KR970701707A - 1,2-부틸렌 산화물의 제조 방법(Process for Preparing 1,2-Butylene Oxide) - Google Patents

1,2-부틸렌 산화물의 제조 방법(Process for Preparing 1,2-Butylene Oxide)

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Publication number
KR970701707A
KR970701707A KR1019960704946A KR19960704946A KR970701707A KR 970701707 A KR970701707 A KR 970701707A KR 1019960704946 A KR1019960704946 A KR 1019960704946A KR 19960704946 A KR19960704946 A KR 19960704946A KR 970701707 A KR970701707 A KR 970701707A
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elements
support
catalyst
periodic table
subgroup
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KR1019960704946A
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English (en)
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크리스토프 지크바르트
프란쯔 요세프 브렉커
롤프 피셔
페터 링겔바흐
Original Assignee
랑핑거, 비베르바흐
바스프 악티엔게젤샤프트
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Publication of KR970701707A publication Critical patent/KR970701707A/ko

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    • 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
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/34—Irradiation by, or application of, electric, magnetic or wave energy, e.g. ultrasonic waves ; Ionic sputtering; Flame or plasma spraying; Particle radiation
    • B01J37/341—Irradiation by, or application of, electric, magnetic or wave energy, e.g. ultrasonic waves ; Ionic sputtering; Flame or plasma spraying; Particle radiation making use of electric or magnetic fields, wave energy or particle radiation
    • B01J37/347—Ionic or cathodic spraying; Electric discharge
    • 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
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02—Impregnation, coating or precipitation
    • B01J37/0215—Coating
    • B01J37/0225—Coating of metal substrates
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D301/00—Preparation of oxiranes
    • 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • B01J23/44—Palladium
    • 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • B01J23/46—Ruthenium, rhodium, osmium or iridium
    • B01J23/464—Rhodium
    • 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/48—Silver or gold
    • B01J23/52—Gold

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Plasma & Fusion (AREA)
  • Health & Medical Sciences (AREA)
  • Optics & Photonics (AREA)
  • Toxicology (AREA)
  • Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Medicines Containing Material From Animals Or Micro-Organisms (AREA)
  • Cosmetics (AREA)
  • Agricultural Chemicals And Associated Chemicals (AREA)
  • Saccharide Compounds (AREA)

Abstract

본 발명의 방법은 하나 이상의 촉진제 원소들의 존재 또는 부재하의 주기율표의 아족 I, Ⅶ 또는 Ⅷ의 원소, 또는 다수의 이들 원소들의 혼합물로 이루어지며, 이들 원소 및 촉진제는 진공 증착기술에 의해 금속박 또는 금망의 지지체에 도포되어 있는 촉매를 사용하는 것을 특징으로 하는, 불균일 촉매상에서 비닐옥시란의 촉매 수소화반응에 의한 1,2-부틸렌 산화물의 제조 방법에 관한 것이다.

Description

1,2-부틸렌 산화물의 제조 방법(Process for Preparing 1,2-Butylene Oxide)
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음

Claims (8)

  1. 하나 이상의 촉진제 원소들의 존재 또는 부재하의 주기율표의 아족 I, Ⅶ 또는 Ⅷ의 원소, 또는 다수의 이들 원소들의 혼합물로 이루어지며, 이들 원소 및 촉진제는 진공 증착기술에 의해 금속박 또는 금망의 지지체에 도포되어 있는 촉매를 사용하는 것을 특징으로 하는, 불균일 촉매상에서 비닐옥시란의 촉매 수소화반응에 의한 1,2-부틸렌 산화물의 제조 방법.
  2. 제1항에 있어서, 사용된 촉매가 촉진제로서 주기율표의 주족 Ⅳ 또는 아족 Ⅱ 또는 Ⅳ 중 하나 이상의 원소들을 함유함을 특징으로 하는 방법.
  3. 제1 또는 2항에 있어서, 사용된 금속박 또는 금망 지지체가 재료 번호 1.4767, 1.4401 또는 1.4301을 가지는 재료중에 있음을 특징으로 하는 방법.
  4. 제1 내지 3항 중 어느 한 항에 있어서, 지지체가 촉매적으로 활성있는 원소들이 사용되기 전에 600 내지 1100℃이 공기중에서 가열됨을 특징으로 하는 방법.
  5. 제1 내지 4항 중 어느 한 항에 있어서, 사용된 촉매가 금속 지지체에 도포된 주기율표의 아족 I, Ⅶ 또는 Ⅷ중 하나 이상의 원소들을 각 경우에 지지체의 면적(㎡)당 1 내지 300mg의 양으로 포함함을 특징으로 하는 방법.
  6. 제1 내지 5항 중 어느 한 항에 있어서, 사용된 촉매가 주기율표의 아족 I, Ⅶ 또는 Ⅷ의 원소들은 물론, 추가로 금속 지지체에 도포되는 촉진제 원소들을 각 경우에 지지체의 면적(㎡)당 1 내지 300mg의 양으로 포함함을 특징으로 하는 방법.
  7. 제1 내지 6항 중 어느 한 항에 있어서, 사용된 촉매가 촉매적으로 활성있는 원소들이 진공 증착기술에 의해 도포된 후에 20 내지 800℃에서 공기중에서 조절되는 것을 특징으로 하는 방법.
  8. 제1 내지 7항 중 어느 한 항에 있어서, 사용된 촉매가 사용전에 20 내지 300℃에서 수소를 사용하여 환원되는 것을 특징으로 하는 방법.
    ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
KR1019960704946A 1994-03-07 1995-02-23 1,2-부틸렌 산화물의 제조 방법(Process for Preparing 1,2-Butylene Oxide) KR970701707A (ko)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE4407486A DE4407486A1 (de) 1994-03-07 1994-03-07 Verfahren zur Herstellung von 1,2-Butylenoxid
DEP4407486.7 1994-03-07
PCT/EP1995/000656 WO1995024401A2 (de) 1994-03-07 1995-02-23 Verfahren zur herstellung von 1,2-butylenoxid

