GB286622A - Process for removing readily absorbed gases, more particularly carbon dioxide and sulphuretted hydrogen, from gas mixtures by absorption in water under pressure - Google Patents

Process for removing readily absorbed gases, more particularly carbon dioxide and sulphuretted hydrogen, from gas mixtures by absorption in water under pressure

Info

Publication number
GB286622A
GB286622A GB6882/28A GB688228A GB286622A GB 286622 A GB286622 A GB 286622A GB 6882/28 A GB6882/28 A GB 6882/28A GB 688228 A GB688228 A GB 688228A GB 286622 A GB286622 A GB 286622A
Authority
GB
United Kingdom
Prior art keywords
water
tower
carbon dioxide
sulphuretted hydrogen
per cent
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
GB6882/28A
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.)
Linde GmbH
Original Assignee
Gesellschaft fuer Lindes Eismaschinen 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 Gesellschaft fuer Lindes Eismaschinen AG filed Critical Gesellschaft fuer Lindes Eismaschinen AG
Publication of GB286622A publication Critical patent/GB286622A/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
    • C10K1/101Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids with water only

Abstract

286,622. Ges. f³r Linde's Eismaschinen Akt.-Ges. March 5, 1927, [Convention date]. Washing processes for the removal of readily absorbed gases, more particularly sulphuretted hydrogen and carbon dioxide from gas mixtures by absorption in water under pressure which is subsequently regenerated, are effected in two towers in the first of which the sulphuretted hydrogen is washed with water saturated with carbon dioxide withdrawn from the second tower which receives regenerated water, the water containing sulphuretted hydrogen leaving the first tower being regenerated apart from the remaining water. A lignite gas containing 7.5 per cent of sulphuretted hydrogen and 30 per cent of carbon dioxide is compressed in a compressor 1 and the heat of compression absorbed in a refrigerator 2. The gas passes to a tower 3 receiving sufficient water through an inlet 4 to absorb the sulphuretted hydrogen and then enters a tower 8 fed with nearly double the amount of water through an inlet 10. Water from the tower 3 is reduced to atmospheric pressure in a turbine 7 and gas containing about 25 per cent of sulphuretted hydrogen is separated in a vessel 12, a further quantity of gas being removed in a separator 14 by a vacuum pump 15. These gases may be passed to Claus furnaces to recover sulphur. Last traces of sulphuretted hydrogen are removed in a tower 16 fed with ferric oxide or sulphur dioxide, the water collect. ing in a container 17. Water from the tower 8 after reduction of pressure in a turbine 24 passes to a separator 18 in which a gas containing about 75 per cent of carbon dioxide is obtained. A further quantity of carbon dioxide is expelled by aeration in a tower 20. Regenerated water collects in a container 21 and with that from the container 17 is returned to the system by a turbopump 22. To eliminate corrosion of the tower walls or pipes, alkali such as sodium carbonate may be added to the water. The removal of sulphur dioxide in the first tower from gases containing it together with carbon dioxide is referred to.
GB6882/28A 1927-03-05 1928-03-05 Process for removing readily absorbed gases, more particularly carbon dioxide and sulphuretted hydrogen, from gas mixtures by absorption in water under pressure Expired GB286622A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE286622X 1927-03-05

Publications (1)

Publication Number Publication Date
GB286622A true GB286622A (en) 1929-06-05

Family

ID=6059094

Family Applications (1)

Application Number Title Priority Date Filing Date
GB6882/28A Expired GB286622A (en) 1927-03-05 1928-03-05 Process for removing readily absorbed gases, more particularly carbon dioxide and sulphuretted hydrogen, from gas mixtures by absorption in water under pressure

Country Status (1)

Country Link
GB (1) GB286622A (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2416413A (en) * 1943-04-27 1947-02-25 Somerset Henry Beaufort Electrolytic treatment of alkaline process cooking liquors
US2649166A (en) * 1950-05-02 1953-08-18 Allied Chem & Dye Corp Absorption of carbon dioxide from gases containing the same
US2718275A (en) * 1953-04-27 1955-09-20 Infilco Inc Degasifying apparatus and method
US2720280A (en) * 1953-02-25 1955-10-11 Cons Mining & Smelting Co Method of treating gases
US2727587A (en) * 1950-12-14 1955-12-20 Linde Eismasch Ag Method for the purification and separation of gas mixtures
US2781862A (en) * 1952-04-03 1957-02-19 Blaw Knox Co Cold recovery absorption system
US2881137A (en) * 1954-07-01 1959-04-07 Dorroliver Inc Bacterial digestion of organic matter
US3085380A (en) * 1959-10-23 1963-04-16 Engineers & Fabricators Inc Adsorption process
US3104958A (en) * 1960-06-23 1963-09-24 Black Sivalls & Bryson Inc Method and apparatus for dehydrating and acidic gas stream
US4780115A (en) * 1986-04-18 1988-10-25 Linde Aktiengesellschaft Process for removing undesirable components from gases

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2416413A (en) * 1943-04-27 1947-02-25 Somerset Henry Beaufort Electrolytic treatment of alkaline process cooking liquors
US2649166A (en) * 1950-05-02 1953-08-18 Allied Chem & Dye Corp Absorption of carbon dioxide from gases containing the same
US2727587A (en) * 1950-12-14 1955-12-20 Linde Eismasch Ag Method for the purification and separation of gas mixtures
US2781862A (en) * 1952-04-03 1957-02-19 Blaw Knox Co Cold recovery absorption system
US2720280A (en) * 1953-02-25 1955-10-11 Cons Mining & Smelting Co Method of treating gases
US2718275A (en) * 1953-04-27 1955-09-20 Infilco Inc Degasifying apparatus and method
US2881137A (en) * 1954-07-01 1959-04-07 Dorroliver Inc Bacterial digestion of organic matter
US3085380A (en) * 1959-10-23 1963-04-16 Engineers & Fabricators Inc Adsorption process
US3104958A (en) * 1960-06-23 1963-09-24 Black Sivalls & Bryson Inc Method and apparatus for dehydrating and acidic gas stream
US4780115A (en) * 1986-04-18 1988-10-25 Linde Aktiengesellschaft Process for removing undesirable components from gases

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