GB1356289A - Process for reducing the total sulphur content of claus off-gases - Google Patents

Process for reducing the total sulphur content of claus off-gases

Info

Publication number
GB1356289A
GB1356289A GB3321771A GB3321771A GB1356289A GB 1356289 A GB1356289 A GB 1356289A GB 3321771 A GB3321771 A GB 3321771A GB 3321771 A GB3321771 A GB 3321771A GB 1356289 A GB1356289 A GB 1356289A
Authority
GB
United Kingdom
Prior art keywords
gases
claus
hydrogen
absorbent
sulphide
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
Application number
GB3321771A
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.)
Shell Internationale Research Maatschappij BV
Original Assignee
Shell Internationale Research Maatschappij BV
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 Shell Internationale Research Maatschappij BV filed Critical Shell Internationale Research Maatschappij BV
Publication of GB1356289A publication Critical patent/GB1356289A/en
Expired legal-status Critical Current

Links

Classifications

    • 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
    • B01D53/46Removing components of defined structure
    • B01D53/48Sulfur compounds
    • B01D53/52Hydrogen sulfide
    • 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
    • C01B17/16Hydrogen sulfides
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10KPURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K1/00Purifying combustible gases containing carbon monoxide
    • C10K1/08Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors
    • C10K1/10Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids
    • C10K1/12Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids alkaline-reacting including the revival of the used wash liquors
    • C10K1/14Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids alkaline-reacting including the revival of the used wash liquors organic
    • C10K1/143Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids alkaline-reacting including the revival of the used wash liquors organic containing amino groups

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Environmental & Geological Engineering (AREA)
  • Analytical Chemistry (AREA)
  • Treating Waste Gases (AREA)
  • Casting Support Devices, Ladles, And Melt Control Thereby (AREA)

Abstract

1356289 Desulphurizing Claus off-gases SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ NV 15 July 1971 [17 July 1970] 33217/71 Heading C1A Off-gases containing sulphur dioxide from a Claus kiln are passed at a temperature above 175‹ C. together with a gas containing free hydrogen and/or free carbon monoxide over a sulphided Group VI and/or Group VIII metal catalyst supported on an inorganic oxide carrier, the reduced gases being then passed through a liquid and regeneratable absorbent for hydrogen sulphide and the unabsorbed portion, optionally after incineration, is discharged to the atmosphere, the hydrogen sulphide enriched absorbent being regenerated for re-use and the hydrogen sulphide rich gas mixture liberated being passed to a Claus process. Group VI metals specified are molybdenum, tungsten and chromium; Group VIII metals specified are iron, cobalt and nickel. The inorganic oxide carrier may be alumina, silica, magnesia, boron oxide, thoria, zirconia or a mixture of these compounds. The sulphiding may be carried out by use of the Claus off-gases themselves, the preferred temperature being between 300 and 400‹ C. The reducing gas preferably contains at least 20% by volume of free hydrogen or an equivalent amount of hydrogen/carbon monoxide mixture. Should any carbonyl sulphide be formed when carbon monoxide is used as the reducing gas it may be decomposed in known manner by passage over a heated bed of alumina. Amines and substituted amines in aqueous solution are the preferred absorbents, in particular alkali metal salts of dialkyl substituted amino acids (e.g. potassium dimethylamino-acetate) and polyalkanolamines such as di- or tri-ethanolamine and diisopropanolamine. After absorption, the H 2 S enriched absorbent is regenerated by heating and/or stripping, the H 2 S enriched gas mixture being recycled to the Claus plant and the regenerated absorbent re-used. Using high gas velocities at temperatures lower than 40‹ C. the selectivity of the H 2 S/CO 2 ratio is enhanced, CO 2 being usually present in the off-gases when the Claus process is operated using air. Other gases present which may be reduced to hydrogen sulphide by the present process include carbonyl sulphide and carbon disulphide.
GB3321771A 1970-07-17 1971-07-15 Process for reducing the total sulphur content of claus off-gases Expired GB1356289A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NLAANVRAGE7010604,A NL171144B (en) 1970-07-17 1970-07-17 PROCESS FOR REDUCING THE TOTAL SULFUR CONTENT OF CLAUSE GASES.

