GB1239112A - - Google Patents
Info
- Publication number
- GB1239112A GB1239112A GB1239112DA GB1239112A GB 1239112 A GB1239112 A GB 1239112A GB 1239112D A GB1239112D A GB 1239112DA GB 1239112 A GB1239112 A GB 1239112A
- Authority
- GB
- United Kingdom
- Prior art keywords
- liquid
- duct
- tube
- vapour
- gas
- 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
- B01D1/00—Evaporating
- B01D1/06—Evaporators with vertical tubes
- B01D1/10—Evaporators with vertical tubes with long tubes, e.g. Kestner evaporators
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/06—Evaporators with vertical tubes
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Sorption Type Refrigeration Machines (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
1,239,112. Evaporators; polymerization; gas-liquid absorption. WIEGAND APPARATEBAU G.m.b.H. 14 Aug., 1969 [15 Aug., 1968], No. 40746/69. Headings B1B and B1X. In order to evaporate a liquid, or carry out a liquid-gas absorption process or a chemical reaction such as the polymerization of a solution or emulsion, the liquid is fed to a tubular duct, which is helically or spirally coiled about one or more axes, while a stream of gas and/or vapour is passed through the duct so that the liquid flows down the internal wall of the duct in the form of a annular film and issues from the entire periphery at the end of the duct. The diameter of the helix should be 0.25 to 8 times the diameter of the duct, and the spacing of consecutive turns of the helix should be between 1.75 and 150 times the diameter of the helix. The duct may be surrounded by a heating-or a cooling-chamber whereby the temperature of the liquid may be controlled. The liquid is supplied at a rate dependent on the hydraulic diameter of the duct. The gas (vapour) is supplied at a rate dependent on the viscosity of the liquid. The Fig. shows an evaporator comprising a helical tube 1 inside a heating chamber 4. Liquid to be concentrated, e.g. an aqueous solution of glucose, is preheated and fed into tube 1 through valve 8 and pipe 7. At the same time, saturated steam flows into tube 1 from chamber 5 which is supplied with steam through valve 11 and pipe 10. As the solution flows down the internal wall of tube 1, evaporation of some of the water takes place. The concentrated solution and vapour enter separator 15; and the concentrated solution is withdrawn from chamber 19 by pump 21. The vapour flows through pipe 22 to condenser 23, which is evacuated by pump 26. Tube 1 may be made of stainless steel and lined with polytetrafluoroethylene. Instead of using a helical tube, the process may be carried out in a helical channel in a block of heat-conductive material. The sulphonation of olefins with SO 3 is referred to; also the nitration or halogenation of aromatic compounds and the halogenation of alkanes.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CH1229568 | 1968-08-15 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1239112A true GB1239112A (en) | 1971-07-14 |
Family
ID=4381663
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1239112D Expired GB1239112A (en) | 1968-08-15 | 1969-08-14 |
Country Status (5)
Country | Link |
---|---|
JP (1) | JPS4812318B1 (en) |
DE (1) | DE1938749A1 (en) |
FR (1) | FR2015736A1 (en) |
GB (1) | GB1239112A (en) |
NL (1) | NL6912472A (en) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS49121686A (en) * | 1973-03-28 | 1974-11-20 | ||
DE2614587A1 (en) * | 1976-04-05 | 1977-10-13 | Metallgesellschaft Ag | PROCEDURE FOR EVAPORATING WATER-BASED LIQUIDS |
DE2811902A1 (en) * | 1978-03-18 | 1979-09-27 | Bayer Ag | PROCESS AND DEVICE FOR REMOVING SOLVENTS AND REACTING SUBSTANCE COMPONENTS IN MIXTURES |
LU79605A1 (en) * | 1978-05-05 | 1979-12-06 | P Laguilharre | PROCESS FOR IMPROVING THE TRANSFER COEFFICIENT IN THE TUBES OF A FALLING FLOAT EVAPORATOR |
JPS60250884A (en) * | 1984-05-29 | 1985-12-11 | Takao Kinzoku Kogyo Kk | Welding device |
JPS60255283A (en) * | 1984-05-29 | 1985-12-16 | Takao Kinzoku Kogyo Kk | Welding device |
JPH0451027Y2 (en) * | 1986-01-24 | 1992-12-01 |
-
1969
- 1969-07-30 DE DE19691938749 patent/DE1938749A1/en active Pending
- 1969-08-14 GB GB1239112D patent/GB1239112A/en not_active Expired
- 1969-08-14 FR FR6928099A patent/FR2015736A1/fr not_active Withdrawn
- 1969-08-14 JP JP6444569A patent/JPS4812318B1/ja active Pending
- 1969-08-15 NL NL6912472A patent/NL6912472A/xx unknown
Also Published As
Publication number | Publication date |
---|---|
DE1938749A1 (en) | 1970-02-19 |
JPS4812318B1 (en) | 1973-04-19 |
FR2015736A1 (en) | 1970-04-30 |
NL6912472A (en) | 1970-02-17 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed | ||
PLNP | Patent lapsed through nonpayment of renewal fees |