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SS DES-04
1
Increase CIT to VDU furnace to enable higher
VDU throughput Presented byWisit Rienprakasit
Process Engineering Design Petrochemical & Refinery 2 Division
Agenda Description
Lube Base Oil Overview
Conceptual Design
Project Procedure and Time Frame
PRO/II Simulation
HEXTRAN Simulation
Comparison between simulation and actual result
Benefit
Q&A
2
Lube Base Oil Overview
Conceptual Design
Project Procedure and Time Frame
PRO/II Simulation
HEXTRAN Simulation
Comparison between simulation and actual result
Benefit
Q&A
IRPC Business
Refinery & Lube base oil-Crude distillation Capacity 215,000 bbl/day-Lube base oil capacity 320,000 ton/year
3
Power Plant-Coal firing generating capacity 108 MW.-NG gas Firing (CHP) generating 200 MW.
IRPC Asset ManagementBusinessIRPC industrial park area is about 6,000 rai and hasempty plots of land can be developed as industrialzone about 4,000 rai
IRPC Business
4
PetrochemicalVarious products until upstream to downstreampetrochemical for example HDPE, PP, EPS, SAN, PS,ABS, Ethylene cracker, EBSM.
IRPC Asset ManagementBusinessIRPC industrial park area is about 6,000 rai and hasempty plots of land can be developed as industrialzone about 4,000 rai
PortIRPC port consist of 2 terminals :-Liquid & Chemical Terminal-Bulk & Container Terminal
IRPC Business
5
PortIRPC port consist of 2 terminals :-Liquid & Chemical Terminal-Bulk & Container Terminal
RefineryUpstream
PetrochemicalDownstream
Petrochemical
Petrochemical
Petroleum & Petrochemical
CRUDE
6
RefineryUpstream
Petrochemical IntermediatePetrochemical
DownstreamPetrochemical
ProductProduct
Petroleum & Petrochemical Products
Petroleum Products Upstream & IntermediatePetrochemical Products
Fuel
LPG
Jet fuel
Diesel
Fuel Oil
Base Oil
Base Oil
Extract
Bitumen
Wax
Ethylene
Propylene
Butadiene
EthyleneCracker BTX & EBSM
Benzene
Toluene
Xylene
StyreneMonomer
Downstream Petrochemical Products
HDPE
PP
Styrenic
ABS
SAN
EPS
PS
Polyurethane
Polyols
Poly Olefins
IRPC PRODUCT
7
Package
Bottle
Pipe
Insulation
Toy
Auto Part
Application
Transportation
Industrial Machine
Fishery
Construction
Application
Raw material for
downstream petrochemical
Application
Sour/Sweetcrude
EURO IV HSD blending50 ppmw S
Schematic Flow Diagram of existing IRPC
ADU1&2
LSU/GCU
DKU
ETPHDPE
PP
CD-1
EBSM
SAN
ABS
High Sulfur HSD blending
LPG blending
Kero &GO
Naphthaethylene
propylene
PyGas
NHT/CCR/ISOMEURO IV Gasoline
blending50 ppmw S
P
O
L
Y
M
E
R
S
Benzeneimport
propylene import
Toluene
Benzene
Reformate &isomerate
LPG
8
EURO IV HSD blending50 ppmw S
Petrochemical-oriented upgrade(UHV Project under EPC phase)
ADU1&2
VDU
DAU
ABU
SEU PDU
VGOHT DCC
BTX
ABS
PS/EPS
Group 1 Base oils
Asphalt
HS ATB
EXCESS HS-ATB
P
O
L
Y
M
E
R
S
LS ATB
VGO
propylene to PP
DAO
Ethylene rich to ETP
butanes to LPG blending
Toluene
Ethyl Benzene mix
Mixed xylene
Refinery
Petrochemicals & Plastics
to EURO IV Gasoline blendingPrime G+
Off-sites, utilities andSupporting Units
Lube Base Oils
extractVR
asphaltene
LCO (to FO and diesel) & slurry oil to FO
Lube Base Oil OverviewProduct : Lube Base Oil, Wax, Extract, TDAE, Asphalt
MID SLOP
LT SLOP
D60
D150
UNITUNIT 2121VDUVDU
R150
R500/600
R60
UNITUNIT 2222SEUSEU
HS-ATB 150N
500N/600N
60N
UNITUNIT 2323PDUPDU
SW TO SRU
SW / H2S TO SRU
SW TO SRU
9
MID SLOP
D500/D600
HVY SLOP
VR
DAO
ASPHALTENE
UNITUNIT 2424DAUDAU
AC 60/70
AC 80/100
UNITUNIT 2525ABUABU
EXCESS VGO
DCCDCC
FO BLENDING
UNITUNIT 6161TFLTFL
RBS
EXTRACT
BS150
WAX
Conceptual Design
VR
Higher VDU throughput via higher CIT-> More margin
265 C257 C @ original throughput
LT SLOP
D60
185 C176 C @ original throughput
255 C @ higher throughput
178 C @ higher throughput
10
NEWE01 E02 E03 E04 E05 E06
HS-ATB
360 C
CITIncrease 5 C
E07 E08 E09
257 C @ original throughput
MID SLOP
D500
HVY SLOP
D60
D150
VR
Increase1.66 KBPD
255 C @ higher throughput
Project Procedure and Time Frame
Feasibility Study and issue Basic DesignPackage (include simulation)
Sep07 to May08
Feasibility Study and issue Basic DesignPackage (include simulation)
