BRPI0713183B1 - método para intensificar a conversão de uma corrente de alimentação consistindo essencialmente de nafta parafínica e método para produzir uma corrente de produto consistindo de olefinas leves - Google Patents
método para intensificar a conversão de uma corrente de alimentação consistindo essencialmente de nafta parafínica e método para produzir uma corrente de produto consistindo de olefinas leves Download PDFInfo
- Publication number
- BRPI0713183B1 BRPI0713183B1 BRPI0713183A BRPI0713183A BRPI0713183B1 BR PI0713183 B1 BRPI0713183 B1 BR PI0713183B1 BR PI0713183 A BRPI0713183 A BR PI0713183A BR PI0713183 A BRPI0713183 A BR PI0713183A BR PI0713183 B1 BRPI0713183 B1 BR PI0713183B1
- Authority
- BR
- Brazil
- Prior art keywords
- catalyst
- reactor
- naphtha
- stream
- product stream
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 87
- 238000006243 chemical reaction Methods 0.000 title claims abstract description 40
- 239000012188 paraffin wax Substances 0.000 title claims abstract description 26
- 150000001336 alkenes Chemical class 0.000 title claims abstract description 19
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 8
- 230000002708 enhancing effect Effects 0.000 title claims abstract description 4
- 239000003054 catalyst Substances 0.000 claims abstract description 129
- 229930195733 hydrocarbon Natural products 0.000 claims abstract description 35
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract description 35
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract description 22
- 239000007795 chemical reaction product Substances 0.000 claims abstract description 22
- 239000000047 product Substances 0.000 claims abstract description 21
- 239000003502 gasoline Substances 0.000 claims abstract description 20
- 239000000203 mixture Substances 0.000 claims abstract description 13
- -1 ethylene, propylene, butylenes Chemical class 0.000 claims abstract description 12
- 230000008929 regeneration Effects 0.000 claims abstract description 10
- 238000011069 regeneration method Methods 0.000 claims abstract description 10
- 238000005336 cracking Methods 0.000 claims description 38
- 238000002156 mixing Methods 0.000 claims description 17
- 239000003921 oil Substances 0.000 claims description 8
- 238000004821 distillation Methods 0.000 claims description 7
- 238000005194 fractionation Methods 0.000 claims description 5
- 238000012545 processing Methods 0.000 claims description 5
- 238000000926 separation method Methods 0.000 claims description 5
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 claims description 5
- 238000004523 catalytic cracking Methods 0.000 claims description 4
- 238000009835 boiling Methods 0.000 claims description 3
- 238000004231 fluid catalytic cracking Methods 0.000 claims description 3
- 239000000295 fuel oil Substances 0.000 claims description 3
- 230000001172 regenerating effect Effects 0.000 claims description 3
- 239000000284 extract Substances 0.000 claims description 2
- 239000003208 petroleum Substances 0.000 claims description 2
- 230000000087 stabilizing effect Effects 0.000 claims 2
- 239000007809 chemical reaction catalyst Substances 0.000 claims 1
- 239000012809 cooling fluid Substances 0.000 claims 1
- 239000000571 coke Substances 0.000 abstract description 10
- 238000011084 recovery Methods 0.000 abstract description 6
- 239000006227 byproduct Substances 0.000 abstract description 5
- 230000015572 biosynthetic process Effects 0.000 abstract 1
- 238000000605 extraction Methods 0.000 description 16
- 239000007789 gas Substances 0.000 description 12
- 239000010457 zeolite Substances 0.000 description 11
- 239000000654 additive Substances 0.000 description 9
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 9
- 238000012546 transfer Methods 0.000 description 9
- 229910021536 Zeolite Inorganic materials 0.000 description 7
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 7
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 7
