ES2184741T3 - Arsina como moderador en la conversion de acetileno. - Google Patents

Arsina como moderador en la conversion de acetileno.

Info

Publication number
ES2184741T3
ES2184741T3 ES93911189T ES93911189T ES2184741T3 ES 2184741 T3 ES2184741 T3 ES 2184741T3 ES 93911189 T ES93911189 T ES 93911189T ES 93911189 T ES93911189 T ES 93911189T ES 2184741 T3 ES2184741 T3 ES 2184741T3
Authority
ES
Spain
Prior art keywords
acetylene
moderator
current
hydrogenation
arsina
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
ES93911189T
Other languages
English (en)
Inventor
David Robert Slim
Edgar Lucian Mohundro
Stephen Mark Mayo
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ExxonMobil Chemical Patents Inc
Original Assignee
ExxonMobil Chemical Patents Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by ExxonMobil Chemical Patents Inc filed Critical ExxonMobil Chemical Patents Inc
Application granted granted Critical
Publication of ES2184741T3 publication Critical patent/ES2184741T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G70/00—Working-up undefined normally gaseous mixtures obtained by processes covered by groups C10G9/00, C10G11/00, C10G15/00, C10G47/00, C10G51/00
    • C10G70/02—Working-up undefined normally gaseous mixtures obtained by processes covered by groups C10G9/00, C10G11/00, C10G15/00, C10G47/00, C10G51/00 by hydrogenation
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00—Purification; Separation; Use of additives
    • C07C7/148—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound
    • C07C7/163—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound by hydrogenation
    • C07C7/167—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound by hydrogenation for removal of compounds containing a triple carbon-to-carbon bond

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)
  • Diaphragms For Electromechanical Transducers (AREA)
  • Crystals, And After-Treatments Of Crystals (AREA)
  • Magnetic Resonance Imaging Apparatus (AREA)

Abstract

LA PRESENTE INVENCION DESCRIBE UN PROCESO PARA ELIMINAR EL ACETILENO DE UNA CORRIENTE DE HIDROCARBURO QUE COMPRENDE LA EXPOSICION DE LA CORRIENTE A UN CATALIZADOR DE HIDROGENACION EN PRESENCIA DE UN MODIFICADOR DE UN CONVERTIDOR DE ACETILENO, QUE SOBRE TODO PERMANECE SOBRE EL CATALIZADOR Y PRINCIPALMENTE EMIGRA DENTRO DE LA CORRIENTE. LA EXPOSICION SE HACE BAJO CONDICIONES QUE SON EFICACES PARA SOPORTAR HIDROGENACION DEL ACETILENO CON SELECTIVIDAD REALZADA. EL MODERADOR, QUE PUEDE SER ARSINA O FOSFINA, ES USADO A UN NIVEL DE CONCENTRACION BAJA Y SIRVE PARA PREVENIR EL EMBALAMIENTO DE LA TEMPERATURA DURANTE LA REACCION EXOTERMICA DE HIDROGENACION DEL ACETILENO. CONTROLANDO LA PRESENCIA DE NIVELES DE MODERADOR A UN NIVEL RELATIVAMENTE BAJO, SE IMPIDE EL EMBALAMIENTO DE LA TEMPERATURA DURANTE LA REACCION ALTAMENTE EXOTERMICA DE HIDROGENACION DEL ACETILENO, MIENTRAS SE MANTIENEN NIVELES ACEPTABLES DE ACTIVIDAD DEL CATALIZADOR PARA FINES DE HIDROGENACION DEL ACETILENO.
ES93911189T 1992-05-12 1993-05-12 Arsina como moderador en la conversion de acetileno. Expired - Lifetime ES2184741T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US88190292A 1992-05-12 1992-05-12

Publications (1)

Publication Number Publication Date
ES2184741T3 true ES2184741T3 (es) 2003-04-16

Family

ID=25379434

Family Applications (1)

Application Number Title Priority Date Filing Date
ES93911189T Expired - Lifetime ES2184741T3 (es) 1992-05-12 1993-05-12 Arsina como moderador en la conversion de acetileno.