Sep07 to May08
Detail Engineering Design, Procurementand installationJun08 to Jul10
Detail Engineering Design, Procurementand installationJun08 to Jul10
11
Detail Engineering Design, Procurementand installationJun08 to Jul10
Detail Engineering Design, Procurementand installationJun08 to Jul10
Benefit trackingAug10 to presently
Benefit trackingAug10 to presently
PRO/II Simulation Procedure
1. Brainstorm to increase margin at VDU.2. Study project feasibility by PRO/II.
2.1 Perform simulation model as actual condition.
M1
E001AB
E002
E003E004AB E005 E006AB
E007
E008 E009
B001
123456789
101112131415161718192021222324252627
C001
1
2
C002
1234
C003
1
2
C004
1
2
C005
P015_P007
P009
P005
P001
P011
SP_VR2
P002P004
P010
E010
E012
E013
E014E015
E016
E017
E018
D001
CA1 CA2
CA3CA4
SP_TPA
M2
SP_MPA
M3
SP_VR1
M4
MV1
E2+E13 E3+E4
CN1
ARL
AXL
BSL
FEED
D500_04
ATB0190.0
231.1222.0
CM3/HRM3/HR
D500_05
ATB02
TPA02198.6158.6140.0
CM3/HRM3/HR
ATB03
TPA04
MPA03
ATB04
MPA04202.1185.2164.5
CM3/HRM3/HR
MPA02
ATB05
MS03
ATB06
MS04
D500_03
ATB07
VR04
VR05263.5113.9100.2
CM3/HRM3/HR
ATB08
VR03
ATB09
VR02
ATB10303.2264.0222.0
CM3/HRM3/HR
VEL-STM
ATB11
TPA01198.1159.2140.0
CM3/HRM3/HR
MPA01301.2222.8182.8
CM3/HRM3/HR
D60_RV
D150RV
MSRV
D500RV
SSC001
VR07265.224.921.9
CM3/HRM3/HR
OHD_E012D60_01
D150_01277.437.131.0
CM3/HRM3/HR
MS01322.5
8.16.6
CM3/HRM3/HR
D500_01340.762.950.6
CM3/HRM3/HR
HS01376.824.419.5
CM3/HRM3/HR
WDS
VR01359.8136.3112.2
CM3/HRM3/HR
SSC002
D60_02196.739.935.2
CM3/HRM3/HR
SSC003
D150_02270.733.828.4
CM3/HRM3/HR
SSC004
MS02280.3
4.03.4
CM3/HRM3/HR
SSC005
D500_02330.053.243.3
CM3/HRM3/HR
VR06
D60_03D150_03
HS02
VR08184.997.589.5
CM3/HRM3/HR
COND_D01
TPA05118.4149.7140.0
CM3/HRM3/HR
D60_0465.836.335.2
CM3/HRM3/HR
D150_0456.329.128.4
CM3/HRM3/HR
MS0587.33.53.4
CM3/HRM3/HR
D500_0653.644.243.3
CM3/HRM3/HR
HS0386.420.219.5
CM3/HRM3/HR
OFFGAS
LGTSL
SW
CRG
TPA02_1
TPA02_2
TPA03
MPA03_1
MPA03_2
MPA05204.1206.1182.8
CM3/HRM3/HR
VR04_1
VR04_2
D60
D150
D500
VR_100C
VR05_1
S1
Stream NameTemperaturePressureTotal Mass RateLiquid RateLiquid Act. DensityLiquid CPTotal Std. Liq. RateTotal Molecular WeightTotal Std. Liq. Sp. GravityLiquid ViscosityLiquid Kinematic ViscosityTBP at 760 MM HG (LV) IBP 5% 10% 30% 50% 70% 90% 95% EBPASTM D2887 at 760 MM HG (WT) IBP 5% 10% 30% 50% 70% 90% 95% EBPASTM D1160 at 760 MM HG (LV) IBP 5% 10% 30% 50% 70% 90% 95% EBP
CKG/CM2GKG/HRM3/HRKG/M3KCAL/KG-CM3/HR
CPCSTOKEC
C
C
ATB0190.0
21.00212296
231.1918.70.48
222.0477.1
0.957224.0344.82
290354379447511583683760815
304378407460511569644808834
289359386451511583683760815
D60_02196.7-0.92
3144139.9
787.60.6135.2
310.50.8950
0.804.12
281301319361377390409416423
264289313354377394415426435
306317328364377390409416423
D150_02270.7-0.92
2602033.8
771.00.6728.4
379.60.9180
0.661.89
362382395419430439451457463
334362380412430443458465474
383394402421430439451457463
MS02280.3-0.913129
4.0783.10.683.4
422.80.9318
0.811.75
415431438451458467480488497
381409421444458471486498509
430439443452458467480488497
D500_02330.0-0.91
4076853.2
766.20.7243.3
457.30.9427
0.641.23
412440451470485502526536545
377419435463485505530545556
435451457473485502526536545
HS01376.8-0.92
1883024.4
771.50.7519.5
533.10.9688
0.690.95
404459487534553570595604614
390452484528553573599613624
407466496537553570595604614
VR01359.8-0.92
112268136.3823.90.71
112.2664.1
1.00151.681.04
467510534583610659777814838
456506534579610653739810827
484521543587610659777814838
VR08184.914.75
8950497.5
917.90.5689.5
664.41.001629.094.87
468510534583610659777814838
456506534579610653739810827
484522543587610659777814838
VR_100C100.014.75
8950493.4
958.50.4889.5
664.41.0016301.2731.67
468510534583610659777814838
456506534579610653739810827
484522543587610659777814838
Stream NameTemperaturePressureTotal Mass RateLiquid RateLiquid Act. DensityLiquid CPTotal Std. Liq. RateTotal Molecular WeightTotal Std. Liq. Sp. GravityLiquid ViscosityLiquid Kinematic ViscosityTBP at 760 MM HG (LV) IBP 5% 10% 30% 50% 70% 90% 95% EBPASTM D2887 at 760 MM HG (WT) IBP 5% 10% 30% 50% 70% 90% 95% EBPASTM D1160 at 760 MM HG (LV) IBP 5% 10% 30% 50% 70% 90% 95% EBP
CKG/CM2GKG/HRM3/HRKG/M3KCAL/KG-CM3/HR
CPCSTOKEC
C
C
D6025.0
-0.0022330
25.2887.50.4425.0
307.10.894112.61
1860.59
314324334353366379395400436
287303317346366383401408429
330335340356366379395400436
D15025.0
-0.0022835
25.2907.80.4425.0
372.40.914337.84
1860.59
369390401414420426437443473
336368383407420430444451471
387399405415420426437443473
D50025.0
-0.0023553
25.1936.60.4325.0
462.90.9430187.75
1860.59
439458465475484497517524562
402436447468484501523534556
455466469477484497517524562
