ethyl acetate rev a

8/10/2019 Ethyl Acetate Rev A

1/33

Tebodin Consultants & Engineers India P Ltd. PUMP CALCULATION BASIC PUMP DATA

'()*+ -en.el P&P )*& +s# P%805 / ev ate escription '.6d

(')+ Pne, &aarastra +# P&P9 2 2"%&a%14 )ssed for pproval P

+) (iofol & 2

+) +# )+*

9*V)'* *tl cetate

Pr;ct +ame: ) *tl cetate P&P (?: 331 "4= 1,040 P @ 9P

Pmping emp, A +&( =8 &B)&& 104 P&P (?: 15 44 4" % MP&P (? )+


2/33

Tebodin Consultants & Engineers India P Ltd. PUMP CALCULATION SEET

'()*+ -en.el P&P )*& +s# P%805 / ev ate escription ppv

(')+ Pne, &aarastra +# P&P9 2 2"%&a%14 )ssed for pproval P

+) (iofol & 2 0 0 0 0 0

+) +# 0 )+* 0 0 0 0 0 0

9*V)'* *tl cetate 0 0 0 0 0

Pr;ct +ame: 6 G 2

()>) *tl cetate #9#


3/33

Chris Stuecheli:

Use this for all new designsS65:

Chris Stuecheli:

For Revamp onlyWill calcualte shut in with normal suction and pump shutin

T65:

Chris Stuecheli:

For revamp onlyUse this for max suction pressure at specied ow (typically at turndown)

U65:


4/33

TEBODIN CONSULTANTS & EN)INEE#S INDIA P-T. LTD.

PUMP S6STEM D#A$IN)

P&P +# P%805 /* 2"%&a%14

D P

'()*+ -en.el

+) (iofol

+# =200=

+) +# 0

9*V)'* *tl cetate

*V# +#

'-T6

T!"#

Recir

A B C D E F G H I J K

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# $

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6/33

Page = of 33Printed: 12/25/2014, 05:08:42

Version: 20110517file:///var/www/apps/conversion/tmp/scratc!1/2555"0722#$ls%9T*'-%Vert

TEBODIN CONSULTANTS ev ate escription '.6d

& EN)INEE#S INDIA 6D#AULIC CI#CUIT S'ETC A 78989+;< Issued 1or A!!ro"al AP A=T

P-T. LTD. + + + + +

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P# +#: 9++

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6file:///var/www/apps/conversion/tmp/scratc!1/2555"0722#$ls6QU9T*'-%Vert


7/33

Tebodin Consultants & Engineers India P"t. Ltd.

P&P +# P%805 /, oEQ: =200=

(ine 9eg# +ame ow

(ine 9eg PI)

Pipe 9pec / (engt asis

9imlation 9tream +ame Q 1

(ine 9egment 9tart an. Pmp iscarge 9plit1

(ine 9egment *nd Pmp 9ction 9plit1 9plit2

()+* 9)*, )+'- / 9'- / ), )+'- 3 std 3#0=8 3 std 3#0=8 3 std

0#00015 1#2 0#0173 0#00015 1#2 0#0173 0#00015 1#

(P *)+))+ M9,,,',,*,N 9

&)+ +& * &)+ +& * &)+ +&

(? (? (? (? (? (? (? (?

P9*& P*99* psig 0#0 0#0 0#0 73#7 =0#7 57#7 QV(*R QV(*

?+9*& P*99* psig QV(*R QV(*R QV(*R QV(*R QV(*R QV(*R QV(*R QV(*

*&P** deg "5 "5 "5 "5 "5 "5 "5 "5

()>) (? *, ) 9P# ) 9P#) 9'* *+9)+ dne/cm2 0#00 0#00 0#00 0#00 0#00

VP (? *, '& QV(*

lE/r 0 0 0 0 0

VP *+9)D, lE/ftW 0#0000 0#0000 0#0000 0#0000 0#0000 0#0000 0#0000 QV(*

VP V)9'9)D, cP 0#00000 0#00000 0#00000 0#00000 0#00000

VP &(*'( ? 0#000 0#000 0#000 0#000 0#000

VP '&P*99))()D ' 0#0000 0#0000 0#0000 0#0000 0#0000

ensit % )n%Place lE/ftW

ensit % -omogenos M&i$edN lE/ftW

P*99* P/1006 psi QV(*R QV(*R QV(*R QV(*R QV(*R QV(*R QV(*R QV(*

()>) *D+(9 +&*

2%P enolds +mEer QV(*R QV(*R QV(*R QV(*R QV(*R QV(*R QV(*R QV(*

V*)V(*+ '('()+ 0 0 0

))+


8/33

Chris Stuecheli:

