tupras study2
TRANSCRIPT
Tupras Fuel Oil Upgrading Study
Tupras Management Overview
Stone & Webster
Offices in UK, Houston, Boston and Toronto
UK Contact - Vince Partington phone +44 1908 602110 fax +44 1908 602366 email [email protected]
Shaw Group purchased S&W in 2000
Shaw is a large piping fabricator and engineering company
Objectives
Design a Refinery / Petrochemical Complex
Process additional 95 MBPD Arab Light Crude
Process Existing Residue Streams from the Refinery
Produce Diesel / Kero / Chemicals
Produce no extra Gasoline
Methodology
Cases CASE 1 – VGO FCC ( Base Case - No SDA) CASE 2 – VGO FCC CASE 3 – VGO DCC CASE 4E – VGO CPP (Max Ethylene) CASE 4P – VGO CPP (Max Propylene) CASE 5E – RESID CPP (Max Ethylene) CASE 5P – RESID CPP (Max Propylene) CASE 6 – VGO HCU CASE 7 – VGO HCU + CCR CASE 8 – VGO DCC + CCR CASE 9 – VGO DCC + CCR + ALPHA
Process Units
CASE 0 CASE 1 CASE 2 CASE 3 CASE 4 CASE 5 CASE 6 CASE 7 CASE 8 CASE 9
CDU X X X X X X X X X XVDU X X X X - X X X X
NAPHTHA HDS X - - - - - - X X XKERO HDS X X X X X X X X X X
DIESEL HDS X X X X X X X X X XCCR X - - - - - - X X XSDA - X X X - X X X X
FCC FEED HDT X X X X - - - X XARDS - - - - X - - - -FCC X X - - - - - - -DCC - - X - - - - X XCPP - - - X X - - - -
HYDROCRACKER - - - - - X X - -FCC NAPHTHA HDS X X X X X - - X X
BTX X X X X X X X X X XALPHA - - - - - - - - X
STEAM CRACKER X X X X X X X X XH2 PLANT - X X X X X X - -
SULPHUR PLANT X X X X X X X X X X
Modelled in “Refine” and by LP
CASE 0 HYDROSKIMMING - BTX RECOVERY
Revenue MM$/Year -10
Cost MM$ ISBL 325
Cost MM$ 1,000-1,500
Payback Years Never
40 MBPD
23 MBPD
KERO HDS
DIESEL HDS
CDU
NHT
BTXRECOVERY
ARAB LIGHT
LPG + NAPHTHA
KEROSENE
DIESEL
ATMOS RESID
ATMOS GASOIL
FUEL OIL
C9+ AROMATICS
XYLENE
TOLUENE
BENZENE
DIESEL
KERO
LPG
RAFFINATECCR
LVN
CASE 1 COMPLEX CONFIGURATION (VGO FCC – NO SDA)
KERO HDS
DIESEL HDS
CDU
VDU
ETHYLENE CRACKER
BTXRECOVERY
VGO HDS
NAPHTHA HDSFCC
40
RECOVERY SYSTEM
ARAB LIGHT
95.0
NAPHTHA
KEROSENE
DIESEL
ATMOS RESID
42.0
ATMOS RESID 12.6
VAC RESID38.0
HVGO HCU BOTTOMS
ATMOS GASOIL
SLURRY OIL
FUEL OIL
C9+ AROMATICS
XYLENE
TOLUENE
BENZENE
DIESEL
KERO
LPG
BUTADIENE
PROPYLENE
ETHYLENE
LCO/DCO
RAFFINATE
PYGAS
C4-
LCNHCN
Revenue MM$/Year 300
Cost MM$ ISBL 1,260
Cost MM$ 2,430
Payback Years 8.172 MBPD
23 MBPD
610 KTA
440 KTA
CASE 2 COMPLEX CONFIGURATION (VGO FCC)
KERO HDS