Stream NameTemperatureLiquid RateTotal Std. Liq. Rate
CM3/HRM3/HR
ATB10303.2264.0222.0
ATB11390.0126.0227.8
TPA01198.1159.2140.0
TPA05118.4149.7140.0
D60_02196.739.935.2
D60_0465.836.335.2
D150_01277.437.131.0
D150_02270.733.828.4
D150_0456.329.128.4
MS01322.5
8.16.6
MS02280.3
4.03.4
MS0587.33.53.4
D500_01340.762.950.6
D500_02330.053.243.3
D500_0653.644.243.3
HS01376.824.419.5
HS0386.420.219.5
VR01359.8136.3112.2
VR05263.5113.9100.2
VR07265.224.921.9
VR08184.997.589.5
MPA01301.2222.8182.8
MPA05204.1206.1182.8
TPA02_1198.6158.6140.0
MPA02301.4222.1182.8
MPA03_1221.8187.8164.5
MS03280.8
4.03.4
D500_03330.552.843.3
VR02360.4134.9112.2
OHD_E012140.0
n/a11.4
HxRig NameHxRig Description
DutyAreaU-ValueU-Value (Fouling)LMTDHx Rig MTDFT FactorHx Rig Tube DPHx Rig Shell DPHx Rig Tube temperature outHx Rig Shell temperature outHx Rig Tube fouling requiredHx Rig Tube Fouling FactorHx Rig Shell fouling factor
M*KCAL/HRM2KCAL/HR-M2-CKCAL/HR-M2-CCC
KG/CM2KG/CM2CCHR-M2-C/KCALHR-M2-C/KCALHR-M2-C/KCAL
E001AB
2.7042472.02
67.965767.0542
86.8585.44010.9837
0.210.06
115.6140.7
n/a0.000000.00020
E002
3.6041459.14
228.6640228.1423
41.8234.40720.8228
0.460.17
149.8148.0
n/a0.000000.00001
E003
1.8331417.36
221.032979.8453
55.9555.00910.9832
0.270.34
202.1163.9
n/a0.000000.00800
E004AB
8.8896833.86
291.0472183.9632
61.9857.95030.9350
0.320.34
221.8235.2
n/a0.000000.00200
E005
0.0908383.40
20.411420.0834
12.5811.79110.9375
0.000.36
236.6235.9
n/a0.000000.00080
E006AB
2.1639264.62
300.8126211.6702
40.0238.63240.9652
0.580.14
252.1252.7
n/a0.000000.00140
E007
1.0937526.31
159.4813149.9177
15.5213.86110.8934
0.360.07
260.1263.5
n/a0.000000.00040
E008
2.1295526.31
176.5720170.5491
26.8423.72430.8839
0.350.09
275.5280.7
n/a0.000000.00020
E009
3.9432521.85
195.1779193.6660
44.9539.01700.8679
0.340.09
303.2309.8
n/a0.000000.00004
Hx NameHx Description
DutyHx Hot Prod TempHx UAHx Hot DPHx Cold DP
M*KCAL/HRCKCAL/HR-CKG/CM2KG/CM2
E010Design 4.5240 MMkcal_H
4.2512184.91
n/a0.000.00
E012
4.849336.00
n/a0.000.00
E013
2.1594118.44
n/a0.000.00
E014Desing 1.8190 MMkcal_H
2.265865.80
n/a0.000.00
E015Design 3.6140 MMkcal_H
3.192856.30
n/a0.000.00
E016
0.263787.30
n/a0.000.00
E017
1.770053.61
n/a0.000.00
E018
3.357486.40
n/a0.000.00
Calculator NameCalculator Description
Result 1Result 2Result 3Result 4Result 5
E2+E13Mkcal_h
5.76356.3500
n/an/an/a
E3+E4
10.72279.2100
n/an/an/a
12
M1
E001AB
E002
E003E004AB E005 E006AB
E007
E008 E009
B001
123456789
101112131415161718192021222324252627
C001
1
2
C002
1234
C003
1
2
C004
1
2
C005
P015_P007
P009
P005
P001
P011
SP_VR2
P002P004
P010
E010
E012
E013
E014E015
E016
E017
E018
D001
CA1 CA2
CA3CA4
SP_TPA
M2
SP_MPA
M3
SP_VR1
M4
MV1
E2+E13 E3+E4
CN1
ARL
AXL
BSL
FEED
D500_04
ATB0190.0
231.1222.0
CM3/HRM3/HR
D500_05
ATB02
TPA02198.6158.6140.0
CM3/HRM3/HR
ATB03
TPA04
MPA03
ATB04
MPA04202.1185.2164.5
CM3/HRM3/HR
MPA02
ATB05
MS03
ATB06
MS04
D500_03
ATB07
VR04
VR05263.5113.9100.2
CM3/HRM3/HR
ATB08
VR03
ATB09
VR02
ATB10303.2264.0222.0
CM3/HRM3/HR
VEL-STM
ATB11
TPA01198.1159.2140.0
CM3/HRM3/HR
MPA01301.2222.8182.8
CM3/HRM3/HR
D60_RV
D150RV
MSRV
D500RV
SSC001
VR07265.224.921.9
CM3/HRM3/HR
OHD_E012D60_01
D150_01277.437.131.0
CM3/HRM3/HR
MS01322.5
8.16.6
CM3/HRM3/HR
D500_01340.762.950.6
CM3/HRM3/HR
HS01376.824.419.5
CM3/HRM3/HR
WDS
VR01359.8136.3112.2
CM3/HRM3/HR
SSC002
D60_02196.739.935.2
CM3/HRM3/HR
SSC003
D150_02270.733.828.4
CM3/HRM3/HR
SSC004
MS02280.3
4.03.4
CM3/HRM3/HR
SSC005
D500_02330.053.243.3
CM3/HRM3/HR
VR06
D60_03D150_03
HS02
VR08184.997.589.5
CM3/HRM3/HR
COND_D01
TPA05118.4149.7140.0
CM3/HRM3/HR
D60_0465.836.335.2
CM3/HRM3/HR
D150_0456.329.128.4
CM3/HRM3/HR
MS0587.33.53.4
CM3/HRM3/HR
D500_0653.644.243.3
CM3/HRM3/HR
HS0386.420.219.5
CM3/HRM3/HR
OFFGAS
LGTSL
SW
CRG
TPA02_1
TPA02_2
TPA03
MPA03_1
MPA03_2
MPA05204.1206.1182.8
CM3/HRM3/HR
VR04_1
VR04_2
D60
D150
D500
VR_100C
VR05_1
S1
Stream NameTemperaturePressureTotal Mass RateLiquid RateLiquid Act. DensityLiquid CPTotal Std. Liq. RateTotal Molecular WeightTotal Std. Liq. Sp. GravityLiquid ViscosityLiquid Kinematic ViscosityTBP at 760 MM HG (LV) IBP 5% 10% 30% 50% 70% 90% 95% EBPASTM D2887 at 760 MM HG (WT) IBP 5% 10% 30% 50% 70% 90% 95% EBPASTM D1160 at 760 MM HG (LV) IBP 5% 10% 30% 50% 70% 90% 95% EBP
CKG/CM2GKG/HRM3/HRKG/M3KCAL/KG-CM3/HR
CPCSTOKEC
C
C
ATB0190.0
21.00212296
231.1918.70.48
222.0477.1
0.957224.0344.82
290354379447511583683760815
304378407460511569644808834
289359386451511583683760815
D60_02196.7-0.92
3144139.9
787.60.6135.2
310.50.8950
0.804.12
281301319361377390409416423
264289313354377394415426435
306317328364377390409416423
D150_02270.7-0.92
2602033.8
