NO20011561L - Fremgangsmåte ved fremstilling av olefiner ved å bruke en pentasil zeolitt-basert katalysator - Google Patents
Fremgangsmåte ved fremstilling av olefiner ved å bruke en pentasil zeolitt-basert katalysatorInfo
- Publication number
- NO20011561L NO20011561L NO20011561A NO20011561A NO20011561L NO 20011561 L NO20011561 L NO 20011561L NO 20011561 A NO20011561 A NO 20011561A NO 20011561 A NO20011561 A NO 20011561A NO 20011561 L NO20011561 L NO 20011561L
- Authority
- NO
- Norway
- Prior art keywords
- hydrocarbon
- passed
- catalyst
- naphtha
- mixtures
- Prior art date
Links
Classifications
-
- 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
-
- 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
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/061—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof containing metallic elements added to the zeolite
-
- 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
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/40—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively
- B01J29/405—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively containing rare earth elements, titanium, zirconium, hafnium, zinc, cadmium, mercury, gallium, indium, thallium, tin or lead
-
- 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
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/82—Phosphates
-
- 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
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/10—After treatment, characterised by the effect to be obtained
- B01J2229/26—After treatment, characterised by the effect to be obtained to stabilize the total catalyst structure
-
- 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
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/30—After treatment, characterised by the means used
- B01J2229/42—Addition of matrix or binder particles
-
- 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
- C07C2529/40—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11
-
- 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
- Y02P30/40—Ethylene production
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Crystallography & Structural Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Catalysts (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
En katalysator og en forbedret prosess for fremstilling av olefiner ved katalytisk krakking av nafta er beskrevet. Prosessen frembringer relativt større utbytter over et kom-mersielt viktig område av naftaomdanning,mens det gir om-trent det samme eller lavere utbytter av aromater og metan over dette området. I prosessen blir et hydrokarbon nafta råstoff omfattende et hydrokarbon med fra ca tre til ca tyve karbonatomer pr. molekyl sendt inn i en reaktor som inneholder en pentasil zeolittkatalysator. Katalysatoren omfatter fra ca 0,1 til ca 10 vekt% fosfor og ca 0,1 til 10 vekt% av et promotormetall valgt fra gruppen som består av gallium, germanium eller tinn og blandinger av disse.yd-rokarbonet kan sendes inn i reaktoren sammen med et for-tynningsmiddel valgt fra gruppen som består av damp, nitro-gen, metan, og etan og blandinger av disse. Alternativt kan hydrokarbonet sendes inn i reaktoren sammen med ekstra pro-pan.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US16184598A | 1998-09-28 | 1998-09-28 | |
US40558299A | 1999-09-27 | 1999-09-27 | |
PCT/US1999/022460 WO2000018853A1 (en) | 1998-09-28 | 1999-09-28 | Process for manufacturing olefins using a pentasil zeolite based catalyst |
Publications (2)
Publication Number | Publication Date |
---|---|
