

The area available without a pad is Sufficient.

Area Required [A]:

= ( d * tr*F + 2 * tn * tr*F * (1-fr1) ) UG-37(c)

= (66.3250*11.0571*1.0+2*12.8750*11.0571*1.0*(1-1.00))

= 733.364 mm²

Reinforcement Areas per Figure UG-37.1

Area Available in Shell [A1]:

= d( E1*t - F*tr ) - 2 * tn( E1*t - F*tr ) * ( 1 - fr1 )

= 66.325 ( 1.00 * 14.4800 - 1.0 * 11.057 ) - 2 * 12.875

( 1.00 * 14.4800 - 1.0 * 11.0571 ) * ( 1 - 1.000 )

= 227.022 mm²

Area Available in Nozzle Projecting Outward [A2]:

= ( 2 * tlnp ) * ( tn - trn ) * fr2

= ( 2 * 32.19 ) * ( 12.88 - 3.22 ) * 1.0000

= 621.389 mm²

Area Available in Inward Weld + Outward Weld [A41 + A43]:

= Wo² * fr2 + ( Wi-can/0.707 )² * fr2

= 10.0000² * 1.0000 + ( 0.0000 )² * 1.0000

= 100.000 mm²

UG-45 Minimum Nozzle Neck Thickness Requirement: [Int. Press.]

Wall Thickness for Internal/External pressures ta = 6.2224 mm

34


Wall Thickness per UG16(b), tr16b = 4.5000 mm

Wall Thickness, shell/head, internal pressure trb1 = 15.1940 mm

Wall Thickness tb1 = max(trb1, tr16b) = 15.1940 mm


Wall Thickness per table UG-45 tb3 = 8.0200 mm

Determine Nozzle Thickness candidate [tb]:

= min[ tb3, max( tb1,tb2) ]

= min[ 8.020 , max( 15.1940 , 4.5000 ) ]

= 8.0200 mm

Minimum Wall Thickness of Nozzle Necks [tUG-45]:

= max( ta, tb )

= max( 6.2224 , 8.0200 )

= 8.0200 mm

Available Nozzle Neck Thickness = 15.8750 mm --> OK

Nozzle Junction Minimum Design Metal Temperature (MDMT) Calculations:

MDMT of Nozzle-Shell/Head Weld for the Nozzle (UCS-66(a)1(b)), Curve: B

----------------------------------------------------------------------





Governing MDMT of all the sub-joints of this Junction : -134 °F

Weld Size Calculations, Description: N9A 2" LLC

Intermediate Calc. for nozzle/shell Welds Tmin 12.8750 mm

Results Per UW-16.1:

35


Required Thickness Actual Thickness

Nozzle Weld 6.0000 = Min per Code 7.0700 = 0.7 * Wo mm

Weld Strength and Weld Loads per UG-41.1, Sketch (a) or (b)

Weld Load [W]:

= ( Ar - A1 )* Sv

= ( 733.3641 - 227.0218 ) * 118

= 59.69 kN

Note: F is always set to 1.0 throughout the calculation.

Weld Load [W1]:

= (A2+A5+A4-(Wi-Can/.707)²*fr2)*Sv

= ( 621.3890 + 0.0000 + 100.0000 - 0.0000 * 1.00 ) * 118

= 85.05 kN

Strength of Connection Elements for Failure Path Analysis

Shear, Outward Nozzle Weld [Sonw]:

= (pi/2) * Dlo * Wo * 0.49 * Snw

= ( 3.1416/2.0 ) * 92.0750 * 10.0000 * 0.49 * 118

= 84. kN

Shear, Nozzle Groove Weld [Sngw]:

= (pi/2) * (Dlr+Wgnva) * (Wgnva-Can) * 0.60 * Sng

= (3.14/2)*(66.325 +15.875 )*(15.875 -3.0000 )*0.6*138

= 138. kN

Strength of Failure Paths:

PATH11 = ( SONW + SNGW )= ( 84 + 138 ) = 221 kN

Summary of Failure Path Calculations:

36


Path 1-1 = 221 kN , must exceed W = 59 kN or W1 = 85 kN

Maximum Allowable Pressure for this Nozzle at this Location:

Converged Max. Allow. Pressure in Operating case 1440.205 psig

Note: The MAWP of this junction was limited by the parent Shell/Head.

The Drop for this Nozzle is : 3.8955 mm

The Cut Length for this Nozzle is, Drop + Ho + H + T : 107.1005 mm


37

PV Elite 2015 SP2 Licensee: SPLM Licensed UserFileName : Sump pipe NPS 12 SCH 100 Nozzle Calcs. : DRAIN PIPE 1 Nozl: 15 6:21pm Oct 2,2015

INPUT VALUES, Nozzle Description: DRAIN PIPE 1 From : 20



Shell Material SA-106 B



Inside Diameter of Cylindrical Shell D 288.89 mm

Shell Finished (Minimum) Thickness t 18.8672 mm

Shell Internal Corrosion Allowance c 3.0000 mm

Shell External Corrosion Allowance co 0.0000 mm

Distance from Bottom/Left Tangent 736.0001 mm



Material SA-106 B


Material Specification/Type Smls. pipe



Diameter Basis (for tr calc only) ID


Diameter 2.0000 in.

