FR2409780A1 - Continuous crystallisation process - has several crystalliser units in series with counterflow through them and rising flow classification in crystal outlet (NO 27.12.77) - Google Patents
Continuous crystallisation process - has several crystalliser units in series with counterflow through them and rising flow classification in crystal outlet (NO 27.12.77)Info
- Publication number
- FR2409780A1 FR2409780A1 FR7735514A FR7735514A FR2409780A1 FR 2409780 A1 FR2409780 A1 FR 2409780A1 FR 7735514 A FR7735514 A FR 7735514A FR 7735514 A FR7735514 A FR 7735514A FR 2409780 A1 FR2409780 A1 FR 2409780A1
- Authority
- FR
- France
- Prior art keywords
- series
- stage
- crystalliser
- counterflow
- units
- 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.)
- Granted
Links
Classifications
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Crystallisation process contains a series of stages in each of which partial crystallisation occurs. The mixture enters a separation stage, as it leaves the final stage. There is a separation between fine crystals and the coarser ones required as product by maintaining an upwards velocity of feed liquor in the crystal outlet passage. The coarse crystals from each stage are fed back to the previous stage on that there is a gradual growth of crystals from one end of the process to the other. The crystal product is taken off in equilibrium with the saturated feed liquor while the spent liquor leaves from the other end of the process. Used for industrial crystallisations esp. of Al(OH)3. The process is simple and economic, it gives a uniform product of reasonable size and is not sensitive to other process variations.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR7735514A FR2409780A1 (en) | 1977-11-25 | 1977-11-25 | Continuous crystallisation process - has several crystalliser units in series with counterflow through them and rising flow classification in crystal outlet (NO 27.12.77) |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR7735514A FR2409780A1 (en) | 1977-11-25 | 1977-11-25 | Continuous crystallisation process - has several crystalliser units in series with counterflow through them and rising flow classification in crystal outlet (NO 27.12.77) |
Publications (2)
Publication Number | Publication Date |
---|---|
FR2409780A1 true FR2409780A1 (en) | 1979-06-22 |
FR2409780B1 FR2409780B1 (en) | 1982-10-29 |
Family
ID=9198065
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
FR7735514A Granted FR2409780A1 (en) | 1977-11-25 | 1977-11-25 | Continuous crystallisation process - has several crystalliser units in series with counterflow through them and rising flow classification in crystal outlet (NO 27.12.77) |
Country Status (1)
Country | Link |
---|---|
FR (1) | FR2409780A1 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0157561A2 (en) * | 1984-03-30 | 1985-10-09 | Kawasaki Steel Corporation | Metal stripping system and an operation process therefor |
FR2881360A1 (en) * | 2005-02-02 | 2006-08-04 | Crystal Evap Consult Sarl | Solution crystallization comprises use of reactor with series of compartments for recycling solution and recuperation of mother liquor |
CN106132496A (en) * | 2014-03-19 | 2016-11-16 | 巴斯夫欧洲公司 | For the method and apparatus that material is separated from solution |
-
1977
- 1977-11-25 FR FR7735514A patent/FR2409780A1/en active Granted
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0157561A2 (en) * | 1984-03-30 | 1985-10-09 | Kawasaki Steel Corporation | Metal stripping system and an operation process therefor |
EP0157561A3 (en) * | 1984-03-30 | 1986-10-01 | Kawasaki Steel Corporation | Metal stripping system and an operation process therefor |
US4830836A (en) * | 1984-03-30 | 1989-05-16 | Kawasaki Steel Corporation | Metal stripping system and an operation process therefor |
FR2881360A1 (en) * | 2005-02-02 | 2006-08-04 | Crystal Evap Consult Sarl | Solution crystallization comprises use of reactor with series of compartments for recycling solution and recuperation of mother liquor |
WO2006082341A1 (en) * | 2005-02-02 | 2006-08-10 | Crystal-Evap Consult | Crystallization method and device |
CN106132496A (en) * | 2014-03-19 | 2016-11-16 | 巴斯夫欧洲公司 | For the method and apparatus that material is separated from solution |
CN106132496B (en) * | 2014-03-19 | 2020-03-13 | 巴斯夫欧洲公司 | Method and device for separating substances from a solution |
Also Published As
Publication number | Publication date |
---|---|
FR2409780B1 (en) | 1982-10-29 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
GB807100A (en) | Improvements in process and apparatus for purification of crystals | |
KR900017631A (en) | Chromatographic Separation Method | |
GB1500892A (en) | Degritting and fibre removal system | |
ATE33454T1 (en) | PROCESS FOR MAKING GRANULES. | |
ATE23276T1 (en) | PROCESS FOR CONTINUOUS PARTIAL CRYSTALLIZATION AND SEPARATION FROM A LIQUID MIXTURE AND DEVICE FOR CARRYING OUT THE PROCESS. | |
BE901129Q (en) | APPARATUS FOR MOLDING CALCIUM SILICATE CRYSTAL SLURRY. | |
ZA744383B (en) | Method and device for separating gaseous or vaporous materials, especially isotopes by means of separation nozzles | |
ES8106697A1 (en) | Purification of acrylonitrile. | |
FR2409780A1 (en) | Continuous crystallisation process - has several crystalliser units in series with counterflow through them and rising flow classification in crystal outlet (NO 27.12.77) | |
JPS5745303A (en) | Countercurrent crystal forming method through recirculation and its device | |
IT1088470B (en) | Continuous crystallisation process - has several crystalliser units in series with counterflow through them and rising flow classification in crystal outlet (NO 27.12.77) | |
ES306649A1 (en) | A procedure for continuous recovery of p-xylene from liquid mixtures containing p-xylene. (Machine-translation by Google Translate, not legally binding) | |
ES252762A1 (en) | Filtration process | |
GB771038A (en) | Improvements in method and apparatus for the purification of crystals | |
ES316213A1 (en) | A procedure for the separation and purification of at least one component of a liquid mixture of multiple components. (Machine-translation by Google Translate, not legally binding) | |
ATE101804T1 (en) | PROCESS AND DEVICE FOR EXCLUDING FINE GRAIN HOT SOLIDS. | |
GB976526A (en) | Filtration apparatus | |
BE857714A (en) | PROCESS FOR SEPARATING ISOTOPES FROM A GASEOUS MIXTURE | |
ES384092A1 (en) | Production of pure p-xylene | |
PL366474A1 (en) | Process for size classifying ammonium sulfate crystals which are present in a suspension | |
NO140226C (en) | PROCEDURE FOR CONTINUOUS CRYSTALLIZATION | |
JPS5316386A (en) | Ozonizer | |
GB1222678A (en) | Process for purifying melamine | |
ES464409A1 (en) | A procedure for continuous crystallization of a solution of at least one crystallizing material. (Machine-translation by Google Translate, not legally binding) | |
JPS5797814A (en) | Thickness controlling method for strip |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
ST | Notification of lapse |