NO20011561D0 NO20011561D0 (no) | 2001-03-27 |
NO20011561L true NO20011561L (no) | 2001-03-27 |
Family
ID=26858166
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
NO20011561A NO20011561L (no) | 1998-09-28 | 2001-03-27 | Fremgangsmåte ved fremstilling av olefiner ved å bruke en pentasil zeolitt-basert katalysator |
Country Status (12)
Country | Link |
---|---|
US (1) | US6548725B2 (no) |
EP (1) | EP1117750B1 (no) |
JP (1) | JP2002525380A (no) |
CN (1) | CN1195714C (no) |
AT (1) | ATE270318T1 (no) |
AU (1) | AU6271299A (no) |
CA (1) | CA2345308A1 (no) |
DE (1) | DE69918451T2 (no) |
ES (1) | ES2224702T3 (no) |
ID (1) | ID29487A (no) |
NO (1) | NO20011561L (no) |
WO (1) | WO2000018853A1 (no) |
Families Citing this family (62)
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EP1195424A1 (en) * | 2000-10-05 | 2002-04-10 | ATOFINA Research | A process for cracking an olefin-rich hydrocarbon feedstock |
AU2004200270B2 (en) * | 2003-01-31 | 2009-11-12 | Chevron U.S.A. Inc. | High purity olefinic naphthas for the production of ethylene and propylene |
GB2408746B (en) * | 2003-01-31 | 2005-10-12 | Chevron Usa Inc | High purity olefinic naphthas for the production of ethylene and propylene |
US7431821B2 (en) | 2003-01-31 | 2008-10-07 | Chevron U.S.A. Inc. | High purity olefinic naphthas for the production of ethylene and propylene |
US7150821B2 (en) | 2003-01-31 | 2006-12-19 | Chevron U.S.A. Inc. | High purity olefinic naphthas for the production of ethylene and propylene |
US7084318B2 (en) * | 2003-08-01 | 2006-08-01 | Saudi Basic Industries Corporation | Toluene methylation process |
US7060864B2 (en) * | 2003-09-30 | 2006-06-13 | Saudi Basic Industries Corporation | Toluene methylation process |
US7060644B2 (en) * | 2004-01-08 | 2006-06-13 | Saudi Basic Industries Corporation | Aromatic alkylation catalyst and method |
US6943131B1 (en) * | 2004-03-02 | 2005-09-13 | Saudi Basic Industries Corporation | Selective zeolite catalyst modification |
CN1332756C (zh) * | 2004-07-14 | 2007-08-22 | 中国石油化工股份有限公司 | 一种含沸石的烃类转化催化剂 |
US7399727B2 (en) * | 2004-04-23 | 2008-07-15 | Saudi Basic Industries Corporation | Zeolite catalyst and method |
US7285511B2 (en) * | 2004-04-23 | 2007-10-23 | Saudi Basic Industries Corporation | Method of modifying zeolite catalyst |
WO2005123251A1 (en) * | 2004-06-09 | 2005-12-29 | Saudi Basic Industries Corporation | Fluoride-modified zeolite catalyst and method |
CN100351344C (zh) * | 2004-07-14 | 2007-11-28 | 中国石油化工股份有限公司 | 一种选择性制取小分子烯烃的催化转化方法 |
EP1856230B1 (en) * | 2005-03-11 | 2010-02-24 | Uop Llc | Catalytic naphtha cracking catalyst and process |
US7304194B2 (en) * | 2005-05-05 | 2007-12-04 | Saudi Basic Industries Corporation | Hydrothermal treatment of phosphorus-modified zeolite catalysts |
KR100598988B1 (ko) * | 2005-05-18 | 2006-07-12 | 주식회사 하이닉스반도체 | 오버레이 버니어 및 이를 이용한 반도체소자의 제조방법 |
US7368410B2 (en) * | 2005-08-03 | 2008-05-06 | Saudi Basic Industries Corporation | Zeolite catalyst and method of preparing and use of zeolite catalyst |
EP1931750B1 (en) * | 2005-10-07 | 2017-01-18 | Sk Innovation Co., Ltd. | Process for production of light olefins from hydrocarbon feedstock |
CN1986505B (zh) * | 2005-12-23 | 2010-04-14 | 中国石油化工股份有限公司 | 一种增产低碳烯烃的催化转化方法 |
KR100651418B1 (ko) * | 2006-03-17 | 2006-11-30 | 에스케이 주식회사 | 고속유동층을 이용하여 탄화수소 원료로부터 경질 올레핀을제조하는 접촉분해 공정 |
US20080025885A1 (en) * | 2006-07-27 | 2008-01-31 | Lubo Zhou | Process for Dehydrocyclodimerization |
US7498473B2 (en) * | 2006-07-27 | 2009-03-03 | Uop Llc | Process for dehydrocyclodimerization |
CN101279881B (zh) * | 2007-04-04 | 2010-08-18 | 中国石油化工股份有限公司 | 催化裂解石脑油生产乙烯和丙烯的方法 |
