Jk1gc Cvd Analysis

8/17/2019 Jk1gc Cvd Analysis

1/37

Feed Stream Component Flow rate kg /hr Temperature

1 2000 kg/hr 70

2 5000 L/hr 70

3 22000 L/hr 70

??? acetylal!cyl!c ac!d ????

" #ater 22000 25

5 $utlet tream %rom the reactor ??? 25

??? &!'er outlet Stream

Crytall!ne al!cyl!c ac!d

L!(u!d acet!c anhydr!de )pure*

L!(u!d concentrated )+5,*phophor!c ac!d


2/37

&olar &a )&-#* &elt!ng .o!nt o!l!ng .o!nt en!ty

13-10 15+ 211 1-""

102-10 73 13+ 1-0

+-00 21 15 1-

10-20 135 1"0 1-35

1-00 0 100 1-00


3/37

Stream!ng heat Capac!ty

"-1" 4/g C

1-7 4/g C

3-"1 4/g C


4/37

eat alace


5/37

Flows: (kg/hr) Processor Feed

2000

5000

phophor!c ac!d 2100

acetylal!cyl!c ac!d 0

6cet!c 6c!d 0#ater

Total

Temp 70

.reure )k.a*

Crytall!ne al!cyl!c ac!d

acet!c anhydr!de )pure*


6/37

Reactor Outlet Mixer Outlet Pump Outlet Cooler Outlet Seperator

70


7/37


8/37

1251

5000

2705

+5

For hot fuid

side o a heat

exchanger let,

mH : mass

fow rate o

the hot fuid

in kg/hrCpH : mass

heat capacity

o the hot

fuid in Joules/kgC!iH and !oH :

"especti#ely

inlet and

outlet

temperatures

on exchangerhot side in C

mC : mass

fow rate o

the cold fuid

in kg/hr


9/37

m 8 Cp 8 )T! To* 9 mC 8 CpC 8 )ToC T!C* : )3*

CpC : mass

heat capacity

o the cold

fuid in

Joules/kgC!iC and !oC :

"especti#ely

inlet and

outlet

temperatures

on exchanger

cold side

in C

Heat lost $y

the hot fuid %

&' % mH (

CpH ( )!oH &

!iH* + )*

Heat gained

$y the cold

side % ' %

mC ( CpC (

)!oC & !iC* +

)-*

Comparinge.uations )*

and )-*,


10/37

Gas Codesate P!" #al$sis %ork&ook%ritte &$ Ro&ert Mott' #ugust *

Th! workheet analye reult %rom C; and CC< tet on a ga condenate %lu!d

ata hould only =e entered on yellow cell

F!rt enter C; data )=elow the dew po!nt* on the heet >C; ata>

Then enter CC< relat!e olume )a=oe the dew po!nt* on the heet >CC< ata>

@ecoery %actor %or !nd!!dual component and %or tock tank o!l and ga are hown on the heet >@ecoery %actor>

The heet >C; analy!> conta!n mater!al =alance calculat!on wh!ch can =e ued a a con!tency check o% C; data

Thee check are decr!=ed !n >.hae eha!or>A S.< &onograph 20A =y #h!ton and rule

The mater!al =alance check calculate l!(u!d phae den!t!e and compo!t!on-

en!t!e and Balue %rom the mater!al =alance calculat!on are d!played a chart-

onmonoton!c =eha!our %or the Balue or l!(u!d den!ty cure w!ll cat ome dou=t on the al!d!ty o% the C; meauremen

D% the l!(u!d compo!t!on ! meaured at the end o% the C;A two other mater!al =alance check can =e ued-

The &ater!al alance check are hown on the heet >&ater!al alance>-

6 >Forward &ater!al alance> calculate the %!nal l!(u!d compo!t!on %rom the or!g!nal compo!t!onA l!(u!d aturat!onA E%actorAamount o% ga remoedA and the ga compo!t!on at each tep-

6 >ackward &ater!al alance> calculate the or!g!nal compo!t!on %rom the %!nal l!(u!d compo!t!onA %!nal l!(u!d aturat!onA %!nalE%actorA the amount o% ga remoedA and the ga compo!t!on at each tep- Th! ! a =etter check %or lean condenate-


11/37

46CB BDF< 1

!trogen 0 2

Car=on !o'!de 0 C$2

&ethane 0-002 2S


12/37

0-000

0-000

0-000

0-002

0-000-15"