771.00.6728.4
379.60.9180
0.661.89
362382395419430439451457463
334362380412430443458465474
383394402421430439451457463
MS02280.3-0.913129
4.0783.10.683.4
422.80.9318
0.811.75
415431438451458467480488497
381409421444458471486498509
430439443452458467480488497
D500_02330.0-0.91
4076853.2
766.20.7243.3
457.30.9427
0.641.23
412440451470485502526536545
377419435463485505530545556
435451457473485502526536545
HS01376.8-0.92
1883024.4
771.50.7519.5
533.10.9688
0.690.95
404459487534553570595604614
390452484528553573599613624
407466496537553570595604614
VR01359.8-0.92
112268136.3823.90.71
112.2664.1
1.00151.681.04
467510534583610659777814838
456506534579610653739810827
484521543587610659777814838
VR08184.914.75
8950497.5
917.90.5689.5
664.41.001629.094.87
468510534583610659777814838
456506534579610653739810827
484522543587610659777814838
VR_100C100.014.75
8950493.4
958.50.4889.5
664.41.0016301.2731.67
468510534583610659777814838
456506534579610653739810827
484522543587610659777814838
Stream NameTemperaturePressureTotal Mass RateLiquid RateLiquid Act. DensityLiquid CPTotal Std. Liq. RateTotal Molecular WeightTotal Std. Liq. Sp. GravityLiquid ViscosityLiquid Kinematic ViscosityTBP at 760 MM HG (LV) IBP 5% 10% 30% 50% 70% 90% 95% EBPASTM D2887 at 760 MM HG (WT) IBP 5% 10% 30% 50% 70% 90% 95% EBPASTM D1160 at 760 MM HG (LV) IBP 5% 10% 30% 50% 70% 90% 95% EBP
CKG/CM2GKG/HRM3/HRKG/M3KCAL/KG-CM3/HR
CPCSTOKEC
C
C
D6025.0
-0.0022330
25.2887.50.4425.0
307.10.894112.61
1860.59
314324334353366379395400436
287303317346366383401408429
330335340356366379395400436
D15025.0
-0.0022835
25.2907.80.4425.0
372.40.914337.84
1860.59
369390401414420426437443473
336368383407420430444451471
387399405415420426437443473
D50025.0
-0.0023553
25.1936.60.4325.0
462.90.9430187.75
1860.59
439458465475484497517524562
402436447468484501523534556
455466469477484497517524562
Stream NameTemperatureLiquid RateTotal Std. Liq. Rate
CM3/HRM3/HR
ATB10303.2264.0222.0
ATB11390.0126.0227.8
TPA01198.1159.2140.0
TPA05118.4149.7140.0
D60_02196.739.935.2
D60_0465.836.335.2
D150_01277.437.131.0
D150_02270.733.828.4
D150_0456.329.128.4
MS01322.5
8.16.6
MS02280.3
4.03.4
MS0587.33.53.4
D500_01340.762.950.6
D500_02330.053.243.3
D500_0653.644.243.3
HS01376.824.419.5
HS0386.420.219.5
VR01359.8136.3112.2
VR05263.5113.9100.2
VR07265.224.921.9
VR08184.997.589.5
MPA01301.2222.8182.8
MPA05204.1206.1182.8
TPA02_1198.6158.6140.0
MPA02301.4222.1182.8
MPA03_1221.8187.8164.5
MS03280.8
4.03.4
D500_03330.552.843.3
VR02360.4134.9112.2
OHD_E012140.0
n/a11.4
HxRig NameHxRig Description
DutyAreaU-ValueU-Value (Fouling)LMTDHx Rig MTDFT FactorHx Rig Tube DPHx Rig Shell DPHx Rig Tube temperature outHx Rig Shell temperature outHx Rig Tube fouling requiredHx Rig Tube Fouling FactorHx Rig Shell fouling factor
M*KCAL/HRM2KCAL/HR-M2-CKCAL/HR-M2-CCC
KG/CM2KG/CM2CCHR-M2-C/KCALHR-M2-C/KCALHR-M2-C/KCAL
E001AB
2.7042472.02
67.965767.0542
86.8585.44010.9837
0.210.06
115.6140.7
n/a0.000000.00020
E002
3.6041459.14
228.6640228.1423
41.8234.40720.8228
0.460.17
149.8148.0
n/a0.000000.00001
E003
1.8331417.36
221.032979.8453
55.9555.00910.9832
0.270.34
202.1163.9
n/a0.000000.00800
E004AB
8.8896833.86
291.0472183.9632
61.9857.95030.9350
0.320.34
221.8235.2
n/a0.000000.00200
E005
0.0908383.40
20.411420.0834
12.5811.79110.9375
0.000.36
236.6235.9
n/a0.000000.00080
E006AB
2.1639264.62
300.8126211.6702
40.0238.63240.9652
0.580.14
252.1252.7
n/a0.000000.00140
E007
1.0937526.31
159.4813149.9177
15.5213.86110.8934
0.360.07
260.1263.5
n/a0.000000.00040
E008
2.1295526.31
176.5720170.5491
26.8423.72430.8839
0.350.09
275.5280.7
n/a0.000000.00020
E009
3.9432521.85
195.1779193.6660
44.9539.01700.8679
0.340.09
303.2309.8
n/a0.000000.00004
Hx NameHx Description
DutyHx Hot Prod TempHx UAHx Hot DPHx Cold DP
M*KCAL/HRCKCAL/HR-CKG/CM2KG/CM2
E010Design 4.5240 MMkcal_H
4.2512184.91
n/a0.000.00
E012
4.849336.00
n/a0.000.00
E013
2.1594118.44
n/a0.000.00
E014Desing 1.8190 MMkcal_H
2.265865.80
n/a0.000.00
E015Design 3.6140 MMkcal_H
3.192856.30
n/a0.000.00
E016
0.263787.30
n/a0.000.00
E017
1.770053.61
n/a0.000.00
E018
3.357486.40
n/a0.000.00
Calculator NameCalculator Description
Result 1Result 2Result 3Result 4Result 5
E2+E13Mkcal_h
5.76356.3500
n/an/an/a
E3+E4
10.72279.2100
n/an/an/a
PRO/II Simulation Procedure (Continuous)
2.2 Add the new heat exchanger in simulation model.
M1
E001AB
E002
E003E004AB E005 E006AB
E007
E008 E009
B001
123456789
101112131415161718192021222324252627
C001
1
2
C002
1234
C003
1
2
C004
1
2
C005
P015_P007
P009
P005
P001
P011
SP_VR2
P002P004
P010
E010
E012
E013
E014E015
E016
E017
E018
D001
CA1 CA2
CA3CA4
SP_TPA
