JP2002522626A5 - - Google Patents

Download PDF

Info

Publication number
JP2002522626A5
JP2002522626A5 JP2000565070A JP2000565070A JP2002522626A5 JP 2002522626 A5 JP2002522626 A5 JP 2002522626A5 JP 2000565070 A JP2000565070 A JP 2000565070A JP 2000565070 A JP2000565070 A JP 2000565070A JP 2002522626 A5 JP2002522626 A5 JP 2002522626A5
Authority
JP
Japan
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.)
Abandoned
Application number
JP2000565070A
Other languages
Japanese (ja)
Other versions
JP2002522626A (ja
Filing date
Publication date
Application filed filed Critical
Priority claimed from PCT/US1999/018568 external-priority patent/WO2000009633A1/en
Publication of JP2002522626A publication Critical patent/JP2002522626A/ja
Publication of JP2002522626A5 publication Critical patent/JP2002522626A5/ja
Abandoned legal-status Critical Current

Links

JP2000565070A 1998-08-17 1999-08-16 触媒寿命が改良され、複雑さが軽減した並列リホーマーにおける芳香族の生産方法 Abandoned JP2002522626A (ja)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US9682698P 1998-08-17 1998-08-17
US60/096,826 1998-08-17
PCT/US1999/018568 WO2000009633A1 (en) 1998-08-17 1999-08-16 Process for production of aromatics in parallel reformers

Publications (2)

Publication Number Publication Date
JP2002522626A JP2002522626A (ja) 2002-07-23
JP2002522626A5 true JP2002522626A5 (cg-RX-API-DMAC7.html) 2005-12-22

Family

ID=22259263

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000565070A Abandoned JP2002522626A (ja) 1998-08-17 1999-08-16 触媒寿命が改良され、複雑さが軽減した並列リホーマーにおける芳香族の生産方法

Country Status (10)

Country Link
US (1) US6143166A (cg-RX-API-DMAC7.html)
EP (1) EP1109880B1 (cg-RX-API-DMAC7.html)
JP (1) JP2002522626A (cg-RX-API-DMAC7.html)
AT (1) ATE255154T1 (cg-RX-API-DMAC7.html)
AU (1) AU5775799A (cg-RX-API-DMAC7.html)
CA (1) CA2339993A1 (cg-RX-API-DMAC7.html)
DE (1) DE69913164T2 (cg-RX-API-DMAC7.html)
ES (1) ES2212622T3 (cg-RX-API-DMAC7.html)
MX (1) MXPA01001723A (cg-RX-API-DMAC7.html)
WO (1) WO2000009633A1 (cg-RX-API-DMAC7.html)