This formula can -e used with the simulation stream num-er in row , and the row index in column d to loo.up values from the raw wor.sheet/ Formula ca0ay need to update ta-le si1e to your simulation data

F18:

Chris Stuecheli:This formula can -e used with the simulation stream num-er in row , and the row index in column d to loo.up values from the raw wor.sheet/ Formula ca0ay need to update ta-le si1e to your simulation data

F23:

Chris Stuecheli:


F24:

Chris Stuecheli:


F25:

cdstuec:

ocated at lower elevationI55:

cdstuec:

2iesel day tan. is m a-ove grade and * m 3

L55:


9/33

Page " of 33Printed: 12/25/2014, 05:08:42

Version: 20110517file:///var/www/apps/conversion/tmp/scratc!1/2555"0722#$ls%&-P ata 9t

R TEBODIN CONSULTANTS CENT#I(U)AL PUMP *V * *9')P)+ D PPV# 9-** 1 1

4 & EN)INEE#S INDIA P#OCESS DATA SEET A 9/Ma3/;< Issued 1or A!!ro"al AP A=T 9P*'# +#:

5 P-T. LTD. P# +#: 9++

'()*+: en>el

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+*: PP()'(* )+>)D MB N P'-9* M N 9 )( M N

1 SE#-ICE: DE) T#ANS(E# PUMP ITEM NO.: P/?+7 A8B

2 P&P9 P** )+ MP((*(N ; +# & )V*+ ; +# )+* )V*+

3 M9*)*9N ?)- P&P )*& +# P&P )*& +#

4


10/33

Page 10 of 33Printed: 12/25/2014, 05:08:42

Version: 20100"2file:///var/www/apps/conversion/tmp/scratc!1/2555"0722#$ls%aw

'ase :YPro;ectsY1 :YPro;ectsY1 :YPro;ectsY1 :YPro;ectsY1 :YPro;ectsY1 :YPro;ectsY1 :YPro;ectsY1 :YPro;ectsY1 :YPro;ectsY1

lowseet 'ase M&ainN 'ase M&ainN 'ase M&ainN 'ase M&ainN 'ase M&ainN 'ase M&ainN 'ase M&ainN 'ase M&ainN 'ase M&ainN

9tream 1 2 3 4 = 8 " 12 1"

Pase Propert 'omponent nit

(aEel OOOOOOOOOO efiner 9tream 9mmar OOOOOOOOOOO

verall +ame KnoneJ 1 2 3 4 = 8 " 12 1"

verall Vapor raction KnoneJ 0 1 1 0 1 1 1 1 0

verall emperatre 144#54175=4 205#8540178 510 140 205#7824481 205#7824481 510 =00 134#3"183=1

verall Pressre psig 832#""134=2 808#004 ="=#104 17#004 75"#004 75"#004 ="=#104 =2"#=04 =80#5182882verall &olar low lEmole/r =821#0144"3 4774#1 57"7#55724= =821#0144"3 2387#05 2387#05 57"7#55724= 11=1=#88174 140"#317702

verall &ass low lE/r =8753"#8837 23=13#7"522 35557=#83"5 =8753"#8837 1180=#8"7=1 1180=#8"7=1 35557=#83"5 711"22#"1"5 2538"

verall 9tandard )deal (iFid Volme low Earrel/da ==000 10=78#="348 3833"#34=74 ==000 533"#34=738 533"#34=738 3833"#34=74 7=84=#"3544 1741#"=4"47

verall &oleclar ?eigt KnoneJ 100#7"73058 4#"4=22"702 =1#33218257 100#7"73058 4#"4=22"702 4#"4=22"702 =1#33218257 =1#28347827 18#01510048

verall -eat low t/r %572=78457 %14252"57#1 %183250=43 %5757"385" %712=478#54 %712=478#54 %183250=43 %321338885 %1718730=7

verall &olar *ntalp t/lEmole %83"57#114= %2"85#44515 %31=07#"32= %84413#8458 %2"85#44515 %2"85#44515 %31=07#"32= %27==1#0"35 %121"53#57"