Publications (1)

Publication Number Publication Date
GB1356289A true GB1356289A (en) 1974-06-12

Family

ID=19810608

Family Applications (1)

Application Number Title Priority Date Filing Date
GB3321771A Expired GB1356289A (en) 1970-07-17 1971-07-15 Process for reducing the total sulphur content of claus off-gases

Country Status (18)

Country Link
JP (1) JPS5716846B1 (en)
AT (1) AT308768B (en)
AU (1) AU459768B2 (en)
BE (1) BE770058A (en)
CH (1) CH580982A5 (en)
CS (1) CS179372B2 (en)
DE (1) DE2135522C2 (en)
DK (1) DK149328C (en)
ES (1) ES393290A1 (en)
FI (1) FI56320C (en)
FR (1) FR2101724A5 (en)
GB (1) GB1356289A (en)
IE (1) IE35451B1 (en)
IT (1) IT941574B (en)
NL (1) NL171144B (en)
NO (1) NO132088C (en)
SU (1) SU751318A3 (en)
ZA (1) ZA714698B (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4241032A (en) 1978-05-23 1980-12-23 Shell Oil Company Process for the removal of hydrogen sulfide from gas streams
DE3308406A1 (en) * 1982-03-11 1983-09-15 Shell Internationale Research Maatschappij B.V., 2501 Den Haag METHOD AND DEVICE FOR COMBUSTION OF AMMONIA-CONTAINING EXHAUST GASES
EP0375077A2 (en) * 1988-12-23 1990-06-27 Shell Internationale Researchmaatschappij B.V. Removing hydrogen sulphide from a gas mixture
US5266274A (en) * 1992-10-13 1993-11-30 Tpa, Inc. Oxygen control system for a sulfur recovery unit
AU710859B2 (en) * 1996-08-22 1999-09-30 Shell Internationale Research Maatschappij B.V. Process for reducing total sulphur content in gases containing hydrogen sulphide and other sulphur components
WO2019022603A1 (en) 2017-07-26 2019-01-31 Wte-Tech B.V. Process to treat a sulphur compounds comprising gaseous feed

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL7310929A (en) * 1973-08-08 1974-01-25
FR2295784A1 (en) * 1974-12-27 1976-07-23 Inst Francais Du Petrole PROCESS FOR DEPURING A GAS CONTAINING SULFUR COMPOUNDS
GB1470950A (en) * 1976-03-08 1977-04-21 Shell Int Research Process for working-up hydrogen sulphide-containing gases
DE2648190C3 (en) * 1976-10-25 1980-02-21 Metallgesellschaft Ag, 6000 Frankfurt Process for the production of sulfur by the Claus process
GB1563251A (en) * 1976-12-07 1980-03-26 Shell Int Research Process for working hydrogen suphidecontaining gases
NL7701174A (en) * 1977-02-04 1978-08-08 Shell Int Research PROCESS FOR PREPARING A GAS MIX WITH DESIRED H2S / CO2 RATIO.
FR2425886A1 (en) * 1978-05-16 1979-12-14 Elf Aquitaine PROCESS FOR PURIFYING INDUSTRIAL WASTE GASES CONTAINING LOW CONCENTRATIONS OF SULFUR COMPOUNDS
FR2631561B1 (en) * 1988-05-20 1990-07-20 Elf Aquitaine PROCESS AND DEVICE FOR THE REMOVAL OF LOW CONCENTRATION OF H2S IN A GAS ALSO CONTAINING A LARGE QUANTITY OF WATER VAPOR
DE3901600C2 (en) * 1989-01-20 1998-12-24 Krupp Koppers Gmbh Process for the treatment of vacuum exhaust air from tar distillation plants
AU638543B2 (en) * 1990-02-09 1993-07-01 Mitsubishi Jukogyo Kabushiki Kaisha Process for purifying high-temperature reducing gases and integrated coal gasification combined cycle power generation plant
RU2562481C2 (en) * 2014-01-29 2015-09-10 Игорь Анатольевич Мнушкин Method and apparatus for producing elementary sulphur with tail gas post-treatment
EP3067109B1 (en) * 2015-03-12 2018-12-05 Prosernat Process for removing sulfur compounds from a gas with hydrogenation and direct oxidation steps

