AU2006229739B2 - Improved short contact time PCC process - Google Patents
Improved short contact time PCC process Download PDFInfo
- Publication number
- AU2006229739B2 AU2006229739B2 AU2006229739A AU2006229739A AU2006229739B2 AU 2006229739 B2 AU2006229739 B2 AU 2006229739B2 AU 2006229739 A AU2006229739 A AU 2006229739A AU 2006229739 A AU2006229739 A AU 2006229739A AU 2006229739 B2 AU2006229739 B2 AU 2006229739B2
- Authority
- AU
- Australia
- Prior art keywords
- catalyst
- aromatics
- stream containing
- saturates
- stream
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
Links
- 238000000034 method Methods 0.000 title claims description 45
- 230000008569 process Effects 0.000 title claims description 43
- 239000003054 catalyst Substances 0.000 claims description 82
- 238000004231 fluid catalytic cracking Methods 0.000 claims description 37
- 238000000926 separation method Methods 0.000 claims description 29
- 150000002430 hydrocarbons Chemical class 0.000 claims description 24
- 229930195733 hydrocarbon Natural products 0.000 claims description 23
- 239000010457 zeolite Substances 0.000 claims description 18
- 239000004215 Carbon black (E152) Substances 0.000 claims description 17
- 238000005336 cracking Methods 0.000 claims description 15
- 229910021536 Zeolite Inorganic materials 0.000 claims description 14
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical group O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 14
- 239000002904 solvent Substances 0.000 claims description 11
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 claims description 10
- 239000000203 mixture Substances 0.000 claims description 9
- 238000000638 solvent extraction Methods 0.000 claims description 9
- 239000012528 membrane Substances 0.000 claims description 8
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 7
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 6
- 239000012530 fluid Substances 0.000 claims description 5
- 238000004811 liquid chromatography Methods 0.000 claims description 5
- 239000011148 porous material Substances 0.000 claims description 5
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 claims description 4
- HYBBIBNJHNGZAN-UHFFFAOYSA-N furfural Chemical compound O=CC1=CC=CO1 HYBBIBNJHNGZAN-UHFFFAOYSA-N 0.000 claims description 4
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 claims description 2
- 239000000654 additive Substances 0.000 claims description 2
- 230000000996 additive effect Effects 0.000 claims description 2
- 238000011160 research Methods 0.000 claims description 2
- 239000000047 product Substances 0.000 description 27
- 239000002245 particle Substances 0.000 description 21
- 238000006243 chemical reaction Methods 0.000 description 16
- 239000003921 oil Substances 0.000 description 15
- 239000007789 gas Substances 0.000 description 14
- 238000000605 extraction Methods 0.000 description 13
- 239000000571 coke Substances 0.000 description 12
- 239000003502 gasoline Substances 0.000 description 10
- 125000003118 aryl group Chemical group 0.000 description 9
- 239000011159 matrix material Substances 0.000 description 8
- 238000009835 boiling Methods 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 6
- 238000004587 chromatography analysis Methods 0.000 description 6
- 239000003208 petroleum Substances 0.000 description 6
- 239000008186 active pharmaceutical agent Substances 0.000 description 5
- 238000004821 distillation Methods 0.000 description 5
- 230000005484 gravity Effects 0.000 description 5
- 239000002609 medium Substances 0.000 description 5
- 238000010791 quenching Methods 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 230000003247 decreasing effect Effects 0.000 description 4
- 230000006872 improvement Effects 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 238000012986 modification Methods 0.000 description 4
- 230000004048 modification Effects 0.000 description 4
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 4
- 229910052761 rare earth metal Inorganic materials 0.000 description 4