Size and Thickness Basis Nominal

Nominal Thickness tn 160


38







Inside Projection h 0.0000 mm

Weld leg size, Inside Element to Shell Wi 0.0000 mm




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Insert/Set-in Nozzle No Pad, no Inside projection

Reinforcement CALCULATION, Description: DRAIN PIPE 1


Actual Inside Diameter Used in Calculation 1.687 in.



39


Reqd thk per UG-37(a)of Cylindrical Shell, Tr [Int. Press]

= (P*R)/(S*E-0.6*P) per UG-27 (c)(1)

= (1440.00*147.4450)/(118*1.00-0.6*1440.00)

= 13.0777 mm


= (P*R)/(S*E-0.6*P) per UG-27 (c)(1)

= (1440.00*24.42)/(118*1.00-0.6*1440.00)

= 2.1663 mm

Note:

Taking a UG-36(c)(3)(a) exemption for nozzle: DRAIN PIPE 1.

This calculation is valid for nozzles that meet all the requirements of

paragraph UG-36. Please check the Code carefully, especially for nozzles

that are not isolated or do not meet Code spacing requirements. To force

the computation of areas for small nozzles go to Tools->Configuration

and check the box to force the UG-37 small nozzle area calculation or

force the Appendix 1-10 computation in Nozzle Design Options.










= min[ 6.420 , max( 16.0777 , 4.5000 ) ]

= 6.4200 mm


= max( ta, tb )

40


= max( 5.1663 , 6.4200 )

= 6.4200 mm

Available Nozzle Neck Thickness = 0.875 * 8.738 = 7.645 mm --> OK



----------------------------------------------------------------------



Min Metal Temp. w/o impact per UCS-66, Curve B -20 °F



Weld Size Calculations, Description: DRAIN PIPE 1




Nozzle Weld 4.0163 = 0.7 * tmin. 7.0700 = 0.7 * Wo mm

NOTE : Skipping the nozzle attachment weld strength calculations.

Per UW-15(b)(2) the nozzles exempted by UG-36(c)(3)(a)

(small nozzles) do not require a weld strength check.





41




42















Material SA-106 B







Diameter 2.0000 in.




43












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44



= (P*R)/(S*E-0.6*P) per UG-27 (c)(1)

= (1440.00*147.4450)/(118*1.00-0.6*1440.00)

= 13.0777 mm


= (P*R)/(S*E-0.6*P) per UG-27 (c)(1)

= (1440.00*24.42)/(118*1.00-0.6*1440.00)

= 2.1663 mm

Note:

















= min[ 6.420 , max( 16.0777 , 4.5000 ) ]

= 6.4200 mm


= max( ta, tb )

45


= max( 5.1663 , 6.4200 )

= 6.4200 mm




----------------------------------------------------------------------


















46




47















Material SA-106 B







Diameter 2.0000 in.




48












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49



= (P*R)/(S*E-0.6*P) per UG-27 (c)(1)

= (1440.00*147.4450)/(118*1.00-0.6*1440.00)

= 13.0777 mm


= (P*R)/(S*E-0.6*P) per UG-27 (c)(1)

= (1440.00*24.42)/(118*1.00-0.6*1440.00)

= 2.1663 mm

Note:

















= min[ 6.420 , max( 16.0777 , 4.5000 ) ]

= 6.4200 mm


= max( ta, tb )

50


= max( 5.1663 , 6.4200 )

= 6.4200 mm




----------------------------------------------------------------------


















51




52

PV Elite 2015 SP2 Licensee: SPLM Licensed UserFileName : Sump pipe NPS 12 SCH 100 Nozzle Calcs. : N8A Nozl: 18 6:21pm Oct 2,2015

INPUT VALUES, Nozzle Description: N8A From : 20













Material SA-105







Diameter 1.7500 in.




53










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Reinforcement CALCULATION, Description: N8A





54



= (P*R)/(S*E-0.6*P) per UG-27 (c)(1)

= (1440.00*147.4450)/(118*1.00-0.6*1440.00)

= 13.0777 mm



= (1440.00*22.2250)/(138*1.00+0.4*1440.00)

= 1.5554 mm

Note:

Taking a UG-36(c)(3)(a) exemption for nozzle: N8A.
















= min[ 6.220 , max( 16.0777 , 4.5000 ) ]

= 6.2200 mm


= max( ta, tb )

55


= max( 4.5554 , 6.2200 )

= 6.2200 mm




----------------------------------------------------------------------






Weld Size Calculations, Description: N8A












56




57

PV Elite 2015 SP2 Licensee: SPLM Licensed UserFileName : Sump pipe NPS 12 SCH 100 Nozzle Calcs. : N8B Nozl: 19 6:21pm Oct 2,2015

INPUT VALUES, Nozzle Description: N8B From : 20













Material SA-105







Diameter 1.7500 in.