Families Citing this family (49)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2289610C1 (ru) * 2005-08-05 2006-12-20 Владимир Борисович Марышев Способ переработки широкой бензиновой фракции
US8323363B2 (en) * 2007-08-30 2012-12-04 Innovative Energy Solution Reformation of hydrogen-containing fluids in a cyclic flow reactor
US20090166259A1 (en) * 2007-12-28 2009-07-02 Steven Bradley Metal-based coatings for inhibiting metal catalyzed coke formation in hydrocarbon conversion processes
US20090320370A1 (en) * 2008-06-30 2009-12-31 Fecteau David J Catalytic Reformer Recycle Gas Compressor Efficiency
US8128887B2 (en) * 2008-09-05 2012-03-06 Uop Llc Metal-based coatings for inhibiting metal catalyzed coke formation in hydrocarbon conversion processes
US8802912B2 (en) * 2009-06-23 2014-08-12 Uop Llc Effect of wet reduction on catalyst stability and methods of maintaining catalyst stability
CN102041030B (zh) * 2011-01-13 2013-07-03 中国石油天然气股份有限公司 一种控制重整高辛烷值汽油调合组分终馏点超高的方法
US8906226B2 (en) * 2011-04-29 2014-12-09 Uop Llc Process for increasing aromatics production
US8604262B2 (en) * 2011-04-29 2013-12-10 Uop Llc Process for increasing aromatics production
US8845884B2 (en) 2011-04-29 2014-09-30 Uop Llc Process for increasing aromatics production
US8716161B2 (en) 2012-03-05 2014-05-06 Chevron Phillips Chemical Company Methods of regenerating aromatization catalysts
US8912108B2 (en) 2012-03-05 2014-12-16 Chevron Phillips Chemical Company Lp Methods of regenerating aromatization catalysts
US9387467B2 (en) * 2012-09-26 2016-07-12 Chevron Phillips Chemical Company Lp Aromatization catalysts with high surface area and pore volume
RU2558955C1 (ru) 2014-08-12 2015-08-10 Общество С Ограниченной Ответственностью "Новые Газовые Технологии-Синтез" Способ получения концентрата ароматических углеводородов из жидких углеводородных фракций и установка для его осуществления
RU2544017C1 (ru) 2014-01-28 2015-03-10 Ольга Васильевна Малова Катализатор и способ ароматизации с3-с4 газов, легких углеводородных фракций алифатических спиртов, а также их смесей
RU2550354C1 (ru) 2014-03-28 2015-05-10 Общество С Ограниченной Ответственностью "Новые Газовые Технологии-Синтез" Способ получения концентрата ароматических углеводородов из легких алифатических углеводородов и установка для его осуществления
RU2544241C1 (ru) 2014-01-22 2015-03-20 Общество С Ограниченной Ответственностью "Новые Газовые Технологии-Синтез" Способ получения ароматических углеводородов из природного газа и установка для его осуществления
WO2017155424A1 (en) 2016-03-09 2017-09-14 Limited Liability Company "New Gas Technologies-Synthesis" (Llc "Ngt-Synthesis") Method and plant for producing high-octane gasolines
MY193455A (en) 2016-09-08 2022-10-14 Chevron Phillips Chemical Co Lp Acid aromatization catalyst with improved activity and stability
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
WO2019191113A1 (en) * 2018-03-27 2019-10-03 Phillips 66 Company Catalytic activation of isopentane-enriched mixtures
US10233396B1 (en) 2018-06-01 2019-03-19 Chevron Phillips Chemical Company Lp Method of producing aromatic hydrocarbons
KR102948584B1 (ko) * 2019-04-21 2026-04-06 셰브런 유.에스.에이.인크. 개선된 개질 공정
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
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
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
US12000056B2 (en) 2020-06-18 2024-06-04 Saudi Arabian Oil Company Tandem electrolysis cell
US11583824B2 (en) 2020-06-18 2023-02-21 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
RU2747869C1 (ru) 2020-06-29 2021-05-17 Общество С Ограниченной Ответственностью "Новые Газовые Технологии-Синтез" (Ооо "Нгт-Синтез") Способ получения бензинов или концентратов ароматических соединений с различным распределением потоков оксигената и олефинсодержащей фракции
US11718522B2 (en) 2021-01-04 2023-08-08 Saudi Arabian Oil Company Black powder catalyst for hydrogen production via bi-reforming
US11427519B2 (en) 2021-01-04 2022-08-30 Saudi Arabian Oil Company Acid modified red mud as a catalyst for olefin isomerization
US11820658B2 (en) 2021-01-04 2023-11-21 Saudi Arabian Oil Company Black powder catalyst for hydrogen production via autothermal reforming
US11724943B2 (en) 2021-01-04 2023-08-15 Saudi Arabian Oil Company Black powder catalyst for hydrogen production via dry reforming
US11814289B2 (en) 2021-01-04 2023-11-14 Saudi Arabian Oil Company Black powder catalyst for hydrogen production via steam reforming
US12220666B2 (en) 2021-01-12 2025-02-11 Saudi Arabian Oil Company Ultrathin membrane fabrication
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
US11718575B2 (en) 2021-08-12 2023-08-08 Saudi Arabian Oil Company Methanol production via dry reforming and methanol synthesis in a vessel
US12258272B2 (en) 2021-08-12 2025-03-25 Saudi Arabian Oil Company Dry reforming of methane using a nickel-based bi-metallic catalyst
US11617981B1 (en) 2022-01-03 2023-04-04 Saudi Arabian Oil Company Method for capturing CO2 with assisted vapor compression
US12018392B2 (en) 2022-01-03 2024-06-25 Saudi Arabian Oil Company Methods for producing syngas from H2S and CO2 in an electrochemical cell
US11802250B1 (en) 2022-11-10 2023-10-31 Chevron Phillips Chemical Company Lp Systems and processes for processing pyrolysis oil
US11932817B1 (en) 2023-02-13 2024-03-19 Chevron Phillips Chemical Company Lp AROMAX® process for improved selectivity and heavier feeds processing