verall &ass -eat 'apacit t/lE% 0#525188434 1#5"573130" 0#7113"8=55 0#5274324"5 1#5"43""335 1#5"43""335 0#7113"8=55 0#724041"1" 1#0317=007=

verall &ass ensit lE/ft3 42#5"74=783 0#5=01"=803 5#1811"=04 42#28437423 0#5274=0248 0#5274=0248 5#1811"=04 3#"45312342 =1#45"4"312

verall ?atson T KnoneJ 12#223242= 2=#"3387"5 12#25=82301 12#223242= 2=#"3387"5 2=#"3387"5 12#25=82301 12#27153"1= KemptJ

(aEel OOOOOOO Vapor OOOOOOOO

Vapor &olar low lEmole/r %%% 4774#1 57"7#55724= %%% 2387#05 2387#05 57"7#55724= 11=1=#88174 %%%

Vapor &ass low lE/r %%% 23=13#7"522 35557=#83"5 %%% 1180=#8"7=1 1180=#8"7=1 35557=#83"5 711"22#"1"5 %%%

Vapor -eat low t/r %%% %14252"57#1 %183250=43 %%% %712=478#54 %712=478#54 %183250=43 %321338885 %%%

Vapor ctal Volme low Earrel/da %%% 18018=#7548 2"33=0#1=22 %%% "5=84#"7744 "5=84#"7744 2"33=0#1=22 77134=#08=2 %%%

Vapor &ass ensit lE/ft3 %%% 0#5=01"=803 5#1811"=04 %%% 0#5274=0248 0#5274=0248 5#1811"=04 3#"45312342 %%%

Vapor 'ompressiEilit KnoneJ %%% 1#017081387 0#80858585" %%% 1#015"78232 1#015"78232 0#80858585" 0#88008333 %%%

Vapor ermal 'ondctivit t/r%ft% %%% 0#1021"8=41 0#04181353" %%% 0#1020"4005 0#1020"4005 0#04181353" 0#04520""2" %%%

Vapor Viscosit cP %%% 0#0114801=" 0#021=4583 %%% 0#0114==871 0#0114==871 0#021=4583 0#02221"458 %%%

Vapor &olar low lEmole/r %%% 4774#1 57"7#55724= %%% 2387#05 2387#05 57"7#55724= 11=1=#88174 %%%

(aEel OOOOOOO (iFid OOOOOOOO

(igt (iFid &olar low lEmole/r =821#0144"3 %%% %%% =821#0144"3 %%% %%% %%% %%% %%%

(igt (iFid &ass low lE/r =8753"#8837 %%% %%% =8753"#8837 %%% %%% %%% %%% %%%

(igt (iFid &oleclar ?eigt KnoneJ 100#7"73058 %%% %%% 100#7"73058 %%% %%% %%% %%% %%%

(igt (iFid -eat low t/r %572=78457 %%% %%% %5757"385" %%% %%% %%% %%% %%%

(igt (iFid &ass -eat 'apacit t/lE% 0#525188434 %%% %%% 0#5274324"5 %%% %%% %%% %%% %%%

(igt (iFid 9tandard )deal (iFid Volme low Earrel/da ==000 %%% %%% ==000 %%% %%% %%% %%% %%%

(igt (iFid &ass ensit lE/ft3 42#5"74=783 %%% %%% 42#28437423 %%% %%% %%% %%% %%%

(igt (iFid ermal 'ondctivit t/r%ft% 0#0=321"==" %%% %%% 0#0=3=11251 %%% %%% %%% %%% %%%

(igt (iFid Viscosit cP 0#2""157853 %%% %%% 0#30382""4= %%% %%% %%% %%% %%%(igt (iFid 9rface ension dne/cm 1=#435"534" %%% %%% 1=#=8304""4 %%% %%% %%% %%% %%%

(igt (iFid ctal Volme low Earrel/da =8""4#07703 %%% %%% ="504#"41"= %%% %%% %%% %%% %%%

(aEel OOOOOOO Feos (iFid OOOOOOOO

-eav (iFid &olar low lEmole/r %%% %%% %%% %%% %%% %%% %%% %%% 140"#317702

-eav (iFid &ass low lE/r %%% %%% %%% %%% %%% %%% %%% %%% 2538"

