EA014574B1 - Дополнительный крекинг тяжёлых нефтей при работе установки каталитического крекинга в псевдоожиженном слое - Google Patents
Дополнительный крекинг тяжёлых нефтей при работе установки каталитического крекинга в псевдоожиженном слое Download PDFInfo
- Publication number
- EA014574B1 EA014574B1 EA200900186A EA200900186A EA014574B1 EA 014574 B1 EA014574 B1 EA 014574B1 EA 200900186 A EA200900186 A EA 200900186A EA 200900186 A EA200900186 A EA 200900186A EA 014574 B1 EA014574 B1 EA 014574B1
- Authority
- EA
- Eurasian Patent Office
- Prior art keywords
- catalyst
- reactor
- stream
- ecc
- downstream
- Prior art date
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- 239000000295 fuel oil Substances 0.000 title claims abstract description 39
- 238000005336 cracking Methods 0.000 title claims abstract description 28
- 238000010977 unit operation Methods 0.000 title 1
- 239000003054 catalyst Substances 0.000 claims abstract description 127
- 229930195733 hydrocarbon Natural products 0.000 claims abstract description 35
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract description 35
- 239000007795 chemical reaction product Substances 0.000 claims abstract description 22
- 239000003502 gasoline Substances 0.000 claims abstract description 16
- 239000000203 mixture Substances 0.000 claims abstract description 13
- 230000008929 regeneration Effects 0.000 claims abstract description 13
- 238000011069 regeneration method Methods 0.000 claims abstract description 13
- -1 ethylene, propylene, butylenes Chemical class 0.000 claims abstract description 10
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract description 8
- 230000001172 regenerating effect Effects 0.000 claims abstract description 3
- 238000000034 method Methods 0.000 claims description 81
- 238000006243 chemical reaction Methods 0.000 claims description 52
- 230000008569 process Effects 0.000 claims description 37
- 239000002994 raw material Substances 0.000 claims description 25
- 239000000047 product Substances 0.000 claims description 22
- 150000001336 alkenes Chemical class 0.000 claims description 19
- 238000002156 mixing Methods 0.000 claims description 14
- 238000003795 desorption Methods 0.000 claims description 11
- 238000012545 processing Methods 0.000 claims description 10
- 238000004523 catalytic cracking Methods 0.000 claims description 9
- 238000000926 separation method Methods 0.000 claims description 9
- 238000012546 transfer Methods 0.000 claims description 9
- 238000010791 quenching Methods 0.000 claims description 5
- 238000004821 distillation Methods 0.000 claims description 4
- 238000005194 fractionation Methods 0.000 claims description 4
- 230000000171 quenching effect Effects 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 2
- 230000001105 regulatory effect Effects 0.000 claims description 2
- 239000010779 crude oil Substances 0.000 claims 2
- 230000000087 stabilizing effect Effects 0.000 claims 2
- 230000001276 controlling effect Effects 0.000 claims 1
- 239000008240 homogeneous mixture Substances 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 abstract description 10
- 239000006227 byproduct Substances 0.000 abstract description 4
- 238000011084 recovery Methods 0.000 abstract description 3
- 239000003921 oil Substances 0.000 description 38
- 239000007789 gas Substances 0.000 description 24
- 239000000654 additive Substances 0.000 description 12
- 238000009434 installation Methods 0.000 description 11
- 239000000571 coke Substances 0.000 description 10
- 239000010457 zeolite Substances 0.000 description 9
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 8
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 8
- 238000002347 injection Methods 0.000 description 5
