RU2005137698A - Совмещенный способ получения дифенола а из гидропероксида - Google Patents

Совмещенный способ получения дифенола а из гидропероксида Download PDF

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Publication number
RU2005137698A
RU2005137698A RU2005137698/04A RU2005137698A RU2005137698A RU 2005137698 A RU2005137698 A RU 2005137698A RU 2005137698/04 A RU2005137698/04 A RU 2005137698/04A RU 2005137698 A RU2005137698 A RU 2005137698A RU 2005137698 A RU2005137698 A RU 2005137698A
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Russia
Prior art keywords
decomposition
mass
stage
acetone
phenol
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RU2005137698/04A
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English (en)
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RU2339608C2 (ru
Inventor
Прамод Шанкар КУМБХАР (IN)
Прамод Шанкар КУМБХАР
Джегадиш ТХАМПЛ (IN)
Джегадиш ТХАМПЛ
Бхарат СИНГХ (IN)
Бхарат СИНГХ
Джон У. ФУЛМЕР (US)
Джон У. ФУЛМЕР
Прашант Анил ТАТАКЕ (IN)
Прашант Анил ТАТАКЕ
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Дженерал Электрик Компани (US)
Дженерал Электрик Компани
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Publication of RU2005137698A publication Critical patent/RU2005137698A/ru
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Publication of RU2339608C2 publication Critical patent/RU2339608C2/ru

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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C37/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring
    • C07C37/08Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring by decomposition of hydroperoxides, e.g. cumene hydroperoxide
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C37/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring
    • C07C37/11Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring by reactions increasing the number of carbon atoms
    • C07C37/20Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring by reactions increasing the number of carbon atoms using aldehydes or ketones
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C39/00Compounds having at least one hydroxy or O-metal group bound to a carbon atom of a six-membered aromatic ring
    • C07C39/12Compounds having at least one hydroxy or O-metal group bound to a carbon atom of a six-membered aromatic ring polycyclic with no unsaturation outside the aromatic rings
    • C07C39/15Compounds having at least one hydroxy or O-metal group bound to a carbon atom of a six-membered aromatic ring polycyclic with no unsaturation outside the aromatic rings with all hydroxy groups on non-condensed rings, e.g. phenylphenol
    • C07C39/16Bis-(hydroxyphenyl) alkanes; Tris-(hydroxyphenyl)alkanes
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/51Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by pyrolysis, rearrangement or decomposition
    • C07C45/53Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by pyrolysis, rearrangement or decomposition of hydroperoxides
    • 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
    • Y02P20/10Process efficiency
    • 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

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

Claims (10)

1. Способ получения дифенола А, включающий стадии:
(a) разложение гидропероксида кумена в присутствии кислотного катализатора из сульфатированного оксида металла для превращения гидропероксида кумена в массу после разложения, содержащую, главным образом, фенол и ацетон; и
(b) реакции массы после разложения, предпочтительно без промежуточной очистки, в присутствии катионитного катализатора, состоящего из катионообменной смолы и меркаптанового промотора или промотора в виде меркаптоалкановой кислоты для превращения фенола и ацетона в массе после разложения главным образом в дифенол А.
2. Способ по п.1, при котором массу после разложения, полученную на стадии (а), приводят во взаимодействие на стадии (b) без промежуточной очистки.
3. Способ по п.1 или 2, при котором стадию разложения гидропероксида кумена выполняют при температуре от 55 до 65°С.
4. Способ по п.1 или 2, дополнительно включающий стадию добавления фенола к массе или удаления ацетона из массы после разложения, образовавшейся на стадии (а), для достижения мольного отношения ацетон : фенол от 1:20 до 1:10.
5. Способ по п.4, при котором полученное мольное отношение ацетон : фенол равно 1:13.
6. Способ по любому одному из пп.1, 2 или 5, при котором стадию (b) выполняют при температуре от 40 до 100°С.
7. Способ по любому одному из пп.1, 2 или 5, при котором катионитный катализатор включает в качестве промотора пиридилэтилмеркаптан.
8. Способ по п.7, при котором пиридилэтилмеркаптан нагружают на катионообменную смолу в количестве от 20 до 70% по весу.
9. Способ по п.8, при котором пиридилэтилмеркаптан нагружают на катионообменную смолу в количестве 40% по весу.
10. Способ по любому одному из пп.1, 2, 5, 8 или 9, при котором катализатор является сульфатированным диоксидом циркония.
RU2005137698/04A 2003-06-04 2004-04-14 Совмещенный способ получения дифенола а из гидропероксида кумена RU2339608C2 (ru)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US10/250,107 2003-06-04
US10/250,107 US7154010B2 (en) 2003-06-04 2003-06-04 Integrated process for the production of bisphenol A from cumene hydroperoxide

Publications (2)

Publication Number Publication Date
RU2005137698A true RU2005137698A (ru) 2007-06-10
RU2339608C2 RU2339608C2 (ru) 2008-11-27

Family

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Family Applications (1)

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RU2005137698/04A RU2339608C2 (ru) 2003-06-04 2004-04-14 Совмещенный способ получения дифенола а из гидропероксида кумена

Country Status (8)

Country Link
US (1) US7154010B2 (ru)
EP (1) EP1636156A1 (ru)
JP (1) JP4790602B2 (ru)
KR (1) KR20060021338A (ru)
CN (1) CN100369877C (ru)
RU (1) RU2339608C2 (ru)
TW (1) TWI344456B (ru)
WO (1) WO2004108641A1 (ru)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007137021A2 (en) * 2006-05-16 2007-11-29 Shell Oil Company Catalysts comprising a combination of oxidized metals and a method for cleaving phenylalkyl hydroperoxides using the catalysts
US7417003B2 (en) * 2006-12-29 2008-08-26 Uop Llc Solid acid catalyst and process for decomposition of cumene hydroperoxide
US7902408B2 (en) * 2007-05-09 2011-03-08 Stone & Webster, Inc. BPA process improvement
US8803966B2 (en) 2008-04-24 2014-08-12 GM Global Technology Operations LLC Clear path detection using an example-based approach

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* Cited by examiner, † Cited by third party
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US3394089A (en) 1964-12-02 1968-07-23 Dow Chemical Co Ion exchange catalyst for the preparation of bisphenols
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Also Published As

Publication number Publication date
TWI344456B (en) 2011-07-01
JP4790602B2 (ja) 2011-10-12
RU2339608C2 (ru) 2008-11-27
KR20060021338A (ko) 2006-03-07
JP2006526627A (ja) 2006-11-24
EP1636156A1 (en) 2006-03-22
CN100369877C (zh) 2008-02-20
US20040249223A1 (en) 2004-12-09
TW200504001A (en) 2005-02-01
CN1798718A (zh) 2006-07-05
US7154010B2 (en) 2006-12-26
WO2004108641A1 (en) 2004-12-16

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