GB621797A - Improved method and apparatus for the continuous crystallization in vacuo of sugar solutions and the like - Google Patents
Improved method and apparatus for the continuous crystallization in vacuo of sugar solutions and the likeInfo
- Publication number
- GB621797A GB621797A GB13728/46A GB1372846A GB621797A GB 621797 A GB621797 A GB 621797A GB 13728/46 A GB13728/46 A GB 13728/46A GB 1372846 A GB1372846 A GB 1372846A GB 621797 A GB621797 A GB 621797A
- Authority
- GB
- United Kingdom
- Prior art keywords
- compartments
- mass
- compartment
- heater
- solution
- 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
- C13B30/00—Crystallisation; Crystallising apparatus; Separating crystals from mother liquors ; Evaporating or boiling sugar juice
- C13B30/02—Crystallisation; Crystallising apparatus
- C13B30/022—Continuous processes, apparatus therefor
Landscapes
- Chemical & Material Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Organic Chemistry (AREA)
- Saccharide Compounds (AREA)
Abstract
<PICT:0621797/III/1> <PICT:0621797/III/2> Sugar and like solutions are continuously crystallized in vacuo by feeding the solution to the first of a series of heated and interconnecting compartments to commence the evaporation and crystallization, and causing the resulting mass to flow continuously through the succeeding compartments in each of which the mass receives a continuous controlled additional supply of the solution, the displacement of the mass being effected by a difference in the level of the mass in successive compartments or by a difference of pressure between successive compartments. The solution fed to the first compartment may be nearly saturated, and may be seeded before or after it enters the compartment. In the vertical apparatus shown, the annular chamber constituted by axial tube 1 and casing 2 is divided into five compartments 31-35 of increasing volume by means of radial partitions 3 extending from the bottom of the casing up to cap-member 4. The tubular heater 6 may be common to all the compartments or may be itself divided into compartments. The crystallizing mass in compartment 31 circulates through the heating tubes and annular chamber 8, and part of it passes through opening 9 into compartment 32; the transfer being guided by deflector 10 and partition 11. After flowing through the compartments, in each of which it receives a continuous flow of saturated solution through an adjustable cock, the mass is removed from compartment 35 through opening 12 in axial tube 1. The steam pressure inside heater 6 is adjusted so as to properly associate the simultaneous evaporation and crystallization. In exceptional cases, it is possible to adjust the heating by acting on the proportion of incondensable gases in the upper portion of the heater. The speed of evaporation as a whole is adjusted by providing the pipe connecting dome 5 to the condenser with an automatic vacuum regulator. If the displacement of the mass is effected by pressure differences, these are controlled by adjusting the cross-sections of steam-outlets 13, 131 and 132. In a modification, the heater 6 is secured directly to axial tube 1. A horizontal apparatus is also described.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR621797X | 1941-09-30 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB621797A true GB621797A (en) | 1949-04-20 |
Family
ID=8985387
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB13728/46A Expired GB621797A (en) | 1941-09-30 | 1946-05-06 | Improved method and apparatus for the continuous crystallization in vacuo of sugar solutions and the like |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB621797A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2610642A1 (en) * | 1987-02-11 | 1988-08-12 | Eridania | PROCESS AND DEVICE FOR CONTINUOUS CRYSTALLIZATION OF MEDIUM AND LOW PURE MASSES IN A SUGAR REFINERY |
WO2001091875A1 (en) * | 2000-06-01 | 2001-12-06 | The Tongaat-Hulett Group Limited | Continuous vacuum pan |
-
1946
- 1946-05-06 GB GB13728/46A patent/GB621797A/en not_active Expired
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2610642A1 (en) * | 1987-02-11 | 1988-08-12 | Eridania | PROCESS AND DEVICE FOR CONTINUOUS CRYSTALLIZATION OF MEDIUM AND LOW PURE MASSES IN A SUGAR REFINERY |
BE1001951A5 (en) * | 1987-02-11 | 1990-04-24 | Eridania Zucherifici Nazionali | PROCESS AND DEVICE FOR THE CONTINUOUS CRYSTALLIZATION OF MEDIUM AND LOW PURITY MASS-CUITS IN A SUGAR REFINERY. |
WO2001091875A1 (en) * | 2000-06-01 | 2001-12-06 | The Tongaat-Hulett Group Limited | Continuous vacuum pan |
US6991708B2 (en) | 2000-06-01 | 2006-01-31 | The Tongaat-Hulett Group Limited | Continuous vacuum pan |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
GB1443554A (en) | Apparatus for distilling natural water | |
ES349539A1 (en) | Water distillation plant | |
GB1239140A (en) | ||
AR000280A1 (en) | A method and apparatus for separating a substance from a liquid mixture by fractional crystallization | |
GB621797A (en) | Improved method and apparatus for the continuous crystallization in vacuo of sugar solutions and the like | |
GB834467A (en) | A flash evaporator | |
US3174914A (en) | Tandem flash distilling plant | |
GB1203143A (en) | Boiling apparatus for continuous crystallization and method of operating said apparatus | |
GB990425A (en) | Improvements in and relating to heat-exchangers, such as evaporators | |
US3074473A (en) | Vertical tube evaporators with downward pressure liquid flow | |
GB410762A (en) | Improvements in or relating to apparatus for vaporizing or distilling liquids | |
US2759340A (en) | Compression-operated cooling plant | |
US2570211A (en) | Falling film evaporator | |
GB643190A (en) | Improvements relating to evaporators for refrigerating apparatus | |
GB1051622A (en) | ||
GB588214A (en) | Improvements in tray-type evaporators | |
GB1106619A (en) | Method of and apparatus for multi-stage flash evaporation and contact condensation | |
GB1107980A (en) | Apparatus for concentrating liquors | |
FR2208103A1 (en) | Vertical tube-in-shell heat-exchanger - with separate shell compartments for low and high pressure steam | |
GB1033599A (en) | Improvements relating to falling film type evaporators | |
GB855550A (en) | Improvements in or relating to evaporators | |
US2584250A (en) | Solution preheater for absorption refrigeration systems | |
GB815796A (en) | Improvements in and relating to evaporators | |
US2515690A (en) | Sugar sulfitation apparatus | |
GB585583A (en) | An improved process and apparatus for the continuous crystallisation of sugar |