- 239000007924 injection Substances 0.000 description 5
- 229910021536 Zeolite Inorganic materials 0.000 description 4
- 230000008901 benefit Effects 0.000 description 4
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 4
- 230000006872 improvement Effects 0.000 description 4
- 238000011144 upstream manufacturing Methods 0.000 description 4
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 3
- 239000005977 Ethylene Substances 0.000 description 3
- 230000000996 additive effect Effects 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 3
- 238000007654 immersion Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 3
- 238000011027 product recovery Methods 0.000 description 3
- 238000007670 refining Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 2
- 230000001737 promoting effect Effects 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 description 2
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000001273 butane Substances 0.000 description 1
- 238000004517 catalytic hydrocracking Methods 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000011143 downstream manufacturing Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 1
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 1
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 238000004230 steam cracking Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
- C10G51/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only
- C10G51/06—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural parallel stages only
-
- 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
- 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
- C10G2300/4006—Temperature
-
- 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
- C10G2300/4093—Catalyst stripping
-
- 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
-
- 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
- C10G2400/20—C2-C4 olefins
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 (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US11/487,011 US20080011644A1 (en) | 2006-07-13 | 2006-07-13 | Ancillary cracking of heavy oils in conjuction with FCC unit operations |
| PCT/US2007/015950 WO2008008470A2 (en) | 2006-07-13 | 2007-07-11 | Ancillary cracking of heavy oils in conjuction with fcc unit operations |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EA200900186A1 EA200900186A1 (ru) | 2009-10-30 |
| EA014574B1 true EA014574B1 (ru) | 2010-12-30 |
Family
ID=38923918
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EA200900186A EA014574B1 (ru) | 2006-07-13 | 2007-07-11 | Дополнительный крекинг тяжёлых нефтей при работе установки каталитического крекинга в псевдоожиженном слое |
Country Status (11)
| Country | Link |
|---|---|
| US (2) | US20080011644A1 (enExample) |
| EP (1) | EP2046919A4 (enExample) |
| JP (1) | JP5436209B2 (enExample) |
| KR (1) | KR101447299B1 (enExample) |
| CN (1) | CN101743292B (enExample) |
| BR (1) | BRPI0713238A2 (enExample) |
| CA (1) | CA2657615C (enExample) |
| EA (1) | EA014574B1 (enExample) |
| MX (1) | MX2009000383A (enExample) |
| NO (1) | NO20090153L (enExample) |
| WO (1) | WO2008008470A2 (enExample) |
Families Citing this family (44)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20080011644A1 (en) * | 2006-07-13 | 2008-01-17 | Dean Christopher F | Ancillary cracking of heavy oils in conjuction with FCC unit operations |
| WO2012004809A1 (en) | 2010-07-08 | 2012-01-12 | Indian Oil Corporation Ltd. | Two stage fluid catalytic cracking process and apparatus |
| SG11201502991RA (en) * | 2012-10-19 | 2015-06-29 | Saudi Arabian Oil Co | Process for high severity catalytic cracking of crude oil |
| EA201691762A1 (ru) * | 2013-11-19 | 2016-12-30 | Шеврон Ю.Эс.Эй. Инк. | Способ получения средних дистиллятов и тяжелого вакуумного газойля, служащего сырьем флюид-каталитического крекинга |
