GB332983A - - Google Patents
Info
- Publication number
- GB332983A GB332983A GB332983DA GB332983A GB 332983 A GB332983 A GB 332983A GB 332983D A GB332983D A GB 332983DA GB 332983 A GB332983 A GB 332983A
- Authority
- GB
- United Kingdom
- Prior art keywords
- acid
- per cent
- cent strength
- acetic
- vapour
- 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.)
- Active
Links
Classifications
-
- 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
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
332,983. Imperial Chemical Industries, Ltd., and Leicester, F. D. May 17, 1929. Acetic and formic acids; esters.-Acetic and formic acids are concentrated by adsorption of the vapour in active carbon, or, in the case of acetic acid the liquid acid may be treated. The adsorbed acid may be recovered by heating the carbon or by reduction of pressure or both, or by the action of volatile solvents; or the adsorbed acid may be used as such for the production of other bodies, for instance, for the production of esters by reaction with alcohols. In an example, acetic acid of 50 per cent strength is vaporized and the vapour is passed through a tube containing active carbon at. 130‹.: when the adsorption slackens, the admission of vapour is stopped, and the pressure is reduced by a vacuum pump, the acid being collected in fractions of 32 and 96 per cent strength. In another example, acetic acid of 33 per cent strength is passed through a vertical tube filled with active charcoal, the flow being stopped when the exit liquor contains 2 per cent of acid; the column is then allowed to drain, and is subsequently heated to 120‹ C. under vacuum, yielding a first fraction of condensate of 32.5 per cent strength, when the temperature is raised to 200‹ C. and a second fraction of 96 per cent strength is obtained.
Publications (1)
Publication Number | Publication Date |
---|---|
GB332983A true GB332983A (en) |
Family
ID=1743400
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB332983D Active GB332983A (en) |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB332983A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4016180A (en) * | 1975-06-18 | 1977-04-05 | Flambeau Paper Company | Chemical concentration by adsorption |
US4691055A (en) * | 1981-12-07 | 1987-09-01 | Cpc International Inc. | Concentration of organic chemicals from dilute aqueous solutions |
-
0
- GB GB332983D patent/GB332983A/en active Active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4016180A (en) * | 1975-06-18 | 1977-04-05 | Flambeau Paper Company | Chemical concentration by adsorption |
US4691055A (en) * | 1981-12-07 | 1987-09-01 | Cpc International Inc. | Concentration of organic chemicals from dilute aqueous solutions |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US5185481A (en) | Method for the separation of impurities from crude ethanol aqueous solution | |
US4349628A (en) | Fermentation process for the manufacture of an organic compound | |
US1939116A (en) | Process for the continuous production of esters of ethyl alcohol | |
US4225394A (en) | Reclamation of spent glycol by treatment with alkali metal hydroxide and distillation | |
JP2024083523A (en) | Purified 1,3-butanediol and method for producing the same | |
GB332983A (en) | ||
US2239095A (en) | Saccharification of wood | |
Tan et al. | Salting-out: A novel purification technique in biorefinery | |
JP5254462B2 (en) | Plastic processing equipment | |
CN108276293A (en) | A kind of separation method of 1,5- pentanediamines | |
WO1981003182A1 (en) | Process and apparatus for continuous production of ethanol | |
Filachione et al. | Preparation of Methyl Lactate. | |
CN111100027A (en) | Method for recovering N, N-dimethylacetamide | |
US1668380A (en) | Continuous process for the dehydration of volatile fatty acids | |
CN111517924A (en) | Method for producing pyrogallic acid by using tannic acid | |
US20020072100A1 (en) | Method to separate ethanol from a fermentation broth | |
US2199983A (en) | Extraction of fatty acids | |
JP2002128727A (en) | Method for distilling and purifying lactic acid | |
Kwon et al. | Optimization and evaluation of organic acid recovery from Kraft black liquor using liquid-liquid extraction | |
CA1192141A (en) | Concentration of organic chemicals from dilute aqueous solutions | |
CN217757172U (en) | System for fixed bed falling film is concentrated and is retrieved sulfuric acid for pivalic acid production | |
KR20010048482A (en) | Methods and equipments of ammonia recycled percolation for biomass treatment | |
CN214496148U (en) | Acrylic acid refined acid unit raffinate processing system | |
US2519906A (en) | Production of lactig acid esters | |
US1936172A (en) | Treatment of organic compounds |