- 241000894007 species Species 0.000 description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 3
- MCMNRKCIXSYSNV-UHFFFAOYSA-N ZrO2 Inorganic materials O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 238000004523 catalytic cracking Methods 0.000 description 3
- 239000003546 flue gas Substances 0.000 description 3
- 238000005194 fractionation Methods 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 3
- 150000002910 rare earth metals Chemical class 0.000 description 3
- 230000008929 regeneration Effects 0.000 description 3
- 238000011069 regeneration method Methods 0.000 description 3
- 239000000377 silicon dioxide Substances 0.000 description 3
- 239000010454 slate Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- PAYRUJLWNCNPSJ-UHFFFAOYSA-N Aniline Chemical compound NC1=CC=CC=C1 PAYRUJLWNCNPSJ-UHFFFAOYSA-N 0.000 description 2
- CIWBSHSKHKDKBQ-JLAZNSOCSA-N Ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-JLAZNSOCSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- QQONPFPTGQHPMA-UHFFFAOYSA-N Propene Chemical compound CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 150000001336 alkenes Chemical class 0.000 description 2
- 239000010426 asphalt Substances 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 238000004939 coking Methods 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 description 2
- 239000000395 magnesium oxide Substances 0.000 description 2
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000012466 permeate Substances 0.000 description 2
- 239000012465 retentate Substances 0.000 description 2
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical class CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 description 1
- 235000007849 Lepidium sativum Nutrition 0.000 description 1
- 244000211187 Lepidium sativum Species 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000003849 aromatic solvent Substances 0.000 description 1
- LTPBRCUWZOMYOC-UHFFFAOYSA-N beryllium oxide Inorganic materials O=[Be] LTPBRCUWZOMYOC-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- KAKZBPTYRLMSJV-UHFFFAOYSA-N butadiene group Chemical group C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000012504 chromatography matrix Substances 0.000 description 1
- 239000012501 chromatography medium Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 239000012013 faujasite Substances 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 239000001282 iso-butane Substances 0.000 description 1
- 235000013847 iso-butane Nutrition 0.000 description 1
- 239000012263 liquid product Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 230000037361 pathway Effects 0.000 description 1
- 238000005373 pervaporation Methods 0.000 description 1
- 239000011295 pitch Substances 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000003079 shale oil Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000011973 solid acid Substances 0.000 description 1
- 239000008247 solid mixture Substances 0.000 description 1
- 239000011877 solvent mixture Substances 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 239000011275 tar sand Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000004227 thermal cracking Methods 0.000 description 1
- 238000006276 transfer reaction Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 description 1
- -1 zeolites Chemical compound 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G25/00—Refining of hydrocarbon oils in the absence of hydrogen, with solid sorbents
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
- C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G21/00—Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G31/00—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for
- C10G31/11—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for by dialysis
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/44—Solvents
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/80—Additives
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/02—Gasoline
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Applications Claiming Priority (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US66589905P | 2005-03-28 | 2005-03-28 | |