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 5
- 239000005977 Ethylene Substances 0.000 description 5
- 238000002485 combustion reaction Methods 0.000 description 5
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 230000000996 additive effect Effects 0.000 description 3
- 230000001419 dependent effect Effects 0.000 description 3
- 238000002347 injection Methods 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 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
- 238000004064 recycling Methods 0.000 description 3
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 230000002411 adverse Effects 0.000 description 2
- 125000003118 aryl group Chemical group 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000011068 loading method Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000011027 product recovery Methods 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 241000276420 Lophius piscatorius Species 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 238000011021 bench scale process Methods 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 238000011143 downstream manufacturing Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010304 firing Methods 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
- 238000011017 operating method Methods 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000010791 quenching Methods 0.000 description 1
- 229910052761 rare earth metal Inorganic materials 0.000 description 1
- 150000002910 rare earth metals Chemical class 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000012552 review Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 238000004230 steam cracking Methods 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
- 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
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J38/00—Regeneration or reactivation of catalysts, in general
-
- 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
- C10G11/182—Regeneration
-
- 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
- C10G55/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process
- C10G55/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process plural serial 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1037—Hydrocarbon fractions
- C10G2300/1044—Heavy gasoline or naphtha having a boiling range of about 100 - 180 °C
-
- 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)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US11/487,022 US20080011645A1 (en) | 2006-07-13 | 2006-07-13 | Ancillary cracking of paraffinic naphtha in conjuction with FCC unit operations |
| US11/487,022 | 2006-07-13 | ||
| PCT/US2007/016054 WO2008008527A2 (en) | 2006-07-13 | 2007-07-13 | Ancillary cracking of paraffinic naptha in conjunction with fcc unit operations |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| BRPI0713183A2 BRPI0713183A2 (pt) | 2012-04-17 |
| BRPI0713183B1 true BRPI0713183B1 (pt) | 2017-03-07 |
Family
ID=38923953
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| BRPI0713183A BRPI0713183B1 (pt) | 2006-07-13 | 2007-07-13 | método para intensificar a conversão de uma corrente de alimentação consistindo essencialmente de nafta parafínica e método para produzir uma corrente de produto consistindo de olefinas leves |
Country Status (11)
| Country | Link |
|---|---|
| US (2) | US20080011645A1 (no) |
| EP (1) | EP2052058A4 (no) |
| JP (1) | JP5424879B2 (no) |
| KR (1) | KR101526608B1 (no) |
| CN (1) | CN101501164B (no) |
| BR (1) | BRPI0713183B1 (no) |
| CA (1) | CA2657628C (no) |
| EA (1) | EA017596B1 (no) |
| MX (1) | MX345633B (no) |
| NO (1) | NO20090152L (no) |
| WO (1) | WO2008008527A2 (no) |
Families Citing this family (48)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8137631B2 (en) * | 2008-12-11 | 2012-03-20 | Uop Llc | Unit, system and process for catalytic cracking |
| US8889076B2 (en) | 2008-12-29 | 2014-11-18 | Uop Llc | Fluid catalytic cracking system and process |