0-1

0-0

0-3+

1-0++

3-23"

+3-7


13/37

C!+ +ataThe %!rt preure mut =e the dew po!nt preure

The num=er o% preure entr!e mut =e et to d!play the chart correctly

um=er o% preure entr!e

.lu %ract!on

.reure )p!g* 5535 "500 3500


14/37

o o% preure !n C; .lu %ract!o

Gpre 3 Gplu

.luFrac

1

2

3

"

5

en!ty 7

&wre% )l=/%t3*

2-013 +

""-01 103"-07

1-0"

30-07

""-0+

5-12 35-01

5-12 3-"5

72-15 3+-13

72-15 3+-3

-17 "1-1+

ular we!ght !c gra!ty


15/37

n

2

7

C7

C

C7

C

C+

C10

C11

C12


16/37

Geeral ,-ormatio

S1 %lu!d

@eero!r temperature )deg F* 23

Dn!t!al preure )p!g* 10""0

C5

CC. +ataonly enter data at or a=oe dew po!nt preure

enter preure !n decend!ng order

.reure @elat!e

p!g olume10""0 0-3715

5535 1

C"

C5

C

C7

$!l %rac 5

Calculated o!l ga rat!o aume ur%ace o!l 9 C5

Ttd 520 deg @

.td 1"-7 p!a

e%!n!t!on o% o!l %or ur%ace o!l andga recoer!e


17/37


18/37

Forward material &alace ackward material &alace

Calculate re!dual l!(u!d compo!t!on Calculate !n!t!al ga compo!t!on

Calculated den!ty o% re!dual l!(u!d "1-3

en!ty to ue !n calculat!on 51-2

Measured Calculated Measured Calculate

2 0-00 0-20 2 0-3+ 0-

C$2 0-00 1-33 C$2 1-7 2-++

2S 0-00 0-00 2S 0-00 0-00

C1 0-00 37-2 C1 -25 117-"

C2 0-01 5-+ C2 7-02 11-5

C3 0-15 7-2 C3 -3 10-+3

!C" 0-1+ 1-+ !C" 1-"2 2-30

nC" 0-1 3-37 nC" 2-32 3-75

!C5 0-" 1-32 !C5 0- 1-"0

nC5 1-10 1-2 nC5 0-" 1-"0C 3-23 1-+7 C 0-+7 1-5

C7 +3-7 3-12 C7 +-53 17-"7

100-00 100-00 100-00 171-


19/37


20/37

02000"0000000001000012000

0-0,

10-0,

20-0,

30-0,

"0-0,

50-0,

0-0,

70-0,

0-0,

+0-0,

100-0,

Reco0er$ -actors -rom depletio' o water i-lux

C1 C2

C3 C">

C5> C

C7F Ha

$!l

a&adomet pressure (psig)

R e c o

0 e r $ - a c t o r s


21/37

3000 3500 "000 "500 5000 5500 000

0-00

50-00

100-00

150-00

200-00

250-00

Calculated oil gas ratio 1 assumes sur-ace oil 2 C34

pressure (psia)

O G R

( & & l /

M M s c - )


22/37

3000 3500 "000 "500 5000 5500 000

0-0100

0-1000

1-0000

10-0000

510alues calculated -rom material &alace aal$sis o- C!+ data

C$2

C1C2

C3

!C"

nC"

!C5

nC5

C

@ow

12

@ow

127

@ow

12@ow

12+

pressure (psia)


23/37

3000 3500 "000 "500 5000 5500 000

0-00

100-00

200-00

300-00

"00-00

500-00

00-00

700-00

Oil ad Gas +esities calculated -rom material &alace aal$sis o- C!+ data

l!(u!d den!ty)kg/m3*

ga den!ty )kg/m3*

pressure (psia)

d e s i t $ ( 5 g

/ m * )


24/37

Calculated modi-ied &lack oil properties

.reure )p!a* 5535 "500 3500

.reure )p!a* . 55"+-7 "51"-7 351"-7

Moles o- Gas Car=onGno

up to C3 "-0 7-2 +0-3

C" 3-737 3-53 3-"25 "

C5 0 0 0 5

C 0 0 0

***6**7 *896 *396;;<

Moles o- oil

!C" 0 0 0 "

nC" 0 0 0 "