-eav (iFid 9tandard )deal (iFid Volme low Earrel/da %%% %%% %%% %%% %%% %%% %%% %%% 1741#"=4"47

-eav (iFid -eat low t/r %%% %%% %%% %%% %%% %%% %%% %%% %1718730=7

A B C D E F G H I J K L M

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:YPro;ectsY1 :YPro;ectsY1 :YPro;ectsY1 :YPro;ectsY1 :YPro;ectsY1 :YPro;ectsY1 :YPro;ectsY1 :YPro;ectsY1 :YPro;ectsY1 :YPro;ectsY1 :YPro;ectsY1 :YPro;ectsY1 :YPro;ectsY1 :YPro;ectsY1

'ase M&ainN 'ase M&ainN 'ase M&ainN 'ase M&ainN 'ase M&ainN 'ase M&ainN 'ase M&ainN 'ase M&ainN 'ase M&ainN 'ase M&ainN 'ase M&ainN 'ase M&ainN 'ase M&ainN 'ase M&ainN

20 25 2= 27 35 38 41 42 43 44 4= 47 48 4"

20 25 2= 27 35 38 41 42 43 44 4= 47 48 4"

0 1 0 0 0 1 1 0#3=5554="" 1 0 1 0 0 0

134#5745802 14=#==0"323 14=#==0"323 14=#==0"323 304#7553201 54=#075030= 14=#= 14=#==0"323 14=#= 14=#==8"443 123 123 123 124#412512=

=10#504 5"=#504 5"=#504 5"=#504 174#824048" =4=#104 5"=#504 5"=#504 5"=#504 5"=#504 18"#4=4 18"#4=4 18"#4=4 318#03=855=140"#317702 4"4=#35"187 71"2#440175 13"2#30=12= 13150#"2812 114=0#"8171 18#5=708703 13531#1054" 0#04="75"23 13"2#400078 452#=4"5511 3502#50"1=7 12#25744075 3502#50"1=7

2538" 244=5#82873 ="0=1"#51=5 25081#13255 1447358#52 711153#7728 =32#="20=17 7401==#4778 1#=007515= 25083#53331 10735#185"3 220513#=72= 220#8=4545= 220513#=72=

1741#"=4"47 110=4#00234 =700=#"3145 1721#184313 1351="#47"2 7=4"8#47387 54#"48"78"5 7"7"2#11811 0#13"024447 1721#412253 17"8#8=5002 25247#01012 15#155"8275 25247#01012

18#01510048 4#"4=22"702 "=#0201"=17 18#0140"337 110#05751" =2#04""875= 34#07=00021 54#70110"12 34#07=00021 18#014=020= 23#71=32"5= =2#"58771 18#01881404 =2#"58771

%1718730=7 %170427=3#3 %577712582 %1="45=711 %10277=7204 %34"47337" %1="003#13= %7=421205= %427#5887"2 %1="458418 %10=47145#7 %231337==7 %14"7373#11 %231122554

%121"53#57" %3445#4820= %80321#38=8 %121708#152 %78150#8""7 %304"2#1403 %"102#2051" %5=477#=003 %"102#2051" %121701#1== %23521#5"31 %==048#4=0" %12215"#10" %=5"87#0445

1#031"520"7 1#5713==287 0#5337520" 1#033524483 0#=287"583 0#71202"131 0#383388712 0#584"8508" 0#383388712 1#0334"15"" 0#57744"528 0#=00"82=58 1#0314=1=03 0#5"88"1551

=1#4442=833 0#45"2=008= 41#75238174 =1#101874 38#08327102 4#51"14=1=4 4#513=71702 10#54013"37 4#513=71702 =1#0""885=5 0#8104158=4 35#114=7751 =1#=88=833 35#17574774

KemptJ 2=#"3387"5 12#23171=84 14#0"=57114 12#08543=71 12#2=51387= "#2030027=5 12#3003=11= "#2030027=5 12#4783743" 15#3"2287"7 13#32758521 "#3=7"01387 13#32758521

%%% 4"4=#35"187 0 0 %%% 114=0#"8171 18#5=708703 4"4=#35"187 0#04="75"23 %%% 452#=4"5511 0 0 %%%

%%% 244=5#82873 0 0 %%% 711153#7728 =32#="20=17 244=5#82873 1#=007515= %%% 10735#185"3 0 0 %%%