| JP2017502110A (ja) * | 2013-12-02 | 2017-01-19 | サウジ アラビアン オイル カンパニー | 軽質オレフィンの製造のための溶剤脱瀝および流動接触分解の統合された方法 |
| CN106609146B (zh) * | 2015-10-21 | 2018-06-19 | 中国石油化工股份有限公司 | 一种调节费托合成油催化裂化热平衡的方法 |
| CN106609151B (zh) * | 2015-10-21 | 2018-05-18 | 中国石油化工股份有限公司 | 一种生产低碳烯烃的方法 |
| US10844296B2 (en) | 2017-01-04 | 2020-11-24 | Saudi Arabian Oil Company | Conversion of crude oil to aromatic and olefinic petrochemicals |
| US10851316B2 (en) | 2017-01-04 | 2020-12-01 | Saudi Arabian Oil Company | Conversion of crude oil to aromatic and olefinic petrochemicals |
| US10767117B2 (en) | 2017-04-25 | 2020-09-08 | Saudi Arabian Oil Company | Enhanced light olefin yield via steam catalytic downer pyrolysis of hydrocarbon feedstock |
| US10870802B2 (en) | 2017-05-31 | 2020-12-22 | Saudi Arabian Oil Company | High-severity fluidized catalytic cracking systems and processes having partial catalyst recycle |
| US10889768B2 (en) | 2018-01-25 | 2021-01-12 | Saudi Arabian Oil Company | High severity fluidized catalytic cracking systems and processes for producing olefins from petroleum feeds |
| CN108485704B (zh) * | 2018-04-17 | 2020-04-28 | 中国石油大学(华东) | 原油毫秒分级气相催化裂解和加氢组合最大化制取化工原料工艺 |
| US11680521B2 (en) | 2019-12-03 | 2023-06-20 | Saudi Arabian Oil Company | Integrated production of hydrogen, petrochemicals, and power |
| US11193072B2 (en) | 2019-12-03 | 2021-12-07 | Saudi Arabian Oil Company | Processing facility to form hydrogen and petrochemicals |
| US11572517B2 (en) | 2019-12-03 | 2023-02-07 | Saudi Arabian Oil Company | Processing facility to produce hydrogen and petrochemicals |
| US11426708B2 (en) | 2020-03-02 | 2022-08-30 | King Abdullah University Of Science And Technology | Potassium-promoted red mud as a catalyst for forming hydrocarbons from carbon dioxide |
| US11279891B2 (en) | 2020-03-05 | 2022-03-22 | Saudi Arabian Oil Company | Systems and processes for direct crude oil upgrading to hydrogen and chemicals |
| US11492255B2 (en) | 2020-04-03 | 2022-11-08 | Saudi Arabian Oil Company | Steam methane reforming with steam regeneration |
| US11420915B2 (en) | 2020-06-11 | 2022-08-23 | Saudi Arabian Oil Company | Red mud as a catalyst for the isomerization of olefins |
| US11495814B2 (en) | 2020-06-17 | 2022-11-08 | Saudi Arabian Oil Company | Utilizing black powder for electrolytes for flow batteries |
| US12000056B2 (en) | 2020-06-18 | 2024-06-04 | Saudi Arabian Oil Company | Tandem electrolysis cell |
| US11492254B2 (en) | 2020-06-18 | 2022-11-08 | Saudi Arabian Oil Company | Hydrogen production with membrane reformer |
| US11999619B2 (en) | 2020-06-18 | 2024-06-04 | Saudi Arabian Oil Company | Hydrogen production with membrane reactor |
| US11583824B2 (en) | 2020-06-18 | 2023-02-21 | Saudi Arabian Oil Company | Hydrogen production with membrane reformer |
| US11434432B2 (en) | 2020-09-01 | 2022-09-06 | Saudi Arabian Oil Company | Processes for producing petrochemical products that utilize fluid catalytic cracking of a greater boiling point fraction with steam |
| US11352575B2 (en) | 2020-09-01 | 2022-06-07 | Saudi Arabian Oil Company | Processes for producing petrochemical products that utilize hydrotreating of cycle oil |
| US11242493B1 (en) | 2020-09-01 | 2022-02-08 | Saudi Arabian Oil Company | Methods for processing crude oils to form light olefins |
| US11230672B1 (en) | 2020-09-01 | 2022-01-25 | Saudi Arabian Oil Company | Processes for producing petrochemical products that utilize fluid catalytic cracking |
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| US11230673B1 (en) | 2020-09-01 | 2022-01-25 | Saudi Arabian Oil Company | Processes for producing petrochemical products that utilize fluid catalytic cracking of a lesser boiling point fraction with steam |
