GB641992A - Method of purifying liquids - Google Patents
Method of purifying liquidsInfo
- Publication number
- GB641992A GB641992A GB34623/47A GB3462347A GB641992A GB 641992 A GB641992 A GB 641992A GB 34623/47 A GB34623/47 A GB 34623/47A GB 3462347 A GB3462347 A GB 3462347A GB 641992 A GB641992 A GB 641992A
- Authority
- GB
- United Kingdom
- Prior art keywords
- carbon
- liquid
- benzene
- dry
- adsorption
- 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
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B20/00—Purification of sugar juices
- C13B20/12—Purification of sugar juices using adsorption agents, e.g. active carbon
- C13B20/123—Inorganic agents, e.g. active carbon
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D15/00—Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13K—SACCHARIDES OBTAINED FROM NATURAL SOURCES OR BY HYDROLYSIS OF NATURALLY OCCURRING DISACCHARIDES, OLIGOSACCHARIDES OR POLYSACCHARIDES
- C13K1/00—Glucose; Glucose-containing syrups
- C13K1/06—Glucose; Glucose-containing syrups obtained by saccharification of starch or raw materials containing starch
- C13K1/08—Purifying
Abstract
Aqueous solutions of organic acids and salts thereof are passed through one or more columns of granular activated carbon which in dry condition has a volume weight of at most 250 grams per litre, a heat of adsorption for benzene of at least 23 calories per gram of dry carbon, and an adsorption of benzene at 20 DEG C. from a flow of air 92.7 per cent saturated with benzene at that temperature of at least 60 grams per 100 grams of dry carbon, the entirely or partly exhausted carbon being regenerated in situ with an alkaline liquid. The liquid may be previously freed from coarse colloidal impurities by bentonite or bleaching earth, powdered active carbon, and carbonaceous materials treated with chemicals at low temperatures and may be subjected to an after-treatment with decolourizing carbon applied either in suspension or in secondary filters. The liquid to be purified should have an apparent time of contact with the carbon of at least half an hour, and the regenerant liquid, used hot and followed and/or preceded by a dilute acid, is preferably passed through the carbon in the opposite direction to it. The carbon should have a granular size not exceeding 2 mm., preferably 1/2 to 1 1/2 mm. Specifications 228,582 and 273,761, [both in Class 90], are referred to. The Specification as open to inspection under Sect. 91 comprises also the preliminary purification of the liquid with precipitates of calcium phosphate, calcium sulphite, calcium carbonate and aluminium hydroxide, preferably in the form of gel, or combinations of two or more of these substances. This subject-matter does not appear in the Specification as accepted.ALSO:Aqueous solutions of sugars are passed through one or more columns of granular activated carbon which in dry condition has a volume weight of at most 250 grams per litre, a heat of adsorption for benzene of at least 23 calories per gram of dry carbon, and an adsorption of benzene at 20 DEG C from a flow of air 92.7 per cent saturated with benzene at that temperature of at least 60 grams per 100 grams of dry carbon, the entirely or partly exhausted carbon being regenerated in situ with an alkaline liquid. The liquid may be previously freed from coarse colloidal impurities by bentonite or bleaching earth, powdered active carbon, and carbonaceous materials treated with chemicals at low temperatures, and may be subjected to an after-treatment with decolorizing carbon applied either in suspension or in secondary filters. The liquid to be purified should have an apparent time of contact with the carbon of at least half an hour, and the regenerant liquid, used hot and followed and/or preceded by a dilute acid, is preferably passed through the carbon in the opposite direction to it. The carbon should have a granular size not exceeding 2 mm., preferably 1/2 to 1 1/2 mm. Specifications 228,582 and 273,761, [both in Class 90], are referred to. The Specification as open to inspection under Sect. 91, comprises also the preliminary purification of the liquid with precipitates of calcium phosphate, calcium sulphite, calcium carbonate and aluminium hydroxide, preferably in the form of gel, or combinations of two or more of these substances. This subject-matter does not appear in the Specification as accepted.ALSO:Liquids such as aqueous solutions of sugars, organic acids and salts thereof are passed through one or more columns of granular activated carbon which in dry condition has a volume weight of at most 250 grams per litre, a heat of adsorption for benzene of at least 23 calories per gram of dry carbon, and an adsorption of benzene at 20 DEG C from a flow of air 92.7 per cent saturated with benzene at that temperature of at least 60 grams per 100 grams of dry carbon, the entirely or partly exhausted carbon being regenerated in situ with an alkaline liquid. The liquid may be previously freed from coarse colloidal impurities by bentonite or bleaching earth, powdered active carbon, and carbonaceous materials treated with chemicals at low temperatures, and may be subjected to an after-treatment with decolorizing carbon applied either in suspension or in secondary filters. The liquid to be purified should have an apparent time of contact with the carbon of at least half an hour, and the regenerant liquid, used hot and followed and/or preceded by a dilute acid, is preferably passed through the carbon in the opposite direction to it. The carbon should have a granular size not exceeding 2 mm, preferably 1/2 to 1 1/2 mm. Specifications 228,582 and 273,761, [both in Class 90], are referred to. The Specification as open to inspection under Sect. 91 comprises also the preliminary purification of the liquid with precipitates of calcium phosphate, calcium sulphite, calcium carbonate and aluminium hydroxide, perferably in the form of gel, or combinations of two or more of these substances. This subject-matter does not appear in the Specification as accepted.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL641992X | 1943-04-30 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB641992A true GB641992A (en) | 1950-08-23 |
Family
ID=19791800
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB34623/47A Expired GB641992A (en) | 1943-04-30 | 1947-12-30 | Method of purifying liquids |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB641992A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2763580A (en) * | 1951-01-29 | 1956-09-18 | Pittsburgh Coke & Chemical Co | Activated carbon treatment of sugar liquors and regeneration |
US2969298A (en) * | 1959-06-22 | 1961-01-24 | Spreckles Sugar Company | Purification of beet sugar solutions |
EP0026078A1 (en) * | 1979-09-18 | 1981-04-01 | Penicillin Assays, Inc. | Process for removing antibiotics or residues thereof from milk contaminated therewith |
-
1947
- 1947-12-30 GB GB34623/47A patent/GB641992A/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2763580A (en) * | 1951-01-29 | 1956-09-18 | Pittsburgh Coke & Chemical Co | Activated carbon treatment of sugar liquors and regeneration |
US2969298A (en) * | 1959-06-22 | 1961-01-24 | Spreckles Sugar Company | Purification of beet sugar solutions |
EP0026078A1 (en) * | 1979-09-18 | 1981-04-01 | Penicillin Assays, Inc. | Process for removing antibiotics or residues thereof from milk contaminated therewith |
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