MX2019010082A - Metodos para formar olefinas ligeras mediante craqueo. - Google Patents
Metodos para formar olefinas ligeras mediante craqueo.Info
- Publication number
- MX2019010082A MX2019010082A MX2019010082A MX2019010082A MX2019010082A MX 2019010082 A MX2019010082 A MX 2019010082A MX 2019010082 A MX2019010082 A MX 2019010082A MX 2019010082 A MX2019010082 A MX 2019010082A MX 2019010082 A MX2019010082 A MX 2019010082A
- Authority
- MX
- Mexico
- Prior art keywords
- reactor
- reactor section
- light olefins
- cracking
- methods
- 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
- C10G11/182—Regeneration
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C11/00—Aliphatic unsaturated hydrocarbons
- C07C11/02—Alkenes
- C07C11/04—Ethylene
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C11/00—Aliphatic unsaturated hydrocarbons
- C07C11/02—Alkenes
- C07C11/06—Propene
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C11/00—Aliphatic unsaturated hydrocarbons
- C07C11/02—Alkenes
- C07C11/08—Alkenes with four carbon atoms
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C4/00—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
- C07C4/02—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by cracking a single hydrocarbon or a mixture of individually defined hydrocarbons or a normally gaseous hydrocarbon fraction
- C07C4/06—Catalytic processes
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/32—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with formation of free hydrogen
- C07C5/327—Formation of non-aromatic carbon-to-carbon double bonds only
- C07C5/333—Catalytic processes
- C07C5/3335—Catalytic processes with metals
- C07C5/3337—Catalytic processes with metals of the platinum group
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals
- C07C2523/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals of the platinum group metals
- C07C2523/42—Platinum
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2529/00—Catalysts comprising molecular sieves
- C07C2529/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites, pillared clays
- C07C2529/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- C07C2529/064—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof containing iron group metals, noble metals or copper
- C07C2529/068—Noble metals
-
- 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
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/20—C2-C4 olefins
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
- Y02P30/20—Technologies relating to oil refining and petrochemical industry using bio-feedstock
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
- Y02P30/40—Ethylene production
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
De acuerdo con una o más modalidades descritas en la presente, las olefinas ligeras pueden formarse mediante un método que puede comprender introducir una corriente de alimentación en un reactor, hacer reaccionar la corriente de alimentación con un catalizador de craqueo en el reactor para formar una corriente de producto, y procesar el catalizador de craqueo. El reactor puede comprender una sección de reactor corriente arriba y una sección de reactor corriente abajo. La sección de reactor corriente arriba se puede situar debajo de la sección de reactor corriente abajo. La sección de reactor corriente arriba puede tener un área de sección transversal promedio que es al menos el 150% del área de sección transversal promedio de la sección de reactor corriente abajo.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US201762470570P | 2017-03-13 | 2017-03-13 | |
PCT/US2018/021656 WO2018169768A1 (en) | 2017-03-13 | 2018-03-09 | Methods for forming light olefins by cracking |
Publications (1)
Publication Number | Publication Date |
---|---|
MX2019010082A true MX2019010082A (es) | 2019-11-21 |
Family
ID=61692170
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
MX2019010082A MX2019010082A (es) | 2017-03-13 | 2018-03-09 | Metodos para formar olefinas ligeras mediante craqueo. |
Country Status (10)
Country | Link |
---|---|
US (1) | US11459282B2 (es) |
EP (1) | EP3596188A1 (es) |
KR (1) | KR102531502B1 (es) |
CN (1) | CN110337485A (es) |
AR (1) | AR111237A1 (es) |
BR (1) | BR112019016941A2 (es) |
CA (1) | CA3070761A1 (es) |
MX (1) | MX2019010082A (es) |
RU (1) | RU2019130732A (es) |
WO (1) | WO2018169768A1 (es) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US12012555B2 (en) | 2019-08-05 | 2024-06-18 | Sabic Global Technologies B.V. | Turbulent/fast fluidized bed reactor with baffles to maximize light olefin yields |
EP3990583A1 (en) * | 2019-08-05 | 2022-05-04 | SABIC Global Technologies, B.V. | Single and multiple turbulent/fast fluidized bed reactors in ncc process for maximizing aromatics production |