M2
SP_MPA
M3
SP_VR1
MV1
E2+E13 E3+E4
CN1
E052
SP1
M4
ARL
AXL
BSL
FEED
D500_04
ATB0190.0
245.7236.0
CM3/HRM3/HR
D500_05
ATB02
TPA02199.9158.8140.0
CM3/HRM3/HR
ATB03
TPA04
MPA03
ATB04
MPA04198.9184.9164.5
CM3/HRM3/HR
MPA02
ATB05
MS03
ATB06
MS04
D500_03
ATB07
VR04
VR05265.9120.7106.1
CM3/HRM3/HR
ATB08
VR03
ATB09
VR02
ATB10303.2280.7236.0
CM3/HRM3/HR
VEL-STM
ATB11
TPA01199.4159.3140.0
CM3/HRM3/HR
MPA01301.2222.9182.8
CM3/HRM3/HR
D60_RV
D150RV
MSRV
D500RV
SSC001
VR07254.526.223.2
CM3/HRM3/HR
OHD_E012D60_01
D150_01277.437.331.2
CM3/HRM3/HR
MS01322.512.19.8
CM3/HRM3/HR
D500_01340.763.050.6
CM3/HRM3/HR
HS01376.830.324.2
CM3/HRM3/HR
WDS
VR01358.1143.1118.0
CM3/HRM3/HR
SSC002
D60_02197.942.737.6
CM3/HRM3/HR
SSC003
D150_02270.533.928.5
CM3/HRM3/HR
SSC004
MS02286.4
6.85.7
CM3/HRM3/HR
SSC005
D500_02329.753.043.1
CM3/HRM3/HR
VR06
D60_03D150_03
HS02
VR08177.5102.794.6
CM3/HRM3/HR
COND_D01
TPA05116.7149.5140.0
CM3/HRM3/HR
D60_0465.838.837.6
CM3/HRM3/HR
D150_0456.329.228.5
CM3/HRM3/HR
MS0587.36.05.7
CM3/HRM3/HR
D500_0650.343.943.1
CM3/HRM3/HR
HS0386.425.124.2
CM3/HRM3/HR
OFFGAS
LGTSL
SW
CRG
TPA02_1
TPA02_2
TPA03
MPA03_1
MPA03_2
MPA05200.9205.7182.8
CM3/HRM3/HR
VR04_1VR04_2
D60
D150
D500
VR_100C
S1
ATB07_01
VR05_1
VR05_2
VR05_3
VR05_4
Stream NameTemperaturePressureTotal Mass RateLiquid RateLiquid Act. DensityLiquid CPTotal Std. Liq. RateTotal Molecular WeightTotal Std. Liq. Sp. GravityLiquid ViscosityLiquid Kinematic ViscosityTBP at 760 MM HG (LV) IBP 5% 10% 30% 50% 70% 90% 95% EBPASTM D2887 at 760 MM HG (WT) IBP 5% 10% 30% 50% 70% 90% 95% EBPASTM D1160 at 760 MM HG (LV) IBP 5% 10% 30% 50% 70% 90% 95% EBP
CKG/CM2GKG/HRM3/HRKG/M3KCAL/KG-CM3/HR
CPCSTOKEC
C
C
ATB0190.0
21.00225696
245.7918.70.48
236.0477.0
0.957324.0144.82
290354379447511583683760815
322378407460511569644808847
306364386451511583683760815
D60_02197.9-0.92
3360442.7
786.90.6137.6
310.50.8951
0.794.05
281301319361377390409417424
265289313354377394415426440
307318328364377390409417424
D150_02270.5-0.92
2610033.9
770.60.6728.5
378.30.9177
0.651.89
363381394418429438450456462
338361379411429442457465478
384394401420429438450456462
MS02286.4-0.915307
6.8778.50.685.7
420.50.9312
0.751.66
411429436449457465478486496
383407419442457469485497513
428437441451457465478486496
D500_02329.7-0.91
4057353.0
765.70.7243.1
455.60.9422
0.641.24
411439450469484501523533542
387418434462484504528543559
435451457472484501523533542
HS01376.8-0.92
2340030.3
771.70.7524.2
533.30.9690
0.690.95
403458486532552571599609621
400451483526552574602617636
421470495536552571599609621
VR01358.1-0.92
118022143.1824.80.71
118.0664.0
1.00151.711.05
466508533582610660778815838
463505533579610654739809835
493524541587610660778815838
VR08177.514.72
94663102.7921.30.5594.6
664.11.001534.125.45
466508533582610660778815838
463505533579610654739809835
493524541587610660778815838
VR_100C100.014.72
9466398.8
958.40.4894.6
664.11.0015297.5331.67
466508533582610660778815838
463505533579610654739809835
493524541587610660778815838
Stream NameTemperaturePressureTotal Mass RateLiquid RateLiquid Act. DensityLiquid CPTotal Std. Liq. RateTotal Molecular WeightTotal Std. Liq. Sp. GravityLiquid ViscosityLiquid Kinematic ViscosityTBP at 760 MM HG (LV) IBP 5% 10% 30% 50% 70% 90% 95% EBPASTM D2887 at 760 MM HG (WT) IBP 5% 10% 30% 50% 70% 90% 95% EBPASTM D1160 at 760 MM HG (LV) IBP 5% 10% 30% 50% 70% 90% 95% EBP
CKG/CM2GKG/HRM3/HRKG/M3KCAL/KG-CM3/HR
CPCSTOKEC
C
C
D6025.0
-0.0022330
25.2887.50.4425.0
307.00.894112.60
1860.51
314324334353365379395400436
287303317346365383401408440
330335340355365379395400436
D15025.0
-0.0022836
25.2907.80.4425.0
372.30.914337.81
1860.51
369390401413419426437443473
342368383407419430444451481
388399405415419426437443473
D50025.0
-0.0023555
25.1936.70.4325.0
462.80.9431187.33
1860.51
439458465475484498518524562
412436447468484501523533566
456466469477484498518524562
Stream NameTemperatureLiquid RateTotal Std. Liq. Rate
CM3/HRM3/HR
ATB10303.2280.7236.0
ATB11390.0135.5241.8
TPA01199.4159.3140.0
TPA05116.7149.5140.0
D60_02197.942.737.6
D60_0465.838.837.6
D150_01277.437.331.2
D150_02270.533.928.5
D150_0456.329.228.5
MS01322.512.19.8
MS02286.4
6.85.7
MS0587.36.05.7
D500_01340.763.050.6
D500_02329.753.043.1
D500_0650.343.943.1
HS01376.830.324.2
HS0386.425.124.2
VR01358.1143.1118.0
VR05265.9120.7106.1
VR07254.526.223.2
VR08177.5102.794.6
MPA01301.2222.9182.8
MPA05200.9205.7182.8
TPA02_1199.9158.8140.0
MPA02301.4222.2182.8
MPA03_1218.4187.4164.5
MS03286.9
6.85.7
D500_03330.252.643.1
VR02358.7141.6118.0
OHD_E012140.0
n/a11.5
ATB07_01254.8271.4236.0
VR05_1267.5134.2117.9
VR05_3254.5133.2117.8
