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RU2008129491A - METHOD FOR CLEANING STYRENE FROM PENYLACETHYLENE IMPURITIES - Google Patents

METHOD FOR CLEANING STYRENE FROM PENYLACETHYLENE IMPURITIES Download PDF

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Publication number
RU2008129491A
RU2008129491A RU2008129491/04A RU2008129491A RU2008129491A RU 2008129491 A RU2008129491 A RU 2008129491A RU 2008129491/04 A RU2008129491/04 A RU 2008129491/04A RU 2008129491 A RU2008129491 A RU 2008129491A RU 2008129491 A RU2008129491 A RU 2008129491A
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RU
Russia
Prior art keywords
catalyst
impurities
styrene
gold
penylacethylene
Prior art date
Application number
RU2008129491/04A
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Russian (ru)
Other versions
RU2385857C1 (en
Inventor
Владимир Валентинович Смирнов (RU)
Владимир Валентинович Смирнов
Сергей Александрович Николаев (RU)
Сергей Александрович Николаев
Original Assignee
Общество с ограниченной ответственностью "Старт-Катализатор" (RU)
Общество с ограниченной ответственностью "Старт-Катализатор"
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Priority to RU2008129491/04A priority Critical patent/RU2385857C1/en
Publication of RU2008129491A publication Critical patent/RU2008129491A/en
Application granted granted Critical
Publication of RU2385857C1 publication Critical patent/RU2385857C1/en

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Abstract

Способ очистки стирола от примесей фенилацетилена путем гидрирования молекулярным водородом при повышенной температуре в присутствии золотосодержащего катализатора, включающего гамма-оксид алюминия, отличающийся тем, что катализатор представляет собой частицы металлического золота средним размером 2-3 нм, и суммарное содержание золота в катализаторе составляет 0,01-0,03 мас.%; процесс ведут в газовой фазе при температуре 140-160°С.The method of purification of styrene from phenylacetylene impurities by hydrogenation with molecular hydrogen at elevated temperature in the presence of a gold-containing catalyst, including gamma-alumina, characterized in that the catalyst is a metal gold particles with an average size of 2-3 nm, and the total gold content in the catalyst is 0, 01-0.03 wt.%; the process is conducted in the gas phase at a temperature of 140-160 ° C.

Claims (1)

Способ очистки стирола от примесей фенилацетилена путем гидрирования молекулярным водородом при повышенной температуре в присутствии золотосодержащего катализатора, включающего гамма-оксид алюминия, отличающийся тем, что катализатор представляет собой частицы металлического золота средним размером 2-3 нм, и суммарное содержание золота в катализаторе составляет 0,01-0,03 мас.%; процесс ведут в газовой фазе при температуре 140-160°С. The method of purification of styrene from phenylacetylene impurities by hydrogenation with molecular hydrogen at elevated temperature in the presence of a gold-containing catalyst, including gamma-alumina, characterized in that the catalyst is a metal gold particles with an average size of 2-3 nm, and the total gold content in the catalyst is 0, 01-0.03 wt.%; the process is conducted in the gas phase at a temperature of 140-160 ° C.
RU2008129491/04A 2008-07-21 2008-07-21 Method of purifying styrene from phenylacetylene impurities RU2385857C1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
RU2008129491/04A RU2385857C1 (en) 2008-07-21 2008-07-21 Method of purifying styrene from phenylacetylene impurities

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
RU2008129491/04A RU2385857C1 (en) 2008-07-21 2008-07-21 Method of purifying styrene from phenylacetylene impurities

Publications (2)

Publication Number Publication Date
RU2008129491A true RU2008129491A (en) 2010-01-27
RU2385857C1 RU2385857C1 (en) 2010-04-10

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RU2008129491/04A RU2385857C1 (en) 2008-07-21 2008-07-21 Method of purifying styrene from phenylacetylene impurities

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Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2501606C1 (en) * 2012-11-06 2013-12-20 ФЕДЕРАЛЬНОЕ ГОСУДАРСТВЕННОЕ БЮДЖЕТНОЕ УЧРЕЖДЕНИЕ НАУКИ ИНСТИТУТ ОРГАНИЧЕСКОЙ ХИМИИ им. Н.Д. ЗЕЛИНСКОГО РОССИЙСКОЙ АКАДЕМИИ НАУК (ИОХ РАН) Catalyst for selective removal of acetylene hydrocarbon admixtures from ethylene monomers and method to this end
RU2536043C1 (en) * 2013-10-18 2014-12-20 ФЕДЕРАЛЬНОЕ ГОСУДАРСТВЕННОЕ БЮДЖЕТНОЕ УЧРЕЖДЕНИЕ НАУКИ ИНСТИТУТ ОРГАНИЧЕСКОЙ ХИМИИ им. Н.Д. ЗЕЛИНСКОГО РОССИЙСКОЙ АКАДЕМИИ НАУК (ИОХ РАН) Catalyst for hydroamination of acetylene hydrocarbons and method of hydroamination of acetylene hydrocarbons with thereof application
RU2536042C1 (en) * 2013-10-18 2014-12-20 ФЕДЕРАЛЬНОЕ ГОСУДАРСТВЕННОЕ БЮДЖЕТНОЕ УЧРЕЖДЕНИЕ НАУКИ ИНСТИТУТ ОРГАНИЧЕСКОЙ ХИМИИ им. Н.Д. ЗЕЛИНСКОГО РОССИЙСКОЙ АКАДЕМИИ НАУК (ИОХ РАН) Method of conversion of acetylene hydrocarbons

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU1039550A1 (en) * 1981-07-07 1983-09-07 Институт органического катализа и электрохимии АН КазССР Method of preparing palladium catalyst for hydrating phenylacetylene
FR2603578B1 (en) * 1986-09-10 1989-02-17 Inst Francais Du Petrole PROCESS FOR SELECTIVE HYDROGENATION OF PHENYL-ACETYLENE IN A STYRENE-RICH CUT
US7105711B2 (en) * 2003-07-31 2006-09-12 Fina Technology, Inc. Process for the selective hydrogenation of phenylacetylene

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RU2385857C1 (en) 2010-04-10

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Effective date: 20150722