58










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Reinforcement CALCULATION, Description: N8B





59



= (P*R)/(S*E-0.6*P) per UG-27 (c)(1)

= (1440.41*147.4450)/(118*1.00-0.6*1440.41)

= 13.0816 mm



= (1440.41*22.2250)/(138*1.00+0.4*1440.41)

= 1.5558 mm

Note:

Taking a UG-36(c)(3)(a) exemption for nozzle: N8B.
















= min[ 6.220 , max( 16.0816 , 4.5000 ) ]

= 6.2200 mm


= max( ta, tb )

60


= max( 4.5558 , 6.2200 )

= 6.2200 mm




----------------------------------------------------------------------






Weld Size Calculations, Description: N8B












61




62

PV Elite 2015 SP2 Licensee: SPLM Licensed UserFileName : Sump pipe NPS 12 SCH 100 Nozzle Calcs. : N12 B(2") Nozl: 20 6:21pm Oct 2,2015

INPUT VALUES, Nozzle Description: N12 B(2") From : 20













Material SA-105







Diameter 2.0000 in.


Nominal Thickness tn XXS

Flange Material SA-105

63


Flange Type Weld Neck Flange









Pad Material SA-106 B

Pad Allowable Stress at Temperature Sp 117.90 N/mm²

Pad Allowable Stress At Ambient Spa 117.90 N/mm²

Diameter of Pad along vessel surface Dp 160.3250 mm

Thickness of Pad te 14.0000 mm

Weld leg size between Pad and Shell Wp 10.0000 mm

Groove weld depth between Pad and Nozzle Wgpn 14.0000 mm

Reinforcing Pad Width 50.0000 mm


Class of attached Flange 900

Grade of attached Flange GR 1.1



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64


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Insert/Set-in Nozzle With Pad, no Inside projection

Reinforcement CALCULATION, Description: N12 B(2")






= (P*R)/(S*E-0.6*P) per UG-27 (c)(1)

= (1440.41*147.4450)/(118*1.00-0.6*1440.41)

= 13.0816 mm



= (1440.41*30.1625)/(138*1.00+0.4*1440.41)

= 2.1115 mm

Note:

Taking a UG-36(c)(3)(a) exemption for nozzle: N12 B(2").








65










= min[ 6.420 , max( 16.0816 , 4.5000 ) ]

= 6.4200 mm


= max( ta, tb )

= max( 5.1115 , 6.4200 )

= 6.4200 mm



MDMT of the Nozzle Neck to Flange Weld, Curve: B

----------------------------------------------------------------------





MDMT of Nozzle Neck to Pad Weld for the Nozzle, Curve: B

----------------------------------------------------------------------




66



MDMT of Nozzle Neck to Pad Weld for Reinforcement pad, Curve: B

----------------------------------------------------------------------





MDMT of Shell to Pad Weld at Pad OD for pad, Curve: B

----------------------------------------------------------------------

Govrn. thk, tg = 14.000 , c = 3.0000 mm , E* = 1.00


Pad governing, Conservatively assuming Pad stress = Shell stress(Div. 1 L-9.3)




----------------------------------------------------------------------





Governing MDMT of the Nozzle : -155 °F

Governing MDMT of the Reinforcement Pad : -18 °F


ANSI Flange MDMT including Temperature reduction per UCS-66.1:

Unadjusted MDMT of ANSI B16.5/47 flanges per UCS-66(c) -20 °F

Flange MDMT with Temp reduction per UCS-66(b)(1)(b) -55 °F

67


Flange MDMT with Temp reduction per UCS-66(b)(1)(c) -155 °F

Where the Stress Reduction Ratio per UCS-66(b)(1)(b) is :

Design Pressure/Ambient Rating = 1440.41/2220.00 = 0.649

Note: Using the minimum value from (b)(1)(b) and (b)(1)(c) above

as the calculated nozzle flange MDMT.

Weld Size Calculations, Description: N12 B(2")


Intermediate Calc. for pad/shell Welds TminPad 14.0000 mm




Pad Weld 7.0000 = 0.5*TminPad 7.0700 = 0.7 * Wp mm










68

PV Elite 2015 SP2 Licensee: SPLM Licensed UserFileName : Sump pipe NPS 12 SCH 100 Nozzle Calcs. : N12 A(2") Nozl: 21 6:21pm Oct 2,2015

INPUT VALUES, Nozzle Description: N12 A(2") From : 20













Material SA-105







Diameter 2.0000 in.


