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T-707-Calculations Based on Actual Thickness-R2

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    Calculation No. Aker Powergas Pvt. Ltd.Calculation Cover Sheet - Rev. 0 Sheet 1 of 2 Client ! #CL $aldia Refiner%Pro&ect No !'0(210-1)'(Aishwar%a Pro&ect*C+ ,eed Storage R/ ankui34ent No.-505P6 SA+S State4ent of erification  A609-116-04-41-DS-1706 e!.  A609-00-02-41-#D -0001e! E$ 6-13-00%3-e! 6 &an'alefe( De!iation )ist erified 7% ! *ate !Pro&ect !   Calculations for   * he following was verified  *1. n3uts ! 2. *esign 7asis ! 3. 6ethod of Calculations !   Co43uter86anual/ 4. Assu43tions 6ade !  Confidential 12 INPUT DATA 34%67  DESIGN CODE:API 650 Twelfth Edition, Add.1, Errata, De!. 01 89  DESIGN P#ESS$#EINTE#NA% P#ESS$#E0&&'C 10 E(TE#NA% P#ESS$#E +-, 50&&'C 11  DESIGN TE)PE#AT$#E1 0 1213  OPE#ATING TE)PE#AT$#E110 141%  CAPACIT* +$%% - 'O#ING/ 111.150. 1&2 1617  TAN INSIDE DIA)ETE# 3 D3000&& 1819  TAN 4EIG4T 3 4 300&& 2021  CONTENTS# 2223  SPECIIC G#AIT* O CONTENTS1 242%  OINT EICIENC* 0.8%2627  CO##OSION A%%O'ANCE 7 S4E%%1&& 2829  CO##OSION A%%O'ANCE 7 #OO1&& 3031  CO##OSION A%%O'ANCE 7 8OTTO)1&& 3233  #OO T*PE +CONICA%- DO)E-%AT/ 343%  #OO S%OPE 4.763 de9ree 3637  ).O.C. +S4E%%- #OO- 8OTTO) P%ATE/ S 2062 G 3839  INS$%ATION +T*PE- T4/5&& 4041  INS$%ATION DENSIT*00;9-&2 4243  +'ind Code 7 IS <=5, 8ai! wind >eed ? @ 55.55 &-, 1 @1.0,  @1.0,  @1.0 / 44 Terrain Cate9or @ 2E'i/ent Class  A4%  DESIGN 'IND SPEED +SITE CONDITIONS/    515253  55.55&- 46474849%0  &in. ield st(ess 2%0&/a%1 +SE))##F #::#&,%2  :ensile st(ess 410&/a%3%4 Aker Powergas Pvt. Ltd. 9#7 N#. :P. N#.'0(210-1)'(-505 RPRP*. 7;*AC$<*. 7;*A' CL N ! #CL $aldia Refiner%  Pro&ect ! Aishwar%a Pro&ect2 S+79C ! *esign Calculation1*C+ ,eed Storage R/ ank0 S$ 1 #, 21 o C o C  Confidential 12 SHELL PLATE REQUIRED THICKNESS FOR DESIGN & HYDROTEST CONDITION 3 #ef.: A. .1 4% )aterialIS 06 G# 8 67 8otto& hell thi!;ne +>reli&inar/t  10.00 && 8 )ean dia&eterD  .01&=5. ft 9 Dei9n liBid leel4o  .0 &. <ft 10 4drotet liBid leel4oh  .0 &. <ft 11 Dei9n >rerePi  0.0 &&0.00in w! 12 4drotet >rerePt  0.0 &&0.00in w! 13 Dei9n >e!ifi! 9raitG  1.000 14 Corroion allowan!e + Shell/CA  1.00 &&0.0 in 1%161718 Prere eBialent liBid !ol&n4>@0.0 && 19 4drotet Pr. eBialent liBid !ol&n4h@0.0 && 20 Dei9n liBid !ol&n @ 4 @ 4>  4o 21 4drotet liBid !ol&n @ 4 @ 4h  4oh 22 Dei9n te&>eratreTd1 0 < 23 4drotet te&>eratre 0.0 24 Allowa?le tre +Dei9n/Sd@16 .0 )Pa=<5.= >i 2% Allowa?le tre +4drotet/St@1=5.= )Pa5 < .=1 >i 2627280.8929 St188 3017631 )in. #eBired th;  As /e( %.6.1.1 @6 && 3233 Dei9n4drotet 34 4o4#eBd. T44oh4#eBd. T4 3% 11.<0 .0 .0 8.45 .0 .0 7.16 10.0 36 1.<0 <.10 <.10 7.06 <.10 <.10 6.00 8.0 37 1.<00 6.0 6.0 5.66 6.0 6.0 4.85 8.0 38 1.50 .50 .50 4.26 .50 .50 3.6 6.0 39 51.50 .00 .00 3.10 .00 .00 2.73 6.0 40 61.50 1.50 1.50 1.3 1.50 1.50 1.77 6.0 41 = 42 < 43  44 10 4% 11 46 1 47 1 48 Total.00 49%0 Aker Powergas Pvt. Ltd. 9#7 N#. :P. N#.'0(210-1)'(-505 R PRP*. 7; *AC$<*. 7;*A' CL N! #CL $aldia Refiner%  Pro&ect! Aishwar%a Pro&ect2 S+79C! *esign Calculation1*C+ ,eed Storage R/ ank0 S$ 2 #, 21 o C o  o C#eBre t!ne De9n @ . D 4 7 0. G - S # f  CA # f   @ #e!ton a!tor a >er Tae )71a#eBired thi!;ne +4drotet/ @ . F D F +4 7 0./ - S t  CA 34 t;  of ield St(ess37 t;  of :ensile St(ess Core No.Sta;e width +&/Proided T4  Confidential 1234%6789 @15=0)Pa 10 @1000)Pa 111213141%1617181920212223242%26272829 Nole 'ei9ht on #oof@5009 30 0.05>a 31<ei=;t of a=itato(  0 =s32  0.00>a 33 Nole 'ei9ht on Shell@15009 343%3637383940414243444%46474849%0%1%0 Aker Powergas Pvt. Ltd. 9#7 N#.CALC+LA #N N+67R :P. N#.'0(210-1)'(0-505 RPRP*. 7;*AC$<*. 7;*A'= CL N ! #CL $aldia Refiner% Pro&ect ! Aishwar%a Pro&ect2 S+79C ! *esign Calculation1*C+ ,eed Storage R/ ank0 S$ ' #, 2' >>> E d  @ *on93 &odl H dei9n te&>eratreE a  @ *on93 &odl H a&?ient te&>eratre

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