FI117628B - Förfarande för framställning av fenol och fenolderivat - Google Patents

Förfarande för framställning av fenol och fenolderivat Download PDF

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Publication number
FI117628B
FI117628B FI964102A FI964102A FI117628B FI 117628 B FI117628 B FI 117628B FI 964102 A FI964102 A FI 964102A FI 964102 A FI964102 A FI 964102A FI 117628 B FI117628 B FI 117628B
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FI
Finland
Prior art keywords
benzene
phenol
catalyst
nitric oxide
reaction
Prior art date
Application number
FI964102A
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English (en)
Finnish (fi)
Other versions
FI964102A (sv
FI964102A0 (sv
Inventor
Gennady Ivanovich Panov
Alexandr Sergeevich Kharitonov
Galina Anatolievna Sheveleva
Original Assignee
Solutia Inc
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Publication date
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First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=20154683&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=FI117628(B) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Solutia Inc filed Critical Solutia Inc
Publication of FI964102A0 publication Critical patent/FI964102A0/sv
Publication of FI964102A publication Critical patent/FI964102A/sv
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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
    • C07C37/60—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring by oxidation reactions introducing directly hydroxy groups on a =CH-group belonging to a six-membered aromatic ring with the aid of other oxidants than molecular oxygen or their mixtures with molecular oxygen
    • 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
    • Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00—Capture or disposal of greenhouse gases
    • Y02C20/10—Capture or disposal of greenhouse gases of nitrous oxide (N2O)
    • 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)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Claims (10)

1. Förfarande för oxidering av en aromatisk före-ning under användning av kväveoxidul genom att bringa en 5 fast katalysator i kontakt med en gasformig blandning av den aromatiska föreningen och ett molärt underskott av kväveoxidul.
2. Förfarande enligt patentkrav 1, känneteck-nat av att kväveoxidulens och den aromatiska föreningens 10 molförhällande är inom omrädet 0,9-0,01.
3. Förfarande enligt patentkrav 1, känneteck-n a t av att den aromatiska föreningen är bensen eller sub-stituerat bensen.
4. Förfarande enligt patentkrav 1, känneteck-15 n at av att nämnda katalysator är en zeolit.
5. Förfarande enligt patentkrav 4, känneteck-nat av att nämnda katalysator är en ZSM-5- eller ZSM-11- zeolitkatalysator.
6. Förfarande enligt patentkrav 5, känneteck-20 n at av att nämnda aromatiska förening är bensen.
7. Förfarande enligt patentkrav 6, känneteck- :.**i n a t av att kväveoxidulens och den aromatiska föreningens • * · ϊ,,.ί molförhällande är inom omrädet 0,1-0,01. 'ϊ"ί 8. Förfarande enligt patentkrav 7, känneteck- ·;· 25 n a t av att den gasformiga blandningen föreligger i kon- • * · · • ·*; takt med nämnda katalysator vid en temperatur inom omrädet 250 - 600 °C. • « #
9. Förfarande enligt patentkrav 8, känneteck-n a t av att nämnda gasformiga blandning innehaller bensen, « · · "I 30 kväveoxidul och en eller flera gaser, som är valda ur en • · *"* grupp, som utgörs av helium, kväve, kväveoxid, kvävediox- * , id, koldioxid och argon. :*‘‘i 10. Förfarande enligt patentkrav 9, känneteck- * · * n a t av att nämnda katalysator är en surgjord ZSM-5- eller • t
35 ZSM-ll-zeolit innehällande järn. • · · • · • ·
FI964102A 1994-04-12 1996-10-11 Förfarande för framställning av fenol och fenolderivat FI117628B (sv)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
RU94013070 1994-04-12
RU9494013070A RU2058286C1 (ru) 1994-04-12 1994-04-12 Способ получения фенола или его производных
PCT/RU1995/000066 WO1995027691A1 (en) 1994-04-12 1995-04-12 Method for production of phenol and its derivatives
RU9500066 1995-04-12

Publications (3)

Publication Number Publication Date
FI964102A0 FI964102A0 (sv) 1996-10-11
FI964102A FI964102A (sv) 1996-12-11
FI117628B true FI117628B (sv) 2006-12-29

