GB1029132A - Improvements in the production of crystals from solutions - Google Patents
Improvements in the production of crystals from solutionsInfo
- Publication number
- GB1029132A GB1029132A GB20536/62A GB2053662A GB1029132A GB 1029132 A GB1029132 A GB 1029132A GB 20536/62 A GB20536/62 A GB 20536/62A GB 2053662 A GB2053662 A GB 2053662A GB 1029132 A GB1029132 A GB 1029132A
- Authority
- GB
- United Kingdom
- Prior art keywords
- feed
- mother liquor
- supersaturated
- supersaturated 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/0004—Crystallisation cooling by heat exchange
- B01D9/0013—Crystallisation cooling by heat exchange by indirect heat exchange
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/0018—Evaporation of components of the mixture to be separated
- B01D9/0022—Evaporation of components of the mixture to be separated by reducing pressure
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/0018—Evaporation of components of the mixture to be separated
- B01D9/0031—Evaporation of components of the mixture to be separated by heating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/0036—Crystallisation on to a bed of product crystals; Seeding
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/0059—General arrangements of crystallisation plant, e.g. flow sheets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/0063—Control or regulation
Landscapes
- Chemical & Material Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Crystal growth is effected by contacting a supersaturated solution derived from a feed liquor and recycled mother liquor with a suspension of growing crystals in an aqueous solution. The supersaturated solution has a supersaturation of less than 0.5 gm. of solute per 100 gm. of solvent. The difference in concentration of the feed and mother liquors is maintained below a predetermined value (12 gm./100 gm. water for adipic acid and 2.5 gm./100 gm. water for benzoic acid). A portion of the mother liquor may be fed to a similar subsequent crystallization stage. The supersaturated solution may be obtained by passing a mixture of feed and a portion of the mother liquor to an evaporator (Fig. 2, not shown) or may be formed in the crystallizer itself from supersaturated feed and mother liquor (Fig. 4, not shown).ALSO:Crystal growth is effected by contacting a supersaturated solution derived from a feed liquor and recycled mother liquor with a suspension of growing crystals in an aqueous solution. The supersaturated solution has a supersaturation of less than 0.5 gm of solute per 100 gm of solvent. The difference in concentration of the feed and mother liquors is maintained below a predetermined value (12 gm/100 gm water for adipic acid and 2.5 gm/100 gm water for benzoic acid). A portion of the mother liquor may be fed to a similar subsequent crystallization stage. The supersaturated solution may be obtained by passing a mixture of feed and a portion of the mother liquor to an evaporator (Fig. 2, not shown) or may be formed in the crystallizer itself from supersaturated feed and mother liquor (Fig. 4, not shown).
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB20536/62A GB1029132A (en) | 1962-05-29 | 1962-05-29 | Improvements in the production of crystals from solutions |
FR935972A FR1364200A (en) | 1962-05-29 | 1963-05-24 | Improvements in processes for the production of crystals from a solution of crystallizable dissolved substance |
DE19631468487 DE1468487A1 (en) | 1962-05-29 | 1963-05-27 | Multi-step process for crystallizing an aqueous solution of benzoic acid |
US586301A US3467699A (en) | 1962-05-29 | 1966-10-12 | Production of crystals from solutions |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB20536/62A GB1029132A (en) | 1962-05-29 | 1962-05-29 | Improvements in the production of crystals from solutions |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1029132A true GB1029132A (en) | 1966-05-11 |
Family
ID=10147512
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB20536/62A Expired GB1029132A (en) | 1962-05-29 | 1962-05-29 | Improvements in the production of crystals from solutions |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB1029132A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2014187690A1 (en) * | 2013-05-23 | 2014-11-27 | Siemens Aktiengesellschaft | Separation unit and method for separating salts from a detergent |
-
1962
- 1962-05-29 GB GB20536/62A patent/GB1029132A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2014187690A1 (en) * | 2013-05-23 | 2014-11-27 | Siemens Aktiengesellschaft | Separation unit and method for separating salts from a detergent |
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