Nominal Thickness tn XXS

Flange Material SA-105

69


Flange Type Weld Neck Flange









Pad Material SA-106 B

Pad Allowable Stress at Temperature Sp 117.90 N/mm²

Pad Allowable Stress At Ambient Spa 117.90 N/mm²

Diameter of Pad along vessel surface Dp 160.3250 mm

Thickness of Pad te 14.0000 mm

Weld leg size between Pad and Shell Wp 10.0000 mm

Groove weld depth between Pad and Nozzle Wgpn 14.0000 mm

Reinforcing Pad Width 50.0000 mm


Class of attached Flange 900

Grade of attached Flange GR 1.1



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70


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Insert/Set-in Nozzle With Pad, no Inside projection

Reinforcement CALCULATION, Description: N12 A(2")






= (P*R)/(S*E-0.6*P) per UG-27 (c)(1)

= (1440.41*147.4450)/(118*1.00-0.6*1440.41)

= 13.0816 mm



= (1440.41*30.1625)/(138*1.00+0.4*1440.41)

= 2.1115 mm

Note:

Taking a UG-36(c)(3)(a) exemption for nozzle: N12 A(2").








71










= min[ 6.420 , max( 16.0816 , 4.5000 ) ]

= 6.4200 mm


= max( ta, tb )

= max( 5.1115 , 6.4200 )

= 6.4200 mm



MDMT of the Nozzle Neck to Flange Weld, Curve: B

----------------------------------------------------------------------





MDMT of Nozzle Neck to Pad Weld for the Nozzle, Curve: B

----------------------------------------------------------------------




72



MDMT of Nozzle Neck to Pad Weld for Reinforcement pad, Curve: B

----------------------------------------------------------------------





MDMT of Shell to Pad Weld at Pad OD for pad, Curve: B

----------------------------------------------------------------------

Govrn. thk, tg = 14.000 , c = 3.0000 mm , E* = 1.00


Pad governing, Conservatively assuming Pad stress = Shell stress(Div. 1 L-9.3)




----------------------------------------------------------------------





Governing MDMT of the Nozzle : -155 °F

Governing MDMT of the Reinforcement Pad : -18 °F


ANSI Flange MDMT including Temperature reduction per UCS-66.1:

Unadjusted MDMT of ANSI B16.5/47 flanges per UCS-66(c) -20 °F

Flange MDMT with Temp reduction per UCS-66(b)(1)(b) -55 °F

73


Flange MDMT with Temp reduction per UCS-66(b)(1)(c) -155 °F

Where the Stress Reduction Ratio per UCS-66(b)(1)(b) is :

Design Pressure/Ambient Rating = 1440.41/2220.00 = 0.649

Note: Using the minimum value from (b)(1)(b) and (b)(1)(c) above

as the calculated nozzle flange MDMT.

Weld Size Calculations, Description: N12 A(2")


Intermediate Calc. for pad/shell Welds TminPad 14.0000 mm




Pad Weld 7.0000 = 0.5*TminPad 7.0700 = 0.7 * Wp mm










74















Material SA-105







Diameter 1.7500 in.




75










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76



= (P*R)/(S*E-0.6*P) per UG-27 (c)(1)

= (1440.00*147.4450)/(118*1.00-0.6*1440.00)

= 13.0777 mm



= (1440.00*22.2250)/(138*1.00+0.4*1440.00)

= 1.5554 mm

Note:

















= min[ 6.220 , max( 16.0777 , 4.5000 ) ]

= 6.2200 mm


= max( ta, tb )

77


= max( 4.5554 , 6.2200 )

= 6.2200 mm




----------------------------------------------------------------------


















78




79

PV Elite 2015 SP2 Licensee: SPLM Licensed UserFileName : Sump pipe NPS 12 SCH 100 Nozzle Calcs. : N7 B Nozl: 23 6:21pm Oct 2,2015

INPUT VALUES, Nozzle Description: N7 B From : 20













Material SA-105







Diameter 1.7500 in.




80










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Reinforcement CALCULATION, Description: N7 B





81



= (P*R)/(S*E-0.6*P) per UG-27 (c)(1)

= (1440.41*147.4450)/(118*1.00-0.6*1440.41)

= 13.0816 mm



= (1440.41*22.2250)/(138*1.00+0.4*1440.41)

= 1.5558 mm

Note:

Taking a UG-36(c)(3)(a) exemption for nozzle: N7 B.
















= min[ 6.220 , max( 16.0816 , 4.5000 ) ]

= 6.2200 mm


= max( ta, tb )

82


= max( 4.5558 , 6.2200 )

= 6.2200 mm




----------------------------------------------------------------------






Weld Size Calculations, Description: N7 B












83




84















Material SA-105







Diameter 2.2500 in.




85










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86



= (P*R)/(S*E-0.6*P) per UG-27 (c)(1)

= (1440.21*147.4450)/(118*1.00-0.6*1440.21)

= 13.0797 mm



= (1440.21*28.5750)/(138*1.00+0.4*1440.21)

= 2.0001 mm

Note:

















= min[ 6.420 , max( 16.0797 , 4.5000 ) ]

= 6.4200 mm


= max( ta, tb )

87


= max( 5.0001 , 6.4200 )

= 6.4200 mm




----------------------------------------------------------------------


















88




89


INPUT VALUES, Nozzle Description: N6B From : 20













Material SA-105







Diameter 2.2500 in.




