GB912091A - Process and apparatus for the desorption of charged absorbents - Google Patents

Process and apparatus for the desorption of charged absorbents

Info

Publication number
GB912091A
GB912091A GB14371/59A GB1437159A GB912091A GB 912091 A GB912091 A GB 912091A GB 14371/59 A GB14371/59 A GB 14371/59A GB 1437159 A GB1437159 A GB 1437159A GB 912091 A GB912091 A GB 912091A
Authority
GB
United Kingdom
Prior art keywords
air
tower
absorbent
solution
water
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
GB14371/59A
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.)
Hoechst AG
Original Assignee
Hoechst AG
Farbwerke Hoechst AG
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 Hoechst AG, Farbwerke Hoechst AG filed Critical Hoechst AG
Publication of GB912091A publication Critical patent/GB912091A/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
    • B01D53/14Separation 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 by absorption
    • 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
    • Y02P20/10Process efficiency
    • Y02P20/129Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
    • 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)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Analytical Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Gas Separation By Absorption (AREA)

Abstract

<PICT:0912091/III/1> Liquid absorbent, which has been used for selectively absorbing an ingredient of a gaseous mixture, is treated to expel the gas by passing humid air therethrough, the humid air being prepared by first passing air through liquid absorbent which has already been stripped of gas, and then treating the air with warm water so that it attains a humidity of 95-100% saturation and a temperature which is 5 DEG -15 DEG C. above the temperature of the unstripped absorbent. The process is particularly suitable for the removal of gaseous weak acids (e.g. CO2, H2S or HCN) from their solutions, the absorbent liquid being, for example, an alkaline solution or an organic solvent. Thus, the removal of H2S from sodium carbonate solution, and the removal of CO2 from potassium taurinate solution, are mentioned. In the drawing, the liquid absorbent is sprayed down a packed column 19 and is stripped therein by a countercurrent of humid air which is produced in packed tower 1. Tray 7, having covered vents, divides tower 1 into two parts, air entering the lower part through pipes 9 and 10 and moist air leaving the upper part through pipe 23. Stripped absorbent from column 19 enters the lower part of tower 1 through spray 3 and runs from the base of the tower into receiver 14. Water from tank 17 is pumped by pump 16, through heater 15, to the distributer 6 in the upper part of tower 1, while water collecting in tray 7 flows back to tank 17. Make-up water, to replace that consumed in moistening the air, is fed into tank 17, the flow of make-up water being controlled by the level in tray 7. Where the absorbent liquid is a solution, the passage of air through it, in the lower part of tower 1, alters the concentration of the solution. The concentration may be maintained at the desired value by means of impulse transmitter 12 in receiver 14. This transmitter, in response to changes in the concentration of the solution in receiver 14, operates the flow regulator 11, so that the proportion of air entering tower 1 through the pipe 9 is varied.
GB14371/59A 1958-04-25 1959-04-27 Process and apparatus for the desorption of charged absorbents Expired GB912091A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DEF25590A DE1099501B (en) 1958-04-25 1958-04-25 Method and device for the desorption of loaded absorbents

Publications (1)

Publication Number Publication Date
GB912091A true GB912091A (en) 1962-12-05

Family

ID=7091695

Family Applications (1)

Application Number Title Priority Date Filing Date
GB14371/59A Expired GB912091A (en) 1958-04-25 1959-04-27 Process and apparatus for the desorption of charged absorbents

Country Status (2)

Country Link
DE (1) DE1099501B (en)
GB (1) GB912091A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9011576B2 (en) 2009-06-25 2015-04-21 Paul Dinnage Liquid sorbant, method of using a liquid sorbant, and device for sorbing a gas

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3426562A1 (en) * 1984-07-19 1986-01-30 Bergwerksverband Gmbh, 4300 Essen METHOD FOR THE REMOVAL OF VOLATILE INGREDIENTS FROM WATER RESULTING FROM CARBON REFINING PROCESSES
CN116199293A (en) * 2021-11-30 2023-06-02 中国石油化工股份有限公司 Reinforced negative pressure gas stripping device and gas stripping method thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9011576B2 (en) 2009-06-25 2015-04-21 Paul Dinnage Liquid sorbant, method of using a liquid sorbant, and device for sorbing a gas

Also Published As

Publication number Publication date
DE1099501B (en) 1961-02-16

Similar Documents

Publication Publication Date Title
GB1333635A (en) Method and apparatus for cleaning waste flue gases
GB845755A (en) &#34;improvements in and relating to low-temperature gas absorption&#34;
GB912091A (en) Process and apparatus for the desorption of charged absorbents
GB1056067A (en) Improvements relating to gas scrubbers
ES318539A1 (en) Procedure for the separation of carbon dioxide and ammonia from a mixture of them with water vapor. (Machine-translation by Google Translate, not legally binding)
CN110479059A (en) Trimethylamine exhaust gas recovery system and method in a kind of Parylene production process
GB956608A (en) Process and regulating installation for concentrating hydrochloric acid from gases containing hydrogen chloride
DE3161844D1 (en) Process and apparatus for regulating the ammonia content in a liquid for washing a gas
US1851163A (en) Apparatus for effecting alpha partial separation of mixed gases
GB881941A (en) Improvements in or relating to processes of heat recovery between gas humidification and de-humidification processes
JPS5649958A (en) Measuring device for ammonia nitrogen present in water
FR1141196A (en) Process for separating methane from its mixtures with air, which is rich in methane
GB882797A (en) Method and apparatus for sampling liquid
ES462645A1 (en) Humidifying air
SU713580A1 (en) Gas drying method
JPS52128897A (en) Desulfurization of flue gas by wet line-gypsum process
SU138407A1 (en) The method of determining the coefficients of mass transfer during the absorption of ethyl alcohol vapor by water
JPS56143977A (en) Tritium water vapor capturing device
GB906413A (en) Improvements in or relating to removal of dissolved carbon dioxide
GB747280A (en) Process for drying phosgene
ES8308221A1 (en) Process and apparatus for conditioning saliferous atmospheric intake air
JPS51111913A (en) An injection method of the liquid-gas
GB1023913A (en) An improved process for the manufacture of sodium carbonate
SU511349A1 (en) The method of purification of sugar-containing solution
JPS6441857A (en) Automatically measuring apparatus for acid gas in atmospheric air