KR960003799A - 수소첨가에 유용한 고체 촉매 조성물의 제조방법 - Google Patents

수소첨가에 유용한 고체 촉매 조성물의 제조방법 Download PDF

Info

Publication number
KR960003799A
KR960003799A KR1019950018768A KR19950018768A KR960003799A KR 960003799 A KR960003799 A KR 960003799A KR 1019950018768 A KR1019950018768 A KR 1019950018768A KR 19950018768 A KR19950018768 A KR 19950018768A KR 960003799 A KR960003799 A KR 960003799A
Authority
KR
South Korea
Prior art keywords
alkali metal
composition
reducing
reducing agent
temperature
Prior art date
Application number
KR1019950018768A
Other languages
English (en)
Other versions
KR100379870B1 (ko
Inventor
피이터 쳉 틴-택
엠 존슨 마아빈
에이취 브라운 스코트
에이 지즈만 스탄
비이 킴블 제임즈
Original Assignee
제이 이이 휘립프스
휘립프스 피트로오리암 캄파니
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=23028412&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=KR960003799(A) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by 제이 이이 휘립프스, 휘립프스 피트로오리암 캄파니 filed Critical 제이 이이 휘립프스
Publication of KR960003799A publication Critical patent/KR960003799A/ko
Application granted granted Critical
Publication of KR100379870B1 publication Critical patent/KR100379870B1/ko

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C5/00Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
    • C07C5/02Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation
    • C07C5/08Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation of carbon-to-carbon triple bonds
    • C07C5/09Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation of carbon-to-carbon triple bonds to carbon-to-carbon double bonds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • B01J23/44Palladium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/48Silver or gold
    • B01J23/50Silver
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/54Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/66Silver or gold
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/16Reducing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/16Reducing
    • B01J37/18Reducing with gases containing free hydrogen
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C5/00Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
    • C07C5/02Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation
    • C07C5/08Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation of carbon-to-carbon triple bonds
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00Purification; Separation; Use of additives
    • C07C7/148Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound
    • C07C7/163Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound by hydrogenation
    • C07C7/167Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound by hydrogenation for removal of compounds containing a triple carbon-to-carbon bond
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2521/00Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
    • C07C2521/02Boron or aluminium; Oxides or hydroxides thereof
    • C07C2521/04Alumina
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2521/00Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
    • C07C2521/06Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/02Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the alkali- or alkaline earth metals or beryllium
    • C07C2523/04Alkali metals
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals
    • C07C2523/40Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals of the platinum group metals
    • C07C2523/44Palladium
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals
    • C07C2523/48Silver or gold
    • C07C2523/50Silver
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals
    • C07C2523/54Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals combined with metals, oxides or hydroxides provided for in groups C07C2523/02 - C07C2523/36
    • C07C2523/66Silver or gold
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

팔라듐, 은 및 지지물질(바람직하게 알루미나)을 포함하는 초갬 조성물을 비교적 낮은 온도에서(약 60℃이상) 효율적인 환원제(바람직하게는 알칼리 금속 수소화 붕소, 히드라진, 포름알데히드, 포름산, 아스크로빈산, 덱스트로스, 알루미늄 분말)를 포함하는 액체 조성물과 접촉시킨다. 바람직하게, 하나 이상의 알칼리 금속 화합물(보다 바람직하게 KOH, RbOH, CsOH, KF)이 또한 액체 조성물내 존재한다. 아세틸렌을 (에틸렌으로)선택적으로 수소 첨가하기 위한 개선된 방법은 상기 습식-환원된 촉매 조성물을 사용하다.

Description

수소첨가에 유용한 고체 촉매 조성물의 제조방법
내용없음

Claims (15)