90










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Reinforcement CALCULATION, Description: N6B





91



= (P*R)/(S*E-0.6*P) per UG-27 (c)(1)

= (1440.21*147.4450)/(118*1.00-0.6*1440.21)

= 13.0797 mm



= (1440.21*28.5750)/(138*1.00+0.4*1440.21)

= 2.0001 mm

Note:

Taking a UG-36(c)(3)(a) exemption for nozzle: N6B.
















= min[ 6.420 , max( 16.0797 , 4.5000 ) ]

= 6.4200 mm


= max( ta, tb )

92


= max( 5.0001 , 6.4200 )

= 6.4200 mm




----------------------------------------------------------------------






Weld Size Calculations, Description: N6B












93




94


INPUT VALUES, Nozzle Description: N9A 2" LLC From : 30



Shell Material SA-234 WPB



Inside Diameter of Elliptical Head D 288.89 mm

Aspect Ratio of Elliptical Head Ar 2.00

Head Finished (Minimum) Thickness t 17.4800 mm

Head Internal Corrosion Allowance c 3.0000 mm

Head External Corrosion Allowance co 0.0000 mm

Distance from Head Centerline L1 0.0000 mm



Material SA-105







Diameter 3.6250 in.



95











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Reinforcement CALCULATION, Description: N9A 2" LLC





96


Reqd thk per UG-37(a)of Elliptical Head, Tr [Int. Press]

= (P*K1*D))/(2*S*E-0.2*P) per UG-37(a)(3)

= (1440.21*0.883*294.8900)/(2 *117.90*1.00-0.2*1440.21)

= 11.0571 mm



= (1440.21*46.0375)/(138*1.00+0.4*1440.21)

= 3.2224 mm

UG-40, Limits of Reinforcement : [Internal Pressure]

Parallel to Vessel Wall (Diameter Limit) Dl 132.6500 mm

Parallel to Vessel Wall, opening length d 66.3250 mm

Normal to Vessel Wall (Thickness Limit), no pad Tlnp 32.1875 mm


= 1.000


= min( 1, Sn/S )

= min( 1, 137.9/117.9 )

= 1.000


= min( fr2, fr4 )

= min( 1.0 , 1.0 )

= 1.000

Results of Nozzle Reinforcement Area Calculations:

AREA AVAILABLE, A1 to A5 Design External Mapnc

Area Required Ar 733.364 NA NA mm²

Area in Shell A1 227.022 NA NA mm²

Area in Nozzle Wall A2 621.389 NA NA mm²

Area in Inward Nozzle A3 0.000 NA NA mm²

97


Area in Welds A41+A42+A43 100.000 NA NA mm²

Area in Element A5 0.000 NA NA mm²

TOTAL AREA AVAILABLE Atot 948.411 NA NA mm²

The Internal Pressure Case Governs the Analysis.

Nozzle Angle Used in Area Calculations 90.00 Degs.

The area available without a pad is Sufficient.

Area Required [A]:

= ( d * tr*F + 2 * tn * tr*F * (1-fr1) ) UG-37(c)

= (66.3250*11.0571*1.0+2*12.8750*11.0571*1.0*(1-1.00))

= 733.364 mm²

Reinforcement Areas per Figure UG-37.1

Area Available in Shell [A1]:

= d( E1*t - F*tr ) - 2 * tn( E1*t - F*tr ) * ( 1 - fr1 )

= 66.325 ( 1.00 * 14.4800 - 1.0 * 11.057 ) - 2 * 12.875

( 1.00 * 14.4800 - 1.0 * 11.0571 ) * ( 1 - 1.000 )

= 227.022 mm²

Area Available in Nozzle Projecting Outward [A2]:

= ( 2 * tlnp ) * ( tn - trn ) * fr2

= ( 2 * 32.19 ) * ( 12.88 - 3.22 ) * 1.0000

= 621.389 mm²

Area Available in Inward Weld + Outward Weld [A41 + A43]:

= Wo² * fr2 + ( Wi-can/0.707 )² * fr2

= 10.0000² * 1.0000 + ( 0.0000 )² * 1.0000

= 100.000 mm²



98









= min[ 8.020 , max( 15.1940 , 4.5000 ) ]

= 8.0200 mm


= max( ta, tb )

= max( 6.2224 , 8.0200 )

= 8.0200 mm




----------------------------------------------------------------------






Weld Size Calculations, Description: N9A 2" LLC



99




Weld Strength and Weld Loads per UG-41.1, Sketch (a) or (b)

Weld Load [W]:

= ( Ar - A1 )* Sv

= ( 733.3641 - 227.0218 ) * 118

= 59.69 kN

Note: F is always set to 1.0 throughout the calculation.