| US60/665,899 | 2005-03-28 | ||
| US66853205P | 2005-04-05 | 2005-04-05 | |
| US60/668,532 | 2005-04-05 | ||
| PCT/US2006/008453 WO2006104661A1 (en) | 2005-03-28 | 2006-03-10 | Improved short contact time pcc process |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| AU2006229739A1 AU2006229739A1 (en) | 2006-10-05 |
| AU2006229739B2 true AU2006229739B2 (en) | 2011-05-12 |
Family
ID=36586066
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AU2006229739A Ceased AU2006229739B2 (en) | 2005-03-28 | 2006-03-10 | Improved short contact time PCC process |
Country Status (10)
| Country | Link |
|---|---|
| US (1) | US20060231458A1 (ja) |
| EP (1) | EP1866389A1 (ja) |
| JP (1) | JP2008534737A (ja) |
| CN (1) | CN101151350B (ja) |
| AU (1) | AU2006229739B2 (ja) |
| CA (1) | CA2603717A1 (ja) |
| MX (1) | MX2007010782A (ja) |
| SG (1) | SG158890A1 (ja) |
| TW (1) | TW200704765A (ja) |
| WO (1) | WO2006104661A1 (ja) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5879038B2 (ja) * | 2008-03-13 | 2016-03-08 | 中国石油化工股▲ふん▼有限公司 | 低品質の原料から軽質燃料を得るための方法 |
| US8128879B2 (en) | 2010-03-31 | 2012-03-06 | Uop Llc | Apparatus for increasing weight of olefins |
| US8471084B2 (en) | 2010-03-31 | 2013-06-25 | Uop Llc | Process for increasing weight of olefins |
| CN101972638B (zh) * | 2010-11-12 | 2012-07-04 | 南开大学 | 一种燃油深度脱氮方法 |
| US9828309B2 (en) | 2011-05-24 | 2017-11-28 | Jx Nippon Oil & Energy Corporation | Method for producing monocyclic aromatic hydrocarbons |
| FR2984917B1 (fr) | 2011-12-23 | 2014-01-10 | Total Raffinage Marketing | Procede pour optimiser la production de distillats comprenant une etape de craquage catalytique. |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB698332A (en) * | 1950-07-04 | 1953-10-14 | Standard Oil Co | Improvements in or relating to the refining and catalytic cracking of hydrocarbons |
| GB733862A (en) * | 1951-11-30 | 1955-07-20 | Standard Oil Dev Co | Improved process for the removal of asphaltic constituents from residual oils |
| US2790753A (en) * | 1954-12-29 | 1957-04-30 | Gulf Research Development Co | Quality of slurry oil recycle in fluid catalytic cracking |
| US2850431A (en) * | 1955-12-30 | 1958-09-02 | Texas Co | Solvent deasphalting |
| US4784748A (en) * | 1987-10-28 | 1988-11-15 | Mobil Oil Corporation | FCC unit combined with a circulating fluid bed combustor |
| US5976355A (en) * | 1984-03-09 | 1999-11-02 | Stone & Webster Engineering Corp. | Low residence time catalytic cracking process |
Family Cites Families (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US733862A (en) * | 1903-02-02 | 1903-07-14 | John A Miller | Steam-generator. |
| US3182011A (en) * | 1961-06-05 | 1965-05-04 | Sinclair Research Inc | Cracking a plurality of hydrocarbon stocks |
| US3193489A (en) * | 1962-09-13 | 1965-07-06 | Phillips Petroleum Co | Solvent extraction process |
| US3164542A (en) * | 1962-10-08 | 1965-01-05 | Phillips Petroleum Co | Catalytic process for the cracking of hydrocarbon oils containing metallic contaminants |
| US3303123A (en) * | 1964-10-16 | 1967-02-07 | Phillips Petroleum Co | Catalytic cracking of residuum oils containing metal contaminants in several stages |
| US3639228A (en) * | 1969-10-28 | 1972-02-01 | Gulf Research Development Co | Fcc process utilizing divided catalyst injection |
| US4388175A (en) * | 1981-12-14 | 1983-06-14 | Texaco Inc. | Hydrocarbon conversion process |
| JPS6031594A (ja) * | 1983-07-30 | 1985-02-18 | Jgc Corp | 蒸留残渣油の接触改質方法 |
| US4606810A (en) * | 1985-04-08 | 1986-08-19 | Mobil Oil Corporation | FCC processing scheme with multiple risers |
| US4985136A (en) * | 1987-11-05 | 1991-01-15 | Bartholic David B | Ultra-short contact time fluidized catalytic cracking process |
| US4976868A (en) * | 1989-10-16 | 1990-12-11 | Exxon Research And Engineering Company | Polyester membranes for aromatics/saturates separation |
| US5254795A (en) * | 1992-10-07 | 1993-10-19 | Exxon Research And Engineering Company | Removal of 2-ring aromatics from low boiling streams containing low concentrations of same using membranes |