  1. 하기로 구성되는, 수소 첨가에 유용한 고체 촉매 조성물의 제조방법 : (1) 팔라듐, 은 및 무기지지 물질을 포함하는 고체 조성물(a), 및 (i) 하나 이상의 환원제가 히드라진, 수소화 붕소 알칼리 금속, 분자당 1-6개 탄소 원자를 함유한 알데히드, 분자당 1-6개의 탄소원자를 함유한 케톤, 분자당 1-6개 탄소원자를 함유한 카르복실산, 알데히드기 또는-히드록시케톤기를 함유한 당, 알루미늄 금속 또는 아연 금속인 하나 이상의 환원제, 및 (ⅱ) 하나 이상의 비-환원 액체 성분을 포함하는 액체 환원 조성물 (b)를 약 1초 이상의 기간동안 약 60℃이하의 온도에서 접촉시켜 습식-환원된 고체 조성물을 생성시키고; (2) 단계 (1) 내 생성된 상기 습식-환원된 고체 조성물을 상기 액체 환원 조성물로부터 실질적으로 분리하고; 및 (3) 단계 (2)에서 얻은 실질적으로 분리된 습식-환원된 고체 조성물을 건조시키고, 환원제 (i)가 상기 알데히드, 상기 케톤, 상기 카르복실산, 상기 당, 상기 알루미늄 금속 또는 상기 아연 금속인 경우, 상기 액체 환원 조성물은 알칼리 금속 수산화물 또는 알칼리 금속 플루오르화물인 하나 이상의 용해된 알카리 금속 화합물을 더 포함하고, 및 부가로 환원제가 상기 당이라면, 상기 방법은 부가로 하기를 포함한다; (4) 단계 (3)에서 얻은 건조된 습식-환원된 고체 조성물을 약 10분 이상의 시간동안 약 300℃-약 700℃의 온도에서 산화 가스 분위기내에서 가열한다.
  2. 제1항에 있어서, 상기 액체 환원 조성물이 본질적으로 상기 하나 이상의 환원제, 상기 하나 이상의 비-환원 액체 성분, 및 상기 하나 이상의 알칼리 금속 화합물로 구성되는 방법.
  3. 제1항에 있어서, 상기 환원제가 상기 히드라진, 상기 수소화 붕소 알칼리 금속, 상기 알데히드, 상기 케톤, 상기 카르복실산, 상기 알루미늄 금속 또는 상기 아연 금속이고, 상기 방법은 단계 (3)에서 얻은 건조된 습식-환원된 고체 조성물을 약 10분 이상의 시간동안 약 300℃-700℃의 온도에서 산화 가스 분위기내에 가열하는 상기 단계(4)를 부가로 포함하는 방법.
  4. 제1항에 있어서, 상기 하나 이상의 환원제가 상기 히드라진 또는 상기 수소화 붕소 알칼리 금속이고 상기 액체 환원 조성물이 할로겐화물, 수산화물, 탄산염, 중탄산염, 질산염 또는 카르복실산염인 하나 이상의 알칼리 금속 화합물을 포함하는 방법.
  5. 제1항에 있어서, 수소화 붕소 알칼리 금속이 수소화붕소나트륨 또는 수소화붕소 칼륨인 방법.
  6. 제1항에 있어서, 상기 하나 이상의 환원제가 텍스트로스, 포름알데히드, 포름산, 아스크로빈산 또는 알루미늄 금속이고, 상기 하나 이상의 알칼리 금속화합물이 수산화칼륨, 플루오르화칼륨, 수산화 루비듐, 플루오르화 루비듐, 수산화 세슘 또는 플르오르화 세슘인 방법.
  7. 제6항에 있어서, 상기 하나 이상의 알칼리 금속 화합물이 수산화칼륨 또는 플루오르화칼륨인 방법.
  8. 제1-7항 중 임의의 한 항에 있어서, 상기 무기 지지 물질이 알루미나, 티타니아, 지르코니아 또는 임의의 두개 이상의 상기 지지 물질의 혼합물이고; 상기 하나 이상의 비-환원 액체 성분이 물, 메탄올 또는 상기의 혼합물이고; 상기 접촉 온도는 약 10℃-60℃이고; 및 상기 접촉시간은 약 10초-약 10시간인 방법.
  9. 제8항에 있어서, 상기 접촉 온도가 약 20℃-50℃이고, 상기 시간 기간이 약 0.02-2시간이고, 및 상기 접촉중에 압력이 대략 대기압인 방법.
  10. 제8항에 있어서, 상기 무기 지지 물질이-알루미나이고, 및 상기 고체 조성물이 약 0.01-0.2중량% 팔라듐 및 약 0.02-2중량%의 은을 함유하는 방법.
  11. 제1-7항 중 임의의 한 항에 있어서, 단계 (4)를 약 0.2-20시간의 기간동안 약 400℃-600℃의 온도에서 공기중에서 수행하는 방법.
  12. 제1-7항 중 임의의 한 항에 있어서, 상기 액체 환원 조성물내 상기 하나 이상의 환원제의 중량%가 약 0.5-50중량%인 방법.
  13. 제1-7항 중 임의의 한 항에 따른 방법에 의해 제조된 조성물과 상기 아세틸렌을 접촉시키는 것으로 구성되는, 수소 가스를 사용하여 아세틸렌을 에틸렌으로 선택적으로 수소 첨가하기 위한 방법.
  14. 제13항에 있어서, 상기 아세틸렌이 에틸렌 스트림내 불순물로서, C2H2약 1-50,000 ppm 양으로 존재하는 방법.
  15. 제13항에 있어서, 약 0℃-150℃의 반응 온도에서 수행하는 방법.
    ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
KR1019950018768A 1994-07-01 1995-06-30 수소첨가에유용한고체촉매조성물의제조방법 KR100379870B1 (ko)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US8/269723 1994-07-01
US08/269723 1994-07-01
US08/269,723 US5488024A (en) 1994-07-01 1994-07-01 Selective acetylene hydrogenation

