KR930021596A - 고순도 페놀의 제조방법 - Google Patents

고순도 페놀의 제조방법 Download PDF

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Publication number
KR930021596A
KR930021596A KR1019930005377A KR930005377A KR930021596A KR 930021596 A KR930021596 A KR 930021596A KR 1019930005377 A KR1019930005377 A KR 1019930005377A KR 930005377 A KR930005377 A KR 930005377A KR 930021596 A KR930021596 A KR 930021596A
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South Korea
Prior art keywords
phenol
crude
alumina
high purity
producing high
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KR1019930005377A
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English (en)
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KR960002596B1 (ko
Inventor
다쓰오 시라하다
데쓰오 이마무라
Original Assignee
다께바야시 쇼오고
미쓰이쎄끼유 가가꾸고오교오 가부시끼가이샤
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Application filed by 다께바야시 쇼오고, 미쓰이쎄끼유 가가꾸고오교오 가부시끼가이샤 filed Critical 다께바야시 쇼오고
Publication of KR930021596A publication Critical patent/KR930021596A/ko
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Publication of KR960002596B1 publication Critical patent/KR960002596B1/ko

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    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C37/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring
    • C07C37/68—Purification; separation; Use of additives, e.g. for stabilisation
    • C07C37/86—Purification; separation; Use of additives, e.g. for stabilisation by treatment giving rise to a chemical modification
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C39/00—Compounds having at least one hydroxy or O-metal group bound to a carbon atom of a six-membered aromatic ring
    • C07C39/02—Compounds having at least one hydroxy or O-metal group bound to a carbon atom of a six-membered aromatic ring monocyclic with no unsaturation outside the aromatic ring
    • C07C39/04—Phenol
    • 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
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

쿠멘 하이드로퍼옥사이드의 산분해생성물로 부터 얻어지고α-메틸스티렌 함량이 15중량%이하인 조페놀을 비표면적이 80- 400㎡/g 범위이고 하메트의 산도함수(Ho)에 의한 산강도가 3Ho6. 8인 산성r-알루미나로 접촉처리하여 조페놀증에 함유되어 있는 지방족 및 방향족 카보닐 화합물들을 조페놀중에 함유되어 있는α-메틸렌스티렌이 디머를 실질적으로 형성하지 않고 고비등화합물들로 변환한후에 증류에 의해서 페놀과 그와같이 형성된 고비등 화합물들을 분리시키는 고순도 페놀의 제조방법.

Description

고순도 페놀의 제조방법
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음

Claims (8)

  1. 쿠멘 하이드로퍼옥사이드의 산분해생성물로 부터 얻어지고α-메틸스티렌 함량이 15중%이하인 조페놀로부터 고순도의 페놀을 제조하는 방법에 있어서, (1) 비표면적 80-400㎡/g 범위이고 하메트의 산도함수(Ho)에 의한 산성도가 3Ho6. 8인 산성r-알루미나 매의 존재하에 상기 조페놀을 접촉처리하여조페놀증에 함유되어 있는 지방족 및 방향족카보닐 화합물을 조페놀에 함유되어 있는α-메틸스티렌이 디머를 실질적으로 형성함이 이 고뇌등화합물로 변환시키는 단계와. (2) 단계(1)에서 얻은 접촉처리생성물을 증류하여 페놀을 회수하는 단계로 구성된, 고순도페놀의 제조방법.
  2. 제1항에 있어서. 상기 조페놀을 150-300℃의 온도범위에서 접촉처리하는 것을 특징으로 하는 고순도 페놀의 제조방법.
  3. 제1항에 있어서, 상기 조페놀을 1~50분 동안 접촉처리하는 것을 특징으로 하는 고순도 페놀의 제조방법.
  4. 제1항에 있어서, 상기 산성r-알루미나의 산도함수(Ho)에 의한 산강도가 3Ho6. 8인 것을 특징으로 하는 고순도 페놀의 제조방법.
  5. 제1항에 있어서, 상기 산성r-알루미나가 150~300㎡/g범위의 비표면적을 갖는 것을 특징으로 하는 고순도페놀의 제조방법.
  6. 제1항에 있어서, 상기 조페놀을 기상으로 산성 r-알루미나로 접촉처리하는 것을 특징으로 하는 고순도 페놀의 제조방법.
  7. 제1항에 있어서, 상기 조페놀을 액상으로 산성 r-알루미나로 접촉처리하는 것을 특징으로 하는 고순도 페놀의 제조방법.
  8. 제1항에 있어서, 상기 접촉처리 생성물을 스팀증류 또는 유기용제 추출증류에 의해서 회수하는 것을 특징으로하는 고순도 페놀의 제조방법.
    ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
KR1019930005377A 1992-04-03 1993-03-31 고순도 페놀의 제조방법 KR960002596B1 (ko)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP4082200A JPH05286879A (ja) 1992-04-03 1992-04-03 高純度フェノールの製造方法
JP92-82200 1992-04-03

Publications (2)

