ES2030286T3 - Procedimeinto de preparacion de un catalizador apto para promover la conversion oxidante del metano en hidrocarburos superiores. - Google Patents

Procedimeinto de preparacion de un catalizador apto para promover la conversion oxidante del metano en hidrocarburos superiores.

Info

Publication number
ES2030286T3
ES2030286T3 ES198989401840T ES89401840T ES2030286T3 ES 2030286 T3 ES2030286 T3 ES 2030286T3 ES 198989401840 T ES198989401840 T ES 198989401840T ES 89401840 T ES89401840 T ES 89401840T ES 2030286 T3 ES2030286 T3 ES 2030286T3
Authority
ES
Spain
Prior art keywords
methane
coprecipitate
promote
catalyst suitable
procedure
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
Application number
ES198989401840T
Other languages
English (en)
Inventor
Christian Forquy
Didier Residence Le Vallon Des Sources Tichit
Didier Anglerot
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.)
Societe National Elf Aquitaine
Elf Aquitaine Norge AS
Original Assignee
Societe National Elf Aquitaine
Elf Aquitaine Norge AS
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 Societe National Elf Aquitaine, Elf Aquitaine Norge AS filed Critical Societe National Elf Aquitaine
Application granted granted Critical
Publication of ES2030286T3 publication Critical patent/ES2030286T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • 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
    • B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/20—Carbon compounds
    • B01J27/232—Carbonates
    • 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
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S585/00—Chemistry of hydrocarbon compounds
    • Y10S585/929—Special chemical considerations
    • Y10S585/943—Synthesis from methane or inorganic carbon source, e.g. coal

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

SE PONE EN CONTACTO UNA FASE ACUOSA QUE CONTIENE CATIONES DE POR LO MENOS UN METAL DEL GRUPO DE LOS LANTANIDOS Y CATIONES DE POR LO MENOS UN METAL ALCALINOTERREO, CON UNA CANTIDAD SUFICIENTE DE UNA FUENTE DE IONES CARBONATO Y, EVENTUALMENTE, DE UNA FUENTE DE IONES HIDROXILO, PARA FORMAR UN COPRECIPITADO DE CARBONATOS E HIDROXICARBONATOS DE DICHOS METALES, QUE CONTIENEN POR LO MENOS 5 % EN PESO DE CARBONATOS, Y LLEVAR EL PH DEL MEDIO REACCIONANTE A UN VALOR SUPERIOR A 8. EL COPRECIPITADO OBTENIDO SE MANTIENE EVENTUALMENTE ENTRE 60 Y 150 (GRADOS) C DURANTE 30 MINUTOS POR LO MENOS, DESPUES SE SOMETE A LAVADO Y A CONTINUACION A SECADO. EL COPRECIPITADO LAVADO Y SECO SE CALCINA AL FIN ENTRE 400 Y 1000 (GRADOS) C. EL COPRECIPITADO CALCINADO ES UTIL COMO CATALIZADOR APTO PARA PROMOVER LA CONVERSION OXIDANTE DE METANO EN HIDROCARBUROS CON UNA SELECTIVIDAD Y UNA ACTIVIDAD ELEVADAS.
ES198989401840T 1988-06-29 1989-06-27 Procedimeinto de preparacion de un catalizador apto para promover la conversion oxidante del metano en hidrocarburos superiores. Expired - Lifetime ES2030286T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR8808766A FR2634398B1 (fr) 1988-06-29 1988-06-29 Procede de preparation d'un catalyseur apte a promouvoir la conversion oxydante du methane en hydrocarbures superieurs

Publications (1)

Publication Number Publication Date
ES2030286T3 true ES2030286T3 (es) 1992-10-16

Family

ID=9367871

Family Applications (1)

Application Number Title Priority Date Filing Date
ES198989401840T Expired - Lifetime ES2030286T3 (es) 1988-06-29 1989-06-27 Procedimeinto de preparacion de un catalizador apto para promover la conversion oxidante del metano en hidrocarburos superiores.

Country Status (9)

Country Link
US (1) US5061670A (es)
EP (1) EP0349419B1 (es)
JP (1) JP2733588B2 (es)
AU (1) AU615091B2 (es)
CA (1) CA1326008C (es)
DE (1) DE68900812D1 (es)
ES (1) ES2030286T3 (es)
FR (1) FR2634398B1 (es)
WO (1) WO1990000086A1 (es)

