Computer-simulaties van een deisobutanizer

(1)

I""

-BIJLAGEN

COMPUTER-SIMULATIES VAN EEN DEISOBUTANIZER

G-opdracht

Technische Universiteit Delft Lab. Apparatenbouw Procesindustrie Leeghwaterstraat 44

2628 CA Delft

maart/juni

1989

(2)

BIJLt\GEN

COMPUTER-SIMULATIES VAN

EEN DEISOBUTANIZER

J-.j'l..),

SoV1ci~s

(L{33::5f

VV1

J

'

U"'01~

\

?:l>22?

16~'::::. \~141L

(3)

INHOUDSOPGAVE

Bijlage 1 .•. Het afgegeven vermogen van de reboiler . . . 2

Bijlage 2 .•. Het afgegeven vermogen van de compressor ... 3

Bij lage

.

3 . . . 4

stap C (=arcokc. ou t) . . . 5

Voedingswissel (=arkcva en arkcvb) . . . 8

Peng Robinson van stap C (=pengkc.out) . . . 14

Stap D (=arcokd.out) . . . 17

Het totale zijcircuit . . . 22

Totale eindversie met dichtheden, etc. op

iedere schotel (=arcot.out) . . . .

.

. . . 28

Repack1, kolom en zijcircuit(=repackz1.out) . . . 50

Repack2

kolom en zijcircuit(=repackz2.out) . . . 58

Bijlage 4 ... Nmin . . . 66

Bijlage 5 ... Warmtewisselaars . . . 71

(4)

Bijlage.l. Het afgegeven vermogen van de reboiler. CHEMCAD: Chemical Engineering Simulation System

Stream nLlmber-Equip. connection: TemperatLlre, C F'reSSL\re, bars Enthal py, l'lJ I hr-Vapor fracti on F 1 oi-·..Jr(~'\tEs Watl?l~ ---- Totals ----: 1 From 143.611 4.00(2)(110 16308.3 1.00000 ;2) to KgmDI/hr 331.000 331.000 Vg/hr 5964.62 59,-:'4.62 2 .Erom 1 to 143.611 4.00000 3708.29 .B56207E-02 Kgmol/hr ::'31.0:2)0 331.000 Kg /hl· -5964.62 5964.62

(5)

Bijlage 2. Het afgegeven vermogen van de compressor. 0,9

*

0,9

*

4,4

=

3,5 MW.

CH~MCAD: Ch~mical En~ineering Simulatlon System (Cl Copyright, COADE / McGraw-Hill, 1986

2 Strearn

number-Equip. connection: From (1) to 449.000 64.(2)0(2)(2) 149895. From to iZl TemperatLlre, C F'r-essur-e., bars Enthal py, r1J /hr VapDr fr-action Flowt-ates I;J;:üel--- Totale 1. (2)(1)i2!(1)0 :<.gmo.l /hr-2528. ':i0 2528.(2)(1) Kg/hr 45554.6 45554.6 255.(2)40 12. Ql(2)12)12l 134073. 1 • (2)Ql(2)(2)(2) Kgmol/hr 2528.0Ql 2528.(2)0 :<g /hr 45554.6 45554.6

(6)

(7)

at'cokc.·OUT 7-Jun-8'7' 10: 15 am CHEI'lCAD: . Chemica 1 Eng i n'::;E't"' i ng Si mu 1 a tion Sysb::!lT!

ë!('CDkc: TDF'OLClCiY 1. COU"l 2 H.X:EF: Stream Connections St~eam Equipmsnt 2 ,~, I :3 Ft"O,T, TD (; 1 1. ., J. 1 1 i) 2

o

Stt-'esm Numbet's 1 . _.:...,

_"

~. _-5 7

-

!+

0 0 0 6 4"

Kvalue option: Saave-Redlich-Kwong

Enthalpy option: SO.3ve-Redlich-Kwong lvi I SCELL,~i'lEI]US

Recycle calculations are converged.

Recycle equipment list (KE2l:

-8 (>

6,.

Stt'eams used in con\'. t'outine O<E4): ( 0) () =Delay factor'

Preferred cut stream list (KE3): 7

-6 I) 7, F'age 1.

o

.-' _o~

(8)

f**EXCHANGER/CONDENSERS*** E::ql..!ipment no.

t:~;.~ tE~I" n a I n.s iTI(?

Heat transfer coeff.

~~t"'ea

1\lumbet' of she 11 s

Shell passes Tub(? pa·=.ses 1"Iode

Min" delta T or T-aut

Delta P, stream 1 Delta P, stream 2 0, stt'eam 1 t1.J/ht' Water usage, DM3/hr Corrected delta T .000'.)0 .. 00000 .0 ,,0 .0 5.,0 52.00 .. 00000 .00000 68692. .00000

***

RIG. FRACTIDNATORS ***

Equipment no. E;.; tst'n al r, a l1'Ii2 Number of stages Feed 1. t sta'~e # Feed 2, stage # F'?ed 3, '3ta'~e # I:;-E~ed 4, 3tage # F'eed ~j, '3ta';:)8 # CcmdenSEt' type

Cand. deg. subcooled

C:ondensel·" lTIode

Value of cand.spee.

C'JlTip. list position FE,b':Ji 1.E;~I" mode

Val. of r9boiler spec

CaITlp. list. positic.trl Sidestrs3iT1 # 1 stage

Sidestream # 1 spec

Sidestream # 2 stage

Sidestream # 2 spec Sidestream # 3 stage Sidest.ream # 3 spec

Sidestream # 4 spec Cand. delta P bars Calm. delta P bars

98.0 12.0 44. ,) 6i3.0 86.0 .0 .0 .00 ,::,.0 .98800 2. ,)

,s ..

:)

.36000 I~ .. ,_, 84.0 9 /-1-0.00 86. (I -3350.0 • (J ,,00000 .0 " 00000 .00000 .90000 1

eend. pressure bars 3.9000 ,

eond duty MJ/hr -90522.

Rebr duty MJ/hr 2605.9,

Est. temp stg 1 C

28:bo

Est. temp stg 2 C 28.00 Est. temp stg N-l C 85 .. 00 Est. temp stg N C 85.00

Est dist rate Kgmol/hr 1138.0

Est . reflux Kgmol/hr 4207.0 Top tray effic .80000 Bott tray e f f i c .80000 ['lade

SO'-H-·CE:~ ::. tr"e 3 rTl #

Dest. stt'earn Ij:

I/O Opti'on TmJR equip # ~;tage # F'hase option !.3ca 1.e H;<ER equ i p # (7'8. <) 12_ I) l~j~,. 0 68.0 86.0 .0 .0 .00000 6.0

(9)

~:. tl-' E'a IT, n LliTlb e~- Equip. conneetIon: T:=mpet'a tut--e, C F't'essut'e, bat'-3 Enthalpy, MJ/iit' '/apot' ft'acticm Flo'JoJt'ates Ft' op ane i-But.ane n --Bu tane i -F'en tane n--F'en t~,ne neo-F'entane

----

T otals Stt'e-3m numbet' Equip. connection: Tempet'atut-'&.', C F't' essu t' e, bat'-:: En tha J.py, tvl.] /ht' "v'apDt"' ft"'ac t i eli! F'ropane i -E:utane r-:-Butane i --F'en tane n-F·&.'ntane - - - - Tot als Str"'.=:aITI number'

Equip. connection: Te!TI p ~ t-a tu r' e ~ C

F't' eS3Ut' e, bat'-3

En 'Lha 1. p~/, r~,J / ht ... '/ap or' ft'ac t i on I:: 1 OWt' a tes

F't'opane -i.--B'.Jtane n-E;utane i -F'en tane ri--j='En tane neo-F'en t ane --- '·:Jta 1 s _ _ _ _ I I :3tt'eaiTI numbet' Equip. connection: Tempet'-3t.:w--e, C F't' E':5SU t' e, bat' s En tha 1 py, MJ iht' \'/apot' ft'action 1 Ft"'(Jrïr 0 to 1.

·

28.8000 4.00000 3516.40 :.000000 I<·::!mo 1 /ht' 432000 3lj2. 706 6. 86200 000000

·

000000

·

000000 350. 000 3 Ft'orT! 0 to 83.6000 4.60000 2.".)536. 7 1.00000 f:::g mo 1 / hr' .950000 272.360 381.690 .000000 .000000 .000000 655.000 5 1<9/ht' 1 ,.... 7 . 04:36 19918. 1 398. 81~

·

000000

·

000000

·

000000 20335. 9 I<g / ht' 41.88'73 15829.6 221.83.8 .000000 .000000 .000000 38055.3 Ft'om 1 to 0 28.6118 3.90000 10005.0 .000000 Kgmo 1 /ht' 3.47298 985.964 8.50233 . 290500E-08 .145154E-11 . 15.!t036E-05 997.939 Ft'om 48.3731 4.68751 41895.4 :.000000 7 1 to f<'3/ht' 153.138 57304.2 494.155 .209584E-06: · 104T23E-09: · 111131 E -03 : 57951.5 2 ~. ..:.:.. Ft'om 0 tD 71.7000 L~. 30000 32378.5 1.00000 i<glTlo 1 /hr' 09100 551 .337 366. 086 9. 22200 9. 02800 2. 23600 940.000 f:::,~ /

rl

r' 92. 20i_')6 :32043. 7 21276. 9 6lS5. 3-:::0 651 334 161. 318 54890. 8 Ft'om 2 to 1 52.0000 4.68751 .110579 .. 1.00000 f:::glTlol/ht' • l.j. 73789E -05 327.856 2735.79 126.345 1 /+4. :;::82 15.6242 3350.00 f:g/ht' .208913E-03 19055.0 1590<).!..l· .. 9115.29 10L~16. b 1127.22 19871 (3 .. Ft'OIT, 1 to 0 45.8314 4.66876 30066.2 1.00000 I<gmol/ht' .225642E-04 180.998 747.036 ~L 83170 3.94672 2.18785 940.000 Cl u Ft'oITI 1 to 80.8161

+

4.80001 -1 T:::' '"153

I

.

000000 1<9/ ht' . 9911_946E-03 10519.6 43417.7 leO.73'+ 284.740 157.8.Lf5 54800 .. 7 <)

(10)

- ~ ' .• ' ". ' . ..:: j ! :

CHEMCAD: Chemical EngineerIng Simulation Syst~m

(C) Copyright, COADE / McGraw-Hill, 1986

o

() () Sb'ealT! f\julT!bet'S 1 .-. L . ..::' 4 -5 '-8 7 -4 0 0 0 0 L 4, ... ~} ~'

Kvalue option: Soave-Redlich-Kwong

Enth~lp~ aptlon: Soave-Redlich-Kwong

Recycle calculations are converged.

Recycle equipment l i s t (KE2):

Stn?31T1S '_!5ed in conv. t-'::,utine n<E4): ( 0)

()=Delay factor'

Preferred cut strealTl l i s t (KE3l: 7.