DIESEL HDS
CDU
VDU
SDA
ETHYLENE CRACKER
BTXRECOVERY
VGO HDS
NAPHTHA HDSFCC
65
RECOVERY SYSTEM
ARAB LIGHT
NAPHTHA
KEROSENE
DIESEL
ATMOS RESID
ATMOS RESID
VAC RESID
HVGO HCU BOTTOMS
ATMOS GASOIL
SLURRY OIL
FUEL OIL
C9+ AROMATICS
XYLENE
TOLUENE
BENZENE
DIESEL
KERO
LPG
BUTADIENE
PROPYLENE
ETHYLENE
LCO/DCO
RAFFINATE
PYGAS
C4-
LCNHCN
Revenue MM$/Year 390
Cost ISBL 1,600
Cost MM$ 3,119
Payback Years 7.950 MBPD
23 MBPD
730 KTA
570 KTA
CASE 3 COMPLEX CONFIGURATION (VGO DCC/CPP)
KERO HDS
DIESEL HDS
CDU
VDU
SDA60
ETHYLENE CRACKER
BTXRECOVERY
VGO HDS
NAPHTHA HDSDCC
65
RECOVERY SYSTEM
ARAB LIGHT
NAPHTHA
KEROSENE
DIESEL
ATMOS RESID
ATMOS RESID
VAC RESID
HVGO HCU BOTTOMS
ATMOS GASOIL
SLURRY OIL
FUEL OIL
C9+ AROMATICS
XYLENE
TOLUENE
BENZENE
DIESEL
KERO
LPG
BUTADIENE
PROPYLENE
ETHYLENE
LCO/DCO
RAFFINATE
PYGAS
C4-
LCNHCN
Revenue MM$/Year 570
Cost ISBL 1,600
Cost MM$ 3,134
Payback Years 5.4
42 MBPD
23 MBPD
770 KTA
1,080 KTA
CASE 6 COMPLEX CONFIGURATION (VGO HCU)
KERO HDS
DIESEL HDS
CDU
VDU
SDA60
ETHYLENE CRACKER
BTXRECOVERYHCU
71
RECOVERY SYSTEM
ARAB LIGHT
NAPHTHA
KEROSENE
DIESEL
ATMOS RESID
ATMOS RESID
VAC RESID
HVGO HCU BOTTOMS
ATMOS GASOIL
SLURRY OIL
FUEL OIL
C9+ AROMATICS
XYLENE
TOLUENE
BENZENE
DIESEL
KERO
LPG
BUTADIENE
PROPYLENE
ETHYLENE
RAFFINATE
PYGAS
NAPHTHA
KERO
DIESEL
HCU BOTTOMS
Revenue MM$/Year 560
Cost MM$ ISBL 1,630
Cost MM$ 3,185
Payback Years 5.6
33 MBPD
50 MBPD
940 KTA
510 KTA
CASE 5 COMPLEX CONFIGURATION (RESID CPP)
KERO HDS
DIESEL HDS
CDU
ETHYLENE CRACKER
BTXRECOVERY
ARDS
100
NAPHTHA HDSRCPP
110
RECOVERY SYSTEM
ARAB LIGHT
NAPHTHA
KEROSENE
DIESEL
ATMOS RESID
ATMOS RESID
VAC RESID
HVGO HCU BOTTOMS
ATMOS GASOIL
SLURRY OIL
C9+ AROMATICS
XYLENE
TOLUENE
BENZENE
DIESEL
KERO
LPG
BUTADIENE
PROPYLENE
ETHYLENE
LCO/DCO
RAFFINATE
PYGAS
C4-
LCNHCN
Revenue MM$/Year 940
Cost MM$ ISBL 1,900
Cost MM$ 3,679
Payback Years 3.9Zero Fuel Oil
23 MBPD
1,120 KTA
1,740 KTA
Conclusions
Refinery / Petrochemical Complex is Feasible
Further cases can fine tune the results but the overall pattern will remain
ARDS/CPP has the best payback
CPP and Hydrocracking have a similar payback
FCC is not a cost effective process for Chemicals
Ethylene and Propylene production is world scale
S&W can develop downstream chemical product options
Other Comments
Tupras Vacuum Residue is too high in Metals to Process in an RFCC without pre-treatment.
