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
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
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 (de) |
EP (1) | EP2052058A4 (de) |
JP (1) | JP5424879B2 (de) |
KR (1) | KR101526608B1 (de) |
CN (1) | CN101501164B (de) |
BR (1) | BRPI0713183B1 (de) |
CA (1) | CA2657628C (de) |
EA (1) | EA017596B1 (de) |
MX (1) | MX345633B (de) |
NO (1) | NO20090152L (de) |
WO (1) | WO2008008527A2 (de) |
Families Citing this family (44)
Publication number | Priority date | Publication date | Assignee | Title |
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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 |
CN102365349B (zh) * | 2009-03-27 | 2015-01-07 | 千代田化工建设株式会社 | 芳香族烃的制造方法 |
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 (de) | 2010-07-08 | 2018-12-12 | Indian Oil Corporation Ltd. | Aufstromregeneration eines fcc-katalysators für mehrstufiges cracken |
US9458394B2 (en) | 2011-07-27 | 2016-10-04 | Saudi Arabian Oil Company | Fluidized catalytic cracking of paraffinic naphtha in a downflow reactor |
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 |
KR102061187B1 (ko) | 2012-03-20 | 2019-12-31 | 사우디 아라비안 오일 컴퍼니 | 원유의 처리를 위한 통합된 수소화공정 및 유체 촉매 크래킹 방법 |
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 |
WO2014062465A1 (en) | 2012-10-19 | 2014-04-24 | 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 |
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 |
CN110603311A (zh) | 2017-05-10 | 2019-12-20 | 沙特基础全球技术有限公司 | 使用径向流移动床反应器系统催化裂化石脑油的方法 |
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 |
WO2020049372A1 (en) | 2018-09-06 | 2020-03-12 | Sabic Global Technologies B.V. | Process for catalytic cracking of naphtha using multi-stage radial flow moving bed reactor system |
US11572517B2 (en) | 2019-12-03 | 2023-02-07 | Saudi Arabian Oil Company | Processing facility to produce hydrogen and petrochemicals |
US11193072B2 (en) | 2019-12-03 | 2021-12-07 | Saudi Arabian Oil Company | Processing facility to form 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 |
US11492254B2 (en) | 2020-06-18 | 2022-11-08 | Saudi Arabian Oil Company | Hydrogen production with membrane reformer |
US11583824B2 (en) | 2020-06-18 | 2023-02-21 | Saudi Arabian Oil Company | Hydrogen production with membrane reformer |
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 |
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 |
US11230672B1 (en) | 2020-09-01 | 2022-01-25 | Saudi Arabian Oil Company | Processes for producing petrochemical products that utilize fluid catalytic cracking |
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 |
US11242493B1 (en) | 2020-09-01 | 2022-02-08 | Saudi Arabian Oil Company | Methods for processing crude oils to form light olefins |
US11352575B2 (en) | 2020-09-01 | 2022-06-07 | Saudi Arabian Oil Company | Processes for producing petrochemical products that utilize hydrotreating of cycle oil |
US11505754B2 (en) | 2020-09-01 | 2022-11-22 | Saudi Arabian Oil Company | Processes for producing petrochemical products from atmospheric residues |
US11718522B2 (en) | 2021-01-04 | 2023-08-08 | Saudi Arabian Oil Company | Black powder catalyst for hydrogen production via bi-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 |
US11820658B2 (en) | 2021-01-04 | 2023-11-21 | Saudi Arabian Oil Company | Black powder catalyst for hydrogen production via autothermal reforming |
US11718575B2 (en) | 2021-08-12 | 2023-08-08 | Saudi Arabian Oil Company | Methanol production via dry reforming and methanol 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 |
US11578016B1 (en) | 2021-08-12 | 2023-02-14 | Saudi Arabian Oil Company | Olefin production via dry reforming and olefin synthesis in a vessel |
US11617981B1 (en) | 2022-01-03 | 2023-04-04 | Saudi Arabian Oil Company | Method for capturing CO2 with assisted vapor compression |
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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 |
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-
2006
- 2006-07-13 US US11/487,022 patent/US20080011645A1/en not_active Abandoned
-
2007
- 2007-07-13 CN CN2007800265994A patent/CN101501164B/zh not_active Expired - Fee Related
- 2007-07-13 BR BRPI0713183A patent/BRPI0713183B1/pt not_active IP Right Cessation
- 2007-07-13 JP JP2009519558A patent/JP5424879B2/ja not_active Expired - Fee Related
- 2007-07-13 EA EA200900185A patent/EA017596B1/ru not_active IP Right Cessation
- 2007-07-13 MX MX2009000384A patent/MX345633B/es active IP Right Grant
- 2007-07-13 CA CA2657628A patent/CA2657628C/en not_active Expired - Fee Related
- 2007-07-13 WO PCT/US2007/016054 patent/WO2008008527A2/en active Application Filing
- 2007-07-13 EP EP07796864A patent/EP2052058A4/de not_active Ceased
- 2007-07-13 KR KR1020097002916A patent/KR101526608B1/ko 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 |
---|---|
EA017596B1 (ru) | 2013-01-30 |
EA200900185A1 (ru) | 2009-06-30 |
WO2008008527A3 (en) | 2008-04-24 |
MX345633B (es) | 2017-02-08 |
US20110240520A1 (en) | 2011-10-06 |
MX2009000384A (es) | 2009-04-06 |
EP2052058A4 (de) | 2011-11-16 |
CN101501164B (zh) | 2013-08-28 |
JP2009543899A (ja) | 2009-12-10 |
KR101526608B1 (ko) | 2015-06-05 |
EP2052058A2 (de) | 2009-04-29 |
JP5424879B2 (ja) | 2014-02-26 |
CN101501164A (zh) | 2009-08-05 |
WO2008008527A2 (en) | 2008-01-17 |
US20080011645A1 (en) | 2008-01-17 |
BRPI0713183A2 (pt) | 2012-04-17 |
CA2657628C (en) | 2015-11-10 |
CA2657628A1 (en) | 2008-01-17 |
KR20090043514A (ko) | 2009-05-06 |
NO20090152L (no) | 2009-04-02 |
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