Publications (1)

Publication Number Publication Date
KR970701707A true KR970701707A (ko) 1997-04-12

Family

ID=6512032

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019960704946A KR970701707A (ko) 1994-03-07 1995-02-23 1,2-부틸렌 산화물의 제조 방법(Process for Preparing 1,2-Butylene Oxide)

Country Status (11)

Country Link
US (2) US5869707A (ko)
EP (1) EP0749431B1 (ko)
JP (1) JPH09509950A (ko)
KR (1) KR970701707A (ko)
CN (1) CN1096452C (ko)
AT (1) ATE158285T1 (ko)
DE (2) DE4407486A1 (ko)
DK (1) DK0749431T3 (ko)
ES (1) ES2109100T3 (ko)
GR (1) GR3025709T3 (ko)
WO (1) WO1995024401A2 (ko)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19532645A1 (de) * 1995-09-05 1997-03-06 Basf Ag Verfahren zur selektiven Hydrierung von Vinyloxiran zu Butylenoxid
DE19602710A1 (de) * 1996-01-26 1997-07-31 Basf Ag Verfahren zur selektiven Hydrierung von Vinyloxiran zu 1,2-Butylenoxid an Heterogenkatalysatoren
US6180559B1 (en) 1999-03-02 2001-01-30 Eastman Chemical Company Supported catalysts and catalyst support materials and process for the manufacture of 1,2-epoxybutane
US8949187B1 (en) * 2008-05-30 2015-02-03 Symantec Corporation Systems and methods for creating and managing backups based on health information
CN109513445B (zh) * 2018-11-08 2022-05-13 中国科学院工程热物理研究所 三元金属氧化物薄膜催化剂及其制备方法

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2561984A (en) * 1949-04-25 1951-07-24 Phillips Petroleum Co Production of primary alcohols and aldehydes
DE2431929C3 (de) * 1974-07-03 1981-04-02 Basf Ag, 6700 Ludwigshafen Katalysator zur partiellen Hydrierung
US4132668A (en) * 1977-04-06 1979-01-02 Gryaznov Vladimir M Method of preparing a hydrogen-permeable membrane catalyst on a base of palladium or its alloys for the hydrogenation of unsaturated organic compounds
EP0053884A1 (en) * 1980-11-27 1982-06-16 Johnson Matthey Public Limited Company Three dimensional interstitial catalyst supports, its manufacture and use
US4560817A (en) * 1984-03-02 1985-12-24 Phillips Petroleum Company Hydrogenation catalyst
US4772578A (en) * 1986-02-04 1988-09-20 The Dow Chemical Company Method of preparing supported catalysts
US4990377A (en) * 1988-05-02 1991-02-05 Pcr Group, Inc. Buffered silane emulsions having low volatile organic compounds when cured
DE3926561A1 (de) * 1989-08-11 1991-02-14 Basf Ag Palladiumkatalysatoren
US5077418A (en) * 1990-05-03 1991-12-31 Eastman Kodak Company Process for the selective hydrogenation γ,δ-epoxyalkenes to epoxyalkanes
US5117013A (en) * 1990-05-03 1992-05-26 Eastman Kodak Company Process for the selective hydrogenation γ, δ-epoxyalkenes to epoxyalkanes
JPH04354544A (ja) * 1991-05-31 1992-12-08 Hideo Kameyama 触媒体
DE4209631A1 (de) * 1992-03-25 1993-09-30 Basf Ag Monolithischer Trägerkatalysator, Verfahren zu seiner Herstellung und seine Verwendung
DE4333293A1 (de) * 1993-09-30 1995-04-06 Basf Ag Verfahren zur selektiven Hydrierung von Butindiol-1,4 zu Buten-2-diol-1,4 und dafür geeigneter Katalysator

Also Published As

Publication number Publication date
DK0749431T3 (da) 1997-10-20
GR3025709T3 (en) 1998-03-31
ES2109100T3 (es) 1998-01-01
WO1995024401A2 (de) 1995-09-14
ATE158285T1 (de) 1997-10-15
CN1096452C (zh) 2002-12-18
US5869707A (en) 1999-02-09
CN1145069A (zh) 1997-03-12
EP0749431B1 (de) 1997-09-17
DE59500687D1 (de) 1997-10-23
EP0749431A1 (de) 1996-12-27
US6002027A (en) 1999-12-14
DE4407486A1 (de) 1995-09-14
WO1995024401A3 (de) 1995-10-05
JPH09509950A (ja) 1997-10-07

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