TABLE 3.1 – FEED & PRODUCT PRICES USED FOR THE STUDY
FEEDSSG $/T $/BBL
ARAB LIGHT 0.864 171 23.49ATMOS RESID 0.967 114 17.53
VAC RESID 1.025 79 12.87SLURRY OIL 1.052 163 27.26
HVGO 0.922 166 24.33HCU BOTTOMS 1.052 163 27.26
PRODUCTSSG $/T $/BBL
PROPANE 0.5076 289 23.32BUTANE 0.58 289 26.65
JET / KERO 0.798 234 29.69DIESEL 0.845 222 29.82
3.5% FUEL OIL 0.98 116 18.07ASPHALTS 1.2 122 23.28ETHYLENE 0.347 512 28.25
PROPYLENE 0.523 469 39.00BUTENES 0.61 361 35.01BENZENE 0.885 395 55.58TOLUENE 0.872 333 46.16XYLENE 0.875 350 48.69
C9+ AROMATICS 0.875 180 25.04SULPHUR - 125 -
Feeds
5.2 EXPLANATION OF THE CASES
For all the cases, the feed streams to the refinery / petrochemical complex is always the same, namely:
Crude (Arab Light) 95,000 BPSDAtmospheric Residue 12,600 BPSDVacuum Residue 38,000 BPSDHVGO 6,500 BPSDSlurry Oil 1,400 BPSDHydrocracker Bottoms 1,600 BPSD
Each of the nine cases has been selected to promote a different operating scenario and aprogressive addition of specialised units. Dependent on what products can be sold mayalter the perception of the importance of some of these cases.
TABLE 6.1 – SUMMARY OF THE REFINERY PRODUCTS (TPA)
CASE CASE 1 CASE 2 CASE 3 CASE 4 CASE 5 CASE 6 CASE 7 CASE 8 CASE 9CASE TYPE VGO FCC VGO FCC VGO DCC VGO CPP RSD CPP VGO HCU VGO HCU + VGO DCC + VGO DCC +
(NO SDA) CCR CCR CCR + ALPHAOPERATION - - MAX C3= MAX C2= MAX C3= MAX C2= MAX C3= MAX JET/DSL AROMATICS AROMATICS AROMATICS
ETHYLENE 613,313 732,137 704,005 1,111,818 778,342 1,691,302 1,118,286 941,865 268,908 432,953 419,070PROPYLENE 437,457 571,384 983,232 834,056 1,080,257 1,220,236 1,741,972 512,482 146,324 835,744 840,226
BUTYLENE 401,475 513,113 677,566 401,577 634,051 629,469 925,925 353,039 100,810 575,975 90,220LPG 180,042 235,991 263,618 197,592 239,229 197,229 394,973 375,788 541,185 352,519 511,924
JET/KERO 466,951 466,951 466,951 466,951 466,951 466,951 466,951 1,174,481 1,174,481 466,951 466,951DIESEL 570,482 709,565 709,565 709,565 709,565 554,919 565,216 1,112,236 1,112,236 709,565 709,565
FUEL OIL 3,904,801 2,741,764 2,316,531 2,103,915 2,245,641 0 0 1,780,819 1,780,819 2,316,531 2,316,531
BENZENE 195,699 231,401 183,339 153,496 161,277 179,448 193,680 301,723 235,834 165,807 216,283TOLUENE 102,429 126,301 145,128 102,235 113,443 140,373 160,849 123,875 576,969 361,388 538,297
XYLENE 106,579 137,009 190,615 122,597 140,417 183,458 215,933 92,654 853,508 528,026 653,009C9+ AROMATICS 224,648 304,010 225,768 142,900 164,567 217,053 256,685 96,014 579,927 361,171 443,795
SULPHUR 46,667 82,540 82,222 78,730 81,270 176,190 204,762 99,048 99,683 82,857 82,8577,250,543 6,852,166 6,948,538 6,425,432 6,815,009 5,656,628 6,245,231 6,964,023 7,470,683 7,189,486 7,288,728