-,,~ 0 7, 1,. -7 0 8!,

(11)

Equip. connection:

T'?iïlpE:W'a tut'e, C

F't'ess'-lt'e, bat's

Entha lpy, r1J Iht'

'.lap Ot' ft'dC t i on F lowt'a tes F't'opane i -8utane n-8utane i-F'entane n-F'entane neo-Pentane - - - - _Totals Stt'eafT! numbel" Equip. connection: Ternpet'atut-·E.', C F't'e'SSLH' e, bat' s Enthalpy, M,l/ ht' Vaç;,ol" f t'ac t i on Flm.wates F'r"'opane i-Bu tane n-Bu tane i -F'en t.ane n-Pentane neo-F'entane - - - - Totals ~:tt"'?"'1TI nUIT,bet' Equip. connection: T':?IT!pet'a tut'e, C F't'essut'e, bat's l::nthalpy,1'1,l/ht' Vapot' ft'action F 1 OWt' a t!=~s F't'opane i -Bu tanE:' n-8utane i-F'entane n-Pentane neo-Pentane - - - - _Totals Stt'eam nl-lmbet' Equip. connection: Tempet'atUt~e, C F'r'EsSut'e, bat's Ft'OfT! I) to 28.8000 4.00000 3516.40 .000000 f<9fT!01/ht' . 432000 .3<4·2.706 6.86200 .000000 .000000 .000000 350.000 3 f:::g/ht' 19 . 0486 19918. 1 398. 819 . 000000 . 000000 . 000000 20335. 9 Ft-'OfT! <) to 1 83.6000 4.60000 23536.7 1.00000 f<gmol/ ht' .950000 272. :360 381.6'7'0 .000000 .000000 .000000 655.000 5 f<g I ht' 41.88'7'3 15829.6 22183.8 .000000 .000000 .000000 38055.3 Ft'OfT! 1 to 0 28.6117 3.90000 10002.7 .000000

Kgmo 1 Iht' ~<g Iht'

3.47300 153. 138 985. 7~·1 57291.3 8.4'7'959 493.996 .322114E-07 . 232392E -()5 : .000000 .000000 .7!1-0682E-06 . 534372E -()!j. : 997.713 57938.4 7 Ft'om 1 to 2 48.lJ.067 lJ..68751 2 Ft'oIT! (> to 1. 2. 71.7000 4.30000 32378.5 1.00000 f:::gmo 1 Ihr' 09100 551. •. 337 366. 086 9 . 22200 '~

.

02800 2 . 23600 940.000 J~. I<g Iht' 92.2006 32043. 7 21276.9 665.330 651.334 161.318 54890. 8 Ft'orTl 2 to 1 52.0000 4.68751 1105'';>4 .. 1.00000 f:::g fT! 0 1 I ht' • 116248E-05 326.885 2732 .. 55 127.966 146.967 15.6286 3350.00 6 kg Iht' .512581_-1-E--_(l_' 18998.6 158816. 9232.2J

+

J.Ot,03.1 1127.54 19877"7 .. Ft'GIT! 1 to 0 45.8377 L~. 66876 30067.2 1.00000 I(gmol/ht'

.

150303E-05 180.9!i9 746.965 5.89396 4.00150 2.19040 940.000 ~.3 Kg/hl" . 662746E-<)L 10516.8 43!1-13.6 425. 22é) 288.692 158.029 54802.3 Ft'orTl 1 to 0 8L0096 4.80001

(12)

~**EXCHANGER/CONDENSERS*** Equiprnent no.

[-=: ;,: t'~t'n El 1 n a me

AI"ea

Number of shells

E;he 11 pas';:;es

Tube passe':; lvIode

Min. delta T or T-out

Delta

P

,

stream

1

Delta P, stream 2 Q, stt'eam 1 t1,J/ht' Water usage, DM3/hr Corrected delta T .00000 .00000 .0 " 0 .<) 5 .. 0 52.00 .00000 .• 00000, 68692 •. .00000 ,,00

...

***

RIG. FRACTIONATORS *** Equipment no. E:-:tet'na 1 naiTIe 1'~ulTlbet' of stages Feed 1, sta'3e jj' Feed 2, stage # Feed 3, stage # Feed 4, stage # Feed 5, sta'~e # Condenset' type

Cond. deg. subcooled

Condensel" mode

Value of cand. spec.

Comp. l i s t pasitian F<:eboilet' mode

Val. of reboiler spec

COfTlp. l i s t positian

Sidestream # 1 spec Sidestream # 2 stage Sidestream # 2 spec Sidestream # 3 stage Sidestream # 3 spec Sidestream # 4 stage Sidestream # 4 spec

Cond. delta P bars

Colm. delta P bars Cand. pressure bars

Cond duty MJ/hr Rebr duty MJ/hr Est. temp stg 1 C Est. temp stg 2 C Est. temp,stg N-1 C Est. temp stg N C

Est dist rate Kgmol/hr Est. reflux Kgmol/hr

Top tt'ay effic

Bott tt'ay effic t'klde SOUt'ce sb'earn # De·;:;t. sb'eam # IlO option TOlrJF: equip # Stage # F'hase option Scale HXER equip # 98.0 12,,0 47.0 6::'.0 86.0 .0 .0 .00 6.0 .98800 2.0 6,,0 .36000 ILO 84.0 940.00 86.0 -335(). () .0 .00000 .0 .00000 .00000 .90000 3.9000 -90582. 2'666.2 28.00 28.00 85.00 85.00 113i3" 0 420]_ 0, .80000 .80000, 98.0 12.0 47.0 63.0 86.0 • (J .0 .00000 6"0 1

(13)

at'kc.vb. OUT '7'-Jun-89 9:42 arro

CHEMCAD: Ch~rroical Engineering Simulation System

(Cl Copyright, COADE / McGraw-Hill, 1986

at'kcvb

TOF'OLOGY

Equipme.nt Stt'earro Numbe,·'s

1 COLM 1 2 3 4 -5 -8 2 H><ER 7 -Lf <) ₀ ₀ Stream Connections Stream Equiprroent Ft'om TD 0 1 2 0 1. . .,.. 0 :l . ...:. ij. ₂ ₁ L:' -1 I) . ...J 6 1 I) 7 1 2 8 1. 0 COt-1F'OhIENTS I D nurnbet's 4, 5,

Kvalue option: Soave-Redlich-Kwong

Enthalpy option: Soave-Redlich-Kwong

11 I SCELUil\JEOLJ::l

Recvcle calculations are converged.

Recycle equiprroent list (KE2l: 2, Strearros used in conv. routine (KE4l: ( Ol

()=Delay factOt'

Preferred cut strearro list (KE3l: 7,

<) -6 0 7, 1, F'age 1 -7 0 8, q _,

,

(14)

***EXCHANGER/CONDENSERS***

Equipment no. ,.. :: -,

E,.: tet'na 1 name

Pwea

Numbet' of she 1 L:;

~hell passe:; Tubc? passes lVIode

Delta P, stream 1 Delta P, stream 2 Q, s tt'eam 1 r'IJ /ht' Water usage, DM3/hr Carrected delta T .00000 .00000 .0 " 0 .0 , 5. (I 52.00 .00000 .00000 68693 • . 00000 .00 w • • • • • • • • • • • • • • • • • • • • • • • • • • • • • • • • • •

***

RIG. FRACTIONATORS

***

E~quipment no. 1

E:-: tet'na I name

Numbet' of stages Feed l., sta':;Je lj, Feed 2, sta'~e # Feed 3, stage # FE'ed 4, sta'~e # Feed 5, stage 1* Condenset' type

Cend. deg. subcooled Condenset' fnode

Value of cand. spec. Camp. l i s t position F<:ebo i Ie," mode

Val. of reboiler spec

COITlp. li=,t position

Sidestream # 1 stage Sidestream # l. spec Sidestream # 2 stage Sidestream # 2 spec Sidestream # 3 stage Sidestream # 3 spec Sidestream # 4 stage Sidestream # 4 spec

Cand. delta P bars

Colm . . delta

P

bars

Cand. pressure bars

Cond duty MJ/hr Rebr duty MJ/hr Est. temp stg 1 C Est. tem~ stg 2 C Est. temp stg N-l C Est. temp stg N C

Est dist rate Kgmol/hr Est. reflux Kgmol/hr TCJp tt'ay effic Bot t tt, a y e f f i c !'lade Sm.wee stt'eam # Dest. stt'eam # I/O Option TOWR equip # Stage # F'hase option Beale H><ER equ i. p #: 98.0 12.0 50.0 SE!.. 0 86.0 .0 .0 " 00 6.0 .98800 2.0 6.0 .36000 ~" 0 84.0 91_+0.00 86.0 -3350.0 .0 .00000 .0 .00000 .00000 .90000 3.9000 -92066. 4152.3 28.00 28.00 8S.00 85.00 1138.0 4207.0 . , .80000 .80000 98 .. 0 12.0

so.o

58.0 86 .. 0 .0 .. 0 .00000 6.0

(15)

:_-_':!_ •. ~J .. • ='~I-,;-'~~'': ::1·:);-',;

T.:?iTi!-J!2i·-·(3 tUI-'e, C

Pt' eSS'Jt'e, bat's l'::nthalpy,l'l,J/t-H' 'Japot' ft'action I~ 1 OWt' a 'les F~t'opane {-Butane n-Butane i-F'entane n-F'entane neo-F'en tane

----

Totals :3tt-'eam nurnbet' Equip. connection: Tempet'a tut'e, C F't'essu"'e, ba t'S E:nth.31py,IYIJ/ht' VapcH' ft'ac t i on ;:: ~"'or;, ,_; '_'''': 28.8000 4.00000 3516.40 .000000 Kgrr,o 1 fht, .432000 3J.t2.706 6. 86200 .000000 .000000 .000000. 350.000 3 i J. I<,~ fht' 19.0486 19918. 1 398.819 .000000 .000000 .000000 203~!.5 • 9 Ft'om 0 to 1 83.6000 4.60000 23536.7 1.00000 I I , 2. 71.7000 L~. 30000 32378. ~5 1.00000 ~:::grnol /ht' 09100 551.337 366. 086 9.22200 9.02800 2.236(H) 940.000 1. 1<:<;.1 f ht' 92.2006 :'::::Z0l.l3. 7 21276.9 665.330 651.334 :l61..318 5J.t890.8 Ft'om 2 to 1 52.0000 4.68751 11.0593 .. 1.00000 ---~---F lOl-wa tes F't'opane i -E:u tane n-Butane i --:='en t.ane n-F'entane neo-F'er, tane --- Tata 1 s t3b ' eam numbet' Equip. connection: T,?r;-:pet'a t:'lt'e, C Ft'ess'Jt'e, bat's Ep th alp y , i"U f h t' ',Iapet' ft'ac t i on f:::grTlo 1 / ht' .950000 272.360 381.690 .000000 .000000 .000000 655.000 5 f:::g/ht' lt1.8893 15829.6 22183.8 .000000 .000000 .000000 38055.3 Ft'ofT! to 0 28.6109 3.90000 9962.90 .000000 f:::grno 1 /ht' .160265E-08 328.40(> 2730.75 128.018 147.218 15.6119 3350.00 6 f:::gfht' .706673E-07 19086.6 158711. 9235.99 10621.2 1126.31.1· 198781 " F,·' om 1 t'::J <) >45.8029 L~.66876 30060.5 1.00000

---F lowI'a tes Ft":Jpane i.-Bu t.3ne n-8lJtane i-F'entane n-F'entane neo-F'en tane

----

Totals Sb'eam numbet' Equip. connection: Tempel'atIJr'e, C F't, eSSut'e, ba~'s Enthalpy, MJ/hr' Vapot' ft'action I<'öjmolfht' I<g /hr' 3.47298 153. 138 981.828 57063.8 8.45203 491.232

.

125081.E-04 .902409E-03 .000000 .000000 .3J.t1176E-06 .246145E-04 993.753 57708.2 7 Ft'orT! 1 to 2 48.3682 1+.68751 41893.1 .000000 I<gmo 1 fht' I<:gfht'

.