Publications (2)

Publication Number Publication Date
KR960003799A true KR960003799A (ko) 1996-02-23
KR100379870B1 KR100379870B1 (ko) 2003-08-19

Family

ID=23028412

Family Applications (2)

Application Number Title Priority Date Filing Date
KR1019950018768A KR100379870B1 (ko) 1994-07-01 1995-06-30 수소첨가에유용한고체촉매조성물의제조방법
KR1020020065187A KR100414260B1 (en) 1994-07-01 2002-10-24 Selective acetylene hydrogenation

Family Applications After (1)

Application Number Title Priority Date Filing Date
KR1020020065187A KR100414260B1 (en) 1994-07-01 2002-10-24 Selective acetylene hydrogenation

Country Status (11)

Country Link
US (2) US5488024A (ko)
EP (2) EP0689872B2 (ko)
JP (1) JP4040700B2 (ko)
KR (2) KR100379870B1 (ko)
AU (1) AU667678B2 (ko)
CA (1) CA2151414C (ko)
DE (2) DE69522053T3 (ko)
ES (2) ES2242660T3 (ko)
GR (1) GR3037067T3 (ko)
MY (1) MY113893A (ko)
SG (1) SG32384A1 (ko)

Families Citing this family (56)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5475173A (en) * 1994-07-19 1995-12-12 Phillips Petroleum Company Hydrogenation process and catalyst therefor
FR2724390B1 (fr) * 1994-09-08 1996-12-13 Inst Francais Du Petrole Hydrogenation selective de coupes hydrocarbonees renfermant des hydrocarbures monoinsatures et polyinsatures
US5583274A (en) 1995-01-20 1996-12-10 Phillips Petroleum Company Alkyne hydrogenation process
US5587348A (en) * 1995-04-19 1996-12-24 Phillips Petroleum Company Alkyne hydrogenation catalyst and process
US6096933A (en) * 1996-02-01 2000-08-01 Phillips Petroleum Company Hydrocarbon hydrogenation and catalyst therefor
AU692723B2 (en) * 1996-02-01 1998-06-11 Phillips Petroleum Company Catalyst composition and process for selecting hydrogenation of diolefins
US6254894B1 (en) * 1996-04-05 2001-07-03 Zodiac Pool Care, Inc. Silver self-regulating water purification compositions and methods
US5859304A (en) * 1996-12-13 1999-01-12 Stone & Webster Engineering Corp. Chemical absorption process for recovering olefins from cracked gases
GB9720333D0 (en) * 1997-09-25 1997-11-26 Ici Plc Selective hydrogenation
FR2770421B1 (fr) * 1997-10-31 1999-12-10 Inst Francais Du Petrole Procede de preparation de catalyseurs utilisables dans les reactions de transformation de composes organiques
FR2770521B1 (fr) * 1997-10-31 1999-12-10 Inst Francais Du Petrole Procede de deshydrogenation d'hydrocarbures aliphatiques satures en hydrocarbures olefiniques
FR2770520B1 (fr) * 1997-10-31 1999-12-10 Inst Francais Du Petrole Procede d'hydrogenation selective des composes insatures
EP1058924B1 (en) * 1998-01-26 2012-06-13 Apple Inc. Method and apparatus for integrating manual input
US6127588A (en) 1998-10-21 2000-10-03 Phillips Petroleum Company Hydrocarbon hydrogenation catalyst and process
US6130260A (en) * 1998-11-25 2000-10-10 The Texas A&M University Systems Method for converting natural gas to liquid hydrocarbons
US6602920B2 (en) * 1998-11-25 2003-08-05 The Texas A&M University System Method for converting natural gas to liquid hydrocarbons
US5958823A (en) * 1999-01-26 1999-09-28 Phillips Petroleum Company Hydrocarbon conversion catalyst composition and processes therefor and therewith
CA2371774A1 (en) * 1999-02-18 2000-08-24 Phillips Petroleum Company Alkyne hydrogenation process
US6417136B2 (en) 1999-09-17 2002-07-09 Phillips Petroleum Company Hydrocarbon hydrogenation catalyst and process
US6258989B1 (en) 1999-09-30 2001-07-10 Phillips Petroleum Company Hydrocarbon upgrading process
US6297414B1 (en) 1999-10-08 2001-10-02 Stone & Webster Process Technology, Inc. Deep selective hydrogenation process
DE10048219A1 (de) * 2000-02-10 2002-04-11 Sued Chemie Ag Katalysator für die Hydrierung von ungesättigten Kohlenwasserstoffen
US6465391B1 (en) * 2000-08-22 2002-10-15 Phillips Petroleum Company Selective hydrogenation catalyst and processes therefor and therewith
KR100838549B1 (ko) * 2001-02-13 2008-06-17 가부시키가이샤 구라레 복합체 및 그 제조방법