| CA2103230C (en) * | 1992-11-30 | 2004-05-11 | Paul E. Eberly, Jr. | Fluid catalytic cracking process for producing light olefins |
| US5824208A (en) * | 1994-05-27 | 1998-10-20 | Exxon Research & Engineering Company | Short contact time catalytic cracking process |
| FR2771418B1 (fr) * | 1997-11-25 | 2001-02-02 | Inst Francais Du Petrole | Procede de separation d'une charge c5-c8 ou d'une charge intermediaire, en trois effluents respectivement riches en paraffines lineaires, monobranchees et multibranchees |
| US6110356A (en) * | 1998-05-06 | 2000-08-29 | Uop Llc | Slurry circulation process and system for fluidized particle contacting |
-
2006
- 2006-02-14 US US11/354,701 patent/US20060231458A1/en not_active Abandoned
- 2006-03-10 MX MX2007010782A patent/MX2007010782A/es unknown
- 2006-03-10 JP JP2008504076A patent/JP2008534737A/ja active Pending
- 2006-03-10 EP EP06737614A patent/EP1866389A1/en not_active Withdrawn
- 2006-03-10 CN CN2006800099928A patent/CN101151350B/zh not_active Expired - Fee Related
- 2006-03-10 SG SG201000286-3A patent/SG158890A1/en unknown
- 2006-03-10 CA CA002603717A patent/CA2603717A1/en not_active Abandoned
- 2006-03-10 AU AU2006229739A patent/AU2006229739B2/en not_active Ceased
- 2006-03-10 WO PCT/US2006/008453 patent/WO2006104661A1/en active Application Filing
- 2006-03-13 TW TW095108475A patent/TW200704765A/zh unknown
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB698332A (en) * | 1950-07-04 | 1953-10-14 | Standard Oil Co | Improvements in or relating to the refining and catalytic cracking of hydrocarbons |
| GB733862A (en) * | 1951-11-30 | 1955-07-20 | Standard Oil Dev Co | Improved process for the removal of asphaltic constituents from residual oils |
| US2790753A (en) * | 1954-12-29 | 1957-04-30 | Gulf Research Development Co | Quality of slurry oil recycle in fluid catalytic cracking |
| US2850431A (en) * | 1955-12-30 | 1958-09-02 | Texas Co | Solvent deasphalting |
| US5976355A (en) * | 1984-03-09 | 1999-11-02 | Stone & Webster Engineering Corp. | Low residence time catalytic cracking process |
| US4784748A (en) * | 1987-10-28 | 1988-11-15 | Mobil Oil Corporation | FCC unit combined with a circulating fluid bed combustor |
Also Published As
| Publication number | Publication date |
|---|---|
| AU2006229739A1 (en) | 2006-10-05 |
| TW200704765A (en) | 2007-02-01 |
| SG158890A1 (en) | 2010-02-26 |
| CA2603717A1 (en) | 2006-10-05 |
| US20060231458A1 (en) | 2006-10-19 |
| CN101151350B (zh) | 2012-02-08 |
| MX2007010782A (es) | 2007-11-07 |
| WO2006104661A1 (en) | 2006-10-05 |
| CN101151350A (zh) | 2008-03-26 |
| EP1866389A1 (en) | 2007-12-19 |
| JP2008534737A (ja) | 2008-08-28 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| WO2006074362A1 (en) | Method and apparatus for selecting dental materials | |
| US11352573B2 (en) | High-severity fluidized catalytic cracking systems and processes having partial catalyst recycle | |
| US9816037B2 (en) | Methods and systems for increasing production of middle distillate hydrocarbons from heavy hydrocarbon feed during fluid catalytic cracking | |
| US20080035527A1 (en) | Dual riser FCC reactor process with light and mixed light/heavy feeds | |
| RU2606971C2 (ru) | Способ максимального получения дистиллята на установках флюид-каталитического крекинга (уфкк) | |
| AU2006229739B2 (en) | Improved short contact time PCC process | |
| US20180079974A1 (en) | Process and apparatus for recycling cracked hydrocarbons | |
| US20010032803A1 (en) | FCC process | |
| US8808535B2 (en) | Vacuum distilled DAO processing in FCC with recycle | |
| US20150136647A1 (en) | Reactor and main fractionator configuration for producing diesel | |
| CN111479903B (zh) | 用于将烃裂化成较轻烃的方法和设备 | |
| KR101560605B1 (ko) | 도핑된 촉매를 사용한 올레핀의 제조 방법 | |
| CN105238438A (zh) | 一种催化裂解烃类原料制备低碳烃的方法 |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FGA | Letters patent sealed or granted (standard patent) | ||
| MK14 | Patent ceased section 143(a) (annual fees not paid) or expired |