Country Status (8)

Country Link
US (1) US5463154A (es)
EP (1) EP0650516B1 (es)
JP (1) JP2784693B2 (es)
AU (1) AU678553B2 (es)
CA (1) CA2135610C (es)
DE (1) DE69332453T2 (es)
ES (1) ES2184741T3 (es)
WO (1) WO1993023499A1 (es)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5880320A (en) * 1997-08-05 1999-03-09 Netzer; David Combination process for manufacturing ethylene ethylbenzene and styrene
DE19840372A1 (de) * 1998-09-04 2000-03-09 Basf Ag Katalysator und Verfahren zur Reinigung von Stoffströmen
US6111156A (en) * 1998-11-10 2000-08-29 Nova Chemicals (International) S.A. Integrated high temperature high conversion olefin/polyolefin process
CN1097480C (zh) * 1999-06-25 2003-01-01 中国石油化工集团公司 炔烃选择加氢催化剂
EP2376224A1 (en) 2008-12-18 2011-10-19 Saudi Basic Industries Corporation Selective catalytic hydrogenation of alkynes to corresponding alkenes
MY171450A (en) * 2010-12-22 2019-10-15 Tpc Group Llc Process for selective removal of acetylenes from gaseous streams

Family Cites Families (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2268454A (en) * 1936-07-07 1941-12-30 Gen Motors Corp Washing machine
US2381198A (en) * 1942-03-23 1945-08-07 Phillips Petroleum Co Catalytic polymerization of olefins
US2837587A (en) * 1954-08-20 1958-06-03 Phillips Petroleum Co Purification of olefin-rich feed prior to polymerization
GB1135979A (en) * 1965-06-11 1968-12-11 Ici Ltd Hydrogenation process
GB1121643A (en) * 1966-02-07 1968-07-31 Ici Ltd Hydrogenation process
GB1182353A (en) * 1966-02-07 1970-02-25 Montedison Spa Cobalt Hydrocarbonyls
GB1183373A (en) * 1966-03-04 1970-03-04 Montedison Spa Cobalt Hydro-Phosphin-Carbonyls
GB1154937A (en) * 1966-08-10 1969-06-11 Ici Ltd Hydrogenation Process
GB1285871A (en) * 1968-06-17 1972-08-16 Ici Ltd Transition metal tetrahydridoaluminates
US3697448A (en) * 1970-06-08 1972-10-10 Phillips Petroleum Co Selective isomerization employing metal arsenide catalyst
US3787511A (en) * 1970-06-08 1974-01-22 Phillips Petroleum Co Selective hydrogenation employing nickel arsenide catalyst
US3917737A (en) * 1970-07-09 1975-11-04 Atlantic Richfield Co Catalytic hydrogenation process
US3697615A (en) * 1971-02-08 1972-10-10 Phillips Petroleum Co Hydrogenation of olefin hydrocarbons using rhodium or iridium halide complexes with metal halides
GB1378747A (en) * 1972-01-17 1974-12-27 British Petroleum Co Hydrogenation catalysts
US3900526A (en) * 1972-05-02 1975-08-19 Phillips Petroleum Co Selective removal of 1,2 polyenes and acetylenic compounds from conjugated-diene feed using a nickel, iron or cobalt arsenide catalyst
US4020119A (en) * 1973-08-23 1977-04-26 Phillips Petroleum Company Selective hydrogenation process
US4227025A (en) * 1979-02-13 1980-10-07 Phillips Petroleum Company Reactivation of arsenic-poisoned noble metal catalyst for removal of acetylene
US4377503A (en) * 1980-12-29 1983-03-22 Mobil Oil Corporation Shape selective metallic catalysis
DE3121927A1 (de) * 1981-06-03 1982-12-23 Wacker-Chemie GmbH, 8000 München Verfahren zur herstellung von uebergangsmetall-komplexen
US4605812A (en) * 1984-06-05 1986-08-12 Phillips Petroleum Company Process for removal of arsenic from gases
US4645849A (en) * 1985-01-22 1987-02-24 General Electric Company Hydrogenation of unsaturated hydrocarbons with cyclometallated transition metal catalysts
GB2171719B (en) * 1985-02-26 1989-02-01 South African Inventions Hydrogenation of unsaturated aliphatic hydrocarbons
US4593148A (en) * 1985-03-25 1986-06-03 Phillips Petroleum Company Process for removal of arsine impurities from gases containing arsine and hydrogen sulfide
FR2588197B1 (fr) * 1985-10-03 1987-11-20 Poudres & Explosifs Ste Nale Catalyseur et procede d'hydrogenation des liaisons ethyleniques ou acetyleniques
FR2629094B1 (fr) * 1988-03-23 1991-01-04 Inst Francais Du Petrole Procede d'hydrogenation catalytique selective en phase liquide d'une charge normalement gazeuse contenant de l'ethylene, de l'acetylene et de l'essence

Also Published As

Publication number Publication date
US5463154A (en) 1995-10-31
WO1993023499A1 (en) 1993-11-25
CA2135610C (en) 2001-04-10
DE69332453T2 (de) 2003-06-18
JP2784693B2 (ja) 1998-08-06
AU678553B2 (en) 1997-06-05
CA2135610A1 (en) 1993-11-25
EP0650516A1 (en) 1995-05-03
DE69332453D1 (de) 2002-12-05
AU4241493A (en) 1993-12-13
EP0650516B1 (en) 2002-10-30
JPH07508026A (ja) 1995-09-07

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