GB664023A - Improved method of dehydrating sodium hydroxide solutions - Google Patents
Improved method of dehydrating sodium hydroxide solutionsInfo
- Publication number
- GB664023A GB664023A GB2611549A GB2611549A GB664023A GB 664023 A GB664023 A GB 664023A GB 2611549 A GB2611549 A GB 2611549A GB 2611549 A GB2611549 A GB 2611549A GB 664023 A GB664023 A GB 664023A
- Authority
- GB
- United Kingdom
- Prior art keywords
- evaporator
- fed
- per cent
- sodium hydroxide
- 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
- C01—INORGANIC CHEMISTRY
- C01D—COMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
- C01D1/00—Oxides or hydroxides of sodium, potassium or alkali metals in general
- C01D1/04—Hydroxides
- C01D1/42—Concentration; Dehydration
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
Aqueous sodium hydroxide solution preconcentrated below 150 DEG C and containing about 50-75 per cent solids is further concentrated by adding sucrose and evaporating at progressively increasing temperatures above 150 DEG C in contact with nickel surfaces. The sucrose reduces any sodium chlorate in the sodium hydroxide to sodium chloride and also reacts with any oxygen in the evaporator whereby corrosion of the nickel surfaces is inhibited. A 50 per cent aqueous NaOH solution is concentrated in a vacuum evaporator 2 at 2811 of Hg. to a 70 per cent solution which is fed at 115 DEG C to a storage tank 7 where it <PICT:0664023/III/1> is held at 100 DEG C and fed with aqueous sugar solution from a supply tank 8. The 70 per cent liquor is then fed to an evaporator 11 which is a continuous single-pass vertical tubular heat-exchanger wherein the tubes and other parts in contact with the liquor are of nickel. The evaporator 11 is heated with "Dowtherm" (R.T.M.) circulated via pipes 13 and 14 and operates at 2011 of Hg. at the top. An entrained mixture of molten NaOH and water vapour at about 370 DEG C. is discharged via pipe 15 to a separator 16. In modifications the sugar is fed to the evaporator 2 and a small flow of inert gas, e.g. nitrogen or natural gas, is fed into the bottom of the evaporator 11 to prevent "bumping" of the liquid in the tubes.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2611549A GB664023A (en) | 1949-10-11 | 1949-10-11 | Improved method of dehydrating sodium hydroxide solutions |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2611549A GB664023A (en) | 1949-10-11 | 1949-10-11 | Improved method of dehydrating sodium hydroxide solutions |
Publications (1)
Publication Number | Publication Date |
---|---|
GB664023A true GB664023A (en) | 1951-01-02 |
Family
ID=10238607
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2611549A Expired GB664023A (en) | 1949-10-11 | 1949-10-11 | Improved method of dehydrating sodium hydroxide solutions |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB664023A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4837002A (en) * | 1987-03-11 | 1989-06-06 | Basf Aktiengesellschaft | Removal of chlorate from caustic soda |
CN102530993A (en) * | 2011-12-29 | 2012-07-04 | 张健 | Device and method for preparing alkali |
CN107349876A (en) * | 2017-08-30 | 2017-11-17 | 重庆博张机电设备有限公司 | A kind of solid caustic soda production equipment and its alkali lye sugaring device |
CN112225229A (en) * | 2020-10-21 | 2021-01-15 | 华融化学股份有限公司 | Method for preparing high-purity potassium hydroxide solution by microwave heating and concentration |
-
1949
- 1949-10-11 GB GB2611549A patent/GB664023A/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4837002A (en) * | 1987-03-11 | 1989-06-06 | Basf Aktiengesellschaft | Removal of chlorate from caustic soda |
CN102530993A (en) * | 2011-12-29 | 2012-07-04 | 张健 | Device and method for preparing alkali |
CN107349876A (en) * | 2017-08-30 | 2017-11-17 | 重庆博张机电设备有限公司 | A kind of solid caustic soda production equipment and its alkali lye sugaring device |
CN112225229A (en) * | 2020-10-21 | 2021-01-15 | 华融化学股份有限公司 | Method for preparing high-purity potassium hydroxide solution by microwave heating and concentration |
CN112225229B (en) * | 2020-10-21 | 2023-04-07 | 华融化学股份有限公司 | Method for preparing high-purity potassium hydroxide solution by microwave heating and concentration |
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