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2361825A (en) * 1941-08-25 1944-10-31 Union Oil Co Reduction of sulphur dioxide to hydrogen sulphide and free sulphur
FR1105475A (en) * 1954-01-24 1955-12-05 Azote Office Nat Ind Process for the desulphurization of industrial gases and vapors
US2860030A (en) * 1954-12-17 1958-11-11 Phillips Petroleum Co Recovery of hydrogen sulfide and/or carbon dioxide substantially free from hydrocarbons and substantially pure hydrocarbons by chemical treatment of an impure hydrocarbon stream
US2887363A (en) * 1956-09-28 1959-05-19 Exxon Research Engineering Co Conversion of methane to produce hydrogen sulfide
US3476513A (en) * 1966-08-25 1969-11-04 Exxon Research Engineering Co Process and apparatus for the conversion of so2 in flue gas to sulfur
GB1116129A (en) * 1967-03-02 1968-06-06 Shell Int Research Catalytic reduction of sulphur dioxide to hydrogen sulphide

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4241032A (en) 1978-05-23 1980-12-23 Shell Oil Company Process for the removal of hydrogen sulfide from gas streams
DE3308406A1 (en) * 1982-03-11 1983-09-15 Shell Internationale Research Maatschappij B.V., 2501 Den Haag METHOD AND DEVICE FOR COMBUSTION OF AMMONIA-CONTAINING EXHAUST GASES
EP0375077A2 (en) * 1988-12-23 1990-06-27 Shell Internationale Researchmaatschappij B.V. Removing hydrogen sulphide from a gas mixture
EP0375077B1 (en) * 1988-12-23 1993-06-02 Shell Internationale Researchmaatschappij B.V. Removing hydrogen sulphide from a gas mixture
US5266274A (en) * 1992-10-13 1993-11-30 Tpa, Inc. Oxygen control system for a sulfur recovery unit
AU710859B2 (en) * 1996-08-22 1999-09-30 Shell Internationale Research Maatschappij B.V. Process for reducing total sulphur content in gases containing hydrogen sulphide and other sulphur components
WO2019022603A1 (en) 2017-07-26 2019-01-31 Wte-Tech B.V. Process to treat a sulphur compounds comprising gaseous feed

Also Published As

Publication number Publication date
DK149328C (en) 1986-10-06
NL7010604A (en) 1972-01-19
DE2135522C2 (en) 1983-01-13
FI56320C (en) 1980-01-10
AU3128371A (en) 1973-01-18
ES393290A1 (en) 1973-08-16
DK149328B (en) 1986-05-05
IE35451B1 (en) 1976-02-18
ZA714698B (en) 1972-04-26
NO132088B (en) 1975-06-09
FR2101724A5 (en) 1972-03-31
AU459768B2 (en) 1975-04-10
IE35451L (en) 1972-01-17
FI56320B (en) 1979-09-28
CS179372B2 (en) 1977-10-31
NO132088C (en) 1975-09-17
NL171144B (en) 1982-09-16
IT941574B (en) 1973-03-10
AT308768B (en) 1973-07-25
CH580982A5 (en) 1976-10-29
DE2135522A1 (en) 1972-01-20
BE770058A (en) 1972-01-17
SU751318A3 (en) 1980-07-23
JPS5716846B1 (en) 1982-04-07

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Legal Events

Date Code Title Description
PS Patent sealed
PCNP Patent ceased through non-payment of renewal fee