ES2212622T3 - Procedimiento para la produccion de compuestos aromaticos en reformadores paralelos. - Google Patents
Procedimiento para la produccion de compuestos aromaticos en reformadores paralelos.Info
- Publication number
- ES2212622T3 ES2212622T3 ES99945063T ES99945063T ES2212622T3 ES 2212622 T3 ES2212622 T3 ES 2212622T3 ES 99945063 T ES99945063 T ES 99945063T ES 99945063 T ES99945063 T ES 99945063T ES 2212622 T3 ES2212622 T3 ES 2212622T3
- Authority
- ES
- Spain
- Prior art keywords
- hydrogen
- catalyst
- stream
- reforming
- gas
- 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 - Lifetime
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)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US9682698P | 1998-08-17 | 1998-08-17 | |
| US96826P | 1998-08-17 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| ES2212622T3 true ES2212622T3 (es) | 2004-07-16 |
Family
ID=22259263
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ES99945063T Expired - Lifetime ES2212622T3 (es) | 1998-08-17 | 1999-08-16 | Procedimiento para la produccion de compuestos aromaticos en reformadores paralelos. |
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)
| 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)
| 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 |
-
1999
- 1999-08-16 ES ES99945063T patent/ES2212622T3/es not_active Expired - Lifetime
- 1999-08-16 DE DE69913164T patent/DE69913164T2/de not_active Expired - Fee Related
- 1999-08-16 US US09/375,196 patent/US6143166A/en not_active Expired - Lifetime
- 1999-08-16 AU AU57757/99A patent/AU5775799A/en not_active Abandoned
- 1999-08-16 AT AT99945063T patent/ATE255154T1/de not_active IP Right Cessation
- 1999-08-16 EP EP99945063A patent/EP1109880B1/en not_active Expired - Lifetime
- 1999-08-16 CA CA002339993A patent/CA2339993A1/en not_active Abandoned
- 1999-08-16 WO PCT/US1999/018568 patent/WO2000009633A1/en not_active Ceased
- 1999-08-16 MX MXPA01001723A patent/MXPA01001723A/es not_active IP Right Cessation
- 1999-08-16 JP JP2000565070A patent/JP2002522626A/ja not_active Abandoned
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 |
| DE69913164T2 (de) | 2004-08-26 |
| AU5775799A (en) | 2000-03-06 |
| WO2000009633A1 (en) | 2000-02-24 |
| US6143166A (en) | 2000-11-07 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| ES2212622T3 (es) | Procedimiento para la produccion de compuestos aromaticos en reformadores paralelos. | |
| US4975178A (en) | Multistage reforming with interstage aromatics removal | |
| US5401386A (en) | Reforming process for producing high-purity benzene | |
| US4435283A (en) | Method of dehydrocyclizing alkanes | |
| EP2155633B1 (en) | Aromatization of alkanes using a germanium-zeolite catalyst | |
| US6051128A (en) | Split-feed two-stage parallel aromatization for maximum para-xylene yield | |
| US5792338A (en) | BTX from naphtha without extraction | |
| US4645586A (en) | Reforming process | |
| US8608941B2 (en) | Reforming process with integrated fluid catalytic cracker gasoline and hydroprocessed cycle oil | |
| JP2000281597A (ja) | 芳香族成分を多量に含む製品生産の3段触媒ゾーンによる接触改質法 | |
| GB2153384A (en) | Method of reforming hydrocarbons | |
| US5683573A (en) | Continuous catalytic reforming process with dual zones | |
| EP1042431B1 (en) | Zeolite l catalyst in a furnace reactor | |
| US4935566A (en) | Dehydrocyclization and reforming process | |
| US8524961B2 (en) | Integrated catalytic cracking and reforming processes to improve p-xylene production | |
| US6358400B1 (en) | Selective reforming process for the production of aromatics | |
| EP0993500B1 (en) | Split-feed two-stage parallel aromatization for maximum para-xylene yield | |
| US4636298A (en) | Reforming process | |
| CA2077457A1 (en) | Multi-stage reforming process | |
| KR100555172B1 (ko) | 방향족 물질 함량이 높은 생성물을 제조하기 위한 3개의 촉매 영역을 갖춘 접촉 개질 방법 | |
| MXPA00006163A (en) | Zeolite l catalyst in a furnace reactor | |
| MXPA99010544A (en) | Split-feed two-stage parallel aromatization for maximum para-xylene yield | |
| WO1994019428A1 (en) | REFORMING USING A Pt LOW-Re CATALYST IN THE LEAD REACTOR |