DE69913164T2 - Verfahren zur herstellung von aromatischen kohlenwasserstoffen in parallelreformern - Google Patents

Verfahren zur herstellung von aromatischen kohlenwasserstoffen in parallelreformern Download PDF

Info

Publication number
DE69913164T2
DE69913164T2 DE69913164T DE69913164T DE69913164T2 DE 69913164 T2 DE69913164 T2 DE 69913164T2 DE 69913164 T DE69913164 T DE 69913164T DE 69913164 T DE69913164 T DE 69913164T DE 69913164 T2 DE69913164 T2 DE 69913164T2
Authority
DE
Germany
Prior art keywords
hydrogen
catalyst
reforming
fraction
acidic
Prior art date
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.)
Expired - Fee Related
Application number
DE69913164T
Other languages
German (de)
English (en)
Other versions
DE69913164D1 (de
Inventor
J. Gerald NACAMULI
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Chevron Phillips Chemical Co LLC
Chevron Phillips Chemical Co LP
Original Assignee
Chevron Phillips Chemical Co LLC
Chevron Phillips Chemical Co LP
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Chevron Phillips Chemical Co LLC, Chevron Phillips Chemical Co LP filed Critical Chevron Phillips Chemical Co LLC
Publication of DE69913164D1 publication Critical patent/DE69913164D1/de
Application granted granted Critical
Publication of DE69913164T2 publication Critical patent/DE69913164T2/de
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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
    • C10G59/00—Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha
    • C10G59/06—Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha plural parallel stages only

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)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)
DE69913164T 1998-08-17 1999-08-16 Verfahren zur herstellung von aromatischen kohlenwasserstoffen in parallelreformern Expired - Fee Related DE69913164T2 (de)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US9682698P 1998-08-17 1998-08-17
US96826P 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
DE69913164D1 DE69913164D1 (de) 2004-01-08
DE69913164T2 true DE69913164T2 (de) 2004-08-26

Family

ID=22259263

Family Applications (1)

Application Number Title Priority Date Filing Date
DE69913164T Expired - Fee Related DE69913164T2 (de) 1998-08-17 1999-08-16 Verfahren zur herstellung von aromatischen kohlenwasserstoffen in parallelreformern

Country Status (10)

Country Link
US (1) US6143166A (enExample)
EP (1) EP1109880B1 (enExample)
JP (1) JP2002522626A (enExample)
AT (1) ATE255154T1 (enExample)
AU (1) AU5775799A (enExample)
CA (1) CA2339993A1 (enExample)
DE (1) DE69913164T2 (enExample)
ES (1) ES2212622T3 (enExample)
MX (1) MXPA01001723A (enExample)
WO (1) WO2000009633A1 (enExample)

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
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
US8906226B2 (en) * 2011-04-29 2014-12-09 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
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
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
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
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
CN109689206A (zh) 2016-09-08 2019-04-26 切弗朗菲利浦化学公司 具有改进活性和稳定性的酸性芳构化催化剂
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
CA3107128A1 (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
KR20220002363A (ko) * 2019-04-21 2022-01-06 셰브런 유.에스.에이.인크. 개선된 개질 공정
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
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
US11999619B2 (en) 2020-06-18 2024-06-04 Saudi Arabian Oil Company Hydrogen production with membrane reactor
US11492254B2 (en) 2020-06-18 2022-11-08 Saudi Arabian Oil Company Hydrogen production with membrane reformer
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
US11724943B2 (en) 2021-01-04 2023-08-15 Saudi Arabian Oil Company Black powder catalyst for hydrogen production via dry reforming
US11427519B2 (en) 2021-01-04 2022-08-30 Saudi Arabian Oil Company Acid modified red mud as a catalyst for olefin isomerization
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
US11820658B2 (en) 2021-01-04 2023-11-21 Saudi Arabian Oil Company Black powder catalyst for hydrogen production via autothermal reforming
US12220666B2 (en) 2021-01-12 2025-02-11 Saudi Arabian Oil Company Ultrathin membrane fabrication
US12258272B2 (en) 2021-08-12 2025-03-25 Saudi Arabian Oil Company Dry reforming of methane using a nickel-based bi-metallic catalyst
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
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
US33323A (en) * 1861-09-17 Improvement in pumps
US3172841A (en) * 1965-03-09 Process for upgrading natural sas condensates
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 (enExample) * 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
EP0993500B1 (en) * 1997-06-16 2002-09-18 Chevron Phillips Chemical Company Lp Split-feed two-stage parallel aromatization for maximum para-xylene yield