| MY160726A (en) * | 2009-03-27 | 2017-03-15 | Chiyoda Corp | Method for producing aromatic hydrocarbons |
| JP4837114B2 (ja) * | 2010-03-26 | 2011-12-14 | 千代田化工建設株式会社 | 芳香族炭化水素の製造方法および芳香族炭化水素の製造プラント |
| EP2591071B1 (en) | 2010-07-08 | 2018-12-12 | Indian Oil Corporation Ltd. | Upflow regeneration of fcc catalyst for multi stage cracking |
| KR101954472B1 (ko) * | 2011-07-27 | 2019-03-05 | 사우디 아라비안 오일 컴퍼니 | 하향류 반응기에서 파라핀계 나프타의 유동접촉분해 방법 |
| JP6117203B2 (ja) | 2011-07-29 | 2017-04-19 | サウジ アラビアン オイル カンパニー | 中間留分の選択的水素化処理方法 |
| CN104245892B (zh) * | 2012-03-20 | 2016-10-12 | 沙特阿拉伯石油公司 | 用于处理原油的集成加氢处理和流体催化裂化 |
| US9452404B2 (en) * | 2012-07-12 | 2016-09-27 | Lummus Technology Inc. | Fluid cracking process and apparatus for maximizing light olefins or middle distillates and light olefins |
| EP2909289B1 (en) * | 2012-10-19 | 2018-05-16 | Saudi Arabian Oil Company | Process for high severity catalytic cracking of crude oil |
| JP6560087B2 (ja) * | 2015-09-30 | 2019-08-14 | ルネサスエレクトロニクス株式会社 | 半導体装置および半導体装置の製造方法 |
| US10851316B2 (en) | 2017-01-04 | 2020-12-01 | Saudi Arabian Oil Company | Conversion of crude oil to aromatic and olefinic petrochemicals |
| US10844296B2 (en) | 2017-01-04 | 2020-11-24 | Saudi Arabian Oil Company | Conversion of crude oil to aromatic and olefinic petrochemicals |
| WO2018207033A1 (en) | 2017-05-10 | 2018-11-15 | Sabic Global Technologies B.V. | Process for catalytic cracking of naphtha using radial flow moving bed reactor system |
| US10870802B2 (en) | 2017-05-31 | 2020-12-22 | Saudi Arabian Oil Company | High-severity fluidized catalytic cracking systems and processes having partial catalyst recycle |
| US10781377B2 (en) * | 2017-11-30 | 2020-09-22 | Uop Llc | Process and apparatus for cracking hydrocarbons to lighter hydrocarbons |
| 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 |
| US11905467B2 (en) | 2018-09-06 | 2024-02-20 | Sabic Global Technologies B.V. | Process for catalytic cracking of naphtha using multi-stage radial flow moving bed reactor system |
| 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 |
| US11680521B2 (en) | 2019-12-03 | 2023-06-20 | Saudi Arabian Oil Company | Integrated production of hydrogen, petrochemicals, and power |
| 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 |
| US11583824B2 (en) | 2020-06-18 | 2023-02-21 | Saudi Arabian Oil Company | Hydrogen production with membrane reformer |
| 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 |
| US11505754B2 (en) | 2020-09-01 | 2022-11-22 | Saudi Arabian Oil Company | Processes for producing petrochemical products from atmospheric residues |
| US11332680B2 (en) | 2020-09-01 | 2022-05-17 | Saudi Arabian Oil Company | Processes for producing petrochemical products that utilize fluid catalytic cracking of lesser and greater boiling point fractions with steam |
| US11230672B1 (en) | 2020-09-01 | 2022-01-25 | Saudi Arabian Oil Company | Processes for producing petrochemical products that utilize fluid catalytic cracking |
| US11242493B1 (en) | 2020-09-01 | 2022-02-08 | Saudi Arabian Oil Company | Methods for processing crude oils to form light olefins |
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| 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 |
| 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 |
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| US11718575B2 (en) | 2021-08-12 | 2023-08-08 | Saudi Arabian Oil Company | Methanol production via dry reforming and methanol 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 |
| 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 |
| 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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Family Cites Families (45)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3424672A (en) | 1967-01-09 | 1969-01-28 | Phillips Petroleum Co | Fluid catalytic stripping |
| US3542667A (en) * | 1968-03-21 | 1970-11-24 | Foster Wheeler Corp | Process for the production of aromatic and olefinic hydrocarbons |