!C5 0-57 0- 0-7 5

nC5 0-"2 0-77 0-757 5

C 0-+ 0-57 0-771

C7 0 0 0 7

C 0 0 0

C+ 0 0 0 +

C10 0 0 0 10

C11 0 0 0 11

C7 +-52+ -2 3-+ 7

!olume o- Oil

!C" 0-0000 0-0000 0-0000 5-12

nC" 0-0000 0-0000 0-0000 5-12

!C5 0-015 0-01" 0-01"1 72-15

nC5 0-0155 0-01"" 0-013+ 72-15

C 0-0203 0-017+ 0-011 -17

C7 0-0000 0-0000 0-0000 100-2

C 0-0000 0-0000 0-0000 11"-2

C+ 0-0000 0-0000 0-0000 12-3

C10 0-0000 0-0000 0-0000 1"2-3

C11 0-0000 0-0000 0-0000 15-3

C7 0-3171 0-15 0-100

6*9< 6* 6;3

Oil1gas ratio (&&l/MMsc-) ;7967 ;;763*


25/37

en!ty )l=/%t3*

35-01

3-"5

3+-13

3+-30

"1-1+

"2-5

""-1+

"5-35

"5-

"-00


26/37

Calculated reco0er$ -actors

Calculated reco0er$ -actors -or each compoet

6=andonment preure )p!a* 10""0 5535 "500 3500 2500 1700

Component

C1 0-0, I;6LJ


27/37

C 0-000 0-0 0-10 0-12 0-105

C7 0-000 0-"+5 0-5" 0-" 0-32

!olume o- oil produced (-t*/mol o- e=uil gas)

!C" 0-000 0-000 0-000 0-000 0-000

nC" 0-000 0-000 0-000 0-000 0-000

!C5 0-000 0-001 0-002 0-002 0-002nC5 0-000 0-001 0-002 0-002 0-002

C 0-000 0-001 0-002 0-003 0-002

C7 0-000 0-015 0-015 0-012 0-00

"otal 6 6;7 6; 6 6;8

Cumulati0e total 6 6;7 68 637 6


28/37

+00 2 2 2 2

I;6LJ


29/37

0-12" 0-252 0-000 0-000 0-000 0-+

0-35" 2-7"5 0-000 0-000 0-000 7 +-52+

0-000 0-000 0-000 0-000 0-000 0-000

0-000 0-000 0-000 0-000 0-000 0-000

0-003 0-00" 0-000 0-000 0-000 0-010-002 0-00" 0-000 0-000 0-000 0-015

0-003 0-005 0-000 0-000 0-000 0-020

0-00+ 0-07" 0-000 0-000 0-000 0-317

6;9 6 6 6 6 6*97

67 6;


30/37

I;6LJ


31/37

en!ty )l=/%t3*

5-12 35-01

5-12 3-"5

72-15 3+-1372-15 3+-3

-17 "1-1+

Dn!t!al o!l


32/37

temperature )deg @* Tre 722-7 deg @

preure )p!a* . 55"+-7 "51"-7 351"-7

welltream produced )cum %ract!on* p 0 0-07+7 0-21+

l!(u!d olume )%ract!on* SL 0 0-17 0-22"2

e( ga E%actor E 1-023 0-+202 0-515

Produced gas phase compositio

ga phae compo!t!on 2 0-3+3 0-"05 0-"33

C$2 1-77 1-2+ 1-3

2S 0 0 0

C1 -25 71-+13 7"-33+

C2 7-02" 7-17 7-2""

C3 -25 -501 -501

!C" 1-"1 1-352 1-312nC" 2-31+ 2-17 2-113

!C5 0-57 0- 0-7

nC5 0-"2 0-77 0-757

C 0-+ 0-57 0-771

C7 0 0 0

C 0 0 0

C+ 0 0 0

C10 0 0 0

C11 0 0 0

C7 +-52+ -2 3-+

Gplu 1+-53 1"+-703 13-501

Gga 37-25+ 30-+5 2-+7

ol o% 1 l= mole )%t3* ; 1-5125 1-50 1-7+0

Ha den!ty )l=/%t3* ga den!ty )l=/%t3* 2"-3" 1+-"17 1"-33

Ha den!ty )Bg/m3* ga den!ty )kg/m3* 3+"-5 311-03 230-0

L= &ole ga produced gaGp 0 0-07+7 0-1"00"