CN101279287B (zh) * | 2007-04-04 | 2011-07-13 | 中国石油化工股份有限公司 | 用于催化裂解制烯烃的催化剂 |
US20110098519A1 (en) * | 2007-08-13 | 2011-04-28 | Kanaparthi Ramesh | Modified catalyst composition for conversion of alcohol to alkene |
US8846559B2 (en) * | 2008-11-03 | 2014-09-30 | Saudi Basic Industries Corporation | Stable shape-selective catalyst for aromatic alkylation and methods of using and preparing |
CN102458657B (zh) * | 2009-06-30 | 2015-07-22 | 吉坤日矿日石能源株式会社 | 单环芳香族烃制造用催化剂及单环芳香族烃的制造方法 |
CN102470352B (zh) * | 2009-07-29 | 2015-07-22 | 吉坤日矿日石能源株式会社 | 单环芳香族烃制造用催化剂及单环芳香族烃的制造方法 |
US8062987B2 (en) * | 2009-10-05 | 2011-11-22 | Saudi Basic Industries Corporation | Phosphorus-containing zeolite catalysts and their method of preparation |
US20110230333A1 (en) * | 2010-03-16 | 2011-09-22 | Uop Llc | Olefin Cracking Catalyst and Manufacturing Process |
US9433912B2 (en) | 2010-03-31 | 2016-09-06 | Indian Oil Corporation Limited | Process for simultaneous cracking of lighter and heavier hydrocarbon feed and system for the same |
JP2012139640A (ja) | 2010-12-28 | 2012-07-26 | Jx Nippon Oil & Energy Corp | 単環芳香族炭化水素製造用触媒および単環芳香族炭化水素の製造方法 |
JP5587761B2 (ja) | 2010-12-28 | 2014-09-10 | Jx日鉱日石エネルギー株式会社 | 単環芳香族炭化水素の製造方法 |
JP2012139641A (ja) * | 2010-12-28 | 2012-07-26 | Jx Nippon Oil & Energy Corp | 単環芳香族炭化水素製造用触媒および単環芳香族炭化水素の製造方法 |
EA028628B1 (ru) * | 2011-08-03 | 2017-12-29 | Тотал Ресерч & Технолоджи Фелай | Применение катализатора на основе модифицированного фосфором цеолита в процессе дегидратации спиртов |
US8772192B2 (en) | 2012-06-29 | 2014-07-08 | Saudi Basic Industries Corporation | Germanium silicalite catalyst and method of preparation and use |
US9278342B2 (en) | 2012-07-02 | 2016-03-08 | Saudi Basic Industries Corporation | Method of modifying a phosphorus-containing zeolite catalyst |
CN112264086A (zh) | 2013-04-29 | 2021-01-26 | 沙特基础工业公司 | 石脑油转化成烯烃的催化方法 |
KR101600430B1 (ko) | 2015-01-08 | 2016-03-07 | 한국화학연구원 | 이산화탄소가 풍부한 합성가스로부터 단환 방향족 화합물 및 장쇄올레핀 화합물의 직접 합성방법 |
CN108431177B (zh) | 2015-12-22 | 2021-04-20 | 沙特基础工业全球技术公司 | 由石脑油生产乙烯和丙烯的方法 |
FR3049954A1 (fr) | 2016-04-08 | 2017-10-13 | Ifp Energies Now | Utilisation de zeolithe nu-86 pour le procede de craquage catalytique de naphtha |
US9981888B2 (en) | 2016-06-23 | 2018-05-29 | Saudi Arabian Oil Company | Processes for high severity fluid catalytic cracking systems |
US11807816B2 (en) | 2016-12-19 | 2023-11-07 | Sabic Global Technologies B.V. | Process integration for cracking light paraffinic hydrocarbons |
EP3622039A1 (en) * | 2017-05-10 | 2020-03-18 | SABIC Global Technologies B.V. | Process for catalytic cracking of naphtha using radial flow moving bed reactor system |
US10870802B2 (en) | 2017-05-31 | 2020-12-22 | Saudi Arabian Oil Company | High-severity fluidized catalytic cracking systems and processes having partial catalyst recycle |
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 |
CN112154132A (zh) * | 2018-04-30 | 2020-12-29 | 沙特基础工业全球技术公司 | 由异构化的直馏石脑油制备低碳烯烃的方法 |
KR102096308B1 (ko) | 2018-05-30 | 2020-04-02 | 한국화학연구원 | 선형 장쇄올레핀 제조용 피셔―트롭쉬 합성반응 촉매 및 이를 이용한 선형 장쇄올레핀의 제조방법 |
US10350585B1 (en) | 2018-08-14 | 2019-07-16 | Saudi Arabian Oil Company | Methods for synthesizing hierarchical zeolites for catalytic cracking |
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 |
EP3620499A1 (en) | 2018-09-06 | 2020-03-11 | INDIAN OIL CORPORATION Ltd. | Process for selective production of light olefins and aromatics from cracked light naphtha |
CN113498360B (zh) * | 2018-12-26 | 2024-06-14 | Ptt全球化学公共有限公司 | 用于从c4-c7碳氢化合物生产轻质烯烃的催化剂 |