Families Citing this family (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2663245B1 (fr) * 1990-06-13 1992-09-18 Rhone Poulenc Chimie Composition a base d'alumine pour catalyseur et procede de fabrication.
US6909024B1 (en) * 1999-11-22 2005-06-21 The Dow Chemical Company Process for the conversion of ethylene to vinyl chloride and novel catalyst compositions useful for such process
US6680415B1 (en) * 1999-11-22 2004-01-20 Dow Global Technologies Inc. Oxyhalogenation process using catalyst having porous rare earth halide support
US6933417B1 (en) 1999-11-22 2005-08-23 Dow Global Technologies Inc. Process for vinyl chloride manufacture from ethane and ethylene with partial CHl recovery from reactor effluent
US6797845B1 (en) 1999-11-22 2004-09-28 Dow Global Technologies Inc. Process for vinyl chloride manufacture from ethane and ethylene with immediate HCl recovery from reactor effluent
US6403523B1 (en) 2000-09-18 2002-06-11 Union Carbide Chemicals & Plastics Technology Corporation Catalysts for the oxidative dehydrogenation of hydrocarbons
AU2002307548B2 (en) 2001-05-23 2007-06-28 Dow Global Technologies Inc. Oxidative halogenation and optional dehydrogenation of C3+ hydrocarbons
US20040152929A1 (en) * 2002-05-08 2004-08-05 Clarke William D Process for vinyl chloride manufacture from ethane and ethylene with air feed and alternative hcl processing methods
US20040161474A1 (en) * 2002-05-24 2004-08-19 Moerck Rudi E. Rare earth metal compounds methods of making, and methods of using the same
US20060083791A1 (en) * 2002-05-24 2006-04-20 Moerck Rudi E Rare earth metal compounds methods of making, and methods of using the same
CN101658789B (zh) * 2009-09-21 2012-04-18 国核电力规划设计研究院 金属掺杂羟基氧化物催化剂及其制备方法和应用
WO2011143475A1 (en) * 2010-05-12 2011-11-17 Spectrum Pharmaceuticals, Inc. Lanthanum carbonate hydroxide, lanthanum oxycarbonate and methods of their manufacture and use
KR101929455B1 (ko) 2012-05-17 2018-12-14 삼성전자주식회사 탄산수 제조 장치를 갖는 냉장고
CN113797913B (zh) * 2020-06-12 2024-05-07 中国石油化工股份有限公司 镁镧复合氧化物及其制备方法和应用
CN113797949B (zh) * 2020-06-16 2024-05-10 中国石油化工股份有限公司 碳酸氧镧催化剂及其制备方法和应用
CN115463678A (zh) * 2021-06-11 2022-12-13 中国石油化工股份有限公司 碳酸氧镧催化剂及其制备方法和应用
CN115463651B (zh) * 2021-06-11 2024-02-13 中国石油化工股份有限公司 含有纳米级棒状氢氧化镧的催化剂及其制备方法和应用
CN115487839B (zh) * 2021-06-17 2024-03-26 中国石油化工股份有限公司 片状催化剂及其制备方法和应用
CN115487840B (zh) * 2021-06-18 2024-05-07 中国石油化工股份有限公司 含有碳酸氧镧的催化剂的制备方法和应用
WO2024103244A1 (zh) * 2022-11-15 2024-05-23 中国石油化工股份有限公司 碳酸氧镧催化剂及其制备方法和应用

Family Cites Families (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB632350A (en) * 1943-12-31 1949-11-21 Koppers Co Inc Improvements in or relating to dehydrogenation catalysts and method of preparing same
US3024199A (en) * 1958-09-02 1962-03-06 Du Pont Stable aquasols of hydrous rare earth oxides and their preparation
US3404100A (en) * 1963-10-21 1968-10-01 Exxon Research Engineering Co Methane production using a promoted catalyst
US3888792A (en) * 1970-06-26 1975-06-10 African Explosives & Chem Catalyst of cobalt oxide and a rare earth metal oxide and its method of preparation
RO61546A (es) * 1971-06-08 1977-05-15
GB1405405A (en) * 1971-06-25 1975-09-10 Johnson Matthey Co Ltd Platinum group metal catalysts
US3885020A (en) * 1971-10-28 1975-05-20 Univ Southern California Method of oxidizing hydrocarbons and oxygenated hydrocarbons to carbon dioxide and water
JPS5844021B2 (ja) * 1978-11-01 1983-09-30 東レ株式会社 酸化エチレン製造用触媒組成物
JPS58119342A (ja) * 1981-12-29 1983-07-15 Kureha Chem Ind Co Ltd 酸化的脱水素二量化用触媒
US4517398A (en) * 1984-04-16 1985-05-14 Atlantic Richfield Company Hydroxylated magnesia support
US4613718A (en) * 1984-04-16 1986-09-23 Atlantic Richfield Company Hydroxylated magnesia support
NZ216388A (en) * 1985-06-14 1990-01-29 Grace W R & Co Catalytic conversion of methane into hydrogen and higher hydrocarbons
US4656155A (en) * 1985-07-25 1987-04-07 Atlantic Richfield Company Reducible metal oxide compositions containing zirconium oxide, yttrium oxide and an alkali metal component
JPS62129227A (ja) * 1985-11-29 1987-06-11 Idemitsu Kosan Co Ltd メタンの部分酸化によるエタン、エチレンの製造方法
US4695668A (en) * 1986-03-24 1987-09-22 The Standard Oil Company Molybdenum-tungsten-containing catalyst and methane conversion process using same
US4826796A (en) * 1988-03-28 1989-05-02 Institute Of Gas Technology Mixed basic metal oxide catalyst for oxidative coupling of methane

Also Published As

Publication number Publication date
CA1326008C (fr) 1994-01-11
EP0349419B1 (fr) 1992-02-05
FR2634398A1 (fr) 1990-01-26
FR2634398B1 (fr) 1990-09-07
US5061670A (en) 1991-10-29
JPH03501100A (ja) 1991-03-14
AU615091B2 (en) 1991-09-19
DE68900812D1 (de) 1992-03-19
WO1990000086A1 (fr) 1990-01-11
EP0349419A1 (fr) 1990-01-03
AU3879089A (en) 1990-01-23
JP2733588B2 (ja) 1998-03-30

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