ARAB LIGHT 4,567,250 4,567,250 4,567,250 4,567,250 4,567,250 4,567,250 4,567,250 4,567,250 4,567,250 4,567,250 4,567,250ATM RESIDUE 677,976 677,976 677,976 677,976 677,976 677,976 677,976 677,976 677,976 677,976 677,976VAC RESIDUE 2,173,090 2,173,090 2,173,090 2,173,090 2,173,090 2,173,090 2,173,090 2,173,090 2,173,090 2,173,090 2,173,090
HVGO 333,730 333,730 333,730 333,730 333,730 333,730 333,730 333,730 333,730 333,730 333,730CLO 80,547 80,547 80,547 80,547 80,547 80,547 80,547 80,547 80,547 80,547 80,547
HCU BOTTOMS 94,948 94,948 94,948 94,948 94,948 94,948 94,948 94,948 94,948 94,948 94,9487,927,541 7,927,541 7,927,541 7,927,541 7,927,541 7,927,541 7,927,541 7,927,541 7,927,541 7,927,541 7,927,541
TABLE 6.2 – SUMMARY OF THE REFINERY PRODUCTS (BPSD)
CASE CASE 1 CASE 2 CASE 3 CASE 4 CASE 5 CASE 6 CASE 7 CASE 8 CASE 9CASE TYPE VGO FCC VGO FCC VGO DCC VGO CPP RSD CPP VGO HCU VGO HCU + VGO DCC + VGO DCC +
(NO SDA) CCR CCR CCR + ALPHAOPERATION - - MAX C3= MAX C2= MAX C3= MAX C2= MAX C3= MAX JET/DSL AROMATICS AROMATICS AROMATICS
ETHYLENE 31,764 37,918 36,461 57,582 40,311 87,594 57,917 48,780 13,927 22,423 21,704PROPYLENE 15,032 19,634 33,786 28,660 37,120 41,930 59,858 17,610 5,028 28,718 28,872
BUTYLENE 11,828 15,117 19,962 11,831 18,680 18,545 27,279 10,401 2,970 16,969 2,658C3/C4 5,950 7,799 8,712 6,530 7,906 6,518 13,053 12,419 17,885 11,650 16,918
JET/KERO 10,516 10,516 10,516 10,516 10,516 10,516 10,516 26,450 26,450 10,516 10,516DIESEL 12,133 15,091 15,091 15,091 15,091 11,802 12,021 23,655 23,655 15,091 15,091
FUEL OIL 71,607 50,279 42,481 38,582 41,181 0 0 32,657 32,657 42,481 42,481
BENZENE 3,974 4,699 3,723 3,117 3,275 3,644 3,933 6,127 4,789 3,367 4,392TOLUENE 2,111 2,603 2,991 2,107 2,338 2,893 3,315 2,553 11,891 7,448 11,094
XYLENE 2,189 2,814 3,915 2,518 2,884 3,768 4,435 1,903 17,530 10,845 13,412C9+ AROMATICS 4,614 6,244 4,637 2,935 3,380 4,458 5,272 1,972 11,911 7,418 9,115
SULPHUR 147 260 259 248 256 555 645 312 314 261 261171,718 172,714 182,275 179,469 182,682 191,668 197,599 184,527 168,693 176,926 176,253
ARAB LIGHT 95,000 95,000 95,000 95,000 95,000 95,000 95,000 95,000 95,000 95,000 95,000ATM RESIDUE 12,600 12,600 12,600 12,600 12,600 12,600 12,600 12,600 12,600 12,600 12,600VAC RESIDUE 38,101 38,101 38,101 38,101 38,101 38,101 38,101 38,101 38,101 38,101 38,101
HVGO 6,505 6,505 6,505 6,505 6,505 6,505 6,505 6,505 6,505 6,505 6,505CLO 1,376 1,376 1,376 1,376 1,376 1,376 1,376 1,376 1,376 1,376 1,376
HCU BOTTOMS 1,622 1,622 1,622 1,622 1,622 1,622 1,622 1,622 1,622 1,622 1,622155,204 155,204 155,204 155,204 155,204 155,204 155,204 155,204 155,204 155,204 155,204
TABLE 6.3 – SUMMARY OF THE REFINERY UNITS AND CAPACITIES (BPSD)
CASE CASE 1 CASE 2 CASE 3 CASE 4 CASE 5 CASE 6 CASE 7 CASE 8 CASE 9CASE TYPE VGO FCC VGO FCC VGO DCC VGO CPP RSD CPP VGO HCU VGO HCU + VGO DCC + VGO DCC +