HxRig NameHxRig Description
DutyAreaU-ValueU-Value (Fouling)LMTDHx Rig MTDFT FactorHx Rig Tube DPHx Rig Shell DPHx Rig Tube temperature outHx Rig Shell temperature outHx Rig Tube fouling requiredHx Rig Tube Fouling FactorHx Rig Shell fouling factor
M*KCAL/HRM2KCAL/HR-M2-CKCAL/HR-M2-CCC
KG/CM2KG/CM2CCHR-M2-C/KCALHR-M2-C/KCALHR-M2-C/KCAL
E001AB
2.6499472.04
68.441967.5177
84.4783.14620.9843
0.230.06
113.7138.3
n/a0.000000.00020
E002
3.8159459.11
232.2057231.6678
43.4235.87700.8262
0.460.19
148.1146.1
n/a0.000000.00001
E003
1.8091417.39
220.808979.8160
55.1854.30500.9841
0.270.38
198.9160.8
n/a0.000000.00800
E004AB
9.2382833.81
294.1401185.1940
63.8359.82670.9373
0.330.38
218.4230.9
n/a0.000000.00200
E005
0.1787383.41
23.907323.4586
20.6019.86920.9643
0.010.41
235.8232.2
n/a0.000000.00080
E006AB
2.2408264.57
303.0814212.7910
41.1939.80280.9664
0.650.14
248.1249.0
n/a0.000000.00140
E007
1.1124526.35
167.3235156.8272
15.0313.47670.8965
0.400.08
262.5265.9
n/a0.000000.00040
E008
2.1538526.36
184.5970178.0244
25.9022.98510.8876
0.390.10
277.1282.3
n/a0.000000.00020
E009
3.9634521.83
202.8384201.2059
43.2737.74810.8724
0.380.10
303.2310.1
n/a0.000000.00004
Hx NameHx Description
DutyHx Hot Prod TempHx UAHx Hot DPHx Cold DP
M*KCAL/HRCKCAL/HR-CKG/CM2KG/CM2
E010Design 4.5240 MMkcal_H
4.2512177.49
n/a0.000.00
E012
4.854636.00
n/a0.000.00
E013
2.1594116.72
n/a0.000.00
E014Desing 1.8190 MMkcal_H
2.446165.80
n/a0.000.00
E015Design 3.6140 MMkcal_H
3.199556.30
n/a0.000.00
E016
0.444787.30
n/a0.000.00
E017
1.770050.29
n/a0.000.00
E018
4.171586.40
n/a0.000.00
E052
0.9606254.46
133176.34380.000.00
Calculator NameCalculator Description
Result 1Result 2Result 3Result 4Result 5
E2+E13Mkcal_h
5.97536.3500
n/an/an/a
E3+E4
11.04739.2100
n/an/an/a
New H/E
13
M1
E001AB
E002
E003E004AB E005 E006AB
E007
E008 E009
B001
123456789
101112131415161718192021222324252627
C001
1
2
C002
1234
C003
1
2
C004
1
2
C005
P015_P007
P009
P005
P001
P011
SP_VR2
P002P004
P010
E010
E012
E013
E014E015
E016
E017
E018
D001
CA1 CA2
CA3CA4
SP_TPA
M2
SP_MPA
M3
SP_VR1
MV1
E2+E13 E3+E4
CN1
E052
SP1
M4
ARL
AXL
BSL
FEED
D500_04
ATB0190.0
245.7236.0
CM3/HRM3/HR
D500_05
ATB02
TPA02199.9158.8140.0
CM3/HRM3/HR
ATB03
TPA04
MPA03
ATB04
MPA04198.9184.9164.5
CM3/HRM3/HR
MPA02
ATB05
MS03
ATB06
MS04
D500_03
ATB07
VR04
VR05265.9120.7106.1
CM3/HRM3/HR
ATB08
VR03
ATB09
VR02
ATB10303.2280.7236.0
CM3/HRM3/HR
VEL-STM
ATB11
TPA01199.4159.3140.0
CM3/HRM3/HR
MPA01301.2222.9182.8
CM3/HRM3/HR
D60_RV
D150RV
MSRV
D500RV
SSC001
VR07254.526.223.2
CM3/HRM3/HR
OHD_E012D60_01
D150_01277.437.331.2
CM3/HRM3/HR
MS01322.512.19.8
CM3/HRM3/HR
D500_01340.763.050.6
CM3/HRM3/HR
HS01376.830.324.2
CM3/HRM3/HR
WDS
VR01358.1143.1118.0
CM3/HRM3/HR
SSC002
D60_02197.942.737.6
CM3/HRM3/HR
SSC003
D150_02270.533.928.5
CM3/HRM3/HR
SSC004
MS02286.4
6.85.7
CM3/HRM3/HR
SSC005
D500_02329.753.043.1
CM3/HRM3/HR
VR06
D60_03D150_03
HS02
VR08177.5102.794.6
CM3/HRM3/HR
COND_D01
TPA05116.7149.5140.0
CM3/HRM3/HR
D60_0465.838.837.6
CM3/HRM3/HR
D150_0456.329.228.5
CM3/HRM3/HR
MS0587.36.05.7
CM3/HRM3/HR
D500_0650.343.943.1
CM3/HRM3/HR
HS0386.425.124.2
CM3/HRM3/HR
OFFGAS
LGTSL
SW
CRG
TPA02_1
TPA02_2
TPA03
MPA03_1
MPA03_2
MPA05200.9205.7182.8
CM3/HRM3/HR
VR04_1VR04_2
D60
D150
D500
VR_100C
S1
ATB07_01
VR05_1
VR05_2
VR05_3
VR05_4
Stream NameTemperaturePressureTotal Mass RateLiquid RateLiquid Act. DensityLiquid CPTotal Std. Liq. RateTotal Molecular WeightTotal Std. Liq. Sp. GravityLiquid ViscosityLiquid Kinematic ViscosityTBP at 760 MM HG (LV) IBP 5% 10% 30% 50% 70% 90% 95% EBPASTM D2887 at 760 MM HG (WT) IBP 5% 10% 30% 50% 70% 90% 95% EBPASTM D1160 at 760 MM HG (LV) IBP 5% 10% 30% 50% 70% 90% 95% EBP
CKG/CM2GKG/HRM3/HRKG/M3KCAL/KG-CM3/HR
CPCSTOKEC
C
C
ATB0190.0
21.00225696
245.7918.70.48
236.0477.0
0.957324.0144.82
290354379447511583683760815
322378407460511569644808847
306364386451511583683760815
D60_02197.9-0.92
3360442.7
786.90.6137.6
310.50.8951
0.794.05
281301319361377390409417424
265289313354377394415426440
307318328364377390409417424
D150_02270.5-0.92
2610033.9
770.60.6728.5
378.30.9177
0.651.89
363381394418429438450456462
338361379411429442457465478
384394401420429438450456462
MS02286.4-0.915307
6.8778.50.685.7
420.50.9312
0.751.66
411429436449457465478486496
383407419442457469485497513
428437441451457465478486496
D500_02329.7-0.91
4057353.0
765.70.7243.1
455.60.9422
0.641.24
411439450469484501523533542
387418434462484504528543559
435451457472484501523533542
HS01376.8-0.92
2340030.3
771.70.7524.2
533.30.9690
0.690.95
403458486532552571599609621
400451483526552574602617636
421470495536552571599609621
VR01358.1-0.92
118022143.1824.80.71