%%% %170427=3#3 0 0 %%% %34"47337" %1="003#13= %170427=3#3 %427#5887"2 %%% %10=47145#7 0 0 %%%

%%% 227718#8202 0 0 %%% =72=74#28== 5""#183870= 227718#8202 1#515"73=84 %%% 5==23#842 0 0 %%%

%%% 0#45"2=008= 0#45"2=008= 0#45"2=008= %%% 4#51"14=1=4 4#513=71702 0#45"2=008= 4#513=71702 %%% 0#8104158=4 0#8104158=4 0#8104158=4 %%%

%%% 1#011=5745= 1#011=5745= 1#011=5745= %%% 0#840=432=3 0#70"218733 1#011=5745= 0#70"218733 %%% 0#"55502503 0#"55502503 0#"55502503 %%%

%%% 0#0"47=004 0#0"47=004 0#0"47=004 %%% 0#042382544 0#0135428"1 0#0"47=004 0#0135428"1 %%% 0#03788783" 0#03788783" 0#03788783" %%%

%%% 0#010=21342 0#010=21342 0#010=21342 %%% 0#02151133= 0#0152==727 0#010=21342 0#0152==727 %%% 0#013=117"" 0#013=117"" 0#013=117"" %%%

%%% 4"4=#35"187 0 0 %%% 114=0#"8171 18#5=708703 4"4=#35"187 0#04="75"23 %%% 452#=4"5511 0 0 %%%

%%% 0 71"2#440175 0 13150#"2812 %%% %%% 71"2#440175 %%% %%% 0 3502#50"1=7 0 3502#50"1=7

%%% 0 ="0=1"#51=5 0 1447358#52 %%% %%% ="0=1"#51=5 %%% %%% 0 220513#=72= 0 220513#=72=

%%% "=#0201"=17 "=#0201"=17 "=#0201"=17 110#05751" %%% %%% "=#0201"=17 %%% %%% =2#"58771 =2#"58771 =2#"58771 =2#"58771

%%% 0 %577712582 0 %10277=7204 %%% %%% %577712582 %%% %%% 0 %231337==7 0 %231122554

%%% 0#5337520" 0#5337520" 0#5337520" 0#=287"583 %%% %%% 0#5337520" %%% %%% 0#=00"82=58 0#=00"82=58 0#=00"82=58 0#5"88"1551

%%% 0 =700=#"3145 0 1351="#47"2 %%% %%% =700=#"3145 %%% %%% 0 25247#01012 0 25247#01012

%%% 41#75238174 41#75238174 41#75238174 38#08327102 %%% %%% 41#75238174 %%% %%% 35#114=7751 35#114=7751 35#114=7751 35#17574774

%%% 0#0=0513502 0#0=0513502 0#0=0513502 0#05248"008 %%% %%% 0#0=0513502 %%% %%% 0#051343118 0#051343118 0#051343118 0#0511"3807

%%% 0#2773=7717 0#2773=7717 0#2773=7717 0#1=3240788 %%% %%% 0#2773=7717 %%% %%% 0#14474"277 0#14474"277 0#14474"277 0#1442""73"%%% 15#=1140201 15#=1140201 15#=1140201 "#"37"82158 %%% %%% 15#=1140201 %%% %%% 10#052=7031 10#052=7031 10#052=7031 "#"723"07"1

%%% 0 70705#84047 0 1=2457#4287 %%% %%% 70705#84047 %%% %%% 0 2=843#8333" 0 2=7"7#22858

140"#317702 0 0 13"2#30=12= %%% %%% %%% 13"2#30=12= %%% 13"2#400078 0 0 12#25744075 %%%

2538" 0 0 25081#13255 %%% %%% %%% 25081#13255 %%% 25083#53331 0 0 220#8=4545= %%%

1741#"=4"47 0 0 1721#184313 %%% %%% %%% 1721#184313 %%% 1721#412253 0 0 15#155"8275 %%%

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N O P Q R S T U ! " # $ AA

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Page 12 of 33Printed: 12/25/2014, 05:08:42




50 51 52 =1 =3 =4 =5 =7 70 71 7" 82 83 84

50 51 52 =1 =3 =4 =5 =7 70 71 7" 82 83 84

0 0 0 1 1 0 0 1 0 1 0 0 0 0

124#412512= 124#412512= 174#7355"54 205#8540178 5"0 133 102#3 103#"8"1047 103#"8"1047 238#701542" 418#"742785 304#8=72372 304#8=17383 41"#02="=25