Family

ID=20154683

Family Applications (1)

Application Number Title Priority Date Filing Date
FI964102A FI117628B (sv) 1994-04-12 1996-10-11 Förfarande för framställning av fenol och fenolderivat

Country Status (17)

Country Link
US (1) US5756861A (sv)
EP (1) EP0755371B1 (sv)
JP (1) JP2961128B2 (sv)
KR (1) KR100231872B1 (sv)
CN (1) CN1071729C (sv)
AT (1) ATE182873T1 (sv)
AU (1) AU684948B2 (sv)
BR (1) BR9507370A (sv)
CA (1) CA2187656C (sv)
DE (1) DE69511256T2 (sv)
DK (1) DK0755371T3 (sv)
ES (1) ES2136288T3 (sv)
FI (1) FI117628B (sv)
PL (1) PL179735B1 (sv)
RU (1) RU2058286C1 (sv)
UA (1) UA44891C2 (sv)
WO (1) WO1995027691A1 (sv)

Families Citing this family (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5874646A (en) * 1996-08-07 1999-02-23 Solutia Inc. Preparation of phenol or phenol derivatives
US5892132A (en) * 1996-08-08 1999-04-06 Solutia Inc. Transport hydroxylation reactor
US5808167A (en) * 1996-08-20 1998-09-15 Solutia Inc. Selective introduction of active sites for hydroxylation of benzene
US5874647A (en) * 1996-08-20 1999-02-23 Solutia Inc. Benzene hydroxylation catalyst stability by acid treatment
KR100544044B1 (ko) * 1996-10-07 2006-01-23 솔루티아인코포레이티드 방향족 화합물 및 벤젠의 하이드록실화 방법 및 이를 위한 반응 혼합물
US6156938A (en) * 1997-04-03 2000-12-05 Solutia, Inc. Process for making phenol or phenol derivatives
RU2127721C1 (ru) 1997-07-29 1999-03-20 Институт органической химии им.Зелинского РАН Способ получения фенола и его производных
ES2167106T3 (es) * 1998-04-30 2002-05-01 Creavis Tech & Innovation Gmbh Procedimiento para preparar compuestos aromaticos que contienen grupos hidroxilo.
US6080226A (en) * 1998-09-30 2000-06-27 Uop Llc Nitrous oxide purification by pressure swing adsorption
AU2509400A (en) * 1999-01-20 2000-08-07 Solutia Inc. Hydroxylation of aromatic compounds at elevated pressures
US6265622B1 (en) 1999-02-26 2001-07-24 General Electric Company Method and composition for hydroxylation of aromatic substrates
US6232510B1 (en) 1999-02-26 2001-05-15 General Electric Company Method and composition for hydroxylation of aromatic substrates
EP1036761A1 (de) * 1999-03-16 2000-09-20 Phenolchemie GmbH & Co. KG Verfahren zur Herstellung von Lachgas
RU2155181C1 (ru) 1999-04-05 2000-08-27 Кустов Леонид Модестович Способ окисления бензола и/или толуола в фенол и/или крезолы
US6437197B1 (en) 2000-04-27 2002-08-20 Shell Oil Company Process for catalytic hydroxylation of aromatic hydrocarbons
US6548718B2 (en) 2000-04-27 2003-04-15 Shell Oil Company Process for catalytic hydroxylation of, saturated or unsaturated, aliphatic compounds
DE10133067A1 (de) * 2001-07-07 2003-01-16 Phenolchemie Gmbh & Co Kg Verfahren zur Hydroxylierung aromatischer Kohlenwasserstoffe
RU2228326C2 (ru) * 2002-05-24 2004-05-10 Институт катализа им. Г.К. Борескова СО РАН Способ получения дигидроксибензолов
RU2220947C1 (ru) * 2002-06-25 2004-01-10 Институт катализа им. Г.К. Борескова СО РАН Способ получения би- и полициклических кетонов и их производных
RU2219160C1 (ru) * 2002-06-25 2003-12-20 Институт катализа им. Г.К.Борескова СО РАН Способ получения карбонильных соединений из ди- и полиеновых циклических углеводородов и их производных
ITMI20050062A1 (it) * 2005-01-20 2006-07-21 Polimeri Europa Spa Processo per la preparazione di fenolo
CN102137832A (zh) * 2008-08-29 2011-07-27 巴斯夫欧洲公司 制备环酮的方法
CN102020535B (zh) * 2009-09-17 2014-04-02 北京化工大学 一氧化二氮氧化苯生产苯酚的方法
CZ301937B6 (cs) 2010-02-05 2010-08-04 Výzkumný ústav anorganické chemie, a. s. Zpusob výroby zeolitu pentasilové struktury s rízenou distribucí hliníkových atomu ve skeletu
CN113801001A (zh) 2014-10-02 2021-12-17 孟山都技术公司 制备2,5-二氯苯酚的方法
CN106588577B (zh) * 2015-10-19 2019-08-06 江苏福瑞康泰药业有限公司 五氟苯酚的合成方法

