GB790287A - Improvements in or relating to method for separating carbon dioxide and hydrogen sulfide from gas mixtures - Google Patents

Improvements in or relating to method for separating carbon dioxide and hydrogen sulfide from gas mixtures

Info

Publication number
GB790287A
GB790287A GB6057/55A GB605755A GB790287A GB 790287 A GB790287 A GB 790287A GB 6057/55 A GB6057/55 A GB 6057/55A GB 605755 A GB605755 A GB 605755A GB 790287 A GB790287 A GB 790287A
Authority
GB
United Kingdom
Prior art keywords
absorber
steam
solution
regenerator
boiling temperature
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
GB6057/55A
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.)
Individual
Original Assignee
Individual
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
Priority to GB6759/53A priority Critical patent/GB725000A/en
Application filed by Individual filed Critical Individual
Priority to GB24313/56A priority patent/GB790288A/en
Priority to GB24314/56A priority patent/GB790289A/en
Priority to GB6057/55A priority patent/GB790287A/en
Publication of GB790287A publication Critical patent/GB790287A/en
Expired legal-status Critical Current

Links

Classifications

    • 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
    • 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
    • B01D53/526Mixtures of hydrogen sulfide and carbon dioxide
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02CCAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00Capture or disposal of greenhouse gases
    • Y02C20/40Capture or disposal of greenhouse gases of CO2
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/151Reduction of greenhouse gas [GHG] emissions, e.g. CO2

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Environmental & Geological Engineering (AREA)
  • Biomedical Technology (AREA)
  • Analytical Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Organic Chemistry (AREA)
  • Treating Waste Gases (AREA)
  • Gas Separation By Absorption (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

<PICT:0790287/III/1> The process of the parent Specification of absorbing carbon dioxide or hydrogen sulphide from gases by alkaline solutions, particularly potassium carbonate, under superatmospheric pressure, regenerating by boiling and steam stripping at about atmospheric pressure and returning the solution to the absorber at about atmospheric boiling temperature, is modified by conducting the regeneration under sub-atmospheric pressure corresponding to a boiling temperature of 170 DEG F. and upwards. The apparatus may be the same as that of the parent Specification with the inclusion of a vacuum pump &c. to maintain sub-atmospheric pressure in the regenerator column; a separate flashing vessel immediately after the absorber may be dispensed with. Part, e.g. 2/3 , of the regenerated solution may be introduced at an intermediate level of the absorber, the remainder being cooled e.g. 30-100 DEG F. and introduced at the top. Or this minor stream, with or without subsequent cooling, may be subjected to more thorough regeneration. Fouled solution from an absorber 202 maintained e.g. at 300 lb. per sq. in. pressure passes through a letdown valve 208 to a regenerator 209 in which a sub-atmospheric pressure, e.g. corresponding to a boiling temperature of 200 DEG F. at the bottom of the column, is maintained by a vacuum pump 215 which draws off carbon dioxide &c. from a separator 212 collecting effluent from the top of column after passage through a condenser 211. Most of the regenerated solution is recycled through a line 204 to an intermediate level of the absorber. A minor quantity is pumped to a secondary regenerator 223 maintained e.g. at about 30 lb. per sq. in. pressure (boiling temperature 290 DEG F.) stripping steam being provided by means of a closed coil receiving exhaust steam from the vacuum pump turbine 217 or by direct input of steam. The regenerated solution passes through a let-down valve 229 to a flashing vessel 320 from which steam is supplied to the main regenerator and the cooled solution through a coole 234 if desired, to the top of the absorber. Corrosion inhibiting material, e.g. 0.2-0.3 p.c. of sodium dichromate by weight of the potassium carbonate may be employed. Sodium carbonate and potassium phosphate may be used as scrubbing solutions. Specifications 790,288 and 790,289 also are referred to.
GB6057/55A 1955-03-01 1955-03-01 Improvements in or relating to method for separating carbon dioxide and hydrogen sulfide from gas mixtures Expired GB790287A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
GB6759/53A GB725000A (en) 1955-03-01 1953-03-11 Improvements in or relating to method for separating carbon dioxide and hydrogen sulphide from gas mixtures
GB24313/56A GB790288A (en) 1955-03-01 1955-03-01 Improvements in or relating to method for separating carbon dioxide and hydrogen sulfide from gas mixtures
GB24314/56A GB790289A (en) 1955-03-01 1955-03-01 Improvements in or relating to method for separating carbon dioxide and hydrogen sulfide from gas mixtures
GB6057/55A GB790287A (en) 1955-03-01 1955-03-01 Improvements in or relating to method for separating carbon dioxide and hydrogen sulfide from gas mixtures

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB6057/55A GB790287A (en) 1955-03-01 1955-03-01 Improvements in or relating to method for separating carbon dioxide and hydrogen sulfide from gas mixtures

Publications (1)

Publication Number Publication Date
GB790287A true GB790287A (en) 1958-02-05

Family

ID=9807630

Family Applications (4)

Application Number Title Priority Date Filing Date
GB6759/53A Expired GB725000A (en) 1955-03-01 1953-03-11 Improvements in or relating to method for separating carbon dioxide and hydrogen sulphide from gas mixtures
GB24313/56A Expired GB790288A (en) 1955-03-01 1955-03-01 Improvements in or relating to method for separating carbon dioxide and hydrogen sulfide from gas mixtures
GB24314/56A Expired GB790289A (en) 1955-03-01 1955-03-01 Improvements in or relating to method for separating carbon dioxide and hydrogen sulfide from gas mixtures
GB6057/55A Expired GB790287A (en) 1955-03-01 1955-03-01 Improvements in or relating to method for separating carbon dioxide and hydrogen sulfide from gas mixtures

Family Applications Before (3)

Application Number Title Priority Date Filing Date
GB6759/53A Expired GB725000A (en) 1955-03-01 1953-03-11 Improvements in or relating to method for separating carbon dioxide and hydrogen sulphide from gas mixtures
GB24313/56A Expired GB790288A (en) 1955-03-01 1955-03-01 Improvements in or relating to method for separating carbon dioxide and hydrogen sulfide from gas mixtures
GB24314/56A Expired GB790289A (en) 1955-03-01 1955-03-01 Improvements in or relating to method for separating carbon dioxide and hydrogen sulfide from gas mixtures

Country Status (1)

Country Link
GB (4) GB725000A (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1083973B (en) * 1954-04-07 1960-06-23 Chemical Construction Corp Two-step process for removing carbon dioxide from gases
US2912301A (en) * 1956-10-18 1959-11-10 Kellogg M W Co Method of removing acidic components from gaseous mixtures
DE2945675C2 (en) * 1979-11-12 1984-08-16 Union Rheinische Braunkohlen Kraftstoff AG, 5000 Köln Process for the production of pure hydrogen sulfide
GB8431597D0 (en) * 1984-12-14 1985-01-30 Ici Plc Treatment of gas mixtures
GB8432657D0 (en) * 1984-12-27 1985-02-06 Ici Plc Separation process
KR20080027873A (en) 2005-06-23 2008-03-28 지알디씨, 엘엘씨 Efficient production of hydrogen
GB0715101D0 (en) * 2007-08-03 2007-09-12 Johnson Matthey Plc Process
FR3087526B1 (en) * 2018-10-18 2020-12-18 Air Liquide INSTALLATION AND PRODUCTION PROCESS OF LIQUEFIED METHANE

Also Published As

Publication number Publication date
GB725000A (en) 1955-03-02
GB790288A (en) 1958-02-05
GB790289A (en) 1958-02-05

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