GB987638A - Apparatus for effecting intimate contact between particulate material and liquid - Google Patents
Apparatus for effecting intimate contact between particulate material and liquidInfo
- Publication number
- GB987638A GB987638A GB4480162A GB4480162A GB987638A GB 987638 A GB987638 A GB 987638A GB 4480162 A GB4480162 A GB 4480162A GB 4480162 A GB4480162 A GB 4480162A GB 987638 A GB987638 A GB 987638A
- Authority
- GB
- United Kingdom
- Prior art keywords
- pellets
- water
- column
- chamber
- calcium carbonate
- 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
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5281—Installations for water purification using chemical agents
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Combustion & Propulsion (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Abstract
A starter of calcium carbonate pellets is placed at the bottom of the main chamber 10 in the annular column 24. The raw-water and lime slurry are pumped through the tangential inlet pipes 26 and injectors 28 respectively and are forced round and up the column. Due to the tapering core which extends from 1/3 to 1/2 the height of the chamber the rotational speed of flow of the water and slurry mixture decreases as it rises in the column so that considerable turbulenece of the mixture is achieved. The water is softened by the chemical reaction of the calcium hydroxide with the calcium bicarbonate and the solution becomes, after a short period of operations, super-saturated with calcium carbonate. The latter crystallizes out of solution and forms on the already present calcium carbonate pellets. The crystallization is greatly assisted by the turbulence brought about by the increasing cross-sectional area of the annular column. The pellets are carried up the column and then fall to the bottom again as they reduce speed. The pellets fall down to <PICT:0987638/C1/1> the region of at least cross-sectional area where they are swept up again by the inflowing slurry and water. The pellets gradually increase in size and other pellets form. From time to time pellets are removed by means of the draw-off pipe 29. For this purpose it is desirable to turn off the flow from the injector and inlet adjacent the draw-off pipe. The softened water rises in the funnel-shaped chamber 12 and flows over the inner wall 14 which forms a weir. The flow proceeds from the trough 17 through the outlet 18. Instead of the construction of a core made up to two tapering portions a simple cone may be provided. Alternatively the core may have a curved profile but the curve must be convex to ensure maximum velocities at the base of the chamber.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB4480162A GB987638A (en) | 1962-11-27 | 1962-11-27 | Apparatus for effecting intimate contact between particulate material and liquid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB4480162A GB987638A (en) | 1962-11-27 | 1962-11-27 | Apparatus for effecting intimate contact between particulate material and liquid |
Publications (1)
Publication Number | Publication Date |
---|---|
GB987638A true GB987638A (en) | 1965-03-31 |
Family
ID=10434807
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB4480162A Expired GB987638A (en) | 1962-11-27 | 1962-11-27 | Apparatus for effecting intimate contact between particulate material and liquid |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB987638A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2354972A1 (en) * | 1976-06-14 | 1978-01-13 | Manahl Robert | LARGE CAPACITY CONTAINER, FOR WASTE WATER AND SLUDGE WATER TREATMENT |
GB2241444A (en) * | 1990-03-03 | 1991-09-04 | Kali & Salz Ag | Apparatus and method for obtaining crystals of a defined grain size from super-saturated solutions, in particular salt solutions |
NL1013238C2 (en) * | 1999-10-07 | 2001-04-10 | Pacques Bv | Crystallization reactor. |
-
1962
- 1962-11-27 GB GB4480162A patent/GB987638A/en not_active Expired
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2354972A1 (en) * | 1976-06-14 | 1978-01-13 | Manahl Robert | LARGE CAPACITY CONTAINER, FOR WASTE WATER AND SLUDGE WATER TREATMENT |
GB2241444A (en) * | 1990-03-03 | 1991-09-04 | Kali & Salz Ag | Apparatus and method for obtaining crystals of a defined grain size from super-saturated solutions, in particular salt solutions |
FR2659028A1 (en) * | 1990-03-03 | 1991-09-06 | Kali & Salz Ag | PROCESS AND DEVICE FOR OBTAINING CRYSTALLIZATION PRODUCTS HAVING A DEFINED GRAIN SIZE FROM SURSATURED SOLUTIONS, IN PARTICULAR SALT SOLUTIONS. |
GB2241444B (en) * | 1990-03-03 | 1994-05-11 | Kali & Salz Ag | Apparatus and method for obtaining crystals of a defined grain size from supersaturated solutions,in particular salt solutions |
NL1013238C2 (en) * | 1999-10-07 | 2001-04-10 | Pacques Bv | Crystallization reactor. |
EP1090681A1 (en) * | 1999-10-07 | 2001-04-11 | Paques B.V. | Crystallisation reactor |
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