US6509292B1 (en) 2001-03-30 2003-01-21 Sud-Chemie Inc. Process for selective hydrogenation of acetylene in an ethylene purification process
US6734130B2 (en) * 2001-09-07 2004-05-11 Chvron Phillips Chemical Company Lp Hydrocarbon hydrogenation catalyst composition, a process of treating such catalyst composition, and a process of using such catalyst composition
CN1281720C (zh) * 2001-10-15 2006-10-25 催化蒸馏技术公司 加氢催化剂和加氢方法
US20030096880A1 (en) * 2001-11-02 2003-05-22 Conoco Inc. Combustion deposited metal-metal oxide catalysts and process for producing synthesis gas
KR20050008675A (ko) * 2002-04-08 2005-01-21 즈도케미 쇼쿠바이 가부시키가이샤 금속수소화물 함유 배기가스 처리제 및 금속수소화물 함유배기가스 처리방법
MY137042A (en) * 2002-06-14 2008-12-31 Chevron Phillips Chemical Co Hydrogenation palladium-silver catalyst and methods
US20040192983A1 (en) * 2003-02-18 2004-09-30 Chevron Phillips Chemical Co. Acetylene hydrogenation catalyst with segregated palladium skin
US7115789B2 (en) * 2003-03-28 2006-10-03 Exxon Mobil Chemical Patents Inc. Process for removal of alkynes and/or dienes from an olefin stream
GB0312769D0 (en) * 2003-06-04 2003-07-09 Johnson Matthey Plc Process for selective hydrogenation of acetylenic compounds and catalyst therefor
US20040260131A1 (en) * 2003-06-23 2004-12-23 Chevron Phillips Chemical Company ("Cpchem") Selective hydrocarbon hydrogenation catalyst and process
US7045670B2 (en) * 2003-09-03 2006-05-16 Synfuels International, Inc. Process for liquid phase hydrogenation
US20050096217A1 (en) * 2003-10-29 2005-05-05 Sud-Chemie, Inc. Selective hydrogenation catalyst
US7199076B2 (en) * 2003-12-19 2007-04-03 Chevron Phillips Chemical Company Lp Methods of making and using a selective hydrogenation catalyst
WO2005103025A1 (en) * 2004-04-21 2005-11-03 Novogen Research Pty Ltd Isoflavene synthetic method and catalyst
US7521393B2 (en) * 2004-07-27 2009-04-21 Süd-Chemie Inc Selective hydrogenation catalyst designed for raw gas feed streams
CN100379492C (zh) * 2005-01-10 2008-04-09 顾明兰 用Sol-gel法制备超细KF/Al2O3超强碱复合催化剂
CA2616481C (en) 2005-07-27 2016-06-14 Chevron Phillips Chemical Company Lp A selective hydrogenation catalyst and methods of making and using same
US20110288353A1 (en) 2008-11-26 2011-11-24 Wei Dai Metal loaded catalyst and preparation method thereof
US20100152022A1 (en) * 2008-12-17 2010-06-17 Qi Sun Catalyst regeneration method
US8921631B2 (en) 2008-12-18 2014-12-30 Saudi Basic Industries Corporation Selective catalytic hydrogenation of alkynes to corresponding alkenes
CN102811807B (zh) 2010-03-19 2016-05-18 国际壳牌研究有限公司 加氢催化剂
US8648225B2 (en) 2010-04-12 2014-02-11 Chevron Phillips Chemical Company Lp Process for hydrogenating highly unsaturated hydrocarbons and catalyst therefor
US20120209042A1 (en) * 2011-02-10 2012-08-16 Saudi Basic Industries Corporation Liquid Phase Hydrogenation of Alkynes
PL215952B1 (pl) 2011-05-05 2014-02-28 Politechnika Lodzka Sposób wytwarzania trójskladnikowej mieszanki naweglajacej i urzadzenie do wytwarzania trójskladnikowej mieszanki naweglajacej
US9617153B2 (en) * 2011-10-11 2017-04-11 Solvay Sa Process for producing hydrogen peroxide
JP6333249B2 (ja) * 2012-08-01 2018-05-30 ビーエーエスエフ ソシエタス・ヨーロピアBasf Se 酸化的脱水素化又はエポキシ化のための貴金属含有担持触媒
CN105732263B (zh) * 2014-12-12 2018-10-16 中国石油天然气股份有限公司 甲醇制烯烃装置中微量乙炔的选择加氢方法
US9758446B2 (en) 2015-11-16 2017-09-12 Chevron Phillips Chemical Company Lp Selective hydrogenation using a flow index
CN106944070A (zh) * 2017-02-27 2017-07-14 北京神雾环境能源科技集团股份有限公司 一种高浓度乙炔选择加氢制乙烯的非贵金属催化剂的合成及应用方法
US10232360B1 (en) * 2017-09-12 2019-03-19 Chevron Phillips Chemical Company, Lp Use of organic dopants to enhance acetylene hydrogenation catalysts
WO2020150354A1 (en) 2019-01-17 2020-07-23 Shell Oil Company A bimetallic nanoparticle-based catalyst, its use in selective hydrogenation, and a method of making the catalyst
US20240034699A1 (en) 2022-07-28 2024-02-01 Chevron Phillips Chemical Company, Lp Flexible Benzene Production Via Selective-Higher-Olefin Oligomerization of Ethylene