Also Published As

Publication number Publication date
EP1109880A1 (en) 2001-06-27
ATE255154T1 (de) 2003-12-15
DE69913164D1 (de) 2004-01-08
JP2002522626A (ja) 2002-07-23
EP1109880B1 (en) 2003-11-26
MXPA01001723A (es) 2002-04-08
CA2339993A1 (en) 2000-02-24
AU5775799A (en) 2000-03-06
WO2000009633A1 (en) 2000-02-24
ES2212622T3 (es) 2004-07-16
US6143166A (en) 2000-11-07

Similar Documents

Publication Publication Date Title
DE69913164T2 (de) Verfahren zur herstellung von aromatischen kohlenwasserstoffen in parallelreformern
DE68909819T2 (de) Verfahren zur Reformierung einer Kohlenwasserstofffraktion mit limitiertem C9+-Gehalt.
DE2526887C2 (de) Verfahren zur Herstellung von aromatischen Kohlenwasserstoffen
DE69030009T2 (de) Verfahren zur reformierung von erdölkohlenwasserstoffen
DE69529286T2 (de) Para-xylen selektives reformieren/aromatisieren
DD281968A5 (de) Katalysatorzusammensetzung fuer die umwandlung von kohlenwasserstoffen
US6051128A (en) Split-feed two-stage parallel aromatization for maximum para-xylene yield
DE69120049T2 (de) Katalysator und Verfahren zum Isomerisieren von Kohlenwasserstoffen
DE2162442A1 (de) Katalytisches Reformierverfahren
DE3781528T2 (de) Verfahren zur oktanzahlsteigerung und zur verringerung des schwefelgehaltes von olefinischen benzinen.
DE1234902B (de) Kontinuierliches Kohlenwasserstoffumwandlungsverfahren
DE2326834A1 (de) Verfahren zur verarbeitung von kohlenwasserstoffnaphtha zu einem fluessigen produkt mit einem hohen aromatengehalt
DE3527095A1 (de) Dehydrocyclisationsverfahren
DE3419280A1 (de) Verfahren zum umwandeln von kohlenwasserstoffen
DE60107805T2 (de) Veredelung von Naphtha durch kombinierte Olefinbildung und Aromatisierung
DE2455375C3 (de) Katalysator für die Behandlung von Kohlenwasserstoffen mit Wasserstoff
DE2065046A1 (de) Verfahren zur Umwandlung von Kohlenwasserstoffen. Ausscheidung aus: 2025377
DE69302287T2 (de) Erniedrigung des Benzolgehaltes von Benzinen durch Isomerisierung
DE69715682T2 (de) Zweistufige aromatisation für maximale para-xylen-ausbeute mit geteilter einspeisung
DE69004250T2 (de) Vielzonen-katalytisches Reformierverfahren mit mehreren Katalysatoren.
DE68917627T2 (de) Verfahren zum Reformieren einer dimethylbutanfreien Kohlenwasserstofffraktion.
DE69321741T2 (de) Erniedrigung des Benzolgehaltes von Benzinen
DE69521319T2 (de) Zweistufiges Verfahren zur Verbesserung von zyklischem Naphtha
DE69302595T2 (de) Verfahren zur Aufarbeitung eines Kohlenwasserstoffeinsatzes
DE4240862C2 (de) Verwendung eines Katalysators zur Herstellung von BTX-Aromaten

Legal Events

Date Code Title Description
8364 No opposition during term of opposition
8339 Ceased/non-payment of the annual fee