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4429176A (en) * 1982-02-08 1984-01-31 Mobil Oil Corporation Active zeolite catalysts of improved stability
IT1150699B (it) * 1982-03-19 1986-12-17 Anic Spa Procedimento per la ossidrilazione di idrocarburi aromatici
US4559314A (en) * 1982-03-22 1985-12-17 Mobil Oil Corporation Zeolite activation
US5098687A (en) * 1984-04-26 1992-03-24 Uop Substituted aluminosilicate compositions and process for preparing same
US4952385A (en) * 1987-03-02 1990-08-28 Georgia Tech Research Corp. Ferrisilicate molecular sieve and use as a catalyst
FR2630733B1 (fr) * 1988-05-02 1990-07-20 Rhone Poulenc Chimie Procede de preparations du phenol
FR2630734B1 (fr) * 1988-05-02 1990-07-27 Rhone Poulenc Chimie Procede de preparation de dihydroxybenzenes
FR2648810B1 (fr) * 1989-06-22 1992-02-28 Rhone Poulenc Chimie Procede de preparation de phenols
RU2010790C1 (ru) * 1989-08-11 1994-04-15 Институт катализа СО РАН Способ получения фенола или его производных
US5110995A (en) * 1991-03-12 1992-05-05 Institute Of Catalysis Preparation of phenol or phenol derivatives
DE4117511A1 (de) * 1991-05-29 1992-12-03 Vaw Ver Aluminium Werke Ag Verfahren zur modifizierung eines rein-anorganisch synthetisierten zeoliths vom pentasil-typ
JPH07110825B2 (ja) * 1993-02-03 1995-11-29 旭化成工業株式会社 フェノールの製造法
US5367099A (en) * 1993-05-28 1994-11-22 Mobil Oil Corp. Selective toluene disproportionation process (STDP) with ex situ selectivated zeolite catalyst
RU2074164C1 (ru) * 1994-04-12 1997-02-27 Институт катализа им.Г.К.Борескова СО РАН Способ получения фенола или его производных

Also Published As

Publication number Publication date
KR100231872B1 (ko) 1999-12-01
DE69511256T2 (de) 2000-02-24
US5756861A (en) 1998-05-26
BR9507370A (pt) 1997-09-23
PL316873A1 (en) 1997-02-17
DK0755371T3 (da) 2000-02-28
JP2961128B2 (ja) 1999-10-12
RU2058286C1 (ru) 1996-04-20
EP0755371B1 (en) 1999-08-04
PL179735B1 (pl) 2000-10-31
CN1071729C (zh) 2001-09-26
AU684948B2 (en) 1998-01-08
MX9604822A (es) 1998-05-31
ES2136288T3 (es) 1999-11-16
EP0755371A1 (en) 1997-01-29
WO1995027691A1 (en) 1995-10-19
AU2376895A (en) 1995-10-30
FI964102A (sv) 1996-12-11
UA44891C2 (uk) 2002-03-15
ATE182873T1 (de) 1999-08-15
DE69511256D1 (de) 1999-09-09
FI964102A0 (sv) 1996-10-11
CN1148844A (zh) 1997-04-30
CA2187656C (en) 2001-08-21
CA2187656A1 (en) 1995-10-19
JPH09511518A (ja) 1997-11-18

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