Weld Load [W1]:

= (A2+A5+A4-(Wi-Can/.707)²*fr2)*Sv

= ( 621.3890 + 0.0000 + 100.0000 - 0.0000 * 1.00 ) * 118

= 85.05 kN

Strength of Connection Elements for Failure Path Analysis

Shear, Outward Nozzle Weld [Sonw]:

= (pi/2) * Dlo * Wo * 0.49 * Snw

= ( 3.1416/2.0 ) * 92.0750 * 10.0000 * 0.49 * 118

= 84. kN

Shear, Nozzle Groove Weld [Sngw]:

= (pi/2) * (Dlr+Wgnva) * (Wgnva-Can) * 0.60 * Sng

= (3.14/2)*(66.325 +15.875 )*(15.875 -3.0000 )*0.6*138

= 138. kN

Strength of Failure Paths:

PATH11 = ( SONW + SNGW )= ( 84 + 138 ) = 221 kN

Summary of Failure Path Calculations:

100


Path 1-1 = 221 kN , must exceed W = 59 kN or W1 = 85 kN







101

PV Elite 2015 SP2 Licensee: SPLM Licensed UserFileName : Sump pipe NPS 12 SCH 100 Nozzle Schedule : Step: 21 6:21pm Oct 2,2015

Nozzle Schedule:

Nominal Flange Noz. Wall Re-Pad Cut

Description Size Sch/Type O/Dia Thk ODia Thick Length

in. Cls in. mm mm mm mm

------------------------------------------------------------------------------

N8A 1.750 - None 1.750 8.890 - - 71.39

N8B 1.750 - None 1.750 8.890 - - 71.39

N7A 1.750 - None 1.750 8.890 - - 71.39

N7 B 1.750 - None 1.750 8.890 - - 71.39

DRAIN PIPE 1 2.000 160 None 2.375 8.738 - - 381.13

DRAIN PIPE 2 2.000 160 None 2.375 8.738 - - 381.13

DRAIN PIPE 3 2.000 160 None 2.375 8.738 - - 381.13

N12 B(2") 2.000 XXS WNF 2.37511.074 160.32 14.000 172.05

N12 A(2") 2.000 XXS WNF 2.37511.074 160.32 14.000 172.05

N6A 2.250 - None 2.25011.875 - - 82.05

N6B 2.250 - None 2.25011.875 - - 82.05

N9A 2" LLC 3.625 - None 3.62515.875 - - 107.10

N9A 2" LLC 3.625 - None 3.62515.875 - - 107.10

General Notes for the above table:

The Cut Length is the Outside Projection + Inside Projection + Drop +

In Plane Shell Thickness. This value does not include weld gaps,

nor does it account for shrinkage.

In the case of Oblique Nozzles, the Outside Diameter must

be increased. The Re-Pad WIDTH around the nozzle is calculated as follows:

Width of Pad = (Pad Outside Dia. (per above) - Nozzle Outside Dia.)/2

For hub nozzles, the thickness and diameter shown are those of the smaller

and thinner section.

Nozzle Material and Weld Fillet Leg Size Details:

102


Shl Grve Noz Shl/Pad Pad OD Pad Grve Inside

Nozzle Material Weld Weld Weld Weld Weld

mm mm mm mm mm

------------------------------------------------------------------------------

N8A SA-105 8.738 10.000 - - -

N8B SA-105 8.738 10.000 - - -

N7A SA-105 8.738 10.000 - - -

N7 B SA-105 8.738 10.000 - - -

DRAIN P SA-106 B 17.480 10.000 - - -

DRAIN P SA-106 B 17.480 10.000 - - -

DRAIN P SA-106 B 17.480 10.000 - - -

N12 B(2 SA-105 17.480 10.000 10.000 14.000 -

N12 A(2 SA-105 17.480 10.000 10.000 14.000 -

N6A SA-105 8.738 10.000 - - -

N6B SA-105 8.738 10.000 - - -

N9A 2" SA-105 15.875 10.000 - - -

N9A 2" SA-105 15.875 10.000 - - -

Note: The Outside projections below do not include the flange thickness.

Nozzle Miscellaneous Data:

Elevation/Distance Layout Projection Installed In

Nozzle From Datum Angle Outside Inside Component

mm deg. mm mm

----------------------------------------------------------------------------

N8A 543.000 0.00 50.80 0.00 SUMP PIPE 12

N8B 543.000 180.00 50.80 0.00 SUMP PIPE 12

N7A 1878.000 0.00 50.80 0.00 SUMP PIPE 12

N7 B 1878.000 180.00 50.80 0.00 SUMP PIPE 12

DRAIN PIPE 1 648.000 0.00 359.08 0.00 SUMP PIPE 12



N12 B(2") 871.000 180.00 150.00 0.00 SUMP PIPE 12

N12 A(2") 1434.000 180.00 150.00 0.00 SUMP PIPE 12

103


N6A 675.000 270.00 60.33 0.00 SUMP PIPE 12

N6B 1163.000 270.00 60.33 0.00 SUMP PIPE 12

N9A 2" LLC 0.00 85.72 0.00 PIPE CAP 12

N9A 2" LLC 0.00 85.72 0.00 PIPE CAP 12"

Note: The Description of Nozzle: N9A 2" LLC is DUPLICATED

Note: For best performance, please do not duplicate nozzle

descriptions.


