GB1334010A - Treatment of sulphur effluent - Google Patents

Treatment of sulphur effluent

Info

Publication number
GB1334010A
GB1334010A GB2128971A GB2128971A GB1334010A GB 1334010 A GB1334010 A GB 1334010A GB 2128971 A GB2128971 A GB 2128971A GB 2128971 A GB2128971 A GB 2128971A GB 1334010 A GB1334010 A GB 1334010A
Authority
GB
United Kingdom
Prior art keywords
sulphur
zone
gas
catalyst
mixture
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
GB2128971A
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.)
BP America Production Co
Original Assignee
BP America Production Co
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 BP America Production Co filed Critical BP America Production Co
Publication of GB1334010A publication Critical patent/GB1334010A/en
Expired legal-status Critical Current

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B15/00—Fluidised-bed furnaces; Other furnaces using or treating finely-divided materials in dispersion
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
    • B01J8/002—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor with a moving instrument
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1836—Heating and cooling the reactor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/26—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations
    • B01J8/28—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations the one above the other
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/44—Fluidisation grids
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B17/00—Sulfur; Compounds thereof
    • C01B17/02—Preparation of sulfur; Purification
    • C01B17/04—Preparation of sulfur; Purification from gaseous sulfur compounds including gaseous sulfides
    • C01B17/0404—Preparation 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
    • C01B17/0426—Preparation 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 characterised by the catalytic conversion
    • C01B17/0439—Preparation 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 characterised by the catalytic conversion at least one catalyst bed operating below the dew-point of sulfur
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/584—Recycling of catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Inorganic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Industrial Gases (AREA)
  • Treating Waste Gases (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)

Abstract

1334010 Removal of H 2 S from gas streams AMOCO PRODUCTION CO 19 April 1971 [30 April 1970] 21289/71 Heading C1A A process for the recovery of sulphur from a gaseous mixture containing H 2 S comprises (i) forming a mixture of H 2 S and SO 2 in a molar ratio 2 :1, (ii) introducing said mixture at a temperature of 450-600‹ F. into a first catalytic zone 10 having sulphur deposited on the catalyst, whereby sulphur is vaporized therefrom simultaneously with the reaction of H 2 S and SO 2 , (iii) passing the gases from said first zone through a condenser 18 to remove vaporized sulphur therefrom, (iv) passing the cooled gas from 18 to a second zone 44 where it is used to cool hot, freshly regenerated catalyst whilst at the same time reaction occurs between H 2 S and SO 2 in said gas to deposit elemental S on said catalyst, (v) when the gas leaving zone 44 contains more than a predetermined amount of H 2 S and SO 2 reversing the flow of said gaseous mixture through said reaction zones and repeating the above cycle. In a preferred embodiment a third catalytic reactor 68 may be incorporated such that a three-stage system as indicated in the drawing can be operated.
GB2128971A 1970-04-30 1971-04-19 Treatment of sulphur effluent Expired GB1334010A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US3339770A 1970-04-30 1970-04-30

Publications (1)

Publication Number Publication Date
GB1334010A true GB1334010A (en) 1973-10-17

Family

ID=21870182

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2128971A Expired GB1334010A (en) 1970-04-30 1971-04-19 Treatment of sulphur effluent

Country Status (6)

Country Link
JP (1) JPS5110199B1 (en)
CA (1) CA938087A (en)
DE (1) DE2109761A1 (en)
FR (1) FR2086477B1 (en)
GB (1) GB1334010A (en)
NL (1) NL7102651A (en)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3890120A (en) * 1972-04-18 1975-06-17 Aquitaine Petrole Process to recover sulphur from the sulphur compounds contained in residual gases
US4462977A (en) * 1982-04-26 1984-07-31 Standard Oil Company (Indiana) Recovery of elemental sulfur from sour gas
US4487754A (en) * 1983-07-29 1984-12-11 Standard Oil Company (Indiana) System and process for producing and recovering elemental sulfur
US4483844A (en) * 1983-07-29 1984-11-20 Standard Oil Company (Indiana) System and process for producing elemental sulfur
US4482532A (en) * 1983-07-29 1984-11-13 Standard Oil Company (Indiana) System and process for producing elemental sulfur
US4507275A (en) * 1983-08-30 1985-03-26 Standard Oil Company (Indiana) Process for producing and recovering elemental sulfur from acid gas
US4508698A (en) * 1983-08-30 1985-04-02 Standard Oil Company (Indiana) Process and system for producing and recovering elemental sulfur
US5015460A (en) * 1989-11-30 1991-05-14 Amoco Corporation Condenser-reactor switching units for extended Claus process
US5141733A (en) * 1989-11-30 1992-08-25 Pendergraft Paul T High pressure-low pressure steam system for extended Claus sulfur recovery plant
US5015459A (en) * 1989-11-30 1991-05-14 Amoco Corporation High pressure-low pressure steam system for extended Claus sulfur recovery plant

Also Published As

Publication number Publication date
FR2086477B1 (en) 1973-06-08
NL7102651A (en) 1971-11-02
JPS5110199B1 (en) 1976-04-02
FR2086477A1 (en) 1971-12-31
DE2109761A1 (en) 1971-11-11
CA938087A (en) 1973-12-11

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Legal Events

Date Code Title Description
PS Patent sealed
PLNP Patent lapsed through nonpayment of renewal fees