156352E-07 .689419E-06 183. 110 1 06J.t2. 4 7J.t4.948 4329,~. 4 5.81961 !~ 19.862 3.94188 284. ·391 2. 18040 157.307 91+0.000 51+800.3 8 Ft'orT! 1 to 0 80.9435 4.80001 197.673

(16)

pengkc.OUT 7-,JLrn-:39 11:::0 am

CHEMCAD: Chemical Engineering Simulation System

(C) Copyright, COADE I McGraw-Hill, 1986

pengkc: TC)F'OUJGY Equipment 1. COU1

H><E-:F:

Stream Connections StrealT! ~quiplT!ent Ft'.::'m TD 1. (; ₁

.

,

U 1 "'-'. ( ., ) ₁ -4- -.., ..:. 1 I:::' 1 ( ) ...; _.. oS J. 0 ,.

_::

8 1 ( ::; COMF'C!/IEI\,TS 1. 7 Sb'ealT! ~ _.₃

...

-4 0 .-::' f'jumber's 4 _-...;.". _-8 0 (I ₀ 4, 6, THI:::Fd10DYNAI"j I CS

Kvalue option: Peng-Robinson

Enthalpy option: Peng-Robinson

1'1 I SCELL_ANE!JUS

Recycle equipment l i s t (KE2): _2,

Streams used in conv. routine (KE4): ( 0)

():Delay factm'

Preferred cut stream list (KE3): 7,

-6 0 7, 1, -7 0

(17)

~~*EXCHANGER/CONDENSERS***

Equiprrtent no. E;d:et'na 1 naine

Heat transfer coeff. f.kea Number of shells Bhell passes Tube passes ""ode

Min. delta T ar T-out

Delta

P,

stream

1

Delt3

P,

s tream

2

Q, stream 1 MJ/hr Water usage, DM3/hr Corrected delts T .00000 ,,00000 .0 .0 .0 5.0 52.00 .00000 .00000 67822. • (JO!)OO .00 2 . . . ot . . . .

***

RIG. FRACTIONATORB

***

Equipment no. E;., tet' n ,] 1 n .~j 1'-';;:' Nurnber of s tages Fee'::l 1, =..ta'3e

**

Fet:~c! 2, stage i* 98.0 12,, 0 44.0 Feed ~, stage # 68.0 Fsed 4, stage # 86.0 Feed 5, stage # ,,0 Condenser type .0

Cand. deg. subcaoled .00

Condenser mode 6.0

'')·:llue '::lf can,j. spec. .98800

Corrq:;" l i s t pa3: tion 2.0

Rebailer mode 6.0

Val. of reboiler spec .36000

Comp. l.ist posltion 4,,0

Sidestream # 1 stage 84.0 Sidestream # spec

Sidest~eam # 2 stage Sidestream # 2 spec Sidestream # 3 stage Sidestream # ~ spec Sidestream # ij stage Sidestt'eam # ti spec

Cand. delta F bars Colm. delta F bars Cand. pressure bars Cond duty MJ/hr F:E;bt' duty ,-1,] /ht' Est. temp stg 1 C Est. telT,p stg 2 C 1="<='-• • • . . J , _ .. t.emp ':; tg ~J-l C Est. temp s t ; N C

Est dist rate Kgmol/hr Est. reflux Kgmol/hr

Top tt'ay effic

Bat t tt'av eff:c ,-1ade 940.00 .... 86.0 -3350.0 .0 .00000 .0 .00000 .00000 .90000 . 3.9000 -90146. 3323.3 28.00 28. <)() 85.0() 85.00 J.138.0 4207.0 .80000 .80000 9)3.0 1

(18)

Ci ". ','

,

:,:-

.

=

,

o:! I::' E

:~:

:5:

t'

~~

:§:

Cl ,...

I::

·.f) (:r L • t·') t<! () LL... • Cl • I'- ::t t··) .-I I) *.1 '::' '::. ()

() c:'

6 () .::. o CD .:,:. u~

ai

I:;~ c ;:I .~ N::t ::tO lfl .;:. c ,'-I 0) .:=-IJ) I~ li)

05

t"~1 I' U 11'1 C U ~ '~'" 0 UI ai ''0 '" ·d D C lJ.! .D ::.o:::: +.' t: r.: L IJ ~.J (I :-J :.. h rtl U !-~ JU ,', ~ lp ~ ("I, '~ .. L ~:1 ''!': a III ifl rTl L Q: ... CL ~n 0 :J

s:

UI II ..:...! cr n! L L. 'U . ) l.d f-· ;L Lti :>

..2

...

0 j... 0', , __ , :jo. rTl CO ... , ... , !T :::. t<! .. (I I"~' t··) -, t'> t··~. t·~, C·

....

r:

:~ [~:I !.i) Ct' ~~; =;~: ~il Cl

e,

~,

..

::;

1)- r"~' Cl <, ".(1 --' I.n L " r l "-', 1'-'" ,11 o .:, t~,

cO

t: ,. ... t"~1 () IJ' 1)'- , • ~ C· ~ .. ü , • ~') ,l) r-I liJ V, c: c· c:: .:-c. C- (;: I;:) ('"'1 (I.) .. i) (::-r-I r-~ r"~' • ("·1 C' Cl .::. ::t I)-- I)-- Cl Û' L ··n ?-; Cl" c· C' C' 1)' ... CO • ",M' () C:' :: (T. ::j 0) (11 .:'. ':.. C' ID ::::::: '.~~.' ~--I c 0::' ' ... ' ':: t:-~ Lt' en .::~. () (:0 t···.1

::

~ ?~;

::;.

.:

::'

c~ ;~i L L "-~ C, .. J) :::.~: ~ :~: t::~ ;~:! IJ' C'I ,-.0 :::.::: t .. ) [',1 co ::t::t • • V· ·<) ;. 0 0 0 0 0 0 0 0 OOO ( 0 0 0 0 0 0 0

ooo

m

·M 111 Iq C lIJ !!.! f;:l n: Ul 111 iJ! C C .p .. ~.! UI 11: C • : !ij 1'1':1 c: "Mi +1 c. '1] 1''1 .j.) -,_.' ill !.~ l1J :1.1 .+-.1 .l) C C Ll .. L CL :J :; ijl nl I l: o (fJ ([J LL (L Cl o '- I I I 111 r-I ü_ ':--1 C .~ C L.. LL ::j I,'~' ~~ i [: .. t-.' Cl '::::..-1 :: ,:...;, Co 111 l;) C-E C, I'- ~) 0 n .:) m l!~! c' L • ...0 <::: c' LJ .. f'-I • _., • ~l ::t .. ~ ... Cl .~.~I ç::, 0 0 0 0 EOO u~o ~ .~ ~M • m::t

'

.

'

, ~ C·I C' : .:::' en 0 1"'10 lf) .;:) VI • , ".J T""'f I! 1 . .1 I.IJ ~: I I; f! (ti ']:; !l' '-:; .. .D L. Ct! Xi F-E .- .c. U :J :.; :J IG r:: ':

"i

1:1' > . liJ .: ft t: ~. :-) ,.-.~ t··) I !U L Cl) 1). "', .. ,-f • O~ 0"' .. .(I =f' VI ::.~ ['1 ,.[.1 t·· IfJ T-t (0 Cl (r' lf:: • T-o! ..-! In ( < .. ', 1: I -', LiJ :-4 OJ r·· .. · t·)

o

c·

=t (I .:: 0' 1-- , U' ('-I 0 " " , t~ ... '-', '--q Cl - ~) -n C·~ t.::; IJ') c..l :::I' r, en IJ, l-I G: ':~I O· I)" ..-~ T-f ...--1

m

o

mo

~N~O

M-ro

.

na :::.::: 1"- Ct" t··) 1'-" ..J)

· m

nM M ~1 Cl I" Cl =t ot··) r"1 r l .c I,':' .. n (0 ._. 0 0 t .. :, C,- 0::' (.:' ... 0 .... r::r. Dl (1- t<. c· C· .:::. liJ :CC:: LU Cl 0.1 0::;. Co .:::. ~) 1': ~ CO .... -4 '.:> C' C:' .:::. ,-< In Cl C· '.:' C· IJ) =t .. -I Cl t·) ·--1 I·.~'· ') ':.::> '."::' • .:) c' () C! C::O ,·0 IJ· C' I.~:' ,'~:1 () E C: , .. ) ··n ':::' '.:' <:-.• ::. CP C, = ; :~~. ' __ : c· .:..:.: In (J ,-i ... "-'. _lil ' .. } ~l -.0 Ij, 1'-·

co

o C~ t·:' ~1! 1.11 C .-1 !li 111 11.! I~] '.!! 'U;II C J .. ! .. ~.'" iil Ili 1.1 L: '(I [ ,r; .IJ L: I] ": .11 ~ J 111 ~- -.'.' ~.I L. c: I~. :~. Ll. :.i 11.\ Il! ! '" Cl fU 1.!1 ,n ,_ W :-' II :J1 _L .. :~

.

b

~

~=~~~

· !

~E.

;t

ie'

It

·.L ti, ri: (I) ! ij ~._" ,) i.:..i .> I , . ~(! In o .~I ... ~! =t~t-, O =tI'- . 0 t: Ü' m ~'.1 () Cl ... .J) 0" C:I L • --0 C. '::1 lJ., -.0 • C· • c' r:t ..f.) ?< ::t ::t t .. :, .... I'- 0 t') c-C'-! c- , c-t: r-,

c:·

(t. () o m c· r·~ C, L • Ü' r-.~ c·

u..rn

• ()

()

c n . ~·I n t··)...-t • .~' I~J ~ cl 1.11 .L C L I) !1: IV ~ r-:. '~i DCru ~ F ~ E ~ ~ u ~ n ~ =. rn r::: ;1 '11 >. L 1/ j ~, • ,', ' .~ ,= ... ::-J ,.-f 'n Cl. i]! 1.11 fr: L !l: "' r~L I.n .e 0 ~_ :" E tli .. u Cl ",,_I n P1 ~'O : : : ITi U) I;J 1- LL t~! .. ,:~ Cl i ~. IJ I .L f'.~ r~=! r! I·· .... ti j t···· t··) '-". ~, !-' .. t···" T'" q, .:::. ei t··, Ir; I',· C!' ot· ::.,: IJ) I·'! [1:1 , 0 c. e· I.:J t· ') ,,:~, Cl m 0:.1 ., .. , C, t·') I···i p .. I1"J ;:t .,'., ;,t ::::. ["-l ",' I.() =t. L I -'-, W ...--I !J1 C) ,... t··) I)~ r·J () (j l.!l ·~O .,...~ ...-! C:o r····. .:' E .,...., [",1 ~') DJ CO [' I 0 G' m -l) ~') c· • :::.::: t) ~ -(I G- C· r'l 0 [",1 (IJ =t ::t .-l 1-- ~1 =t.

n

Û' In _v' (':t _c_· I I L IlJ 11J L (I) Cl [",1 '(I ç. ~J [',1 . ... ~ VI C: L(J I.:" '·0 (1. --, T-l 0" ft c· t'.TJ I'''· C,::. • Co 1"-· ·::" G' : t-L t .. ) ["-I [') ::t c· t··) lJJ IJ-J t·,- IJ· ~< •. :.. .,...., I', ~, in ot ~~I I'. U:I L I I '. lJ.J LU r l

co

"1 I'"'' 1}.. .:::. ;;j' IJl o (t. (j. t·, 1'''- .::. IJ ::t E C-~ 1-f c:: .~~:. ,,:. GJ T""'f :,:TI t',· • (':' Ul :; v! • ~

=t;

O!; =t; ;:=; '~'

Z;

~ t·) 1)' co • • • Û' 111 UI C ,-1 0.1 111 ,1) ,1) IJl flt ll,; C C ,IJ+' iJ,; ~;' c ;n "1 L: f.1 ~..1 I. lil In J.I I! ijl I . ;1.1 I'.; .~I .1.' t. c CL 0: r·· --1 -, 111 nl I 3: ,~' lÏ'J

,:ï;

CL

à

,

0 Cl ! I UI ~'-i i.: . ... r~ L: c: Ii.. 1:0 1',. ,''''. u ~p .~ IJ'- rot :i~ c:· 0 .. ,-. - I , .... , E ~ .::' i···. I~:'

o

t--

a

· 0 ~ ·mOJc, lL..-t . lr: () DJ ::t ~,' • C'l Cl +' ? " CD...., m.:,:> =t ~l . c·

t:

t··) '" .... -1 ( )

ot,rov'.::)

~_ • ...(r 1" .... () LJ_ CD • [".J .;:.

c

,) ' .. -1 =t::t:t .~.I CJ In J'~ !. L U ::.~ f.! Ol IJ.! 'u '-:1 .,,,! .D C UI.J:1 J:' .!.'