| US11820658B2 (en) | 2021-01-04 | 2023-11-21 | Saudi Arabian Oil Company | Black powder catalyst for hydrogen production via autothermal reforming |
| US11814289B2 (en) | 2021-01-04 | 2023-11-14 | Saudi Arabian Oil Company | Black powder catalyst for hydrogen production via steam reforming |
| US11427519B2 (en) | 2021-01-04 | 2022-08-30 | Saudi Arabian Oil Company | Acid modified red mud as a catalyst for olefin isomerization |
| US11724943B2 (en) | 2021-01-04 | 2023-08-15 | Saudi Arabian Oil Company | Black powder catalyst for hydrogen production via dry reforming |
| US11718522B2 (en) | 2021-01-04 | 2023-08-08 | Saudi Arabian Oil Company | Black powder catalyst for hydrogen production via bi-reforming |
| US11718575B2 (en) | 2021-08-12 | 2023-08-08 | Saudi Arabian Oil Company | Methanol production via dry reforming and methanol synthesis in a vessel |
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| US11787759B2 (en) | 2021-08-12 | 2023-10-17 | Saudi Arabian Oil Company | Dimethyl ether production via dry reforming and dimethyl ether synthesis in a vessel |
| US11578016B1 (en) | 2021-08-12 | 2023-02-14 | Saudi Arabian Oil Company | Olefin production via dry reforming and olefin synthesis in a vessel |
| US12018392B2 (en) | 2022-01-03 | 2024-06-25 | Saudi Arabian Oil Company | Methods for producing syngas from H2S and CO2 in an electrochemical cell |
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| US5730859A (en) * | 1992-08-20 | 1998-03-24 | Stone & Webster Engineering Corporation | Process for catalytically cracking paraffin rich feedstocks comprising high and low concarbon components |
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2006
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2007
- 2007-07-11 KR KR1020097002699A patent/KR101447299B1/ko not_active Expired - Fee Related
- 2007-07-11 EA EA200900186A patent/EA014574B1/ru not_active IP Right Cessation
- 2007-07-11 CA CA2657615A patent/CA2657615C/en not_active Expired - Fee Related
- 2007-07-11 WO PCT/US2007/015950 patent/WO2008008470A2/en not_active Ceased
- 2007-07-11 BR BRPI0713238-7A2A patent/BRPI0713238A2/pt not_active Application Discontinuation
- 2007-07-11 EP EP07796837A patent/EP2046919A4/en not_active Ceased
- 2007-07-11 CN CN200780026613.0A patent/CN101743292B/zh not_active Expired - Fee Related
- 2007-07-11 JP JP2009519539A patent/JP5436209B2/ja not_active Expired - Fee Related
- 2007-07-11 MX MX2009000383A patent/MX2009000383A/es active IP Right Grant
-
2009
- 2009-01-12 NO NO20090153A patent/NO20090153L/no not_active Application Discontinuation
-
2011
- 2011-05-19 US US13/111,437 patent/US8877042B2/en active Active
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| US5730859A (en) * | 1992-08-20 | 1998-03-24 | Stone & Webster Engineering Corporation | Process for catalytically cracking paraffin rich feedstocks comprising high and low concarbon components |
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Also Published As
| Publication number | Publication date |
|---|---|
| WO2008008470A2 (en) | 2008-01-17 |
| CA2657615C (en) | 2013-07-02 |
| US20080011644A1 (en) | 2008-01-17 |
| JP2009543898A (ja) | 2009-12-10 |
| WO2008008470A8 (en) | 2009-03-19 |
| CA2657615A1 (en) | 2008-01-17 |
| NO20090153L (no) | 2009-04-02 |
| US20110226668A1 (en) | 2011-09-22 |
| JP5436209B2 (ja) | 2014-03-05 |
| EP2046919A4 (en) | 2012-09-05 |
| WO2008008470A3 (en) | 2008-03-13 |
| EA200900186A1 (ru) | 2009-10-30 |
| CN101743292A (zh) | 2010-06-16 |
| US8877042B2 (en) | 2014-11-04 |
| MX2009000383A (es) | 2009-08-18 |
| BRPI0713238A2 (pt) | 2014-10-29 |
| KR101447299B1 (ko) | 2014-10-06 |
| CN101743292B (zh) | 2014-12-03 |
| EP2046919A2 (en) | 2009-04-15 |
| KR20090069266A (ko) | 2009-06-30 |
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