Family Cites Families (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3325556A (en) * 1964-05-18 1967-06-13 Universal Oil Prod Co Selective hydrogenation of acetylene in a mixture of acetylene and other unsaturated hydrocarbons
US3477962A (en) * 1966-05-06 1969-11-11 Pfizer & Co C Palladium-lead catalysts
US3489809A (en) * 1968-04-17 1970-01-13 Engelhard Min & Chem Selective hydrogenation with a catalyst on a honeycomb support
US3651167A (en) * 1970-08-03 1972-03-21 Universal Oil Prod Co Selective hydrogenation of c4-acetylenic hydrocarbons
AU475486B2 (en) * 1971-11-19 1976-08-26 Mitsubishi Chemical Industries Limited Process for hydrating an unsaturated nitrile
JPS5412435B2 (ko) * 1971-11-22 1979-05-23
US4009126A (en) * 1974-02-19 1977-02-22 Petro-Tex Chemical Corporation Catalyst for removing acetylenic impurities
US4658080A (en) * 1974-02-19 1987-04-14 Petro-Tex Chemical Corporation Acetylene removal process
US4513159A (en) * 1974-02-19 1985-04-23 Petro-Tex Chemical Corporation Acetylene removal process
US4644088A (en) * 1974-02-19 1987-02-17 Petro-Tex Chemical Corporation Acetylene removal process
JPS5136413A (en) * 1974-09-10 1976-03-27 Kuraray Co Fuhowaesuteru no seizoho
US4226809A (en) * 1979-08-07 1980-10-07 Phillips Petroleum Company Hydrogenation of unsaturated dinitriles using catalyst comprising reaction products of nickel compound and of a palladium compound each with an alkali metal borohydride
US4484015A (en) * 1981-05-06 1984-11-20 Phillips Petroleum Company Selective hydrogenation
US4404124A (en) * 1981-05-06 1983-09-13 Phillips Petroleum Company Selective hydrogenation catalyst
JPS58177153A (ja) * 1982-04-12 1983-10-17 Nissan Motor Co Ltd メタノ−ル改質用触媒
FR2536410B1 (fr) * 1982-11-24 1985-10-11 Pro Catalyse Procede d'hydrogenation selective des hydrocarbures acetyleniques d'une coupe d'hydrocarbures c4 renfermant du butadiene
KR900001368B1 (ko) * 1987-03-11 1990-03-09 한국과학 기술원 산화티탄 담지 팔라듐 촉매의 제조방법
FR2619391B1 (fr) * 1987-08-14 1990-01-12 Eurecat Europ Retrait Catalys Procede de reduction d'un catalyseur de raffinage avant sa mise en oeuvre
DE3736557A1 (de) * 1987-10-28 1989-05-11 Sued Chemie Ag Katalysator zur selektiven hydrierung von mehrfach ungesaettigten kohlenwasserstoffen
FR2642670B1 (fr) * 1989-02-07 1991-05-24 Eurecat Europ Retrait Catalys Procede de reduction d'un catalyseur de raffinage avant sa mise en oeuvr

