KR850002241A - 황화수소를 원소유황 및/또는 이산화황으로 산화시키는 방법 - Google Patents

황화수소를 원소유황 및/또는 이산화황으로 산화시키는 방법 Download PDF

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KR850002241A
KR850002241A KR1019840003800A KR840003800A KR850002241A KR 850002241 A KR850002241 A KR 850002241A KR 1019840003800 A KR1019840003800 A KR 1019840003800A KR 840003800 A KR840003800 A KR 840003800A KR 850002241 A KR850002241 A KR 850002241A
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hydrogen sulfide
sulfur
metal
gas
sulfur dioxide
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KR910009571B1 (ko
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그로넨달 뷜럼 (외 2)
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안토니우스토니스푸이슈터
셀 인터나쵸나아레 레사아치 마아츠샤피 비이부이
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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B17/00Sulfur; Compounds thereof
    • C01B17/48Sulfur dioxide; Sulfurous acid
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/06Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
    • B01J21/066Zirconium or hafnium; Oxides or hydroxides thereof
    • 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
    • B01D53/8615Mixtures of hydrogen sulfide and sulfur oxides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/06Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
    • B01J21/063Titanium; Oxides or hydroxides thereof
    • 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
    • C01B17/0456Preparation 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 the hydrogen sulfide-containing gas being a Claus process tail gas
    • 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
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B17/00Sulfur; Compounds thereof
    • C01B17/48Sulfur dioxide; Sulfurous acid
    • C01B17/50Preparation of sulfur dioxide
    • C01B17/508Preparation of sulfur dioxide by oxidation of sulfur compounds

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Environmental & Geological 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)

Abstract

내용 없음

Description

황화수소를 원소유황 및/또는 이산화황으로 산화시키는 방법
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음

Claims (19)