(NO SDA) CCR CCR CCR + ALPHAOPERATION - - MAX C3= MAX C2= MAX C3= MAX C2= MAX C3= MAX JET/DSL AROMATICS AROMATICS AROMATICS
CDU 95,000 95,000 95,000 95,000 95,000 95,000 95,000 95,000 95,000 95,000 95,000VDU 51,086 51,086 51,086 51,086 51,086 - - 51,086 51,086 51,086 51,086
NAPHTHA HDS - - - - - - - - 23,720 7,909 15,549KERO HDS 10,516 10,516 10,516 10,516 10,516 10,516 10,516 10,516 10,516 10,516 10,516
DIESEL HDS 12,120 15,061 15,061 15,061 15,061 9,254 9,254 9,254 9,254 15,061 15,061CCR - - - - - - - - 61,268 36,930 37,649SDA - 60,734 60,734 60,734 60,734 - - 60,734 60,734 60,734 60,734
FCC FEED HDT 42,994 71,071 71,071 71,071 71,071 - - - - 71,071 71,071ARDS - - - - - 98,081 101,620 - - - -
FCC/DCC/CPP 39,972 64,983 64,983 64,983 64,983 107,406 110,571 - - 64,983 64,983HYDROCRACKER - - - - - - - 71,071 71,071 - -
FCC NAPHTHA HDS 26,084 36,979 21,118 11,890 14,303 19,917 24,241 - - 36,928 37,647BTX 39,954 53,301 32,783 22,085 24,883 31,290 36,616 21,834 59,040 38,874 54,804
ALPHA - - - - - - - - - - 7,909STEAM CRACKER 615,721 735,010 706,765 1,116,182 781,410 1,697,957 1,122,676 945,578 269,962 434,659 420,712
H2 PLANT - 5.9 12.8 14.8 14.3 21.5 23.8 122.9 90.7 - -SULPHUR PLANT 147 260 259 248 256 555 655 313 314 261 261
TABLE 6.4 – SUMMARY OF REFINERY CAPITAL COSTS ($ MILLIONS)
CASE CASE 1 CASE 2 CASE 3 CASE 4 CASE 5 CASE 6 CASE 7 CASE 8 CASE 9CASE TYPE VGO FCC VGO FCC VGO DCC VGO CPP RSD CPP VGO HDU VGO HDU + VGO DCC + VGO DCC +
(NO SDA) CCR CCR CCR + ALPHAOPERATION - - MAX C3= MAX C2= MAX C3= MAX C2= MAX C3= MAX JET/DSL AROMATICS AROMATICS AROMATICS
CDU 91.1 91.1 91.1 91.1 91.1 91.1 91.1 91.1 91.1 91.1 91.1VDU 44.6 44.6 44.6 44.6 44.6 - - 44.6 44.6 44.6 44.6
NAPHTHA HDS - - - - - - - - 29.0 14.6 22.3KERO HDS 19.5 19.5 19.5 19.5 19.5 19.5 19.5 19.5 19.5 19.5 19.5
DIESEL HDS 39.5 45.9 45.9 45.9 45.9 32.8 32.8 32.8 32.8 45.9 45.9CCR - - - - - - - - 139.8 99.3 100.6SDA - 75.3 75.3 75.3 75.3 - - 75.3 75.3 75.3 75.3
FCC FEED HDT 221.0 302.6 302.6 302.6 302.6 - - - - 302.6 302.6ARDS - - - - - 386.3 396.8 - - - -
FCC/DCC/CPP 173.9 227.9 284.4 251.8 275.8 346.5 378.4 - - 284.4 284.4HYDROCRACKER - - - - - - - 429.6 429.6 - -
FCC NAPHTHA HDS 30.8 38.3 27.0 18.8 21.2 26.0 29.4 - - 38.3 38.7BTX 32.1 39.2 27.9 21.2 23.0 27.0 30.2 21.0 42.1 31.5 40.0
ALPHA - - - - - - - - - - 22.2STEAM CRACKER 566.5 639.5 595.1 763.4 621.8 995.8 780.0 767.4 320.7 408.9 276.9
H2 PLANT - 13.0 20.8 22.7 22.2 28.4 30.2 81.0 67.5 - -SULPHUR PLANT 41.1 58.5 58.4 56.8 58.0 93.7 103.8 65.7 65.8 58.7 58.7
ONSITE ISBL ($ MILLION) 1,260 1,596 1,593 1,714 1,601 2,047 1,892 1,628 1,358 1,515 1,423
OFFSITES 693.1 877.6 875.9 942.6 880.6 1125.9 1040.7 895.5 746.8 833.1 782.6BOILER PLANT 315.0 398.9 398.1 428.5 400.3 511.8 473.1 407.0 339.5 378.7 355.7