S6~

..

:~

c I.,I ·P 11-' :;. lli '; .. n . ·1 i:: ~. -) ,1] rJ. 111 iJ! 11) "_ tll .~, a i.f! 1: f.J L ~J t:: n.l +l rl ,+-1 cr IJ! :. 1_ !lJ "fi LU i-·~ (L L:J ~> t 1.:.1 L r') -, C.) =t G.' .~, b~;

r

:

!

L

·.

:

~. Ci' :::':~ . _..c'ro ··U t !'" .. iJ' "i. ." :j' C:.· r.-! :cl r'j I . /., I ._. C'J ' I'" I·· .. ' r·J

.2

'

t

i

... UI LU ,-< ~) t··~, Ol-") (r' EO C' =t cr: .,... .... (::0 ::.:: G Cl =t. I, I"', c' I L lJ.J Ct '::" C~ ~~

.

•

f,~ ~: , .... tO ~n 1',') .', t .. , [0 • t·:, ::t ! lIJ .~) =t Ol t··) [".J t··) I·· ~l ... (0 l!1 ro .c IJl c .. ~'j "~. ' .. _ r·. u' ro :~.< .. Ij =t' Cl ... I. J o I' IJ

'

i

'U _ LJ I", I Cl OJ (t, ~') fl Hl cr.. iI j .... ! '.:= U . e - 1 ~-; IJ ... ~~I f .'-', .1 ••• '._.' . c l "-" I.U ., lt'J Cl ' .. t C'I ., .;~ .. Ç) o t· ". q., ç~: O.:~ I.·J n·, c:. E CO ".0 = t·:! ; .. ) ~.o • IJl 0" r ._. " : IJ' ,;::. .:..:.: In c· t.') I .. ·.. -(I " ~l ~1 I') ~"- 1''-1 =t ~'J v' 1,":' ["-I ,-, ?~ .. " t··) III li'j c I.n :1.: I).! 'C 11 tl' C C I') lï.l ill ·1'

.!

Il; iTl !.! .p 111 1].1 ,.1 t: 11: do I !P In .. ~.1 .. J L: C ~J L U ~J :J ,", 11i ! 3: (J ,~[! fD ... Ll.. 0 Cl

.-

t

~ ! ~ 1]1 LL

:

'

,

\0 M

(19)

-. . . . ' ."

a:arcokd.OUT 11: 20 am

CHEMCAD: Chemical Engineering Simulation

CC) Copyright, COADE / McGraw-Hill, 1986

TiJF'OLCJCJY

EquipmeÏit Stl·'E,3m ~-lurTibet's

1 COLM 1 . .., ~ ₄ e _-6 .::.

_-

,J ,..., H><EF ""- 8 -5 (; (; 0 ~ H><EF: 6 -10 <) ₀ (; 4 ))'.)jjf;: ₁<) -1 1 -1 (> ₀ Stream CQnnections Stream Equip~ent Ft-·om Tt] L~ ; J. 0 1 ... 0 :l 1.1- (; 1 1._- . ..., ., . ...J ... .L 6 1 -~ -,

"

1 <) 8 :[ .. :.:. 9 1 <) 10 .3 ~+ 1 1 4 <) COt'lF'ONENTS 4

,

~value option: Soave-Redlich-Kwong

Enthalpy option: Soave-Redlich-Kwong

MI :3CELLANEOU:3

Recycle equipment l i s t (KE2l:

Streams used in conv. routine (KE4):

()=Delay factor'

P~e~erred cut stream l i s t (KE3l:

() () 0

"'

'-'

,

<) .:,

,

System -9 -7 0 <) 0 0 I) ₀ 7, 4, '":)

-,

8, -·El 0 0 (; 8, 9, 1

,

(20)

CHEMCAD: Chemical Engineering Simulatian System

DIVIDERS

E::quipment no. E:>:. +:et' 11 ," 1 narTIe j.":'"t-··~ct.iDn./f lo~ .... j i10de :;tt-·'=,3lT1 'ft: C;omp. 10

_4*

Ci::JITII:-J ..

ID

# Camp. ID 4: CDmp. 10 # Camp. 1D 4: CO:flp. ID '1* Comp. 10

_1*

Comp.

ID

# Camp. ID l* CCJiTqJ. ID # 2 3 .19254 .80746 " OOOO() .OO(i(iO " (lf)OO() .. (i • (i .0 .0 .. 0 .0 .0 .0 .. 0 .0 .. (i .0

...

.

..

....

...

.

...

***EXCHANGER/CONDENSERS*** Equipment 110.

Heat transfer caeff.

AI"ea

Numbet' of shells Shell pa';ses TI.Jbe passes

I'lode

Delta

P,

stream

1

Delta P, stream 2 S, stream 1 MJ/hr Water usage, DM3!hr Corrected delta T . 0(;(:')0 n OO()f)() .0 .0 • \:1 5.0 52.00 .00000 .00000 68691. .Oüü(;() .O() 2 .00000 .00000 .0 .0 .0 5,,0 28.65 .00000 .00(l()(l -88319. .00000 .00 3 2=" "' . . . . . . . . . . . . . . . " . . . . . . . .. . . . . · • • • • • • • • • • • • • • • • • • • • • • • • • • • • • • • • •

(21)

***

RIG. FRACTIONATORS

***

Equipment no. r~>:tEt-'nal namE

Number of stages Feed 1, ':5tage # F(;?\2d 2, stage

**

Feed 3, ·:;tage # F"eed 4, stag!2 # FE~ed 5, stage # Cond,?nset' type

Cend. deg. subcooled

C::onoensel" mode

Value of cand. spec.

C':::lITq:'. 1 i ,==t posi t ion Fi:eboi le\" modE'

Val. af reboiler spec

Corrlp. l i s t position

Sidestream # 1 spec '::;: i eii-::s b'eam # Siclestt'eam

**

Sid,:,sb'eam # Side:;tt'eam # 2 2 '-' ..,.. . .;. stag,? spec stage spec 4 stage :3 i cl ':= s t \., e a !Ti # Sidestream

**

4 spee

Cand. delta P bars

Colm. delta P bars Cc,nti • pi"'eSSUt'e bat's

Cor,Q duty M,] / hr' ~~:ebr' dIjt,;! MJ /ht' Est. t'=mp stg 1 C Est. temp stg 2 C ç:-.- .... ... ::l , _ . terTlp stl₃ 1'J-1 C Est. temp stg N C

Est dist rate ~qmol;hr

Est. reflux Kgmol/hr

Top tt'ay eff ie

Be; t t t t ' a y ef f ic l"lade Sout'ce :.tt'eam # Dest. stt'eam

'*

IlO Option TOWR equip

**

Stage # F'hase optian Seale H)(ER equip # 97.0 1.0 11.0 L~3" (> 67.0 85 .. () 1.0 .00 2.0 .00000 .0 6,,0 .36000 4.0 83.0 940.00 85.0 -3350.0 .0 .0000(; .0 .00000 • OO(lI)(J .90000 3.9000 .00000 2627.1 28,,00 28.00 85.0U 85.00 ,,00000 .00000 .80000 .80000 97 .. () 1.0 11" 0 43.0 67 .. (j 85. (I 1. (> .00000 2"0 1

(22)

1

5 ti" e.,::; 'Ti n Llfnb et'

Equip. connection: Ft'oITi 4 to 1 Fr'om (> 1:0 1 Ternpet'atUt'E, C

PressI.Jt'e, bat's

Enthalpy, M.J/ ht'

Vapot' ft'act ion

Flolowates F't'opane i-Butane n-bl...1 tane i-F'entan.:' n --F":;:;n t::;ne neo-F'en tane - - -.- Totals Stt'eam numbet' Equip. connection: Tempe"atUt'E, C F'r'E?S'::;U 1'-' e, bat-··s Enth::;lpy , M.J/ht-· 'v' a p IJ t' f ,-. ·3 C t ic) n F 1 OI.>'Iit-'::t t2S F't'opane i -E~.J tane r,-Bu tane i ·-F'en t,:;,n,= n-Pen+':ane nE'D-P'~nt3ne - - - - Tot-als Str"l~örn numbe~'" Equip. connection: Tr=:iTlP;:=: .... a "tut-'e , C F't-·e·:;·::;.,_we, bat's Entl'~;alpy~ t .. 1,],/h'· ... V.3pCW ft'action F J. O\loJt' a te·s i -BI...! tanè~ i-F'entane . n~F'!~r!tane neo-F'entane ---- TDtals ~8.6450 3.90000 51331.5 .115691

.

....--_. . ...

-Kgmol/ht' 14. 564,~ 4138.18 :36.0053 .726070E-ll .000000 . 534796E-05 4188.75 71.7000 4.30000 32378.5 1.00000 f:::grr:ol/ ht' 2.09100 551.337 366.086 9.22200 9.02800 :2. 23bOO 940.000 3 5 Ft'orn 2 to 52.0000 4.68751 110613. 1.00000 1< '3 rr,,:) 1 / h r' .49l)479E-OS ·325.164 272':t.03 130 .. 3U9 14"? 80i 15 .. 6540 335<). Cl() 7 Kg/ht' 642.211 240511. 2092.63 .523830E-09: .000000 • 3858304-E-(J3: 243246. 28.8000 4.00000 3516.40 .000000 ... ~"_ ...

_

,

I<gmol/hr' .432000 342.706 6.86200 .000000 .000000 .000000 350.000 l~. f<g/ht' 19.0486 19918.1 398.819 " ()(;<)oon .000000 • ()OOOOO 2('335.9 Ft'olTl (> to 1 83.6000 4.60000 kg/ht' '7'2.2006 320lJ.3.7 21276.9 665.330 651.334 161.318 1.00000 f:~gmol /h~' .950000 272. 36() 381.690 .000000 .000000 .000000 655.000 iS 1 Ft'om 1. tD 28.7387 3.90000 151886. 1.00000 Kg/hr Kgmol/ hr .216272E-03: 18.0376 18898.5 5124.76 158':,11 . 44.6004 9404.16 .739710E-l1 10807.5 .000000 1129.37 . 727272E-05 198851. 5187.40 8 f:::q / ;"':t' 41.8893 15829.6 221 ::3-5"."3 • ()(,OOOU " ()(;OC!C:!~) • O()OOi)i:l ~8(i~~5". 3 I<g /~t' 795.350 :297851. 2592.18 • 53367::'

=:

--O~·:· • (}~)OOO() • S::!.fb':;'2E -0::; 301239. Stt'earn n'.Jmbe~'

Equip. connection: Ft' elfT, 1 t Cl <) Fr'om 1 to Tempet'at'Jt'e, C F'r" ~?':5'5Ui"""e 'J b :3t""':. Enthalpy, 1'1,]/ht' t,,/ap(J~'" fr'de t i on r:"l O', ... Jj" ...