Family Cites Families (34)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3172841A (en) * 1965-03-09 Process for upgrading natural sas condensates
US33323A (en) * 1861-09-17 Improvement in pumps
US2740751A (en) * 1952-02-23 1956-04-03 Universal Oil Prod Co Reforming of both straight run and cracked gasolines to provide high octane fuels
US2867576A (en) * 1955-10-14 1959-01-06 Sun Oil Co Reforming straight-run naphtha
US2944959A (en) * 1958-02-26 1960-07-12 Gulf Research Development Co Process for upgrading a wide range gasoline
US3018244A (en) * 1958-12-18 1962-01-23 Kellogg M W Co Combined isomerization and reforming process
US3003949A (en) * 1959-06-10 1961-10-10 Socony Mobil Oil Co Inc Process for manufacturing 104-106 r.o.n. leaded gasoline
US3409540A (en) * 1966-12-22 1968-11-05 Chevron Res Combination catalytic hydrocracking, pyrolytic cracking and catalytic reforming process for converting a wide boiling range crude hydrocarbon feedstock into various valuable products
US3431195A (en) * 1967-04-17 1969-03-04 Universal Oil Prod Co Purifying make hydrogen in a catalytic reforming process
US3516924A (en) * 1968-04-19 1970-06-23 Universal Oil Prod Co Catalytic reforming process
NL7016985A (cg-RX-API-DMAC7.html) * 1970-11-19 1972-05-24
US3753891A (en) * 1971-01-15 1973-08-21 R Graven Split-stream reforming to upgrade low-octane hydrocarbons
US3776949A (en) * 1971-09-07 1973-12-04 Lummus Co Production of aromatic polycarboxylic acids
US3864240A (en) * 1973-03-09 1975-02-04 Universal Oil Prod Co Integration of a reaction system having gravity-flowing catalyst particles with a fixed-bed system
FR2323664A1 (fr) * 1975-09-10 1977-04-08 Erap Procede de deshydrocyclisation d'hydrocarbures aliphatiques
US4213849A (en) * 1976-04-05 1980-07-22 Compagnie Francaise De Raffinage Method of using catalysts for reforming or isomerizing hydrocarbons
US4212726A (en) * 1977-11-23 1980-07-15 Cosden Technology, Inc. Method for increasing the purity of hydrogen recycle gas
US4157355A (en) * 1978-03-13 1979-06-05 Uop Inc. Combination process for selected aromatic hydrocarbon production
US4347394A (en) * 1980-12-10 1982-08-31 Chevron Research Company Benzene synthesis
US4645586A (en) * 1983-06-03 1987-02-24 Chevron Research Company Reforming process
US4483766A (en) * 1983-06-20 1984-11-20 Uop Inc. Process for catalytic reforming
US4568451A (en) * 1983-08-11 1986-02-04 Uop Inc. Process for producing a hydrogen-rich gas stream from the effluent of a catalytic hydrocarbon conversion reaction zone
USRE33323E (en) * 1984-12-07 1990-09-04 Exxon Research & Engineering Company Reforming process for enhanced benzene yield
US4613424A (en) * 1984-12-26 1986-09-23 Exxon Research And Engineering Co. Catalytic reforming process
US4897177A (en) * 1988-03-23 1990-01-30 Exxon Chemical Patents Inc. Process for reforming a hydrocarbon fraction with a limited C9 + content
US5157180A (en) * 1989-05-26 1992-10-20 Union Oil Company Of California Alkylation and transalkylation processes
US5178751A (en) * 1991-11-27 1993-01-12 Uop Two-stage process for purifying a hydrogen gas and recovering liquifiable hydrocarbons from hydrocarbonaceous effluent streams
US5278344A (en) * 1992-12-14 1994-01-11 Uop Integrated catalytic reforming and hydrodealkylation process for maximum recovery of benzene
US5332492A (en) * 1993-06-10 1994-07-26 Uop PSA process for improving the purity of hydrogen gas and recovery of liquefiable hydrocarbons from hydrocarbonaceous effluent streams
US5391292A (en) * 1993-12-17 1995-02-21 Exxon Research And Engineering Company Cyclic reforming catalyst regeneration
US5935415A (en) * 1994-12-22 1999-08-10 Uop Llc Continuous catalytic reforming process with dual zones
US5602290A (en) * 1995-05-30 1997-02-11 Raytheon Engineers & Constructors, Inc. Pretreatment of dilute ethylene feedstocks for ethylbenzene production
US5958217A (en) * 1995-11-15 1999-09-28 Chevron Chemical Company Llc Two-stage reforming process that enhances para-xylene yield and minimizes ethylbenzene production
WO1998058041A1 (en) * 1997-06-16 1998-12-23 Chevron Chemical Company Llc Split-feed two-stage parallel aromatization for maximum para-xylene yield

Similar Documents

Publication Publication Date Title
BE2013C051I2 (cg-RX-API-DMAC7.html)
BE2013C001I2 (cg-RX-API-DMAC7.html)
BE2012C036I2 (cg-RX-API-DMAC7.html)
JP2002516697A5 (cg-RX-API-DMAC7.html)
BE1025464I2 (cg-RX-API-DMAC7.html)
JP2002510814A5 (cg-RX-API-DMAC7.html)
BE2008C046I2 (cg-RX-API-DMAC7.html)
BE2010C011I2 (cg-RX-API-DMAC7.html)
JP2002527206A5 (cg-RX-API-DMAC7.html)
BE2008C047I2 (cg-RX-API-DMAC7.html)
BE2011C004I2 (cg-RX-API-DMAC7.html)
JP2002510901A5 (cg-RX-API-DMAC7.html)
JP2002522626A5 (cg-RX-API-DMAC7.html)
JP2002501256A5 (cg-RX-API-DMAC7.html)
JP2002510188A5 (cg-RX-API-DMAC7.html)
JP2002507470A5 (cg-RX-API-DMAC7.html)
JP2001118244A5 (cg-RX-API-DMAC7.html)
JP2002531793A5 (cg-RX-API-DMAC7.html)
JP2002519727A5 (cg-RX-API-DMAC7.html)
JP2000301517A5 (cg-RX-API-DMAC7.html)
IN192082B (cg-RX-API-DMAC7.html)
IN190581B (cg-RX-API-DMAC7.html)
IN185970B (cg-RX-API-DMAC7.html)
IN185212B (cg-RX-API-DMAC7.html)
FR2775681A3 (cg-RX-API-DMAC7.html)