| US3784463A (en) * | 1970-10-02 | 1974-01-08 | Texaco Inc | Catalytic cracking of naphtha and gas oil |
| US3776838A (en) * | 1970-10-02 | 1973-12-04 | Texaco Inc | Catalytic cracking of naphthas |
| US3856659A (en) * | 1972-12-19 | 1974-12-24 | Mobil Oil Corp | Multiple reactor fcc system relying upon a dual cracking catalyst composition |
| US4051013A (en) * | 1973-05-21 | 1977-09-27 | Uop Inc. | Fluid catalytic cracking process for upgrading a gasoline-range feed |
| US3928172A (en) * | 1973-07-02 | 1975-12-23 | Mobil Oil Corp | Catalytic cracking of FCC gasoline and virgin naphtha |
| US4090949A (en) * | 1974-07-31 | 1978-05-23 | Mobil Oil Corportion | Upgrading of olefinic gasoline with hydrogen contributors |
| US4097363A (en) * | 1976-07-12 | 1978-06-27 | Gulf Research & Development Company | Thermal cracking of light gas oil at high severity to ethylene |
| US4116814A (en) * | 1977-07-18 | 1978-09-26 | Mobil Oil Corporation | Method and system for effecting catalytic cracking of high boiling hydrocarbons with fluid conversion catalysts |
| US4297203A (en) * | 1980-04-14 | 1981-10-27 | Standard Oil Company (Indiana) | Apparatus for the catalytic cracking of hydrocarbons |
| US4310489A (en) * | 1980-08-14 | 1982-01-12 | Standard Oil Company (Indiana) | Apparatus for the catalytic cracking of hydrocarbons |
| US4385985A (en) * | 1981-04-14 | 1983-05-31 | Mobil Oil Corporation | FCC Reactor with a downflow reactor riser |
| US4693808A (en) * | 1986-06-16 | 1987-09-15 | Shell Oil Company | Downflow fluidized catalytic cranking reactor process and apparatus with quick catalyst separation means in the bottom thereof |
| US4830728A (en) * | 1986-09-03 | 1989-05-16 | Mobil Oil Corporation | Upgrading naphtha in a multiple riser fluid catalytic cracking operation employing a catalyst mixture |
| US4814067A (en) * | 1987-08-11 | 1989-03-21 | Stone & Webster Engineering Corporation | Particulate solids cracking apparatus and process |
| US5049360A (en) * | 1988-01-19 | 1991-09-17 | Mobil Oil Corporation | Multi-stage conversion of alkanes to gasoline |
| US5053204A (en) * | 1988-12-30 | 1991-10-01 | Mobil Oil Corporation | Multiple feed point catalytic cracking apparatus using elutriable catalyst mixture |
| US5372704A (en) * | 1990-05-24 | 1994-12-13 | Mobil Oil Corporation | Cracking with spent catalyst |
| FR2667609B1 (fr) * | 1990-10-03 | 1993-07-16 | Inst Francais Du Petrole | Procede et dispositif de craquage catalytique en lit fluide a courant descendant. |
| US5314610A (en) * | 1992-05-29 | 1994-05-24 | Abb Lummus Crest Inc. | Staged catalytic cracking process |
| CN1089641A (zh) * | 1992-08-20 | 1994-07-20 | 史东及韦伯斯特工程公司 | 含高和低康拉逊残炭组分的富石蜡原料的催化裂化方法 |
| US5435906A (en) * | 1992-08-20 | 1995-07-25 | Stone & Webster Engineering Corporation | Process for catalytically cracking feedstocks paraffin rich comprising high and low concarbon components |
| US5584986A (en) * | 1993-03-19 | 1996-12-17 | Bar-Co Processes Joint Venture | Fluidized process for improved stripping and/or cooling of particulate spent solids, and reduction of sulfur oxide emissions |
| US5582712A (en) * | 1994-04-29 | 1996-12-10 | Uop | Downflow FCC reaction arrangement with upflow regeneration |
| JP3580518B2 (ja) * | 1996-06-05 | 2004-10-27 | 新日本石油株式会社 | 重質油の流動接触分解法 |
| FR2753454B1 (fr) * | 1996-09-18 | 1999-06-04 | Inst Francais Du Petrole | Procede et dispositif de craquage catalytique descendant mettant en oeuvre l'injection d'une charge sous un angle adequat sur un catalyseur conditionne |
| US5904837A (en) * | 1996-10-07 | 1999-05-18 | Nippon Oil Co., Ltd. | Process for fluid catalytic cracking of oils |
| US6045690A (en) * | 1996-11-15 | 2000-04-04 | Nippon Oil Co., Ltd. | Process for fluid catalytic cracking of heavy fraction oils |
| US5846403A (en) * | 1996-12-17 | 1998-12-08 | Exxon Research And Engineering Company | Recracking of cat naphtha for maximizing light olefins yields |