· =

tes F'1·'op.:;ne i. '-Bu t.3ne n-Butane 45.8631 4.66876 30071.7 1.00000 f:::giTIol/ht' .. 224"267E-Oli· 180.197 747.361 i-Pentane 6.12196 n-F'entane 4. 108~3 neo-Pen~ane 2.21135 - - - - Tot31s - - - -: 940.000 48.4564 4.68751 '';'1'::;28. 1 .000000 Kg/hr Kgmol/hr . 988883E-03: .503505E-05 10473. 0 32~.786 43436.6 2727.39 441~675 296.407 159.540 5)-!-807.3 131.168 150. 99i_-J. 15.6571 3350.00 18876.:: 1 ~,)::':3 5 H, 9463.25 t 12Q _"_..:/ ₎

(23)

Ett'eam nUlTobel" Equip. connection: Tempet-'a tut'e, C F't' e·;:,sut' e, bar' s Enthalpy,l'lJ/hl" VapOt' ft'action F 1 O\l>!t' a t.es F'r'op.::;ne i.-Butane r: ~'-'E:u ta p e i '-F'en tane r~ --'pl::?n tan(~

necJ-F'en tane

- .. -.--- T (J t.::t 1 s

:~=jü'e,3IT! number"

~qUlp. connection: Ternpe~""atur'e~ .: t='! .. , e-3SL': t'" i~ ') ba;·-·s Enthalpy, !'l,J/ht' F' r' '::lp a" e :L - :E::u t ·3 ij t~ n-F'en ':ane --- Tota1-= 9 Ft'om 1 to 84.0078 4.80001 115.363

":

'000006

1<:';3fT10 1 /hr' . 148c:93E-13 . 246253E-02 .3<)5730 2.28670 3.7351+4 .216120E-Ol 6.35194 11 <) ~<g Ihr' .656529E-12; .llt3122 17.76'iO 16lt.976 269.1+97 1.55922 453. ''745 Fr'om 4 t·:J 0 28.6450 3.90000 12214-0 ,. 1 .115691 986.7'55 ,-, cr.c·c::-i ,~ .. ,.J CJ "_i·-I .L . 17:3131E-11 .OO<)()OO . 127523E-(l5 998.813 f<g / hr' . 153.137 57350.2 498.990 . 124908E-09: .000000 .920028E-04: 58002.3 Ft'om 28.6450 3.90000 6~r:.·""1 .

:,

:~i~~69~

10 3 to KgfTIO 1 /hr' 18.0376 512lt.93 44.5908 .899202E-l1 .000000 .662319[-05 5187.56 1.(. 1<<;.I/hr' 795.350 297::361 " 2591.62 .64·873(3E-(j9 .000000 .477837[--03 301248.

(24)

arcoze.OUT '7'-,Jun-89 3:57 pm

CH~MCAD: Chemical Engineering Simulation System

(Ci Copyt'ight., COADE / McGt'=n,.-Hi.lJ., 19t:1"S

4,

va_~e opt:on: Soave-Redlich-Kwong

Ent~alpy option: Soave-Redlich-Kwong

Recyc~e equipment list (KE2l:

Stre3~s used in conv. routine (KEil):

\""'=i)el'3"Y" factot'

1 6, IS,. 1

,

0 ) 8, 7

,

12, c;-

,

"~ i , 1

,

13, 1 6

,

"-' ..;;., le::: ~, ,....,...., ~ . ..;..

,

₄ c:' _8, _'_~ 10.

,

,.J., 16 ~.'

(25)

(e) Cop'y't'ight, COADE / MC(3t'aI-J-Hill, 1''?86

l:n:'

OI"VÎriËRS

'

:t::u:

Equ i

pment

--

iî

-

';:

- '"

-E;; tet"·!l':; 1 !lame Ft"· ·3;': t li.J n / f 1 0;') :l Mode :;::, tt'eam C':.:liTIj:; C:.CJiT.p CC:':T,!:~ _" CCJmp r::::':::;ITiP CClmp eDiTlp _" C";;::m,p Cc,mi:!

.

C;cJmp

**

ID ID ID ID ID ID

ID

10 cD 10 0\1: #:

**

#:

**

#: # ij: '", .. :.:. ":r . ..:. 4 .70000 .25000 .50000E-Ol .00000 • (H)O;)O .00000 .0 .0 .0 ,,0 .0 • (i " (> .,0 .0 ., (:, .0 .0 13 .80600 • 19LJ.00 .00000 .00000 .. ()OOOO ti (>()OOO .. (; ,,0 .0 .0 " Ct .. 0 ,,0 .0 .. (I " 0 .. " '" . . . . " " . . . . Ol " . . . . .. " . . . .. . . " " . . . .. . . " .. .

*llGENERAL FLASH UNITS *t~

Equipm~?nt t-ii-:l. E;< te~" n c3 1 na ïi,i,:' rleat dut.y I<- va J.ue #: :<:-v.,;:; :Lu?:

**

1<: -v.:; 1 u e

**

'O:'-V,J l,-.J.;?

**

:<

-

\/

,3

1 ue # ij: -' :l "

.,.

M.] / ht' :3.0 3.0000 . 00000 ,,00000 3.0252 1.2632 .92356 .39035 .29172 .66536 2 12 6.0 ~5.670 .00000 .00000 2.1411 . 9980l~ .76213 .35833 .27977 " 5,~700 8 .. 0 6.0000 .00000 .00000 2.1561 .99806 .75997 .. 35·J.~90 .27632 ='" " . . . " • • • ,. . . . " . . . . . . . . . .. . . . . . . . . . .. . . . ,." . .. VALVES

Equ:i.!:iTient nCJ"

E~<tet'nal name

7

Dutlet pressur2 bars -.10000E-01 6.2000

8 1~..,. "

3.9000

IS

6.1000

(26)

CHEMCAD: Chemical Engineering Simulation Syst~m

(C) Copyt'ight, COADE I t1cGt'aw-Hill, 1986

:+::n:ÊXC"HÄNGER1CONDENSERS:t::+:* -:~

EquiPrr;èntrio·.~'·· , .... :..-..'-_ .... - 5 6

E~<tet-'na 1 namf?

AI" 2·:3

Number of shells

Shell passes

TujJ(::? passes

I'''~ode

Min. delt a T or T-out

Delta P, stream 1 Delta P, stream ::::: 0, s t ream 1 MJ/hr W~ter Gsage, DM3/hr Corrected delta T .00000 · :)00<)0 • I) .0 .0 8.0 65.34 .. 00000 -1.0000 .. 00000 .00

***

SIMPLE MIXERS

**

*

t:~q __ i.L D~!I:?n t nD" E;<'!::et'na 1 nalTt~~ 1

***

ENTROPY MACHINES

***

Equipml;?nt no. 3

E;; ter-' n ':'11 rEi ITIE~

jojode

Outlet pressure bars

Adiabatic efficiency

TheOt' e t ica i hp

Actual horsepower

Entropy in KJ/deg C

Entxopy out, id,?al

Entrapy out, actual

• I) 8.3000 4859.6 6074.5 · 3::::::::::::'jOE +06 .3:2265E+06 · :~::3T:'6E+06 .00000 .00000 .0 .0 • I) 9.0 53.00 .00000 .00000 69071. .00000 .00 9 10 .. OO(i()O " t)OOOO .0

.

() .0 5 .. 0 44.00 ,,00000 .00000 -33980.

.

oooou

.. 00 11

(27)

btl"eaiTI ilumbet-Equip. cannection: T,:::mpet'atut'e, C F't-· eS·:;I.J r' e , t:.3 t' S Enthalpy, M,l/hr' VapOt' ft'ac t i on F lowt'a tes F't'opaile i -81J tane n-··8u tan!:=2 i -F'en tanl;ö\ n-"F'en tane n eo-F'en t3 n e - - - - Tota l-;:; Sb-·e?ITI nIJmber-' Equip. COnG2ctlon: Temper'.:; t'Jt-'e, C Pro (·=s·:;u:--· e '! b.Ei t'" ~=. Enthal;J'y', t'1Ji_i_-w 1) a pDt-· fl'''' .. 3(:·~ i i:=n

rl

DWt~':3 tes F:Ot'opane i-E:u·t6n;~ n-81J tane:' i--F't?n<:-.ane n-F'entane - - - - Tot:=,ls :3 ti" '2-3 fTI n u mb er' Equip. connection: T ~:?lTIp t~t-'a tu t'" (? ~ C F'I'-'E,::;sUt'e, b·:=,t'5 En-!.:halpy, i'1.]i ht' \/.3p ,:w ft' a c: t i ':;n F 1. OWt':=, tes. F't-·Dpar.e i-Butane r"'\--E~u taliE i --'F'en t:lne n-··!::'I.=?rt t .. 3ni= neD-;::'en tan e ----.-- Total'::; ~)tt'eaITi m_HTibet·, Equip. connection: Tempet'atut'e, C F't'>::;'SSUI" e ~ t at"::; Enthalpy, MJ/ ht' 1 Ft'om <) te) 28.7523 3.90000 15189:::. 1.00000 I<gmo 1 Iht' 18.0376 51.24.76 44.6004 .000000 .000000 .000000 5187.39 3 Kg/ht' 795.350 297B51. 2592.1E: .000000 .000000 .000000 301239. 2 Ft"'om to ~2 30.6115 3.90000 161080. 1.00000 Kgmo 1 /ht' 19.0684 5405.30 47.0196 . 73602<;'E -13 .576560E-13 .115173E-12 5~71.39 I:'':'' ._J Kg/ht' 840.802 31 !t156. 2732.7:3 .5::'10t6:::-0[1 .415965E-l1 .. 830?27E--l1 317730. Ft-'om 2 tD 3 Ft-'DlTI 3 to 4 28.6209 3.00000 i61080. 1.00000 k·;rrlol/ht"' 19.0684 5405.30 47.0196 .736Co'2'7'E-13 .576560E-·13 .11S:73E-12 5~71.39 6 Ft'OITl 4 tel 65.3366 8.30000 124173. 1.00000 I<grr;o:>1 Ihr' 13.3:"79 3783.71 :::2.9137 .515220E-13 .403592E-13 .806208E-13 3829.97 8 65.3366 8.30000 1.00000 Kg/ hr Kgmol/hr 840.802 19.0684 314156. 5405.30 2732.78 47.0196 .531016E-11: .736029E-13 . 415965E-l1 : .576560E-13 .830927E-11: .115173E-12 317730. 5~71.39 7 .,. .--! Ft'olTI Lf t.D 65.3366 8.30000 44347.5 1.00000 Kg/hr Kgmol/hr 588.562 4.76709 219909. 1351.33 1912.94 11.7549 .371711E-l1: . 184007E-13 .291175E-l1: .144140E-13 .5:31647E-ll: .287931E-13 2214il. 1367.85 q f:::g i'ht' 8~fU. 8_':'::: 314156. ::7~32. 72 .53101t:E-l ! . .. LflS'?6:=:é::-·L i. · 83092'E - 11 317730 .. f3 !<g./ 1-~., 210.2()O 683.195 • 1 327CS4E --1 1 · 1039'7'1 E - 1 1 .207T3.lE--ll 79432.7 Ft'c)!Tl -4 to 1 Ft'om 5 to 6 65.3366 8.30000 12·4172. 65.3366 8.30000 88,~'7'. 50

(28)

Equip. connection: T'=lTipe,-'a tur'e, C

F't'ess' ... Jt'e, bat's Enthalpy, M,J/ht' Vapor ft'action F lOWt'ates F't'opane i-hJtane r-I-~ Bu ta ti (~~ i -F'en tane n--F~n t,::,ne neo-F'en tane _ ..

