KR927003495A - 에테르의 제조방법 - Google Patents

에테르의 제조방법 Download PDF

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Publication number
KR927003495A
KR927003495A KR1019920701231A KR920701231A KR927003495A KR 927003495 A KR927003495 A KR 927003495A KR 1019920701231 A KR1019920701231 A KR 1019920701231A KR 920701231 A KR920701231 A KR 920701231A KR 927003495 A KR927003495 A KR 927003495A
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KR
South Korea
Prior art keywords
zeolite
olefin
ray diffraction
diffraction pattern
alcohol
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KR1019920701231A
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English (en)
Other versions
KR0161298B1 (ko
Inventor
케이 벨 웰돈
오토 하아그 웨너
오웬 말러 데이비드
Original Assignee
에드워드 에이취. 발란스
모빌오일 코퍼레이션
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Publication of KR927003495A publication Critical patent/KR927003495A/ko
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Publication of KR0161298B1 publication Critical patent/KR0161298B1/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
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
    • C07C2/02—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons
    • C07C2/04—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation
    • C07C2/06—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation of alkenes, i.e. acyclic hydrocarbons having only one carbon-to-carbon double bond
    • C07C2/08—Catalytic processes
    • C07C2/12—Catalytic processes with crystalline alumino-silicates or with catalysts comprising molecular sieves
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C41/00—Preparation of ethers; Preparation of compounds having groups, groups or groups
    • C07C41/01—Preparation of ethers
    • C07C41/05—Preparation of ethers by addition of compounds to unsaturated compounds
    • C07C41/06—Preparation of ethers by addition of compounds to unsaturated compounds by addition of organic compounds only
    • 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
    • C07C2529/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups C07C2529/08 - C07C2529/65

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

Abstract

내용 없음

Description

에테르의 제조방법
[도면의 간단한 설명]
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음

Claims (12)

  1. 표 I
    표 II
    명세서중의 표 I 에 기재된 라인을 갖는 X-선 회절 패턴을 나타내는 다공성의 산성 합성 결정성 제올라이트를 촉매로 사용하여 에테르화 반응 조건하에서 적어도 하나의 올레핀을 적어도 하나의 알콜과 반응시킴을 특징으로 하여 에테르 또는 에테르 혼합물을 제조하는 방법.
  2. 제1항에 있어서, 제올라이트가 명세서중의 표 II에 기재된 라인을 갖는 X-선 회절 패턴을 나타내는 방법.
  3. 제1항에 있어서, 제올라이트가 명세서중의 표 III에 기재된 라인을 갖는 X-선 회절 패턴을 나타내는 방법.
  4. 제1항에 있어서, 제올라이트가 명세서중의 표 VI에 기재된 라인을 갖는 X-선 회절 패턴을 나타내는 방법.
  5. 제1 내지 4항중의 어느 하나에 있어서, 제올라이트가 사이클로헥산 증기의 경우에는 4.5 중량% 이상이고, n-헥산 증기의 졍우에는 10중량% 이상인 평형 흡착 용량을 갖는 방법.
  6. 제l 내지 4항중의 어느 하나에 있어서, 제올라이트가 몰관계식 X2O3: (n)YO2인 조성을 가지며, 여기에서 n은 적어도 10이고 X는 3가 윈소이며 Y가 4가 윈소인 방법.
  7. 제6항에 있어서, X가 알루미늄을 포함하며 Y가 실리콘을 포함하는 방법.
  8. 제1 내지 4항중의 어느 하나에 있어서, 올레핀이 3 내지 10개의 탄소원자를 갖는 방법.
  9. 제8항에 있어서, 올레핀이 이소부텐 또는 이소펜텐인 방법.
  10. 제8항에 있어서, 알콜이 8개 이하의 탄소원자를 갖는 방법.
  11. 제9항에 있어서, 알콜이 메탄올, 에탄올, n-프로판올, 이소프로판올 부탄올 또는 이들의 혼합물인 방법.
  12. 제1 내지 4항중의 어느 하나에 있어서, 에테르화 반응 조건이 20 내지 200℃의 온도, 100 내지 20260kpa (1 내지 200 가압)의 총시스템 압력 및 0.1 내지 5의 올레핀/알콜 몰비율인 방법.
    ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
KR1019920701231A 1989-12-26 1990-04-09 에테르의 제조방법 KR0161298B1 (ko)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US07/456,702 US4962239A (en) 1988-10-06 1989-12-26 Process for preparing ethers
US456,702 1989-12-26
PCT/US1990/001922 WO1991009829A1 (en) 1989-12-26 1990-04-09 Process for preparing an ether

Publications (2)

Publication Number Publication Date
KR927003495A true KR927003495A (ko) 1992-12-18
KR0161298B1 KR0161298B1 (ko) 1999-01-15

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019920701231A KR0161298B1 (ko) 1989-12-26 1990-04-09 에테르의 제조방법

Country Status (13)

Country Link
US (1) US4962239A (ko)
EP (1) EP0507770B1 (ko)
JP (1) JP2806630B2 (ko)
KR (1) KR0161298B1 (ko)
AT (1) ATE126192T1 (ko)
AU (1) AU632803B2 (ko)
CA (1) CA2072102A1 (ko)
DD (1) DD298379A5 (ko)
DE (1) DE69021588T2 (ko)
DK (1) DK0507770T3 (ko)
ES (1) ES2075204T3 (ko)
WO (1) WO1991009829A1 (ko)
ZA (1) ZA904078B (ko)

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US8927769B2 (en) 2012-08-21 2015-01-06 Uop Llc Production of acrylic acid from a methane conversion process
US9023255B2 (en) 2012-08-21 2015-05-05 Uop Llc Production of nitrogen compounds from a methane conversion process
US9370757B2 (en) 2012-08-21 2016-06-21 Uop Llc Pyrolytic reactor
US9434663B2 (en) 2012-08-21 2016-09-06 Uop Llc Glycols removal and methane conversion process using a supersonic flow reactor
US8933275B2 (en) * 2012-08-21 2015-01-13 Uop Llc Production of oxygenates from a methane conversion process
US9656229B2 (en) 2012-08-21 2017-05-23 Uop Llc Methane conversion apparatus and process using a supersonic flow reactor
US9308513B2 (en) 2012-08-21 2016-04-12 Uop Llc Production of vinyl chloride from a methane conversion process
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Also Published As

Publication number Publication date
CA2072102A1 (en) 1991-06-27
EP0507770B1 (en) 1995-08-09
JP2806630B2 (ja) 1998-09-30
EP0507770A1 (en) 1992-10-14
DE69021588D1 (de) 1995-09-14
DE69021588T2 (de) 1996-01-18
ES2075204T3 (es) 1995-10-01
WO1991009829A1 (en) 1991-07-11
ATE126192T1 (de) 1995-08-15
ZA904078B (en) 1992-01-29
JPH05502855A (ja) 1993-05-20
AU632803B2 (en) 1993-01-14
DK0507770T3 (da) 1995-12-11
EP0507770A4 (en) 1993-03-31
KR0161298B1 (ko) 1999-01-15
AU5428790A (en) 1991-07-24
DD298379A5 (de) 1992-02-20
US4962239A (en) 1990-10-09

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