| US6187272B1 (en) * | 1997-03-13 | 2001-02-13 | Nippon Mitsubishi Oil Corporation | Recycling fluidization system |
| JP3933745B2 (ja) * | 1997-03-14 | 2007-06-20 | 新日本石油株式会社 | 気固分離器 |
| US5965012A (en) * | 1997-12-05 | 1999-10-12 | Uop Llc | FCC process with short primary contacting and controlled secondary contacting |
| US6113776A (en) * | 1998-06-08 | 2000-09-05 | Uop Llc | FCC process with high temperature cracking zone |
| FR2785907B1 (fr) * | 1998-11-13 | 2001-01-05 | Inst Francais Du Petrole | Procede et dispositif de craquage catalytique comprenant des reacteurs a ecoulements descendant et ascendant |
| FR2802211B1 (fr) * | 1999-12-14 | 2002-02-01 | Inst Francais Du Petrole | Procede et dispositif de craquage catalytique comprenant en parallele au moins un reacteur a ecoulement ascendant et au moins un reacteur a ecoulement descendant |
| US20010042702A1 (en) * | 2000-04-17 | 2001-11-22 | Stuntz Gordon F. | Cycle oil conversion process |
| FR2811327B1 (fr) * | 2000-07-05 | 2002-10-25 | Total Raffinage Distribution | Procede et dispositif de craquage d'hydrocarbures mettant en oeuvre deux chambres reactionnelles successives |
| US6656346B2 (en) * | 2001-06-07 | 2003-12-02 | King Fahd University Of Petroleum And Minerals | Fluid catalytic cracking process for heavy oil |
| US6866771B2 (en) * | 2002-04-18 | 2005-03-15 | Uop Llc | Process and apparatus for upgrading FCC product with additional reactor with catalyst recycle |
| AU2003236150A1 (en) * | 2002-04-26 | 2003-11-10 | China Petroleum And Chemical Corporation | Downflow catalytic cracking reactor and use thereof |
| US20040110629A1 (en) * | 2002-08-29 | 2004-06-10 | Dennis Stamires | Catalyst for the production of light olefins |
| US7087154B2 (en) * | 2002-12-30 | 2006-08-08 | Petroleo Brasileiro S.A. - Petrobras | Apparatus and process for downflow fluid catalytic cracking |
| US7144498B2 (en) * | 2004-01-30 | 2006-12-05 | Kellogg Brown & Root Llc | Supercritical hydrocarbon conversion process |
| BRPI0514218A (pt) * | 2004-08-10 | 2008-06-03 | Shell Internationale Rsearch M | processo e aparelho para fabricar destilado médio e olefinas inferiores |
-
2006
- 2006-07-13 US US11/487,022 patent/US20080011645A1/en not_active Abandoned
-
2007
- 2007-07-13 EP EP07796864A patent/EP2052058A4/en not_active Ceased
- 2007-07-13 CN CN2007800265994A patent/CN101501164B/zh not_active Expired - Fee Related
- 2007-07-13 MX MX2009000384A patent/MX345633B/es active IP Right Grant
- 2007-07-13 JP JP2009519558A patent/JP5424879B2/ja not_active Expired - Fee Related
- 2007-07-13 BR BRPI0713183A patent/BRPI0713183B1/pt not_active IP Right Cessation
- 2007-07-13 KR KR1020097002916A patent/KR101526608B1/ko not_active Expired - Fee Related
- 2007-07-13 CA CA2657628A patent/CA2657628C/en not_active Expired - Fee Related
- 2007-07-13 WO PCT/US2007/016054 patent/WO2008008527A2/en not_active Ceased
- 2007-07-13 EA EA200900185A patent/EA017596B1/ru not_active IP Right Cessation
-
2009
- 2009-01-12 NO NO20090152A patent/NO20090152L/no not_active Application Discontinuation
-
2011
- 2011-06-09 US US13/156,440 patent/US20110240520A1/en not_active Abandoned
Also Published As
| Publication number | Publication date |
|---|---|
| EP2052058A2 (en) | 2009-04-29 |
| MX345633B (es) | 2017-02-08 |
| BRPI0713183A2 (pt) | 2012-04-17 |
| KR20090043514A (ko) | 2009-05-06 |
| US20110240520A1 (en) | 2011-10-06 |
| CA2657628C (en) | 2015-11-10 |
| EP2052058A4 (en) | 2011-11-16 |
| CA2657628A1 (en) | 2008-01-17 |
| EA200900185A1 (ru) | 2009-06-30 |
| US20080011645A1 (en) | 2008-01-17 |
| JP5424879B2 (ja) | 2014-02-26 |
| EA017596B1 (ru) | 2013-01-30 |
| MX2009000384A (es) | 2009-04-06 |
| JP2009543899A (ja) | 2009-12-10 |
| WO2008008527A3 (en) | 2008-04-24 |
| NO20090152L (no) | 2009-04-02 |
| WO2008008527A2 (en) | 2008-01-17 |
| CN101501164B (zh) | 2013-08-28 |
| KR101526608B1 (ko) | 2015-06-05 |
| CN101501164A (zh) | 2009-08-05 |
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