GB760810A - Improvements in and relating to processes and installations for crystallizing substances from solutions - Google Patents
Improvements in and relating to processes and installations for crystallizing substances from solutionsInfo
- Publication number
- GB760810A GB760810A GB23594/53A GB2359453A GB760810A GB 760810 A GB760810 A GB 760810A GB 23594/53 A GB23594/53 A GB 23594/53A GB 2359453 A GB2359453 A GB 2359453A GB 760810 A GB760810 A GB 760810A
- Authority
- GB
- United Kingdom
- Prior art keywords
- evaporator
- crystallizer
- liquor
- heater
- pump
- 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
-
- 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
-
- 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
Abstract
<PICT:0760810/III/1> <PICT:0760810/III/2> <PICT:0760810/III/3> A crystallizing apparatus comprises means for producing supersaturation in a liquid (a heater and an evaporator or a cooler or a heater only) and a crystallizer arranged in two circuits, the circuit containing the crystallizer forming a shunt to the circuit containing the supersaturator and the flow through the shunt circuit being smaller than that through the primary circuit. By this means more efficient use may be made of the supersaturating system. The crystallizer may be of the type in which crystals are maintained in suspension until they grow to the required size. Entrained small crystals may be wholly or partially separated from the liquor returning from the crystallizer to the primary circuit. As described, Fig. 1, liquor is circulated from an evaporator B via pumps F and G to heater A and back to evaporator B while liquor is also taken from B to crystallizer H and then by overflow K back to the primary circuit. In Fig. 2 liquor is circulated by pump F through heater A and evaporator B, liquor also being taken from the evaporator at M to crystallizer H from which it is returned by pump G to the evaporator. In Fig. 3 liquor is circulated by pump F from evaporator B through heater A back to the evaporator. A secondary flow is also maintained by pump G from evaporator B crystallizer H and separator N which removes entrained crystals and returns them at P to the crystallizer. In all arrangements fresh liquor is introduced at E.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL316720X | 1952-09-01 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB760810A true GB760810A (en) | 1956-11-07 |
Family
ID=19783825
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB23594/53A Expired GB760810A (en) | 1952-09-01 | 1953-08-26 | Improvements in and relating to processes and installations for crystallizing substances from solutions |
Country Status (4)
Country | Link |
---|---|
CH (1) | CH316720A (en) |
FR (1) | FR1086976A (en) |
GB (1) | GB760810A (en) |
NL (1) | NL172193B (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104874200A (en) * | 2015-05-28 | 2015-09-02 | 山西长林环保机械设备有限公司 | Crystallizing device for treating coking and desulfurizing waste liquid |
CN109173329A (en) * | 2018-10-31 | 2019-01-11 | 浙江新和成股份有限公司 | Device for evaporative crystallization |
-
0
- NL NLAANVRAGE7803475,A patent/NL172193B/en unknown
-
1953
- 1953-08-26 GB GB23594/53A patent/GB760810A/en not_active Expired
- 1953-08-28 CH CH316720D patent/CH316720A/en unknown
- 1953-08-31 FR FR1086976D patent/FR1086976A/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104874200A (en) * | 2015-05-28 | 2015-09-02 | 山西长林环保机械设备有限公司 | Crystallizing device for treating coking and desulfurizing waste liquid |
CN109173329A (en) * | 2018-10-31 | 2019-01-11 | 浙江新和成股份有限公司 | Device for evaporative crystallization |
CN109173329B (en) * | 2018-10-31 | 2023-08-29 | 浙江新和成股份有限公司 | Device for evaporative crystallization |
Also Published As
Publication number | Publication date |
---|---|
FR1086976A (en) | 1955-02-17 |
CH316720A (en) | 1956-10-31 |
NL172193B (en) |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
GB431812A (en) | Improvements in crystallization | |
GB392829A (en) | Improvements in crystallization processes | |
US2029467A (en) | Distillation of ammonia from aqueous ammoniacal brines | |
GB760810A (en) | Improvements in and relating to processes and installations for crystallizing substances from solutions | |
GB1010840A (en) | A process of recovering alkali metal dithionite from a solution thereof by cooling and crystallizing | |
GB377337A (en) | Improvements in methods of and apparatus for crystallisation | |
GB460834A (en) | Improvements in or relating to apparatus for accelerated crystallisation | |
GB1169786A (en) | Process for the Recovery of rho-Xylene from a Hydrocarbon Feed | |
ES386356A1 (en) | Continuous process for crystallization | |
ES295523A1 (en) | Crystallization of sugar | |
US2738254A (en) | Process for the separation of sodium tetraborate from liquors containing both sodium tetraborate and potassium chloride | |
US1794553A (en) | Process of recovering salts from minerals | |
US1284380A (en) | Art of preparing ammonium perchlorate. | |
US1916825A (en) | Separating substances from solutions thereof | |
GB815791A (en) | Improvements in or relating to the production of crystals from solutions | |
US1500995A (en) | Manufacture of caustic soda | |
US1921481A (en) | Process for recovering potash salts from liquors containing borax | |
SU692612A1 (en) | Vacuum crystallizer | |
US1356806A (en) | Process of separating nitrates of potassium and sodium | |
GB663876A (en) | Separation of solutes by continuous solvent extraction | |
GB370793A (en) | Process of and apparatus for obtaining coarse crystals of ammonium salts formed in an acid saturator | |
GB808176A (en) | Improvements in and relating to methods of crystallization | |
GB1046730A (en) | Treatment of honey and similar substances | |
SU106874A1 (en) | The method of obtaining highly concentrated anhydrous calcium chlorate | |
GB191412475A (en) | A Two Stage Evaporation Process for Recovering Nitrate of Soda from Liquors containing it and Sodium Chloride in Solution, and an Apparatus for carrying out such Process. |