_---

_{fDta]. s} Sb'eaIT! nurr.bet' Equ:~. connection: Tem~et"'a t ur'e f C F't'e==,j[" 2; bar's En tha] py, t1J /hr' \/ Ct r:' '.Ji-· f t-· act i Oll F 1 DHr-ë, t ,?s F:'t·, ':Jp an 0:' i -E:,..,i ~ane n-8;jtane i _c, en t . .;-3ï': (? n-Pen'cane r, ;2'='-~'en t,~ r, ,Cf ~--- Ta t.a 1 s S t~·"?3iT1 numbet' Equip. connection: Tel:j~, '?r-':3 ·~:u t" c:?~.' C F't'e-::=lJr'e ~ b,:wS E n .~.:j-~.:; i p Y 'I !"~·I,J / h ('

\lap:Jt' f t'action

Ft'on', 6 to 7 56.9610 8.30000 55101.0 .000000 KgrMJI/ht' ~~:g Iht' 13.31+77 588.5511-3783.71 219909. 32. '7'137 1912.

911-·

515124E-13 .371641E-11

·

403515E-13 .2'1'1120E-l 1

·

806070E-13 .581547E-l1 3829.97 22241 1

.

12 Ft'orT! 8 to 9 61. 9836 6.20000 ~43li·7. 5 1.00000 kglTlo 1 /hr' f<'=öI /ht' 4.76709 211₎_.20t) 135i.33 73539.3

·

11. 7549 .184007E-13 .144140E-13 .287S'31E- 13 1367.85 683.195 .132754E-ll: .103991E-l1: · 207731E-l1 : 79432.7 14 Fr'om 10 te) 11 44.0000 6.18889 21270.8 .000000

..

. l .l FI"orr. 7 ti:l 11 56.9578 8.29000 55101. (; .000000 KgmoI/ht' 13.3477 3783. 71 .,..~ 9137 . .;

.

..;:.. 51512L~E-13

.

1+03515E-13 .806070E-13 3829.97 ~<g/ht' 588.554 219909" 1912.9L~

·

3716!t1E-l J

·

291120E-1 :l " 581547E-'1 J 222411

.

Ft' orT, '-=J t o l (> 58.6120 6.18889 55251.2 1.00000 f<grno 1 /ht' 7.42527 1702.67 14.0888 .241630E-l1 .189651E-ll .377082E-11 17211-.19 15 V'3/hr' 327,4tO 98959.2 8l8" 8!11 • 174326E-t)l, • t 36826E-V' • 272050E - (i i:: 100105" Ft'cJIT, 11 to 12 52.9353 6.18889 76371.8 .000000

---

-

---I::: J. Ol'oot' i j tes

F',' ':JO ,3 r. e i -31.Jt.~ne I l -=:.J t.an e i,-F'entane n-F·2ntane ne':l-F'en tane ---- Tota Is :3 b' o:aIT, n '.J mbet" Eq~ip. connection: Tempet'ab .. we, C F'~"s'ss'-we, bat's Enthölpy, MJ/rw 'vapCt' ft'action f<grno I /ht' 7.42527 1702. ,f::,7 14.0:338 .241630E-l1 . 189651E- l1 • 377082E -11 1724.19 16 Ft'OITI

1::

to 45.6700 6.18890 10905 .. 0 1.00000 f:::'3/hr' 327.410 98959.2 818.841 . 174326E-(i9: · 136826E -09 : · 27205()E -09 : 100105. 9 Kgmol/hr Kg/hr 20.7730 915.965 5486.38 318868. 47.0025 2731.79 .100000E-09 . 721460E-OE .100000E-09 . 721460E-OE .lOOOOOE-09 . 721ll_60E-_OE 555~.15 322516. 17 Ft-'om 12 to 13 ~5.6700 6.18890 6~'51~,b6.8 .000000 _ ..

_---_

.

_---_

.

_---_

._-Flm'wate'::; F't'cpane i.-3utane n-But,ane i-c:::?nt.ane n-F';:nt.ane

!-"O?c-;::'en tane

- - - - 1'0 t,a 15 _ _ _ _ I , ~:::g mo 1 /h t' 2.65'7'30 2.33416 • 2:::'779bE-:~ 1 . 188214E-ll • :3742:l :2E·-l1 356.384 f<g /ht' 117.259 135.661 • 1 73003E·-<)9 : . 135789E-09: .269979E-09: 20675.8 KglTlol/ht' 18.1.137 5134.99 44.6684 .976020E-l0 .981179E-l() .962579E-l0 5197.77 f:::g/hl" 798.706 298446. ::?59:S .. 13 .704159E-OE " 70788U::·,():, . 6<7'4462E-O:~ 301 (=]!l() "

(29)

:

; t i·-e~ITI number-"'

Equip. cannection: Tempet'atut'e, C F't··essut'e, bat'S Enthalpy, M,j/ht' Vapar ft'acti.an F lowt'd tes F't'apane i-Butane n--Bu tane. i-F'entane n--F'en tane neo-F'en tane --_ ... TDta L::, Equio. connection: T€!mpet'ab.we, C F' ,., 2:' S3 U I' 0::>, b .3 , .. , ';3 EnthaJ.py, f1,J/ht' F'r"'opdne i ·-:~:u tane n-'Butane 1 "-;::''?n t ë.l n e n-Pentane _.--- Tata l':; ~:3ti"""f?·~rrl nu filb et ... Eqwip. eonneetion: T(~iTjper-· a tUl··' e ~ C

Fre':;:;ut'e, bat's

En tha 1 py, t1,j lhl" -'/apot' ft'aetion 1 t3 From 13 to 14 45.6700 6.18890 52766.2 .000000 I<gmol/ht' 14.5996 41::::8.80 36.0027 . 786672E-10 .790830E-I0 • T15:3::::9E -10 4189.40 20 ~<g /ht' 643.755 240547. 2092.48 .. 56755=E-08: • 570552E-<)8! . 559737E-08: 243283. Ft'om :[ 4 t:;, 0 28.6448 3.90000 52766.2 .133432 f<'~fTI01 Ir'!\"~ 1 4. 5'?96 4138.80 36.0027 .78·S67:E-l0 · 79083C'E -10 · 7758:39E-1 0 4189.40 f<q /ht' 2405-47. 2092 .. !4-8 u567552E-08: .570552E-OS: . 559737E-(l8: 243283 .. Ft'OITl 16 to 1 44.4633 6.00000 317.974 1.00000 1 Cj Ft'om 13 to 15 45.6700 6.18890 12700.6 .000000 Kgmol/ht, 3.51406 996.188 8.66567 .189348(-10 . 190349E-l0 • 186740E-I0 1008.37 :~ 1 f(g / h t' 154.949 57E198. 1~. 503.6Wi .136607t;:-··y' · 137329E - Ol: · 131

+

_725E_·_··_{Ci: .} 58557.0 Ft'OIT' 15 to 16 45.1057 6.10000 12700"S • 525837E-02 f<gmo 1 jhr' 3.51406 996.188 8.66567 . 189348E-10 . 190349E-10 • 186740E-I0 1008.37 Kg/hl" 57898. L~ 503" 6i_"9 · 136607E -':>' · 137:::~9E-(> .134725E-()F 58557" ~) Ft'om 16 t iJ 0 44.4633 6.00000 12382.6 .000000 --~---1::"1 mOoit' a tes pr··· :~~' 2 r: e i -8'..1 tane q-·Eu tElni3;! i -F'en t .:;ne 1-, -'='::;n tane neo-Pentane -._-- Total:5 _ _ _ _ I , Stt'eam n'Jrr,bet'

Equip. connection:

Tempe~'atUt'e, C Ft··· -,.::;.,·:::;·::;u r"' e, b a~"' ~=. . 773950E-Ol 10,,~779 . 682451.J.E-Ol .6c;'9311E-13 .5.iJ.7798E-13 .1094-27E-12 10.4235 24 Kg/hr Kgmol/hr 3.4-1266 3.43666 597.352 985.910 3.96642 8.59742 · 504525E-l1: . 188649E-10 .395214E-11: .789472E-11: 6()4.731 . 189801E-l0 . 185646E-10 997.944 """\r:::" L--J I<:r;/ht .. · 151.S:::S 57301 . :J. 499.682 · 1361 ~)3E _·CO;:: .136934E-(ir · 133936E -(,~ 57952.3 Ft'oIT! (> to 6 _Ft'OIT' ₆ _to ₀ 48.4564 4.68751 53.0000 4.68751

(30)

a: arcot. OUT 12-.]un-139 5:06 prn

(C) CopYt'ight, COADE I McGt'aw-Hill, 1986

at'.;:ot

TDF"]LCJCiY

Equipment Stt'earn Numbet's

1. COLlyj # 1 1 3 5 -6 -9 -7 -8 .3 ""!f11>< AD8F Er,jTI" D\/DR 7 HX.EF: #7 8 'v'i:".:iL I.) #::3 ':;' 'v'AL') #9 10 1'"1;"1 1 >< # 1 (> J1 H;{EF: #11 1 '2 r'U1 I >< # 12 13 AD8F #13 14 D',JDF: # 14 i5 '.,i AU/ #15 16 ~,/AL',) #lb 1.7 ADBF #17 6 29 16 -10 10 - l l 11 -1::: 13 -14 i4 -17 "I .-a -~..::. (> -15 <)

o

-16 8 17 -5 -18 18 -19 15 -20

o

24 21 19 20 -21 (; 23 -24 25 -26 -27 26 -1 0 27 -28 0 28 -29 -30 <) (l

o

(I I) (I

o

Stream Connections

Strearn Equipment

1 2 '-. ...J :, 7 8 9 10 11 12 13 14 15 1<:'0 17 1:3 19 20 Ft-· orTt T Cl 15

o

U 7 1 1 1 1 2 3 3 5 5 5 oS 7 8 9 10 11 13 1 1 1. 1 j 2

o

7 4,

o

5 2 7 :3 < ., 1. .. ::" 10 11 1:2 .. -;0-.l. .• :' iO (l (> <)

o

Ü Cl

o

(>

o

<)

o

(> (l (l

o

(> (l (l

o

(> (> <) <)

o

,-, , .. ()

o

(;

o

<)

o

(l <)

o

<) (i

o

<) I)

o

<) (> (;

o

(>

o

(> <) {) Page 1

(31)

CHEI<ICAD F:EF'ORT Stream Connections Stream Equipment .1::.· . ..; 26 ."-\,-, .';:'0 30 Ft'Clm Tc) 13 1.4 14 16 17 17 p~ 15 1.:-, 17 2 I D nurnbet's

Kvalue option: Soave-Redlich-Kwong Enthalpy option: Soave-Redlich-Kwong

I"ll SCELU\NF~iJU~3

Recycle calculations are NOT converged.