104

PV Elite 2015 SP2 Licensee: SPLM Licensed UserFileName : Sump pipe NPS 12 SCH 100 Nozzle Summary : Step: 22 6:21pm Oct 2,2015

Nozzle Calculation Summary:

Description MAWP Ext MAPNC UG45 [tr] Weld Areas or

psig psig Path Stresses

---------------------------------------------------------------------------

N9A 2" LLC 1440.00 ... ... OK 8.02 OK Passed

DRAIN PIPE 1 1440.00 ... ... OK 6.42 OK NoCalc[*]



N8A 1440.00 ... ... OK 6.22 OK NoCalc[*]

N8B 1440.00 ... ... OK 6.22 OK NoCalc[*]

N12 B(2") 1440.00 ... ... OK 6.42 OK NoCalc[*]

N12 A(2") 1440.00 ... ... OK 6.42 OK NoCalc[*]

N7A 1440.00 ... ... OK 6.22 OK NoCalc[*]

N7 B 1440.00 ... ... OK 6.22 OK NoCalc[*]

N6A 1440.00 ... ... OK 6.42 OK NoCalc[*]

N6B 1440.00 ... ... OK 6.42 OK NoCalc[*]

N9A 2" LLC 1440.00 ... ... OK 8.02 OK Passed

---------------------------------------------------------------------------

Min. - Nozzles 1440.00 N9A 2" LLC

Min. Shell&Flgs 1440.00 30 40 2044.61

Computed Vessel M.A.W.P. 1440.00 psig

[*] - This was a small opening and the areas were not computed or

the MAWP of this connection could not be computed because

the longitudinal bending stress was greater than the hoop stress.

Note: MAWPs (Internal Case) shown above are at the High Point.

Check the Spatial Relationship between the Nozzles

From Node Nozzle Description X Coordinate, Layout Angle, Dia. Limit

10 N9A 2" LLC 0.000 0.000 132.650

105

PV Elite 2015 SP2 Licensee: SPLM Licensed UserFileName : Sump pipe NPS 12 SCH 100 Nozzle Summary : Step: 22 6:21pm Oct 2,2015

20 DRAIN PIPE 1 736.000 0.000 97.700

20 DRAIN PIPE 2 1235.000 0.000 97.700

20 DRAIN PIPE 3 1807.000 0.000 97.700

20 N8A 631.000 0.000 76.184

20 N8B 631.000 180.000 76.184

20 N12 B(2") 959.000 180.000 92.059

20 N12 A(2") 1522.000 180.000 92.059

20 N7A 1966.000 0.000 76.184

20 N7 B 1966.000 180.000 76.184

20 N6A 763.000 270.000 88.884

20 N6B 1251.000 270.000 88.884

30 N9A 2" LLC 0.000 0.000 132.650

The nozzle spacing is computed by the following:

= Sqrt( ll² + lc² ) where

ll - Arc length along the inside vessel surface in the long. direction.

lc - Arc length along the inside vessel surface in the circ. direction

If any interferences/violations are found, they will be noted below.

No interference violations have been detected !


106

PV Elite 2015 SP2 Licensee: SPLM Licensed UserFileName : Sump pipe NPS 12 SCH 100 MDMT Summary : Step: 23 6:21pm Oct 2,2015

Minimum Design Metal Temperature Results Summary :

Curve Basic Reduced UG-20(f) Thickness Gov E*

Description MDMT MDMT MDMT ratio Thk

Notes °F °F °F mm

----------------------------------------------------------------------------

PIPE CAP 12 "[10] B 11 -4 0.842 17.480 1.000

PIPE CAP 12 " [7] B 11 2 0.903 17.480 1.000

SUMP PIPE 12" [8] B 16 -2 0.824 18.867 1.000

PIPE CAP 12" [10] B 11 -4 0.842 17.480 1.000

PIPE CAP 12" S[7] B 11 2 0.903 17.480 1.000

N9A 2" LLC [1] B 6 -134 0.250 15.875 1.000

DRAIN PIPE 1 [1] B -20 -55 0.466 7.645 1.000

DRAIN PIPE 2 [1] B -20 -55 0.466 7.645 1.000

DRAIN PIPE 3 [1] B -20 -55 0.466 7.645 1.000

N8A [1] B -20 -155 0.264 8.890 1.000

N8B [1] B -20 -155 0.264 8.890 1.000

N12 B(2") [1] B -1 -18 0.824 14.000 1.000

Nozzle Flg [4] -20 -155 0.316

N12 A(2") [1] B -1 -18 0.824 14.000 1.000

Nozzle Flg [4] -20 -155 0.316

N7A [1] B -20 -155 0.264 8.890 1.000

N7 B [1] B -20 -155 0.264 8.890 1.000

N6A [1] B -10 -150 0.225 11.875 1.000

N6B [1] B -10 -150 0.225 11.875 1.000

N9A 2" LLC [1] B 6 -134 0.250 15.875 1.000

----------------------------------------------------------------------------

Required Minimum Design Metal Temperature 32 °F

Warmest Computed Minimum Design Metal Temperature 2 °F

Notes:

[ ! ] - This was an impact tested material.