  1. 황화수소 함유기체를 유리 산소 함유기체 존재하에 실리카함 유운반체상에 원소주기율표 3b 및/또는 4b족의 금속 적어도 하나를 함유하는 1차 촉매조성물과 접축시키는 것으로 구성된 황화수소를 원소유황 및/또는 이산황으로 산화시키는 방법.
  2. 제1항에 있어서, 상기 금속 또는 금속들이 그의 산화물이나 황화염상태로 적용되는 방법.
  3. 제2항에 있어서, 티타늄, 질코늄 및/토륨 산화물중 적어도 하나가 운반체상에 적용되는 방법.
  4. 제1항 내지 3항중 어느 하나에서 상기금속 또는 금속들이 실리콘에 대한 금속 또는 금속(들)의 원자비가 0.001-1.0범위인 상태로 촉매조성물내 적용되는 방법.
  5. 제4항에 있어서, 원자비가 0.03-0.3범위로 적용되는 방법.
  6. 제1항 내지 5항중 어느하나에서 적어도 75중량%의 실리카가 운반체중에 적용되는 방법.
  7. 제6항에 있어서, 적어도 90중량%의 실리카겔 운반체중에 적용되는 방법.
  8. 제1항 내지 7항중 어느 하나에서 운반체가 하기 단계 a)-a)에 의해 제조되는 방법.
    a) 알칼리금속 실리케이트 수용액을 산수용액과 혼합하여 실리카하이드로솔을 제조하고, b) 하이드로솔을 소적형태로 전환시키고, c) 소적을 공기중에서 또는 물롸 혼화하지 않는 액체중에서 소적으로 형상화하고, d) 얻어진 하이드로겔 입자를 일부 미리건조하고, e) 일부 미리 건조된 입자를 열수처리하고, f) 이렇게 처리된 하이드로겔 입자의 양이온 함량을 건량을 기준으로 10중량%이하로 감소시키고, g) 이렇게 제조된 실리카 입자를 건조한 후 임의로 소성화한다.
  9. 제1항내지 8항중 어느하나에서 황화수소를 250-450℃에서 이산화황으로 산화시키는 방법.
  10. 제1항내지 9항중 어느하나에서 황화수소를 이산화황으로 산화시키는데 필요한 화학양론적 양의 산소의 5배까지의 양으로 유리산소 함유기체를 공급하여 황화수소를 이산화황으로 산화시키는 방법.
  11. 제10항에 있어서 유리산소 함유기체를 화학양곤적 양의 산소량에 20-280%초과량으로 공급하는 방법.
  12. 제1항 내지 8항중 어느하나에서 황화수소를 150-350℃에서 원소유황으로 산화시키는 방법.
  13. 제12항에 있어서 황화수소를 180-250℃에서 원소유황으로 산화시키는 방법.
  14. 제1항내지 8항중 어느 하나나 12항 또는 13항에 있어서, 황화수소를 원소유황으로 산화시키는데 있어 이 황화수소는 앞서 정의한 클라우스레일 기체를 175℃ 이상에서 유리산소-및/또는 일산화 탄소함유 기체로 원소주기율표 6족 및/또는 8족의 금속황화물과 상기 금속 황화물(들)을 지지하는 무기 산화운반체로 구성된 2차 촉매조성물상에서 환원하여 얻은 것인 방법.
  15. 제14항에 있어서 황화수소를 유황으로 산화시키기에 앞서 환원된 기체를 건조하여 물을 제거하는 방법.
  16. 제14항 또는 15항에 있어서 원소유황을 1차 촉매조성물과 접촉시킨 후 기체로 부터 제거하고 유황이 제거된 기체내 남아있는 H2S를 제1항 내지 10항중 어느한 방법으로 이산화황으로 산화시키는 방법.
  17. 제1항 내지 11항중 어느 하나에서, 황화수소를 이산화황으로 산화시키는데 있어, 이 황화수소는 클라우스테일기체를 175℃이상에서 유리산소 및/또는 일산화탄소 함유기체로 원소주기율표 6족 또는 8족의 금속황화물과 상기 금속황화물을 지지하는 무기산화물운반체로 구성된 2차 촉매조성물상에서 환원시킨 다음 환원된 기체내 존재하는 H2S를 흡착시키고 이어 H2S를 탈착시킨 후 탈착된 H2S를 클라우스테일공정내로 재순환시켜 얻은 것이며 이산화황으로 산화된 황화수소는 상기 H2S흡착으로 부터 생긴 최종배기가스 내 남게되는 방법.
  18. 제1항에 있어서, 앞서 실시예들을 참조로 설명한 바와 실질적으로 같은 방법.
  19. 제1항 내지 18항 그리고 12항 내지 18항중 어느하나에서 청구한 바와 같은 방법에 의해 제조된 원소 유황.
    ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
KR1019840003800A 1983-07-04 1984-07-02 황화수소를 원소유황 및/또는 이산화황으로 산화시키는 방법 KR910009571B1 (ko)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB838318098A GB8318098D0 (en) 1983-07-04 1983-07-04 Oxidation of hydrogen sulphide to elemental sulphur
GB8318098 1983-07-04

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KR850002241A true KR850002241A (ko) 1985-05-10
KR910009571B1 KR910009571B1 (ko) 1991-11-21

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EP (1) EP0134594B2 (ko)
JP (1) JPS6036309A (ko)
KR (1) KR910009571B1 (ko)
AU (1) AU569898B2 (ko)
CA (1) CA1232429A (ko)
DE (1) DE3467748D1 (ko)
DK (1) DK166535B1 (ko)
ES (1) ES8602529A1 (ko)
GB (2) GB8318098D0 (ko)
NZ (1) NZ208743A (ko)
SG (1) SG47687G (ko)
ZA (1) ZA845023B (ko)