US20220259505A1 (en) * | 2019-08-05 | 2022-08-18 | Sabic Global Technologies B.V. | A method for catalytic cracking of hydrocarbons to produce olefins and aromatics without steam as diluent |
KR102653716B1 (ko) | 2020-03-03 | 2024-04-03 | 한국화학연구원 | 이산화탄소가 포함된 합성가스로부터 선형 알파 올레핀을 제조하기 위한 촉매 및 이를 이용한 선형 알파 올레핀의 제조방법 |
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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 |
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 |
US11505754B2 (en) | 2020-09-01 | 2022-11-22 | Saudi Arabian Oil Company | Processes for producing petrochemical products from atmospheric residues |
US11352575B2 (en) | 2020-09-01 | 2022-06-07 | Saudi Arabian Oil Company | Processes for producing petrochemical products that utilize hydrotreating of cycle oil |
US11242493B1 (en) | 2020-09-01 | 2022-02-08 | Saudi Arabian Oil Company | Methods for processing crude oils to form light olefins |
US11230672B1 (en) | 2020-09-01 | 2022-01-25 | Saudi Arabian Oil Company | Processes for producing petrochemical products that utilize fluid catalytic cracking |
Family Cites Families (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3972832A (en) * | 1974-09-23 | 1976-08-03 | Mobil Oil Corporation | Phosphorus-containing zeolite catalyst |
US4112056A (en) * | 1977-05-02 | 1978-09-05 | Mobil Oil Corporation | Preparation of zeolites |
US4356338A (en) * | 1979-07-27 | 1982-10-26 | Mobil Oil Corporation | Extending catalyst life by treating with phosphorus and/or steam |
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US4801567A (en) * | 1981-06-19 | 1989-01-31 | Union Oil Company Of California | Oxidation catalyst |
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US5166455A (en) * | 1992-01-16 | 1992-11-24 | Mobil Oil Corporation | Process for the production of tertiary alkytl ethers from FCC light naphtha |
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US5476823A (en) * | 1993-05-28 | 1995-12-19 | Mobil Oil Corp. | Method of preparation of ex situ selectivated zeolite catalysts for enhanced shape selective applications and method to increase the activity thereof |
-
1999
- 1999-09-28 WO PCT/US1999/022460 patent/WO2000018853A1/en active IP Right Grant
- 1999-09-28 AU AU62712/99A patent/AU6271299A/en not_active Abandoned
- 1999-09-28 JP JP2000572303A patent/JP2002525380A/ja active Pending
- 1999-09-28 ID IDW20010946A patent/ID29487A/id unknown
- 1999-09-28 EP EP99949945A patent/EP1117750B1/en not_active Expired - Lifetime
- 1999-09-28 ES ES99949945T patent/ES2224702T3/es not_active Expired - Lifetime
- 1999-09-28 CN CNB998114413A patent/CN1195714C/zh not_active Expired - Fee Related
- 1999-09-28 CA CA002345308A patent/CA2345308A1/en not_active Abandoned
- 1999-09-28 DE DE69918451T patent/DE69918451T2/de not_active Expired - Fee Related
- 1999-09-28 AT AT99949945T patent/ATE270318T1/de not_active IP Right Cessation
-
2001
- 2001-03-27 NO NO20011561A patent/NO20011561L/no unknown
- 2001-07-31 US US09/918,925 patent/US6548725B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
CN1320148A (zh) | 2001-10-31 |
CN1195714C (zh) | 2005-04-06 |
NO20011561D0 (no) | 2001-03-27 |
ATE270318T1 (de) | 2004-07-15 |
US6548725B2 (en) | 2003-04-15 |
ES2224702T3 (es) | 2005-03-01 |
EP1117750B1 (en) | 2004-06-30 |
US20010056217A1 (en) | 2001-12-27 |
WO2000018853A1 (en) | 2000-04-06 |
CA2345308A1 (en) | 2000-04-06 |
ID29487A (id) | 2001-08-30 |
EP1117750A1 (en) | 2001-07-25 |
DE69918451T2 (de) | 2005-07-28 |
JP2002525380A (ja) | 2002-08-13 |
AU6271299A (en) | 2000-04-17 |
DE69918451D1 (de) | 2004-08-05 |
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