Also Published As

Publication number Publication date
DE69522053D1 (de) 2001-09-13
SG32384A1 (en) 1996-08-13
DE69534206D1 (de) 2005-06-16
DE69534206T2 (de) 2006-01-12
ES2159585T3 (es) 2001-10-16
JPH08173807A (ja) 1996-07-09
AU667678B2 (en) 1996-04-04
MY113893A (en) 2002-06-29
KR100379870B1 (ko) 2003-08-19
DE69522053T2 (de) 2002-03-21
EP0689872B2 (en) 2013-12-11
AU2324695A (en) 1996-01-18
EP1110606B1 (en) 2005-05-11
EP0689872B1 (en) 2001-08-08
DE69522053T3 (de) 2014-07-03
ES2242660T3 (es) 2005-11-16
GR3037067T3 (en) 2002-01-31
EP0689872A1 (en) 1996-01-03
KR100414260B1 (en) 2004-01-07
EP1110606A1 (en) 2001-06-27
CA2151414C (en) 2000-01-25
US5488024A (en) 1996-01-30
US5510550A (en) 1996-04-23
JP4040700B2 (ja) 2008-01-30
CA2151414A1 (en) 1996-01-02

Similar Documents

Publication Publication Date Title
KR960003799A (ko) 수소첨가에 유용한 고체 촉매 조성물의 제조방법
KR100734762B1 (ko) 비닐 아세테이트 제조용 촉매 및 비닐 아세테이트의제조방법
Fukue et al. Direct synthesis of alkyl 2-alkynoates from alk-1-ynes, CO2, and bromoalkanes catalysed by copper (I) or silver (I) salt
Lloyd et al. Oxidations of olefins with alcoholic palladium (II) salts
US2004135A (en) Production of polyhydric alcohols
JPS5926336B2 (ja) 部分的水素化のための触媒
US3886219A (en) Process for preparing saturated alcohols
KR970011084B1 (ko) 촉매 조성물 및 이의 제조방법과 이들 조성물에 의한 1,1,2-트리클로로-1,2,2-트리플루오로에탄의 수소화 방법
US2930765A (en) Production of a supported catalyst
IL23403A (en) Dehydrogenation of hydrocarbons and catalyst therefor
US3739032A (en) Process for the preparation of unsaturated ethers
US3830834A (en) Process for the continuous preparation of vinyl acetate
US2930766A (en) Production of a supported catalyst
US4000207A (en) Isomerization of alpha-pinene to beta-pinene with neutralized alumina-supported mixed metal catalyst
Kagami et al. Formation of C (2)-oxygenated compounds from the reaction of CO and H 2 over alkali-metal doped rhodium catalysts under mild conditions
Mitsui et al. Stereochemistry and mechanism of the catalytic hydrogenation of dimethylcyclohexenes
US3974102A (en) Mixed metal catalyst for isomerization of alpha-pinene to beta-pinene
US4247723A (en) Preparation of dihydromyrcenol
US2886596A (en) Process for the production of cyclohexanone oxime
GB818314A (en) 2-butyne-1:4-diol
US4039584A (en) Catalytic cleavage of isobutyraldehyde
JP3939042B2 (ja) 飽和ケトン化合物の製造方法
JPH0430394B2 (ko)
US2426450A (en) Process for producing butadiene
US2837524A (en) Process for the manufacture of polymethyleneimines

Legal Events

Date Code Title Description
A201 Request for examination
E902 Notification of reason for refusal
A107 Divisional application of patent
E701 Decision to grant or registration of patent right
GRNT Written decision to grant
FPAY Annual fee payment

Payment date: 20120312

Year of fee payment: 10

LAPS Lapse due to unpaid annual fee