118.0664.0
1.00151.711.05
466508533582610660778815838
463505533579610654739809835
493524541587610660778815838
VR08177.514.72
94663102.7921.30.5594.6
664.11.001534.125.45
466508533582610660778815838
463505533579610654739809835
493524541587610660778815838
VR_100C100.014.72
9466398.8
958.40.4894.6
664.11.0015297.5331.67
466508533582610660778815838
463505533579610654739809835
493524541587610660778815838
Stream NameTemperaturePressureTotal Mass RateLiquid RateLiquid Act. DensityLiquid CPTotal Std. Liq. RateTotal Molecular WeightTotal Std. Liq. Sp. GravityLiquid ViscosityLiquid Kinematic ViscosityTBP at 760 MM HG (LV) IBP 5% 10% 30% 50% 70% 90% 95% EBPASTM D2887 at 760 MM HG (WT) IBP 5% 10% 30% 50% 70% 90% 95% EBPASTM D1160 at 760 MM HG (LV) IBP 5% 10% 30% 50% 70% 90% 95% EBP
CKG/CM2GKG/HRM3/HRKG/M3KCAL/KG-CM3/HR
CPCSTOKEC
C
C
D6025.0
-0.0022330
25.2887.50.4425.0
307.00.894112.60
1860.51
314324334353365379395400436
287303317346365383401408440
330335340355365379395400436
D15025.0
-0.0022836
25.2907.80.4425.0
372.30.914337.81
1860.51
369390401413419426437443473
342368383407419430444451481
388399405415419426437443473
D50025.0
-0.0023555
25.1936.70.4325.0
462.80.9431187.33
1860.51
439458465475484498518524562
412436447468484501523533566
456466469477484498518524562
Stream NameTemperatureLiquid RateTotal Std. Liq. Rate
CM3/HRM3/HR
ATB10303.2280.7236.0
ATB11390.0135.5241.8
TPA01199.4159.3140.0
TPA05116.7149.5140.0
D60_02197.942.737.6
D60_0465.838.837.6
D150_01277.437.331.2
D150_02270.533.928.5
D150_0456.329.228.5
MS01322.512.19.8
MS02286.4
6.85.7
MS0587.36.05.7
D500_01340.763.050.6
D500_02329.753.043.1
D500_0650.343.943.1
HS01376.830.324.2
HS0386.425.124.2
VR01358.1143.1118.0
VR05265.9120.7106.1
VR07254.526.223.2
VR08177.5102.794.6
MPA01301.2222.9182.8
MPA05200.9205.7182.8
TPA02_1199.9158.8140.0
MPA02301.4222.2182.8
MPA03_1218.4187.4164.5
MS03286.9
6.85.7
D500_03330.252.643.1
VR02358.7141.6118.0
OHD_E012140.0
n/a11.5
ATB07_01254.8271.4236.0
VR05_1267.5134.2117.9
VR05_3254.5133.2117.8
HxRig NameHxRig Description
DutyAreaU-ValueU-Value (Fouling)LMTDHx Rig MTDFT FactorHx Rig Tube DPHx Rig Shell DPHx Rig Tube temperature outHx Rig Shell temperature outHx Rig Tube fouling requiredHx Rig Tube Fouling FactorHx Rig Shell fouling factor
M*KCAL/HRM2KCAL/HR-M2-CKCAL/HR-M2-CCC
KG/CM2KG/CM2CCHR-M2-C/KCALHR-M2-C/KCALHR-M2-C/KCAL
E001AB
2.6499472.04
68.441967.5177
84.4783.14620.9843
0.230.06
113.7138.3
n/a0.000000.00020
E002
3.8159459.11
232.2057231.6678
43.4235.87700.8262
0.460.19
148.1146.1
n/a0.000000.00001
E003
1.8091417.39
220.808979.8160
55.1854.30500.9841
0.270.38
198.9160.8
n/a0.000000.00800
E004AB
9.2382833.81
294.1401185.1940
63.8359.82670.9373
0.330.38
218.4230.9
n/a0.000000.00200
E005
0.1787383.41
23.907323.4586
20.6019.86920.9643
0.010.41
235.8232.2
n/a0.000000.00080
E006AB
2.2408264.57
303.0814212.7910
41.1939.80280.9664
0.650.14
248.1249.0
n/a0.000000.00140
E007
1.1124526.35
167.3235156.8272
15.0313.47670.8965
0.400.08
262.5265.9
n/a0.000000.00040
E008
2.1538526.36
184.5970178.0244
25.9022.98510.8876
0.390.10
277.1282.3
n/a0.000000.00020
E009
3.9634521.83
202.8384201.2059
43.2737.74810.8724
0.380.10
303.2310.1
n/a0.000000.00004
Hx NameHx Description
DutyHx Hot Prod TempHx UAHx Hot DPHx Cold DP
M*KCAL/HRCKCAL/HR-CKG/CM2KG/CM2
E010Design 4.5240 MMkcal_H
4.2512177.49
n/a0.000.00
E012
4.854636.00
n/a0.000.00
E013
2.1594116.72
n/a0.000.00
E014Desing 1.8190 MMkcal_H
2.446165.80
n/a0.000.00
E015Design 3.6140 MMkcal_H
3.199556.30
n/a0.000.00
E016
0.444787.30
n/a0.000.00
E017
1.770050.29
n/a0.000.00
E018
4.171586.40
n/a0.000.00
E052
0.9606254.46
133176.34380.000.00
Calculator NameCalculator Description
Result 1Result 2Result 3Result 4Result 5
E2+E13Mkcal_h
5.97536.3500
n/an/an/a
E3+E4
11.04739.2100
n/an/an/a
Heat duty = 0.9606 Gcal/h at approach temperaturebetween hot stream outlet and cold stream inlet 5 C @original throughput (257.1 C - 252.1 C).
PRO/II Simulation Procedure (Continuous)
3. CIT can increase 5 CVDU throughput can increase 11 m3/h or 1.66 KBPSD
4. Calculate thermal design to find sizing of new heatexchanger by HEXTRAN program.
14
Thermodynamic fluid package E1-E9 Heat Duty(Gcal/h)
Design 23.516
Peng-Robinson (PR) 22.955
PRO/II Simulation Problem
How to select thermodynamic fluid package for VDU?
15
Peng-Robinson (PR) 22.955
Soave-Reldich-Kwong (SRK) 23.116
Grayson-Streed (GS) 22.869
Braun K10 (BK10) 23.253
Section Packingtype
Packingheight (m)
EstimatedHETP (m)
Estimatednumber of
stages
EstimateTray
SumTray
Drawoff
bed 7 M2X 1.5 0.75 2.00 2 2 D60
PRO/II Simulation Problem (Continuous)
How to know number of Packed Stage?