[ 1] - Governing Nozzle Weld.

[ 4] - ANSI Flange MDMT Calcs; Thickness ratio per UCS-66(b)(1)(c).

107

PV Elite 2015 SP2 Licensee: SPLM Licensed UserFileName : Sump pipe NPS 12 SCH 100 MDMT Summary : Step: 23 6:21pm Oct 2,2015

[ 5] - ANSI Flange MDMT Calcs; Thickness ratio per UCS-66(b)(1)(b).

[ 6] - MDMT Calculations at the Shell/Head Joint.

[ 7] - MDMT Calculations for the Straight Flange.

[ 8] - Cylinder/Cone/Flange Junction MDMT.

[ 9] - Calculations in the Spherical Portion of the Head.

[10] - Calculations in the Knuckle Portion of the Head.

[11] - Calculated (Body Flange) Flange MDMT.

[12] - Calculated Flat Head MDMT per UCS-66.3

[13] - Tubesheet MDMT, shell side, if applicable

[14] - Tubesheet MDMT, tube side, if applicable

[15] - Nozzle Material

[16] - Shell or Head Material

UG-84(b)(2) was not considered.

UCS-66(g) was not considered.

UCS-66(i) was not considered.

Notes:

Impact test temps were not entered in and not considered in the analysis.

UCS-66(i) applies to impact tested materials not by specification and

UCS-66(g) applies to materials impact tested per UG-84.1 General Note (c).

The Basic MDMT includes the (30F) PWHT credit if applicable.


108

PV Elite 2015 SP2 Licensee: SPLM Licensed UserFileName : Sump pipe NPS 12 SCH 100 Vessel Design Summary : Step: 24 6:21pm Oct 2,2015

ASME Code, Section VIII, Division 1, 2013

Diameter Spec : 288.890 mm ID

Vessel Design Length, Tangent to Tangent 2614.00 mm

Specified Datum Line Distance 88.00 mm


Head Material SA-234 WPB

Nozzle Material SA-105

Nozzle Material SA-106 B

Re-Pad Material SA-106 B

Internal Design Temperature 170 °F

Internal Design Pressure 1440.000 psig

External Design Temperature 0 °F

Maximum Allowable Working Pressure 1440.000 psig

Hydrostatic Test Pressure 2160.000 psig

Required Minimum Design Metal Temperature 32 °F

Warmest Computed Minimum Design Metal Temperature 2 °F

Wind Design Code ASCE-93

Earthquake Design Code UBC-94

Element Pressures and MAWP: psig

Element Desc | Design Pres. | External | M.A.W.P | Corrosion

| + Stat. head | Pressure | | Allowance

---------------------------------------------------------------------

PIPE CAP 12 " SCH 80 1440.415 0.000 1585.464 3.0000

SUMP PIPE 12" SCH 100 1440.415 0.000 1728.112 3.0000

PIPE CAP 12" SCH 80 1440.415 0.000 1585.464 3.0000

109

PV Elite 2015 SP2 Licensee: SPLM Licensed UserFileName : Sump pipe NPS 12 SCH 100 Vessel Design Summary : Step: 24 6:21pm Oct 2,2015

Liquid Level: 288.89 mm Dens.: 999.542 kg/m³ Sp. Gr.: 1.000

Element "To" Elev Length Element Thk R e q d T h k Joint Eff

Type mm mm mm Int. Ext. Long Circ

-----------------------------------------------------------------------

Ellipse 0.0 88.0 17.5 15.2 4.5 1.00 1.00

Cylinder 2438.0 2438.0 21.4 16.1 No Calc 1.00 1.00

Ellipse 2526.0 88.0 17.5 15.2 4.5 1.00 1.00

Element thicknesses are shown as Nominal if specified, otherwise are Minimum

Weights:

Fabricated - Bare W/O Removable Internals 515.4 kgm

Shop Test - Fabricated + Water ( Full ) 693.0 kgm

Shipping - Fab. + Rem. Intls.+ Shipping App. 515.4 kgm

Erected - Fab. + Rem. Intls.+ Insul. (etc) 515.4 kgm

Empty - Fab. + Intls. + Details + Wghts. 515.4 kgm

Operating - Empty + Operating Liquid (No CA) 693.0 kgm

Field Test - Empty Weight + Water (Full) 693.0 kgm


110

sump pipe nps 12 sch 100

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