6~ 7,

Recycle equiprnent l i s t (KE2l: 7, 8, 1,

1' , 1 2 , 1 3 , Sb'eams used in conv. t'outine (f<EL~) :. ( 0)

i.) =0;::; 1 <3"y' factcw

PrefE~r~d cut stream l i s t O<E3) : Convergence tolerances, F 1 O\'W '0,1 tes: \.jap Ot" ft·, ac t i on : Tempet-·.a 'tt..Jt-,?: F'~'esSLlt'e: Enthalpy: Fldsh calcs: ~1.::s;<. loops in t"ec:ycle calc.: in fl.ash C<31'=5: Ert'ot' .01000000 .01000000 .01000000 .01000000 .01000000 .. 00500000 100 1,

_'-'

L

_,

_8, 8. '"' ...:.:... 14, , ' .10, 3, 4, 15, 16, 17, ..,1.1

_

.

,

F'aqe 2 6, 9 . 10,. 17,

(32)

CHEMCAO: Chemical Engineering Simulation System

***

DIVIDERS

***

Eq/..J i.pmen t no. r::"

iLl· ...J F.:>: ter' r, al name #5 #14 r:t'action/flow 1

_·

70000 .80600 :4' .25000 19~OO .. :..:.

·

3 .50000E-Ol

_·

00000 J.j.

·

00000

_·

00000 <= ₀₀₀₀₀ .00000 ,.1

·

~::o

·

00000

_·

00000 t'1rJde

_·

₀

·

0 Stt"'i?am #

_·

(;

_..

₀ Camp. 10

_**

.. 0

_·

0 COiT,p. 10 #

_·

₀

·

(i Comp.

ID

#

_·

() _..₀ CÜITlp n 10 # 0

·

0 COiT.p. 10 it-

_·

()

_..

() C:OiTip ..

_{ID **}

(;

·

0 Comp.

ID

# 0

_·

() Comp. 10 # 0

_·

0 Comp.

ID

#

_·

<)

·

(; Comp. ID # 0 () ...

...

"" .. " " " " " " "

***GENERAL FLASH UNITS

***

Equipment ilO.

E>:tet'n:. 1 narne

r-lc'cj e

F'at'.:srr,etet' #

F'::i! .... ame tet ...

Heat dl..Jty f<-'la 1 u':?

**

f::: - v a lu e # f:::-·v.'3 1 ue # f:::-value # # .... ~:::-\.i;:j :Lue ** 1(·-\/.:. 1I..Je # M,] ,'ht' 1 4 5 #3 :3. (l 3.0000 .00000 .00000 3.0256 1.2634-.. 92:3t.8 .. 3904(i .29176 .. 6t:,549 3 13 #13 ,'.: .. 0 ~5.670 .00000 .. 000<)0 2.141:3 .9°835 .76233 .35341. .. 279:33 17 jH7 8.0 6.0000 .00000 ,,00000 2.1567 .99837 .76020 ,,35502 .27642 n 5645:~ . . . n . ·' . . . . . . . . . . . . . . . . .. . . . . .. . . . . . . . . . . . . ,. • • • • "' .. . ... s .

VALIJES

Equip:nent ilC. E>: tet'nal name

Outlet pressure bars

#8 -.10000E-01 #9 6.2000 9 15 iHS 3.9000 U::' #1.6 6.1000 ... .... ...

...

"'

...

"

...

" " "

(33)

CHEMCAD: Chemical Engineering Simulatien System

(C) Cepyt'ight, COADE I McGt'aw-Hill, 1986

***EXCHANGER/CONDENSERS***

Equiprnent no.

E>: ter-Ti.:; 1 name

{'wea i\lumb.::;c-·

0+

shells ~3hell p.3sses TU!J2 passes I·'/.:Jde Min. delta T or T-out Delta p. stream 1 Del ta P, stre3ffi 2 Q, stream 1 MJ/hr Water usage, DM3!hr Cor~ected delta T #6 .00000 " 000<)0 .0 .0 " () 8. (:. 65.34 ti O()O()O .0('000 -l.ÛûOO .00000 .. ()(i 6 #7 .00000 .. OOO()(i .0 .0 .0 9 .. 0 52.00 " ()OO<)() " ~)OOOO 66999. .00000 .00 7 11 jUl .00000 ..00000 .0 .. Cl .0 5 .. 0 44.00 " O(i(I()() " OOO()O -35998. .00000 " 0<) Page 4 .. "

...

"

...

..

...

.

"

....

"

...

..

"~

...

,,

..

.

....

...

.

*~* 3IMPLE MIXERS

**

*

l:'qul:::r;ent n·:J. C;: te"na 1 n·3IT,e #2 10 jf 10 12 tj: 1 ::::~ ~ .. " ~ ,. ~ .. '" 11 .. .. .. " .. " .. u .. .. .. " .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. .. " .. " " " .. .. .. .. .. .. .. .. .. " '" .. .. .. .. .. .. '" .. " .. .. *~* ENTROPY MACHINES *~* Equ:lpm.::;nt no. E:<tet-·n.31 nëHTle f'lode

Outl~~ pressure bars

Adiatstic efficiency

The·=,r'st i ca 1 !lp

Act~al horsepower

Entropy in KJ/deg C

t::nti·-·'=:::y Dut, ideal

Ent~cpy out, actual

~1:Ll. .0 8.3000 .00000 4853.1 6066.4 4 .. 3221:2E +(,6 .32227E-'-(',s . 331 S"'7E -h~'·S . .. .. ~~,." .. " " u • • " " .,.:r . . . " . ... " . . . . " • • • • • • • • • • • " . . . "" .~ . . . . " .. "''' :t. "

(34)

CHEMCAD: Chemical Engineering Simulatian System (C) Copyright, COADE / McGraw-Hill, 1986

***

RIG. FRACTIONATORS *~*

Equipment na.

E:::,-:tet'r;al name

Number af st3ges

Feed 1, sta'~e #

Feed '-', -:;ta'32 # FE\f~d 3'J '5töge # F·eed 4,5t.39E' j:j: ~-:·(=~:.::d 5., ;;.tage # #l 97.0 1.0 11.0 43.0 67,,0 85 .. 0 CaMdenser type 1.0 CQnd. deg. subcooled .00 Condenser made 2.0 './a1'-'e of cond. sp,sc. .00000 Cmnp. 1 i;:i t pos 1. t j Dr, 0 Reboller mode 6.0 Val. of reboiler 5pec .36000 C(JlTip~ l i s t p(J"=:;i t icin 4.() S i de':; t i'··eam :3 i cJ e ~ ~ t' e alTI Sid~·str'eam :3 i d(·?s tr' eaIT! :3 i des t~"'e3rT1 ~3id?stt'e3m 1* # # # # #

..

" . 1 ''-; t.,,, '::1 e 83" C' S!J2C 9~O.00 .-, ...:.:. st,a':;!e 85" ()

"

3p"-"e -3350.0 ,~, st.~·:;Jl:; ,,()

"

·::;pt~C .OOÜC'O 14- ~)ta·~'2 .. 0 Sidestream # 4 spec

Cand. delta P bars

Celm. delta P bars

Cand. pressure bars

Cend duty MJ/hr .00000 • (H)()(H) .90000 3.9000 .00000 2825.1 28. (JO 2~3.

oe'

85.00 F(ebl' dl...lty Mj/ht' E;3L temp '5 tg 1 C Est. temp stg . ..::. ...., C !::,"::: ' .. temp sti_{' ;} ~.~-₁ _C

Est.. temp stg f\i C 85 .. ()()

Est dist rats Kgmol/hr .00000

Es~. reflux Kgmol/ hr

.!-,=';J ~~"'.;3.;/ I~ f f ie

:Sott tr'ay e·Hic

SOI-lt"=e stt'e·31T1 :ft: De·"t.. sb'EalT! :ft: I/O Optian T(J!,o.JF equip # Etage

**

Phase eptioll Seale H><EF: equ lt"J # .80000 .80000 97. () 1" 0 11.0 Lf::::"

°

67.0 85 .. 0 1.0 • (10U00 2. () J.

(35)

CHEMCAD: Chemical Engineering Simulation System (C) Copyright, COADE I McGraw-Hill, 1986

Stl····I:::?:::tm nUITrbe~··

Equip. connection:

T •. 2ITip '=t-·.:3 tu('e? C

F'I'-' eS';:,I_W e, oat'S

F.~n +:b a : iJ 'y, ['l,J Ih ,,-, 'v'apOt' fr' a,= t i on F 1. ClWt' a tes F'r4 • DP 3 ;! E' i.-8u L"ne n- Bu tane i -F'er! tane r. '-41::'·::-r. ta n ~~ neO-F"E'nt.5ne --_.--'.- "Y'.::'t.al';:: :3 tt'e a rr, nUfnbet' Equic. conne~tion: Te.fnpe" ,:;tut"e, C Fr" ~..?' ... ::;s;.J j'" e ~ b a~-' ,=. Enthalpy, I"\.J/ht-, ;·)dlJDt... ft"' 3C t .: cin r-:1 1::'".'Jt-·E.! te:=. F't"'Dpane i '-Bu c.~ne n-81...l tane i "-Ff.?!-i t.,.:;: n i::" n-F'er, tane nE.'C--=':=;; tane --- T 0 t,:3 l: 1 Ft'clfTl 15 to 1 28.6639 3.90000 52729.1 .133220 F"'OrT: () tD 1 1<':lITiO 1 /ht' 14.764(; 4129.7l 42.2170 • OOO·.)(!() .00ÜOOO .8i7712E-05 4186.69 28.8000 4.00000 3516.40 .000000 Kg/hr Kgmol/hr 651 ~ 001.t . 432000 240019. 342.706 2453.65 6.86200 .000000 .000000 .000000 .000000 . 589947E-03: .000000 243123. 350.000 lj. i<:,:;! /' t-, ,", 19.0486 1. (?';t:L 8:: 1 398.81'7 .. OOO()(:ti) .000000 .OOOO(i() 20335. '~

Fr'om (> tel 1 Ft'olTl 0 t8 1

83.6000 4.60000 71.7000 4.30000 32378.5 1.00000 i<g [T, 0 1./ r, t' 2.091(;1) 551.337 366.1:)86 9.22200 9.02800 940.000 f:::g Iht' 92.2006 32043.7 21276.9 665.330 651.331i· 16i.318 54890.8 1.00000 f:::grTlO 1 /ht' .950000 272.360 381.690 .000000 .000000 .000000 655.000 Kg /I-,t' L~j. 8893 15829.6 2218:3" E! .000000 .0(H)OCr) • ()()(H) (l ,) 38055 .. 3

(36)

CHEMCAD: Chemical Engineering Simulatien System

(C) Cepyt'ight, COADE / McGt'aw-Hill, 1986

S'b'earn nUiTIbe~-'

Equip. connection:

T(~fflpEr-'a +:Ut"'E, C

F't-· ES·:;·U t' e, b ·:31' 5

E~r; tha ]. p Y', i"1,] I hr' 'v'apcw f t '.:3c t ion F 1 OWt' a t.es F'~~· op.~ n e i. -Bu tanE.' r-,····ijut,3ne i-Fentane n '-":='E'l tane nec-F'en t.:lnE --.---- TDt"ds: 0:-. ..J Ft'om 7 to 52.0000 !t.68751 1 089'-? 1. 1.00000 1<9mo 1 /ht-· .. 578163E'-05 32:3 .. 279 2701.7:3 1 :::::::. 175 166 .21::-15.5550 3350.00 7 6 1 Ft'om 1. i:o 28.7582 3.90000 151705. 1.00000 K9/hr Kgmol/hr .254935E-03: 18.2135 19079.6 5109.94 157027.. 52.4035 9968.77 .000000 11991.6 .000000 1122.23 .101844E-04 199190. 5180.55 1<0:;) .. iht' 803.106 :29 (:;,99() °l .. OOO()()O .OOOOC!O . 73Il·76ÜE-O~: 300839. Sb'eam numbet'

EqU1P. connectlon: Ft"'om ta 0 F~'OrTi ! téJ 7

Tempet'ab_we, C ~-:'r' '~'sS;_j t'" e., iJ a~" .:; Enthalpy, !"IJ/hl" I,) a iJ Dr" f t~ -3 ct i tJn f=-1 D~····.lt'" a tas FYopane i ·-E:, .. ; t.3 ne n-E:'..Jtane i. -F'en tan>=:' n-F·en-t..:ane ne':J-Fe:-, -:ar,e

--- To l:l1 s !t5.8571 !t.66876 30069 .. 2 1.00000 .25L;.846E-()!f 152.966 71_PL₀₆₅ 6.33:202 4.43536 2. :20154 939.999 1+8.6209 !t.68751 L~1992. 7 .000000 Kgihr Kgmol/hr . 112372E-02: . 577587E-05 10634.0 328.180 43245.1 2701.73 456.830 138.242 319.993 166.295 158.832 15.5564 54814.7 3350.00 f<g,l h~' .2546:3 J.f:ë --O~:; 19073.8 1 '.S702~5, 9973. ,::;,1 1l997,,5 1122.33 1'7'91.9:: ..

(37)

CHEMCAD: Chemical Engineering Simulation System (C) Copyright, COADE / McGraw-Hill, 1986

S t"'earn numbet-· Equip. connectien: T (;?!TJp et-· a tl..J t' e, C F't't?ssur'e, bat's En tha 1 p,!, t'1,] /ht' '';apol' tt'·3ction F lowt'B c:.es i-But~ne neo-F'en tar,l? . -- - - Tc [.3 1 :; EDuio. connec~ion: Tempet-.::; tu'-,?, C En thë 1 P'l, t1J /h;' -'v';3POt- -tt' ae t i Dn F 1 o~·,lt"\ ~ !.s·s F'I"opant? i---t:utane n-8,-, tane i "-F'::=n t..3r-e n--F"en tane neD-F":?n t,3n~ - - - - Tc;t.31s Ft'CHTi 83.1675 ~.80001 1~1. 2'::?1 .000000 f:::gm';J I /hr' .000000 . 392703E-02 . 472461 2.82557 4.51372 " ::::313T?E -(; 1 7.8~881 11 Ft".JfTI 3 to 28.6272 3.00000 160:380. 1.00000 f:::g rTiO 1/ rt' 19.2543 538'=?65 .408371E-10 .269324E-l0 • 1 072f3,:SE--·:) 4 51+64.15

o

f::g/hr' .0(;0000 .22823<7' 27,,~594 203. 8511, :325.647 2.39048 55'7'.579 4 f:::':;J/ht' 848.999 31::::46. 3210.32 . 294623E-08: . 194307E-08: . 774026E-03: 317306. 10 FI'OITI 2 to 30.6176 3.90000 160880. 1.00000 l<gmD I/hl' 19.2543 5389.65 55. 236() .408371E-10 .269324E-l0 .107286E-04-546~.15 ~ -:0" .1.'.> Ft'DlTt 4- to 65.3420 8.30000 17716i3" 1.00000 f:::grrlol/ht' 19.2543 5389.65 55.2360 .408371E-10 .269324E-l() .107286E-04 5~6~.15 .. ~ !<g/hr·· 81.J.8. 991~ 31324(~ .. 3210.:::::::: . 191.J.307E-08 .771.1·02:'::E-03 31730~, . K·~ /;-!r' 848.9:::'-= 31324-6. 3210.3:: . 294623E-08 .194307E--O(3 . 774026E-(J3 31 730,,s.

(38)

CHEMCAD: Chemical Engineering Simulaticn System (C) Copyt' ight, COADE / McGt'aw-Hi 11, 1986

Equip. connection:

T(~iTlpe,'·at:.,Jr'e, C Ft"e'55Ut'e, bat's En tl-ia Ij:-'/, r'1,j /ht'" V:::;PCt' ft"ae: t i cr, F 1 (JWt' a tes 1"'1""' Dp.~ r, 2 i-Butane i -F'en tane n-!='en~:3n!~ neO-F'E'ît.:;ne .---- i,~ta l'::: :=.; tt"' eam nf.J!.lbe~'" Equic. c~nnecticn : TI=mpe~-'atur"'e" C I:~ ,., ,:~S·:;·;.J i' '=', b d ,"'3 En tha 1 Vi, 1'1J / hr' 1../ a p C j"""

+ ('

-3 C t i Co Ir Ft"opane n-Bu t .:lf"le i·-F'en t .. ::; n e n--Fert t .::Ine n ;:;;"(j--:':' .:?!"'"! t;) r. e - - - - Tat:::;ls - - - -: 14 Ft'om 5 to 6 65.3420 8.30000 124018. 1.00000 K.:;Jmol/ht' 13.4780 3772.76 38.6652 .2858S9E-I0 . 185527E-l0 .751001E-05 3824.90 16 F" om 5 te' 65.3420 8.30000 885·3" ~·2 1.00000 0 '''''-1-'' • ,,".:J.::.. / L / f<g Ihr' 594.299 -::'10'/7 " 4 -.... ,_ .. '_'. 2~47.22 .206236E-08: . 136015E-08 : .541817E-03 : 222114. 2 f'::,;,/ hl" Lt2 .. 4500 lS6ó2 .. .!+ 160.516 .147311E-09 : 15 Ft'om 5 to 9 65.3420 8.30000 lt~292., 1 1.00000 f:::gmol/ ht' 4.81358 13!j·7.41 13.8090 .102093E-J.O .673311E-l1 . 26S215E-05 1366.04 17 Ft'DITI

,

s

te. 65.3420 8.30000 121~·017" 1.00000 f:::gmol/ ht' 13.4780 3772.76 38.6652 .285859E-l0 1< SJ /t',·' 212.250 78:::11,5 .485767~-09 • 19~~::506c--O:-?: 79326.3 ~ i f<';1 int' 269.483 2.76180 .204U3SE-l1 . 13466:':E-ll . 536430E-06 273.207 . 971533E-lü: .188527E-·l0 .387013E-04: .751001E-05 SQ L~. 29'"7' 219273 .. 2:::47. 2 :-.206236E-()f:l . 13,Ylt SE-·()i3 .541817E-(\3 15865.3 382~.90 2221:t 1+ ..

(39)

CHEMCAD: Chemical Engineering Simulation System (C) Copyright, COADE / McGraw-Hill, 1986

Equip. connection:

Tamp.:,·a tUt'.? 9 C

F't··es sr..Jt'e, bat's Ent~lïä.lP/'J t/IJ/ hi'" 'v' ap Ot' +t' ac t. i ':ir: F 1 O\l.!t' a tes :::'t"' Dr' ·5n e i -8u tane i. -F'en t.3ne neD-F'en tanË' ~qUIP. connect ion; ~'errlper"'atut" e'l C Entt-,.:ilpy, IvIJ/ r:/""' F' t' opa n E:' 1. '-8u ~·3!d:? n-But.ane i - F,::?n tane n-Pent.ane 18 19 Ft'OITl 7 to 8 Ft'DITI 8 t Cl 12 57.5873 8.29000 57.6381 8.30000 57062.0 .2l4-l4-6l4-1E-01 1<: ';HTi 0 1 /hr' 13.4911 3774.23 38. 5117₃ .2S·5171E-IO .188498E-li ) • 7l+5;3'7"?E -05 3826.27 20 57062.0 .2l4-8l4-87E-Ol Kg/hr Kgmol/hr 594.877 13.4911 219358. 3774.23 2240.37 38.5473 .205739E-08: .285171E-IO .135994E-08: . 188498E-l0 .538136E-03: . 745899E-05 222194. 3826.27 2J (<:<;.1 /~: ~ .. 594 ~ 87·7 22.!.tO.37 222!9lJ.,

Fr'OfTt 9"to 10 Ft'DIT. 10 te. U.

57.8364 6.18659 62.0090 6.20000 1.00000 Kgmc,l/ht' 4.81358 1347.41 13.8()90 .102C'-?3E-lü .b7331iE-l1 .2682:5E-ü5 1366.04 f<g/ht' 212.250 78311.5 802.579 . 736560E-09: . 4857,S7E-O'::;o: . 193506E-03: 79326.3 58628 .. I~ 1.00000 f<gmo I Iht' 8.34938 1808.77 17.416l4-.133L_n1E-1₀ .919b75E-l1 . 320296E-05 183l4-.5l4-f:::g /h~' 3ó8. 1:3;:: 105126. 1012 .. 2" .962651E-(I'-? .231081E-03 10650b"

(40)

S"tI'-eaiTl "uITlbet-·

Equip. connection: TE!lTlp er· -3 tu r" '::;, C Pr-·e·:;:;,_we, b.a r' S Enth.alpy, t1.J/ht-· './ a P Ol' f t' act i on Flm·.jt'.:ótes Fr· Dp.:3 r! 2 i -BIJ tane i-F'entane:' !i·~-F''':?n t,3n~? neD-;::'en talie . __ ._-_.- To-:a l'~ Stt"'E~aiTl number' EqU1C. CDnnectlGn; Tempe"atur'e, C Entnalpi, r1.]/ ht" i..)apot-· f t-· ae"t i I~i-I I"·':::'!:?!! t..:; n e n-F'ert"tane ---- Tertal-=: -FI"om 11 tel 12 44.0000 6.18659 2:2631.1 .000000 f:::gmo 1 /hr' 8.34938 1808.77 17.4164 a 1:::~:!t31E-l0 ,,919b75E-l1 • :::202'~6E -()5 1834.54 f:::g/hr' 368.158 105126. 1012.24 .962651E-09: • 66350S'E -09 : . 23108lE-')3: 1065')6. Ft'om 13 ,_,_, 10 45.6700 6.18664 14272.3 1.00000 k':;HTtol/ ht' 459.297 3.58530 • 311 782E - i 1 .245100E-l1 · 5166S0E -O.~. 466.lt05 f:g /hr' 155.334 26694.3 208.378 .224938E-09: . 176830E-09: .372742E-04: 27058. 1 Ft'OITI 12 tel 13 53. 18LtO 6.18659 Ti693.1 1.00000 I<gmo 1 /ht' 21.8404 5583. ()O 55" '?é:.37 " 1 OOOOOE -'Yi .100000E-(;9 • 1. 06620E -;)Lt 5660.80 25 3252. 6.~ • 721Lt60E-08 " 769221E--O~~:' 328700 . Ft'orn 13 tD 1 LJ. lt5.6700 6.18664 651.~:2Ci 11 8 .000000 f:::grno 1 / ht' 18.3176 5123.70 52. 3781.~ .968822E-l0 .97549(:'E-I0 .101453E-OLt 519ll-.40 f:::g/hr' 3('4L1·.23 .698966E-(ll3 • 70~~::777E--·OE: .731943E-!)::: 301641 "