Publication Number Publication Date
KR930021596A true KR930021596A (ko) 1993-11-22
KR960002596B1 KR960002596B1 (ko) 1996-02-23

Family

ID=13767788

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019930005377A KR960002596B1 (ko) 1992-04-03 1993-03-31 고순도 페놀의 제조방법

Country Status (9)

Country Link
US (1) US5264636A (ko)
EP (1) EP0568817B1 (ko)
JP (1) JPH05286879A (ko)
KR (1) KR960002596B1 (ko)
CN (1) CN1083042A (ko)
CA (1) CA2093284A1 (ko)
DE (1) DE69308924T2 (ko)
SG (1) SG59970A1 (ko)
TW (1) TW315365B (ko)

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Publication number Priority date Publication date Assignee Title
RU2108318C1 (ru) * 1994-03-01 1998-04-10 Закошанский Владимир Михайлович СПОСОБ ПОЛУЧЕНИЯ ФЕНОЛА, АЦЕТОНА И α МЕТИЛСТИРОЛА
US5504251A (en) * 1995-03-09 1996-04-02 General Electric Company Co-cracking of BPA and phenol process tars
DE10060505A1 (de) * 2000-12-06 2003-01-30 Phenolchemie Gmbh & Co Kg Verfahren zur Abtrennung von Phenol aus einem Gemisch, welches zumindest Hydroxyaceton, Cumol, Wasser und Phenol aufweist
US6388144B1 (en) 2001-06-15 2002-05-14 Sunoco, Inc. (R&M) Method for reducing methylbenzofuran levels in high purity phenol
US6576798B1 (en) 2001-11-29 2003-06-10 General Electric Company Method and system for purifying cumene hydroperoxide cleavage products
US6573408B1 (en) 2001-11-29 2003-06-03 General Electric Company System and method for purifying cumene hydroperoxide cleavage products
AU2003222202A1 (en) * 2002-02-08 2003-09-02 General Electric Company Process and catalyst for purifying phenol
RU2217408C2 (ru) * 2002-02-08 2003-11-27 Общество с ограниченной ответственностью "Петрофенол" Способ и катализатор очистки фенола
RU2217409C2 (ru) * 2002-02-08 2003-11-27 Общество с ограниченной ответственностью "Петрофенол" Способ и катализатор получения паракумилфенола
US7205442B2 (en) * 2003-02-06 2007-04-17 Shell Oil Company Method of making high purity phenol
US7019180B2 (en) * 2003-02-06 2006-03-28 Shell Oil Company Method of purifying phenol
US7034192B2 (en) 2004-03-24 2006-04-25 Sunoco Inc. (R&M) Method for removal of acetol from phenol
WO2006087943A1 (ja) * 2005-02-21 2006-08-24 Mitsui Chemicals, Inc. フェノール類の精製方法
CN100363344C (zh) * 2005-05-25 2008-01-23 中国石油天然气股份有限公司 一种用于提纯过氧化氢异丙苯的活性组合物及其应用
US9403029B2 (en) * 2007-07-18 2016-08-02 Visualase, Inc. Systems and methods for thermal therapy
SA113340468B1 (ar) * 2012-04-13 2015-07-07 ميتسوي كيميكالز، انك. عملية لتنقية الفينول
JP6194827B2 (ja) * 2014-03-19 2017-09-13 三菱ケミカル株式会社 フェノールの色相評価方法
CN115260003A (zh) * 2022-07-22 2022-11-01 煤炭科学技术研究院有限公司 一种煤炭热解/气化粗酚除杂方法及除杂系统

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DE134427C (ko) *
GB802054A (en) * 1955-07-16 1958-09-24 Ruetgerswerke Ag Improvements relating to the recovery of pure phenol from crude phenol
GB865677A (en) * 1958-03-04 1961-04-19 Distillers Co Yeast Ltd Purification of phenol
DE1668952A1 (de) * 1968-01-13 1969-11-27 Phenolchemie Gmbh Verfahren zur Gewinnung von Reinphenolen aus Rohphenolen,die bei der Spaltung von Hydroperoxiden alkylaromatischer Kohlenwasserstoffe erhalten worden sind
CA935441A (en) * 1971-03-11 1973-10-16 Union Carbide Corporation Process for the purification and recovery of an aromatic hydroxyl compound
JPS6327446A (ja) * 1986-07-21 1988-02-05 Mitsui Petrochem Ind Ltd フエノ−ル蒸留残渣からの有用物質の回収方法

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Publication number Publication date
DE69308924D1 (de) 1997-04-24
US5264636A (en) 1993-11-23
CN1083042A (zh) 1994-03-02
DE69308924T2 (de) 1997-07-31
SG59970A1 (en) 1999-02-22
EP0568817A2 (en) 1993-11-10
KR960002596B1 (ko) 1996-02-23
EP0568817B1 (en) 1997-03-19
EP0568817A3 (en) 1995-07-26
JPH05286879A (ja) 1993-11-02
CA2093284A1 (en) 1993-10-04
TW315365B (ko) 1997-09-11

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