;ol o% ga !n cell ;ga 1-5125 1-255" 1-170

L= mole o% ga !n cell ga 1-0000 0-7+"2 0-211L= mole o% l!(u!d l!( 0-0000 0-121 0-15+1

&a remoed &gaGp 0-000 2-"" 3-77+

&a o% ga !n cell &ga 37-2 2"-3 1-7

&a o% l!(u!d &l!( 0-00 10-"3 1"-27

o% l!(u!d 2-75 +-+

L!(u!d den!ty )l=/%t3* l!(u!d den!ty )l=/%t3* "0-5 "1-30

L!(u!d den!ty )Bg/m3* l!(u!d den!ty )kg/m3* 50-00 1-57

moles o- each compoet 2 0-3+3 0-31 0-300remaiig i cell C$2 1-77 1-30 1-3+


33/37

(a-ter extra gas has &ee remo0ed) 2S 0 0-000 0-000

C1 -25 2-51" 52-10"

C2 7-02" -"51 5-"37

C3 -25 -10 5-1+

!C" 1-"1 1-310 1-12

nC" 2-31+ 2-1"5 1-"+

!C5 0-57 0-7+3 0-

nC5 0-"2 0-77+ 0-73

C 0-+ 0-+00 0-7+2

C7 0 0-000 0-000

C 0 0-000 0-000

C+ 0 0-000 0-000

C10 0 0-000 0-000

C11 0 0-000 0-000

C7 +-52+ +-03" -"

Total 100-001 +2-025 7-021

moles o- li=uid i cell 2 0-000 0-03+ 0-031

C$2 0-000 0-17 0-212

2S 0-000 0-000 0-000

C1 0-000 5-"0" 5-+32

C2 0-000 0-751 0-+3

C3 0-000 0-+"" 1-15

!C" 0-000 0-23 0-312

nC" 0-000 0-"1 0-537

!C5 0-000 0-15 0-210

nC5 0-000 0-15" 0-203

C 0-000 0-21+ 0-313

C7 0-000 0-000 0-000C 0-000 0-000 0-000

C+ 0-000 0-000 0-000

C10 0-000 0-000 0-000

C11 0-000 0-000 0-000

C7 0-000 "-111 -0

Total 0-000 12-10 15-+12

o% C7 %ract!on !n l!(u!d I;6LJ


34/37

C+ 0-00 0-00

C10 0-00 0-00

C11 0-00 0-00

C7 32-0 3-12

510alues

2 1-3073 2-2137

C$2 1-2+5 1-3+75

2S ID;/0K ID;/0K

C1 1-77+ 1-++"1

C2 1-2051 1-22+1

C3 0-7 0-+30

!C" 0-7210 0-701

nC" 0-0 0-21

!C5 0-3+0 0-500

nC5 0-"3" 0-5+32

C 0-"+33 0-3+22

C7 0-1+02 0-1023

ackward material &alace calculatio

Calculate or!g!nal ga compo!t!on %rom re!dual l!(u!d and produced ga compo!t!on

"51"-7 351"-7

2 69


35/37

JHC 10-732

;cell 1-513

Dn!t ma 37-2


36/37

&eaured

l!(u!d

compo!t!on

1+-3

0-00

0-00

0-00

0-00

0-01

0-15

0-1+

0-1

0-"

1-10

3-23

0-000-00


37/37

0-00

0-00

0-00

+3-7

@e!dual ga @e!dual l!(u!d &ole o% re!dual l!(u!d

0-2+21 0-0000 Ha molar ol 1-7+0

1-2570 0-0000 L!( molar ol 3-5571

0-0000 0-0000 Total mole 0-702

50-150 0-0002 L!( at 0-22"

"-75 0-000 L!( mole %rac 0-1352

"-32 0-012

0-52 0-01+ &ole re!d l!( 0-1055

1-"25 0-0"1 &oleGre!dGga 0-7"7

0-51 0-05

0-5107 0-110

0-5202 0-3"12

0-0000 0-0000

0-0000 0-0000

0-0000 0-0000

0-0000 0-0000

0-0000 0-0000

2-313 +-+03

7-"7 10-550

Date post:	06-Jul-2018
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Jk1gc Cvd Analysis

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