GB912091A - Process and apparatus for the desorption of charged absorbents - Google Patents
Process and apparatus for the desorption of charged absorbentsInfo
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/08—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors
- C10K1/10—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids
- C10K1/12—Purifying 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/14—Separation 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
-
- 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
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/40—Capture or disposal of greenhouse gases of CO2
-
- 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
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
-
- 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
- Y02P20/151—Reduction 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.
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)
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)
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 |
-
1958
- 1958-04-25 DE DEF25590A patent/DE1099501B/en active Pending
-
1959
- 1959-04-27 GB GB14371/59A patent/GB912091A/en not_active Expired
Cited By (1)
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 |
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