NO304501B1 - Process for catalytic oxidation of H2 S present in low concentration in a gas directly to sulfur, as well as using a catalyst for carrying out the process - Google Patents

Process for catalytic oxidation of H2 S present in low concentration in a gas directly to sulfur, as well as using a catalyst for carrying out the process

Info

Publication number
NO304501B1
NO304501B1 NO944356A NO944356A NO304501B1 NO 304501 B1 NO304501 B1 NO 304501B1 NO 944356 A NO944356 A NO 944356A NO 944356 A NO944356 A NO 944356A NO 304501 B1 NO304501 B1 NO 304501B1
Authority
NO
Norway
Prior art keywords
catalyst
sulfur
carrying
well
low concentration
Prior art date
Application number
NO944356A
Other languages
Norwegian (no)
Other versions
NO944356D0 (en
NO944356L (en
Inventor
Didier Anglerot
Guy Demarais
Pierre Mailles
Original Assignee
Elf Exploration Prod
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 Elf Exploration Prod filed Critical Elf Exploration Prod
Publication of NO944356D0 publication Critical patent/NO944356D0/en
Publication of NO944356L publication Critical patent/NO944356L/en
Publication of NO304501B1 publication Critical patent/NO304501B1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B17/00Sulfur; Compounds thereof
    • C01B17/02Preparation of sulfur; Purification
    • C01B17/04Preparation of sulfur; Purification from gaseous sulfur compounds including gaseous sulfides
    • C01B17/0404Preparation of sulfur; Purification from gaseous sulfur compounds including gaseous sulfides by processes comprising a dry catalytic conversion of hydrogen sulfide-containing gases, e.g. the Claus process
    • C01B17/046Preparation of sulfur; Purification from gaseous sulfur compounds including gaseous sulfides by processes comprising a dry catalytic conversion of hydrogen sulfide-containing gases, e.g. the Claus process without intermediate formation of sulfur dioxide
    • C01B17/0465Catalyst compositions
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86Catalytic processes
    • B01D53/8603Removing sulfur compounds
    • B01D53/8612Hydrogen sulfide

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Catalysts (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Treating Waste Gases (AREA)

Abstract

An H2S-containing gas and a free-oxygen-containing gas in amounts such that the molar ratio of O2 to H2S is from 0.5 to 3 are contacted, at a temperature below 200 DEG C, with a catalyst for oxidatively converting H2S into sulphur. Said catalyst consists of an activated carbon substrate incorporating a catalytic phase selected from the oxide, salt or sulphide compounds of one or more transition metals selected from V, Mo, W, Ni and Co. The amount of said catalytic phase, by weight of transition metal, represents 0.1-15 wt % of the calcined catalyst.
NO944356A 1993-03-16 1994-11-15 Process for catalytic oxidation of H2 S present in low concentration in a gas directly to sulfur, as well as using a catalyst for carrying out the process NO304501B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR9302996A FR2702675B1 (en) 1993-03-16 1993-03-16 Process for oxidizing directly into sulfur by catalytic means, with high selectivity, the H2S contained in low concentration in a gas and catalyst for the implementation of this process.
PCT/FR1994/000283 WO1994021358A1 (en) 1993-03-16 1994-03-16 Method for the direct high-selectivity catalytic oxidative conversion of a low concentration of h2s in a gas into sulphur, and catalyst therefor

Publications (3)

Publication Number Publication Date
NO944356D0 NO944356D0 (en) 1994-11-15
NO944356L NO944356L (en) 1995-01-09
NO304501B1 true NO304501B1 (en) 1999-01-04

Family

ID=9444994

Family Applications (1)

Application Number Title Priority Date Filing Date
NO944356A NO304501B1 (en) 1993-03-16 1994-11-15 Process for catalytic oxidation of H2 S present in low concentration in a gas directly to sulfur, as well as using a catalyst for carrying out the process

Country Status (12)

Country Link
EP (1) EP0640004B1 (en)
JP (1) JPH07509436A (en)
CN (1) CN1105174A (en)
AT (1) ATE162102T1 (en)
CA (1) CA2135908A1 (en)
DE (1) DE69407897T2 (en)
DK (1) DK0640004T3 (en)
ES (1) ES2114185T3 (en)
FR (1) FR2702675B1 (en)
NO (1) NO304501B1 (en)
RU (1) RU2107024C1 (en)
WO (1) WO1994021358A1 (en)