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f101 otlet 102otlet f102pass f102rest 201 otlet 201Pass 201rest el


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* 1%1"%11#-9'E" E#

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Version: 20100"23file:///var/www/apps/conversion/tmp/scratc!1/2555"0722#$ls%)nstrctions

Reducer angle override, give source

Equivalent lengths are from Crane Technical Paper 410 Reprinted 12/2001

In the line size / sch set of cells. If you want to manually enter a line size just u

leave the sch cell blank and enter an exact value for ID in the line size cell

1) Note on the K factor

K = fT * (L/D) Eqn 2-4 page 2-8 12/01 Reprint

The L/D is tabulated in Crane appendix A-30 for fully tubulent conditions.

This means that the friction factor is at fully turbulent conditions. In our

pump calculation template, the fully tubulent friction factor is called fT.

Note that the fully turbulent f is always less than the non-fully turbulent f.

This means that the K factor for a given fitting will always be higher for

fully turbulent conditions than for transitional turbulent conditions.

Our pump calc template uses the L/D corresponding to fully turbulent conditions

because this number is only somewhat higher for most of the applications we

will encounter. It is conservative, but not overly conservative for the

majority of the applications we will encounter.

However, in some applications, with very low reynold's numbers, the difference

between using the fully turbulent and transitional region L/D values is very

significant, and using the fully turbulent friction factor is overly

conservative. In this case the user has the option of using the actual

friction factor to calculate the equivalent feet. The user does this by

selecting option "2" on the main page to use the actual friction factor. When

So if the flag on the "Main" worksheet is set to "2", the L/D value will be

prorated by the ratio of the friction factors which will reduce the L/D value

used to calcuate fitting equivalent length

See prose section of crane page 2.8.

A B C D E F G H I J

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29/33

Page 2" of 33Printed: 12/25/2014, 05:08:42


aEle from 'rane Page %2= 25t printing 1""1, 'oprigt 1"88

+ominal e f f ) f f C el *rror

9iHerogness aEle 9cd 409 9cd 'rve it rane %27

0#3 0#5 1 9* inces ft ier version inted 4/10 inces inted 4/10

0#800 0#878 1#000 1 0#5 0#00015 0#027 0#2=0 0#=22 0#025"0 0#025"0

0#700 0#810 1#000 2 0#75 0#00015 0#025 0#024 0#824 0#023"8 0#023"8

0#=40 0#770 1#000 3 1 0#00015 0#023 0#022 1#04" 0#0224" 0#0224"

0#58= 0#741 1#000 4 1#25 0#00015 0#022 0#021 1#38 0#020"7 0#020"7

0#585 0#740 1#000 5 1#5 0#00015 0#021 0#020 1#=1 0#02018 0#02018

0#540 0#700 1#000 = 2 0#00015 0#01" 0#01" 2#0=7 0#018"" 0#018""

0#4"0 0#==0 1#000 7 2#5 0#00015 0#018 0#018 2#4=" 0#01821 0#01821

0#440 0#=20 1#000 8 3 0#00015 0#018 0#017 3#0=8 0#01731 0#01731

0#3"0 0#5"0 1#000 " 4 0#00015 0#017 0#01= 4#02= 0#01=2" 0#01=2"

0#315 0#510 1#000 10 5 0#00015 0#01= 0#015 5#047 0#01550 0#01550

0#300 0#500 1#000 11 = 0#00015 0#015 0#015 =#0=5 0#014"0 0#014"0

13 14 15 1= 8 0#00015 0#014 0#014 8#125 0#01402 0#01402

10 0#00015 0#014 0#013 10#02 0#01343 0#01343

12 0#00015 0#013 0#013 12 0#012"= 0#012"=

14 0#00015 0#013 0#013 13#25 0#01271 0#01271

1= 0#00015 0#013 0#012 15#25 0#01237 0#01237

18 0#00015 0#012 0#012 17#25 0#01208 0#0120820 0#00015 0#012 0#015 Q)V/0R Q)V/0R

22 0#00015 0#012 0#012 Q)V/0R Q)V/0R

24 0#00015 0#012 0#011 Q)V/0R Q)V/0R

3= 0#00015 0#011 Q)V/0R Q)V/0R

" ) 8 , ! *" *) *8 *, *! )"

"/"*

"/"*)

"/"*8

"/"*,

"/"*!