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* Cited by examiner, † Cited by third party
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GB8318099D0 (en) * 1983-07-04 1983-08-03 Shell Int Research Production of elemental sulphur
JPH0832548B2 (ja) * 1985-10-25 1996-03-29 ソシエテ・ナシオナル・エルフ・アキテ−ヌ (プロデユクシオン) 残留ガスに含まれる硫黄化合物を除去する方法
FR2598094B1 (fr) * 1986-04-30 1990-11-23 Rhone Poulenc Chimie Catalyseur a base d'oxyde de zirconium et procede pour le traitement des gaz residuaires industriels contenant des composes du soufre
US5171551A (en) * 1986-04-30 1992-12-15 Rhone-Poulenc Chimie Zirconium dioxide gas desulfurization catalyst
US4705770A (en) * 1986-07-07 1987-11-10 Aristech Chemical Corporation Method of making anatase-titania attrition-resistant catalyst composition
FR2608458B1 (fr) * 1986-12-23 1989-03-10 Rhone Poulenc Chimie Catalyseur a base d'oxyde de cerium et procede pour le traitement de gaz industriels contenant des composes du soufre
US5494650A (en) * 1989-01-19 1996-02-27 Societe Nationale Elf Aquitaine (Production) Process for improving the sulphur yield of a complex for producing sulphur from a sour gas containing H2 S, the said complex comprising a sulphur plant and then an oxidation and hydrolysis unit followed by a purification unit
FR2727101B1 (fr) * 1994-11-17 1996-12-20 Elf Aquitaine Procede pour oxyder directement en soufre par voie catalytique l'h2s contenu en faible concentration dans un gaz et catalyseur pour la mise en oeuvre de ce procede
FR2773085B1 (fr) * 1997-12-29 2000-02-18 Elf Exploration Prod Procede catalytique pour oxyder directement en soufre, a basse temperature, l'h2s contenu en faible concentration dans un gaz et catalyseur pour sa mise en oeuvre
WO1999037389A1 (en) * 1998-01-26 1999-07-29 Tda Research, Inc. Catalysts for the selective oxidation of hydrogen sulfide to sulfur
DE10055343A1 (de) * 2000-11-08 2002-05-29 Messer Griesheim Gmbh Verfahren zum Herstellen von SO2 aus H2S-haltigem Gas
US7060233B1 (en) 2002-03-25 2006-06-13 Tda Research, Inc. Process for the simultaneous removal of sulfur and mercury
DE102007049743A1 (de) * 2007-10-16 2009-04-23 Evonik Degussa Gmbh Silicium-Titan-Mischoxidpulver, Dispersion hiervon und daraus hergestellter titanhaltiger Zeolith
ITMI20131322A1 (it) 2013-08-02 2015-02-03 Milano Politecnico Processo di riduzione di co2 per produzione di gas di sintesi.
PL3963260T3 (pl) 2019-05-03 2023-10-09 Topsoe A/S Sposób wytwarzania siarki pierwiastkowej i kwasu siarkowego

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GB207196A (ko) * 1922-11-20 1924-10-02 Farbenfabriken
GB722038A (en) * 1952-04-01 1955-01-19 North Thames Gas Board Improvements in or relating to the recovery of sulphur from gases
DE3166782D1 (en) * 1980-04-23 1984-11-29 Rhone Poulenc Spec Chim Oxidation process of hydrogen sulfide and organic compounds of sulfur
FR2481254A1 (fr) * 1980-04-23 1981-10-30 Elf Aquitaine Procede pour l'incineration catalytique de gaz residuaires renfermant en faible concentration au moins un compose du soufre choisi parmi cos, cs2, et les mercaptans et eventuellement au moins un membre du groupe forme par h2s, so2, soufre vapeur et/ou vesiculaire
FR2501662A1 (fr) * 1981-03-13 1982-09-17 Rhone Poulenc Spec Chim Catalyseurs et procede d'oxydation de l'hydrogene sulfure et/ou des composes organiques du soufre en anhydride sulfureux
CA1177811A (en) * 1981-04-13 1984-11-13 Theo G. Spek Process for the preparation of silica particles; silica particles with a narrow pore diameter distribution, catalysts made therefrom and use of these catalysts
GB8318099D0 (en) * 1983-07-04 1983-08-03 Shell Int Research Production of elemental sulphur

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DK323684D0 (da) 1984-07-02
CA1232429A (en) 1988-02-09
ES533904A0 (es) 1985-12-01
GB2143225B (en) 1987-01-07
GB8318098D0 (en) 1983-08-03
ES8602529A1 (es) 1985-12-01
ZA845023B (en) 1985-02-27
SG47687G (en) 1987-08-28
JPS6036309A (ja) 1985-02-25
DE3467748D1 (en) 1988-01-07
NZ208743A (en) 1987-03-31
AU569898B2 (en) 1988-02-25
KR910009571B1 (ko) 1991-11-21
EP0134594A1 (en) 1985-03-20
GB8416834D0 (en) 1984-08-08
DK166535B1 (da) 1993-06-07
GB2143225A (en) 1985-02-06
JPH0454603B2 (ko) 1992-08-31
DK323684A (da) 1985-01-05
EP0134594B2 (en) 1994-07-27
AU3007384A (en) 1985-01-10
EP0134594B1 (en) 1987-11-25

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