Families Citing this family (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2727101B1 (en) * 1994-11-17 1996-12-20 Elf Aquitaine PROCESS FOR OXIDIZING SULFUR DIRECTLY BY CATALYTIC H2S CONTAINED IN LOW CONCENTRATION IN A GAS AND CATALYST FOR CARRYING OUT THIS PROCESS
US5597546A (en) * 1995-08-29 1997-01-28 National Science Council Selective oxidation of hydrogen sulfide in the presence of bismuth-based catalysts
US5700440A (en) * 1995-09-05 1997-12-23 National Science Council Selective oxidation of hydrogen sulfide in the presence of iron-based catalysts
FR2773085B1 (en) * 1997-12-29 2000-02-18 Elf Exploration Prod CATALYTIC PROCESS FOR OXIDIZING DIRECTLY SULFUR, AT LOW TEMPERATURE, THE H2S CONTAINED IN LOW CONCENTRATION IN A GAS AND CATALYST FOR IMPLEMENTING IT
US6946111B2 (en) 1999-07-30 2005-09-20 Conocophilips Company Short contact time catalytic partial oxidation process for recovering sulfur from an H2S containing gas stream
US6579510B2 (en) 1999-07-30 2003-06-17 Alfred E. Keller SPOX-enhanced process for production of synthesis gas
US6800269B2 (en) 1999-07-30 2004-10-05 Conocophillips Company Short contact time catalytic sulfur recovery system for removing H2S from a waste gas stream
US6403051B1 (en) * 1999-07-30 2002-06-11 Conoco Inc. Recovery of sulfur from H2S and concurrent production of H2 using short contact time CPOX
US7122170B2 (en) 2000-07-25 2006-10-17 Conocophillips Company Catalysts for SPOC™ enhanced synthesis gas production
ES2292499T3 (en) * 2000-07-25 2008-03-16 Conocophillips Company PROCEDURE IMPROVED BY PARTIAL CATALYTIC OXIDATION OF H2S (SPOX) FOR THE PRODUCTION OF SYNTHESIS GAS.
US7357908B2 (en) 2000-12-18 2008-04-15 Conocophillips Company Apparatus and catalytic partial oxidation process for recovering sulfur from an H2S-containing gas stream
US7326397B2 (en) 2000-12-18 2008-02-05 Conocophillips Company Catalytic partial oxidation process for recovering sulfur from an H2S-containing gas stream
US7108842B2 (en) 2004-01-15 2006-09-19 Conocophillips Company Process for the catalytic partial oxidation of H2S using staged addition of oxygen
US7226572B1 (en) 2006-03-03 2007-06-05 Conocophillips Company Compact sulfur recovery plant and process
US7501111B2 (en) 2006-08-25 2009-03-10 Conoco Phillips Company Increased capacity sulfur recovery plant and process for recovering elemental sulfur
CN101418246B (en) * 2008-12-05 2013-04-03 华陆工程科技有限责任公司 Low temperature methanol washing integrated Claus sulfur recovery system and process
EA032617B1 (en) * 2012-11-08 2019-06-28 Стамикарбон Б.В. Эктин Андер Те Нейм Оф Мт Инновейшн Сентр Sulphur recovery process with concurrent hydrogen production
CN114029048B (en) * 2021-12-10 2023-03-24 福州大学 Preparation method and application of tungsten oxide catalyst coated by porous carbon

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1603452A (en) * 1968-02-02 1971-04-19
DE1809329A1 (en) * 1968-11-16 1970-09-24 Pintsch Bamag Ag Berlin Und Bu Removal of residual hydrogen sulphide from - effluent gases from claus plant
US3790659A (en) * 1971-04-20 1974-02-05 Metallgesellschaft Ag Activated carbon catalyst impregnated with sio2
US4054642A (en) * 1973-08-30 1977-10-18 Rhone-Poulenc Industries Process for the treatment of gases containing various derivatives of sulphur
DE2652099C2 (en) * 1976-11-16 1986-03-27 Bergwerksverband Gmbh, 4300 Essen Process for separating hydrogen sulfide from gas mixtures
US4212852A (en) * 1977-05-06 1980-07-15 Takeda Chemical Industries, Ltd. Method of deodorizing gas containing hydrogen sulfide and ammonia and/or amines
DE4109892C2 (en) * 1991-03-26 1994-12-22 Metallgesellschaft Ag Process for removing hydrogen sulfide from gases using activated carbon

Also Published As

Publication number Publication date
DK0640004T3 (en) 1998-09-14
RU2107024C1 (en) 1998-03-20
ATE162102T1 (en) 1998-01-15
CN1105174A (en) 1995-07-12
EP0640004B1 (en) 1998-01-14
ES2114185T3 (en) 1998-05-16
DE69407897D1 (en) 1998-02-19
EP0640004A1 (en) 1995-03-01
DE69407897T2 (en) 1998-07-23
FR2702675A1 (en) 1994-09-23
JPH07509436A (en) 1995-10-19
NO944356D0 (en) 1994-11-15
NO944356L (en) 1995-01-09
RU94046133A (en) 1996-09-20
FR2702675B1 (en) 1995-04-28
WO1994021358A1 (en) 1994-09-29
CA2135908A1 (en) 1994-09-29

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