"/")

"/"))

"/")8

"/"),

"/")!fT vs 7T2 7chedule


30/33

Page 30 of 33Printed: 12/25/2014, 05:08:43


The %, ta-le is -ased on nominaldiameter and the curve t this exceltemplate uses is -ased on actualinside diameter/ 'ased on the twographs -elow= it is evident that eventhough these are not totallyconsistent= using the curve t

matches reasona-ly well with the fT-ased on >2 when the nominaldiameters are correlated to 7T2schedule actual inside diameters/

%nd in fact= it is li.ely that theactual fT pro-a-ly decreasesincrementally and continuouslyacross the range of diameters/ The


31/33

Page 31 of 33Printed: 12/25/2014, 05:08:43

Version: 20100"23file:///var/www/apps/conversion/tmp/scratc!1/2555"0722#$ls%+otes

#e"ision istor3

ev ate escription

15 g "7 % 'onverted from >attro Pro to *$cel M& pdateN

1= 24 9ep "7 % dded a warning for loop definition M& pdateN

17 1= ec "7 % 'anged fitting T factors to agree wit 'rane MP# 9ainN

dded two entries to pipe ) taEle

'orrected flowmeter calclation on pmp sction

'ommented ot LprintFalitL statement from te Pagesetp sE rotine on te &odle1 seet18 an "8 % general revision: corrections to formlas in certain cells

) for fittins is for same scedle as pipe

1" ct "" dded 3 more allowaEle stream identifiers and one more sction line identifier#

dded two pase flow regime indicator to spreadseet#

dded te aEilit to inpt &in, +orm and &a$ destination pressres#

&odified ctal Pmp 'rve inpt so as rated flow canges pmp crve does not cange#

&odified 9.etc so eiter ated or +ormal flow conditions are sown#

20 1%9ep evised E +#Patel I ;#price#

dded a prorate pmp crve taEle to atomaticall prorate an e$isting crve p to a larger impeller M+P / PN#

dded te P) =10 stoff ead factors as a formla and inclded in te stoff pressre calc#

dded te normal P9 flow as an independent variaEle in calclating te pmp flow#

o not insert an rows or colmns anwere in te templateR

21 8%&ar%02 &igliavacca dded more colmns to te spreadseet

22 1=%&ar%02 i$ed error wit te static ead smmation in te L&ainL ?.seet

9preadseet assmed static ead was constatn for min ma$ and nomr flow# )t is

not wen te streams are two pase Eecase inplace densit canges#

23 2=%ec # &igliavacca i$ed error wit cell +13 on te &ain wor.seet tat cased te an LL stream control valve calclation to malfnction

24 2=%ec

25 ct%1%03

2= 10/12/2004

27 10/12/2004

28 &ar%15%05 i$ed error in s.etc taEle second colmn# e destination row formla was misreferenced#

2" &ar%15%05

30 &ar%15%05


32/33

Page 32 of 33Printed: 12/25/2014, 05:08:43

Version: 20100"23file:///var/www/apps/conversion/tmp/scratc!1/2555"0722#$ls%+otes

44

&ar%12%0" &&

45

&ar%30%0" &&

4=

&ar%31%0" &&

47pr%17%0" &&

48

&a%04%0" &&

4"

l%23%0" &&

50l%31%0" &&

51

ec%30%0" &&

52

an%=%10 &&

53

eE%1"%10 &&

54

eE%22%10 &&

54

eE%25%10 &&

1N dded cells on main page to pll 'p2N dded mltiple scenario st in eads

aN +o flow, ma$ inlet pressre EN +o flow, normal inlet pressre cN &in flow M45C of ratedN, ma$ inlet pressre3N dded macro, macro Etton and paste special region in nprinted portion of wor.seet to pic. p calclated nmEers and pastedtem as vales onl#4N emoved te w/ot safet on te +P9- cells in te 9 and ? smmaries in te main wor.seet#

-)9 +**9 * '-*'T*

1N dded LP*'L field on L&ainL wor.seet so tat te pmp data seet does not print te contents of te L9*V)'*L field wereit is as.ing for pro;ect field#

1N 'anged te wa P at 9P is calclated for min and ma$ rates# Previosl it was calclated E prorating from te pmp flowson te main wor.seet# -owever, if ser decides to overwrite mass rates in eac individal lines segment, te Epd at std wont cangeappropriatel# 9o for te min and ma$ P at 9P ) directl recalclate Eased on te lE/r in te segment and te two spgr6s#