US20220033714A1 (en) * | 2020-07-28 | 2022-02-03 | Saudi Arabian Oil Company | Methods and apparatuses for processing hydrocarbons to produce light olefins |
JP2023544693A (ja) * | 2020-09-30 | 2023-10-25 | ダウ グローバル テクノロジーズ エルエルシー | 流動床システムにおける化学原料分配器のための分配器支持システム |
JP2024536259A (ja) * | 2021-10-04 | 2024-10-04 | ダウ グローバル テクノロジーズ エルエルシー | 化学物質を処理する方法 |
WO2024118461A1 (en) * | 2022-11-29 | 2024-06-06 | Dow Global Technologies Llc | Particulate solid distributors suitable for distributing multiple particulate solid streams |
US11873452B1 (en) | 2022-12-12 | 2024-01-16 | Saudi Arabian Oil Company | Methods for processing hydrocarbons to produce light olefins using catalyst formulations or mixtures |
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US4051013A (en) * | 1973-05-21 | 1977-09-27 | Uop Inc. | Fluid catalytic cracking process for upgrading a gasoline-range feed |
US4458096A (en) | 1983-05-26 | 1984-07-03 | Air Products And Chemicals, Inc. | Process for the production of ethylene and propylene |
US4579716A (en) | 1983-09-06 | 1986-04-01 | Mobil Oil Corporation | Closed reactor FCC system with provisions for surge capacity |
US4719189A (en) * | 1984-04-26 | 1988-01-12 | Mobil Oil Corporation | Reactivation of noble metal-containing zeolite catalyst materials |
US4595567A (en) * | 1984-12-28 | 1986-06-17 | Uop Inc. | Cooling fluidized catalytic cracking regeneration zones with heat pipe apparatus |
US4686028A (en) * | 1985-04-05 | 1987-08-11 | Driesen Roger P Van | Upgrading of high boiling hydrocarbons |
US4840928A (en) * | 1988-01-19 | 1989-06-20 | Mobil Oil Corporation | Conversion of alkanes to alkylenes in an external catalyst cooler for the regenerator of a FCC unit |
US4912273A (en) * | 1988-01-19 | 1990-03-27 | Mobil Oil Corp. | Production of aromatic hydrocarbons from alkanes |
US5000838A (en) * | 1989-12-13 | 1991-03-19 | Mobil Oil Corporation | Low efficiency deasphalting and catalytic cracking |
US5456821A (en) * | 1991-03-12 | 1995-10-10 | Mobil Oil Corp. | Catalytic conversion with improved catalyst |
US5190650A (en) | 1991-06-24 | 1993-03-02 | Exxon Research And Engineering Company | Tangential solids separation transfer tunnel |
US7169293B2 (en) | 1999-08-20 | 2007-01-30 | Uop Llc | Controllable space velocity reactor and process |
US20020024276A1 (en) | 2000-03-23 | 2002-02-28 | Egbert Neuhaus | Drawer which is incorporated in a cupboard, in particular kitchen cupboard drawer |
US6392113B1 (en) * | 2000-10-03 | 2002-05-21 | Abb Lummus Global Inc. | Catalytic hydrocarbon dehydrogenation system with prereaction |
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US6867341B1 (en) | 2002-09-17 | 2005-03-15 | Uop Llc | Catalytic naphtha cracking catalyst and process |
US7128827B2 (en) | 2004-01-14 | 2006-10-31 | Kellogg Brown & Root Llc | Integrated catalytic cracking and steam pyrolysis process for olefins |
RU2508282C2 (ru) | 2004-02-09 | 2014-02-27 | Дзе Дау Кемикал Компани | Способ получения дегидрированных углеводородных соединений |
KR100651418B1 (ko) | 2006-03-17 | 2006-11-30 | 에스케이 주식회사 | 고속유동층을 이용하여 탄화수소 원료로부터 경질 올레핀을제조하는 접촉분해 공정 |
US7758817B2 (en) * | 2006-08-09 | 2010-07-20 | Uop Llc | Device for contacting high contaminated feedstocks with catalyst in an FCC unit |
US7491315B2 (en) | 2006-08-11 | 2009-02-17 | Kellogg Brown & Root Llc | Dual riser FCC reactor process with light and mixed light/heavy feeds |
CN101239868B (zh) | 2007-02-07 | 2011-05-18 | 中国石油化工股份有限公司 | 提高乙烯、丙烯收率的方法 |
CN101348409B (zh) | 2007-07-19 | 2011-06-15 | 中国石油化工股份有限公司 | 一种生产低碳烯烃的方法 |
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-
2018
- 2018-03-07 AR ARP180100534A patent/AR111237A1/es active IP Right Grant
- 2018-03-09 MX MX2019010082A patent/MX2019010082A/es unknown
- 2018-03-09 WO PCT/US2018/021656 patent/WO2018169768A1/en unknown
- 2018-03-09 CA CA3070761A patent/CA3070761A1/en active Pending
- 2018-03-09 EP EP18712415.1A patent/EP3596188A1/en active Pending
- 2018-03-09 US US16/491,331 patent/US11459282B2/en active Active
- 2018-03-09 KR KR1020197028857A patent/KR102531502B1/ko active IP Right Grant
- 2018-03-09 RU RU2019130732A patent/RU2019130732A/ru unknown
- 2018-03-09 CN CN201880012093.6A patent/CN110337485A/zh active Pending
- 2018-03-09 BR BR112019016941A patent/BR112019016941A2/pt not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
US20200017426A1 (en) | 2020-01-16 |
KR20190120352A (ko) | 2019-10-23 |
CN110337485A (zh) | 2019-10-15 |
KR102531502B1 (ko) | 2023-05-12 |
RU2019130732A3 (es) | 2021-06-22 |
EP3596188A1 (en) | 2020-01-22 |
US11459282B2 (en) | 2022-10-04 |
CA3070761A1 (en) | 2018-09-20 |
BR112019016941A2 (pt) | 2020-04-07 |
RU2019130732A (ru) | 2021-03-30 |
AR111237A1 (es) | 2019-06-19 |
WO2018169768A1 (en) | 2018-09-20 |
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