Number of Packed Stages = Packing Height / HETP
16
bed 7 M2X 1.5 0.75 2.00 2 2 D60bed 6 M250Y 2.94 0.45 6.53 7 9 D150bed 5 M2X 1.56 0.75 2.08 2 11 MPAbed 4 M252Y 1.72 0.5 3.44 3 14 MSbed 3 M252Y 1.72 0.5 3.44 3 17 D500bed 2 M250Y 2.31 0.45 5.13 5 22 HS
bed 1 M452Y 0.852 0.32 2.66 3 26ATBfeed
HETP is Height Equivalent to a Theoretical Plate
PRO/II Simulation Problem (Continuous)
Not reliable viscosity product for VDU model
0%
10%
20%
30%
40%
50%
60%
70%
80%
90%
100%
250 300 350 400 450 500 550 600 650 700 750 800 850
%LV
TEMPERATURE (oC)
Feed_Act
D60_Act
D150_Act
D500_Act
FEED Sim
D60_Sim
D150_Sim
D500_Sim
VR_Sim
18
0%
10%
20%
30%
40%
50%
60%
70%
80%
90%
100%
250 300 350 400 450 500 550 600 650 700 750 800 850
%LV
TEMPERATURE (oC)
Feed_Act
D60_Act
D150_Act
D500_Act
FEED Sim
D60_Sim
D150_Sim
D500_Sim
VR_Sim
HEXTRAN Simulation Procedure (Continuous)
2. Specify heat duty as PRO/II
3 Tab “Tube Side”
20
3 Tab “Tube Side”
SHELL AND TUBE EXCHANGER DATA SHEETExchanger Name 21E052 Unit ID 21E052Size 1200 - 6000 Type AES Horizontal Connected 1 Parallel, 2 SeriesArea/Unit 856 m2 853 m2 Required Area/Shell 428 m2Performance of One Unit Shell-Side Tube-SideFeed Stream Number VR_FR_E7 ATB_FR_E6Feed Stream Name VR_FR_E7 VR_OUT ATB_FR_E6 ATB_TO_E7Total Fluid kg/hr 117936 226067
In Out In OutVapor kg/hr 0 0 0 0Liquid kg/hr 117936 117936 226067Steam kg/hr 0 0 0 0Water kg/hr 0 0 0 0Non-Condensible kg/hr 0 0
Temperature C 267.5 254.5 248.1 254.8Pressure kg/cm2 15.72 15.48 18.49 17.24Sp. Gr. Liquid (0 C/0 C H2O) 1.001 1.001 0.959 0.959
Vapor (0 C/0 C AIR) 0.000 0.000 0.000 0.000Density Liquid kg/m3 878.245 884.414 836.797 832.724
Vapor kg/m3 0.000 0.000 0.000 0.000Viscosity Liquid cP 5.951 7.362 1.542 1.422
Vapor cP 0.000 0.000 0.000 0.000Thermal Cond. Liquid kcal/hr-m-C 0.0640 0.0648 0.0658 0.0652
Vapor kcal/hr-m-C 0.0000 0.0000 0.0000 0.0000Spec. Heat Liquid kcal/kg-C 0.6304 0.6185 0.6312 0.6375
Vapor kcal/kg-C 0.0000 0.0000 0.0000 0.0000Latent Heat kcal/kg 0.00 0.00Velocity m/sec 0.44 1.44DP/Shell (Des/Calc) kg/cm2 0.70 0.23 0.70 0.63Fouling Resistance hr-m2-C/kcal 0.00200 0.00203 Required 0.00140Transfer Rate kcal/hr-m2-C Service 120.08 Reqd. 120.08 Clean 223.84Heat Exchanged x 10 6̂ Kcal/hr 0.961 MTD(Corrected) 8.8 FT 0.955
HEXTRAN Simulation Procedure (Continuous)9. Output report
26
SHELL AND TUBE EXCHANGER DATA SHEETExchanger Name 21E052 Unit ID 21E052Size 1200 - 6000 Type AES Horizontal Connected 1 Parallel, 2 SeriesArea/Unit 856 m2 853 m2 Required Area/Shell 428 m2Performance of One Unit Shell-Side Tube-SideFeed Stream Number VR_FR_E7 ATB_FR_E6Feed Stream Name VR_FR_E7 VR_OUT ATB_FR_E6 ATB_TO_E7Total Fluid kg/hr 117936 226067
In Out In OutVapor kg/hr 0 0 0 0Liquid kg/hr 117936 117936 226067Steam kg/hr 0 0 0 0Water kg/hr 0 0 0 0Non-Condensible kg/hr 0 0
Temperature C 267.5 254.5 248.1 254.8Pressure kg/cm2 15.72 15.48 18.49 17.24Sp. Gr. Liquid (0 C/0 C H2O) 1.001 1.001 0.959 0.959
Vapor (0 C/0 C AIR) 0.000 0.000 0.000 0.000Density Liquid kg/m3 878.245 884.414 836.797 832.724
Vapor kg/m3 0.000 0.000 0.000 0.000Viscosity Liquid cP 5.951 7.362 1.542 1.422
Vapor cP 0.000 0.000 0.000 0.000Thermal Cond. Liquid kcal/hr-m-C 0.0640 0.0648 0.0658 0.0652
Vapor kcal/hr-m-C 0.0000 0.0000 0.0000 0.0000Spec. Heat Liquid kcal/kg-C 0.6304 0.6185 0.6312 0.6375
Vapor kcal/kg-C 0.0000 0.0000 0.0000 0.0000Latent Heat kcal/kg 0.00 0.00Velocity m/sec 0.44 1.44DP/Shell (Des/Calc) kg/cm2 0.70 0.23 0.70 0.63Fouling Resistance hr-m2-C/kcal 0.00200 0.00203 Required 0.00140Transfer Rate kcal/hr-m2-C Service 120.08 Reqd. 120.08 Clean 223.84Heat Exchanged x 10 6̂ Kcal/hr 0.961 MTD(Corrected) 8.8 FT 0.955
Construction of One Shell Shell-Side Tube-SideDesign Pressure / Temperature kg/cm2 / C 25 / 296 38 / 328Number of Passes: 1 4Material Low Chrome Steel Low Chrome SteelInlet Nozzle ID / NO mm 152.4 / 1 203.2 / 1Outlet Nozzle ID / NO mm 152.4 / 1 203.2 / 1Tube: Number 1269 OD 19.050 mm Thickness 2.28 mm Length 6.0 m
Type Bare Pitch 25.4 mm Pattern Square - 90 DegreesFins: Number N/A Root OD N/A Height N/A
Thickness N/A Efficiency N/AShell: ID 1200 mm Sealing Strips 0 Pairs Single SegmentalBaffle: Cut 0.250 Spacing (mm) (In/Cent/Out) 500.00 / 140.15 / 510.00 0RHO-V2: Inlet Nozzle 4317.2 kg/m/sec2Total Weight/Shell kg 7795.9 Full of Water 24403.0 Bundle 10131.6
HEXTRAN Simulation Procedure (Continuous)
Output report (continuous)
27
Construction of One Shell Shell-Side Tube-SideDesign Pressure / Temperature kg/cm2 / C 25 / 296 38 / 328Number of Passes: 1 4Material Low Chrome Steel Low Chrome SteelInlet Nozzle ID / NO mm 152.4 / 1 203.2 / 1Outlet Nozzle ID / NO mm 152.4 / 1 203.2 / 1Tube: Number 1269 OD 19.050 mm Thickness 2.28 mm Length 6.0 m
Type Bare Pitch 25.4 mm Pattern Square - 90 DegreesFins: Number N/A Root OD N/A Height N/A
Thickness N/A Efficiency N/AShell: ID 1200 mm Sealing Strips 0 Pairs Single SegmentalBaffle: Cut 0.250 Spacing (mm) (In/Cent/Out) 500.00 / 140.15 / 510.00 0RHO-V2: Inlet Nozzle 4317.2 kg/m/sec2Total Weight/Shell kg 7795.9 Full of Water 24403.0 Bundle 10131.6
Comparison
Case Simulation Actual
CIT increase (deg C) 5 7
Throughput increase(KBSD) 1.66 1.65
28
Throughput increase(KBSD) 1.66 1.65
Benefit
Description Prelim.Budget
FinalBudget
Investment Cost(Mbaht)
40 50
Benefit Cost(Mbaht/Year)
192.6 192.6
29
Benefit Cost(Mbaht/Year)
192.6 192.6
Payback Period(Month)
2.70 3.40
IRR 471% 375%
Note : 1. VDU throughput increasing margin 10 USD/bbl.
Benefit Tracking
cannot take benefit continuously by higher throughputdue to optimization result from LP model.
Take benefit by fuel saving at furnace.Key
parameter Year2011 (Mbaht/Month)
Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov DecFuel saving 5.61 5.63 8.70 8.42 7.36 4.73 7.78 5.05 6.30 5.52 TA TA
30
Fuel saving 5.61 5.63 8.70 8.42 7.36 4.73 7.78 5.05 6.30 5.52 TA TA
Description Final BudgetInvestment Cost (Mbaht) 50Benefit Cost (Mbaht/Year) 81.64Payback Period (Month) 8.49IRR 153%