2N lso canged te formla in te P at P row to se L=2#37O7#481/42O24L instead of 14#575 factor#

1N pdated version nmEer to 0417200"2N dded note to data seet aEot limiting ead rise to BBBC of rated ead3N deleted L&a$L on te improved discarge pressre calclation in several rows#

1N canged s.etc title to Ldralic circitL so tat it is general for all dralic calcs2N dded oter title Eloc. into to s.etc3N pdated version nmEer to 0504200"4N eformatted lines to sow 4 lines per printed letter siHe seet#5N dded row to e$plicitel sow )n%Place densit rigt aEove &i$ed MomogenosN densit=N 'anged te L)n%Place densit sed for static eadL row in te static ead comptation section in te lines wor.seet to readLensit sed for static eadL# ) did tis E/c sometimes Mtermospon calcsN o need to se omogenos wit 1#5 safet factor#

1N canged te eader Ears and revision taEle2N -ad to add rows to te main wor.seet to affect te revision taEle cange# is meant ) ad to revise macro to pll new differentrange#3N dded T G M(/N O f to fitting (/ vales to clarif wat is Eeing calclated#4N dded notes 2 and 3 on &*' data seet#5N 'anged te LdefaltL in note one on te second page of te main page to te actal ead rise nmEer as entered on te first page

of te main wor.seet#=N pdated version nmEer in footer#

1N 'anged page Erea.s in LaElesL wor.seet2N pdated all footers

1N emoved te LO fL for te entrance and e$its on te pipe fittings on te lines wor.seet# T is simpl 1 and 0#5 % not a fnction of f#e eFations were left ncanged# e were not in error % ;st te description2N pdated all footers3N dded comparison graps in te LaElesL wor.seet discssing accrac of f crve fit as sed in te top of te L(inesL wor. foreac line segment#4N 'anged f to f

to clarif wat te smEol was#

5N dded interpolatefor fnction to te stin pressre ead calclation to calclate an interpolated pmp ead Eased on a ser inpt

flowrate Msa commonl sed for a trndown flow rateN#=N eleted te stin conditions on te first page of te main wor.seet and moved te corresponding stin parameters to tesecond page of te L&ainL wor.seet#7N 'anged crve cart tpe sape to point to point instead of smoot line# )f it is set to crve line, te operating points loo. li.e tedont fall on te pmp crve sometimes depending on te crvatre of te pmp crve#8N 9everal of te line segments ave corrpted eFations for fitting lengts# e ad LrefRL errors were cell references sold aveEeen# ese were not readil identified nless te ser entered a nmEer for te fitting cont for tose few pariclar fittings and tennoticed tat te reslting eFivalent feet was Hero# ese ave Eeen f i$ed E coping te fittings Mall fittings e$cept entrance/e$itlosses and redcersN from te first line segment to all line segments#"N Elan. on prpose10N emoved spaces in te nits on te L(inesL spreadseet11N 'orrected mis reference in te Ll)Fid enolds +mEerL row wic sed te ) from te first segment for all segments# is errorwas not propogated to oter calclations Eecase tis cell was not sed in oter calclations#

1N Pmp efficienc taEle description canged from L(itwin taEleL to sow te actal reference from pmp andEoo. 2nd edition# isis on te LaElesL wor.seet#2N dded


33/33

55

eE%2=%10 &&

55

&ar%24%10 &&

5=9ep%22%2010 &&

57

eErar%2%2011 &&

58eE%2=%2011 &&

5"

&a 17, 2011 '9

+eed to e$plain ow te defalt angle wor.s and e$amine wat is reasonaEle for eFivalent lengt calclation

set p comparison Eetween te 2%pase flow correlaion in e$isting vs new versiondd cover page wit revision istor

dd d.ler taitel 2 pase vetical coord and grap

dd d.ler taitel 2 pase oriHontal coord and grap

dd &anane 2p oriHontal grap

dd taE to calcate dP G fM'v, $, ratesN for valve wide open and restriction orifices

dd taE for correcting flow meters for densit and temperatre

o te 'rane *$amples in tis

'ec. te redcer calc vs te mstang standard

'lear p ow tis program andles acceleration loss

'ompare vs# atom

ethyl acetate rev a

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