CONTROL ROOM 151.2 191.5 191.1 205.7 192.1 245.7 227.1 195.4 162.9 181.8 170.7LICENSE FEES 9.1 55.7 60.1 59.6 59.8 44.3 46.3 59.3 68.7 61.2 61.6
TOTAL ($ MILLION) 2,429 3,119 3,118 3,350 3,134 3,975 3,679 3,185 2,676 2,969 2,794
TABLE 6.5 – SUMMARY OF REFINERY PROFITS ($ 000 / DAY)
CASE CASE 1 CASE 2 CASE 3 CASE 4 CASE 5 CASE 6 CASE 7 CASE 8 CASE 9CASE TYPE VGO FCC VGO FCC VGO DCC VGO CPP RSD CPP VGO HCU VGO HCU + VGO DCC + VGO DCC +
(NO SDA) CCR CCR CCR + ALPHAOPERATION MAX C3= MAX C2= MAX C3= MAX C2= MAX C3= MAX JET/DSL AROMATICS AROMATICS AROMATICS
ETHYLENE 897 1,071 1,030 1,626 1,139 2,474 1,636 1,378 393 633 613PROPYLENE 586 766 1,318 1,118 1,448 1,635 2,334 687 196 1,120 1,126
BUTYLENE 414 529 699 414 654 649 955 364 104 594 93LPG 149 195 218 163 198 163 326 310 447 291 423
JET/KERO 312 312 312 312 312 312 312 785 785 312 312DIESEL 362 450 450 450 450 352 359 705 705 450 450
FUEL OIL 1,294 909 768 697 744 0 0 590 590 768 768BENZENE 221 261 207 173 182 203 219 341 266 187 244TOLUENE 97 120 138 97 108 134 153 118 549 344 512
XYLENE 107 137 191 123 140 183 216 93 854 528 653C9+ AROMATICS 116 156 116 73 85 112 132 49 298 186 228
SULPHUR 18 33 32 31 32 69 81 39 39 33 33Total Product Value 4,573 4,939 5,478 5,279 5,491 6,286 6,722 5,459 5,227 5,446 5,455
ARAB LIGHT 2,231 2,231 2,231 2,231 2,231 2,231 2,231 2,231 2,231 2,231 2,231ATMOS. RESIDUE 221 221 221 221 221 221 221 221 221 221 221
VACUUM RSD 490 490 490 490 490 490 490 490 490 490 490CLO 177 177 177 177 177 177 177 177 177 177 177
HVGO 33 33 33 33 33 33 33 33 33 33 33HCU BOTTOMS 44 44 44 44 44 44 44 44 44 44 44
Total Feed Costs 3,198 3,198 3,198 3,198 3,198 3,198 3,198 3,198 3,198 3,198 3,198GROSS MARGIN 1,375 1,741 2,280 2,081 2,293 3,088 3,524 2,261 2,030 2,248 2,257
UTILITIES 135 135 179 174 189 268 296 153 181 198 202OPERATING MARGIN 1,240 1,606 2,101 1,907 2,104 2,820 3,228 2,108 1,849 2,050 2,055
FIXED COSTS 416 527 526 566 528 676 624 537 448 500 470NET PROFIT ($/DAY) 825 1,080 1,576 1,341 1,576 2,145 2,604 1,571 1,400 1,550 1,585
NET MARGIN ($/BBL FEED) 5.3 7.0 10.2 8.6 10.2 13.8 16.8 10.1 9.0 10.0 10.2
TABLE 6.6 – SIMPLE ECONOMIC ANALYSIS OF THE CASES
CASE CASE TYPE CASE MODE CAP COST NET PROFIT NET MARGIN PAYBACK RANK($ MILLION) ($ 000/DAY) ($/BBL) (YEARS) (1=BEST)
CASE 1 VGO FCC (NO SDA) - 2,429 825 5.3 8.1 11CASE 2 VGO FCC - 3,119 1,080 7.0 7.9 10CASE 3 VGO DCC MAX C3= 3,118 1,576 10.2 5.4 6
CASE 4E VGO CPP MAX C2= 3,350 1,341 8.6 6.8 9CASE 4P VGO CPP MAX C3= 3,134 1,576 10.2 5.4 7CASE 5E RSD CPP MAX C2= 3,975 2,145 13.8 5.1 3CASE 5P RSD CPP MAX C3= 3,679 2,604 16.8 3.9 1
CASE 6 VGO HCU MAX JET/DSL 3,185 1,571 10.1 5.6 8CASE 7 VGO HCU + CCR AROMATICS 2,676 1,400 9.0 5.2 4CASE 8 VGO DCC + CCR AROMATICS 2,969 1,550 10.0 5.2 5CASE 9 VGO DCC + CCR + ALPHA AROMATICS 2,794 1,585 10.2 4.8 2