GB1036559A - Production of sodium hydroxide - Google Patents
Production of sodium hydroxideInfo
- Publication number
- GB1036559A GB1036559A GB2986465A GB2986465A GB1036559A GB 1036559 A GB1036559 A GB 1036559A GB 2986465 A GB2986465 A GB 2986465A GB 2986465 A GB2986465 A GB 2986465A GB 1036559 A GB1036559 A GB 1036559A
- Authority
- GB
- United Kingdom
- Prior art keywords
- vessel
- resin
- water
- liquid
- regenerating
- 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
-
- 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
- B01J47/00—Ion-exchange processes in general; Apparatus therefor
- B01J47/10—Ion-exchange processes in general; Apparatus therefor with moving ion-exchange material; with ion-exchange material in suspension or in fluidised-bed form
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01D—COMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
- C01D5/00—Sulfates or sulfites of sodium, potassium or alkali metals in general
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treatment Of Water By Ion Exchange (AREA)
Abstract
Sodium hydroxide is produced from sea water using a resin-transferring ion exchange apparatus comprising a liquid-passing vessel, a regenerating vessel and a water-washing vessel. Sea water is fed into the liquid-passing vessel charged with ion exchange resin in the OH-form to give sodium hydroxide solution and ion exchange resin converted to the Cl-form. This resin is transferred to the regenerating vessel and contacted in countercurrent with a slurry of calcium hydroxide, the treated liquid being removed from the top of the regenerating vessel. The resin regenerated to the OH-form is passed to the water-washing vessel, washed with water and recycled to the liquid-passing vessel. The regenerating vessel may be provided with a stirrer revolving around a shaft suspended from the top of the vessel; alternatively, the regenerating vessel may be of the movable bed type with an inlet and an outlet for liquid at its lower portion and a resin reservoir connected through a check valve to its upper portion, the resin in the Cl-form being passed into the vessel through the upper portion, the slurry of calcium hydroxide being fed into the centre portion, water being fed through the lower portion, and treated liquid being withdrawn from the top of the vessel, the resin thus being regenerated by counter-current contact with the slurry. The resin in the Cl-form is preferably passed into the vessel intermittently at times when no water is being fed to the vessel. By reacting the sodium hydroxide produced above with sea water, the latter may be purified by removal of the magnesium ions as magnesium hydroxide, the calcium ions being removed as calcium carbonate, for example by treating the sea water with carbon dioxide or sodium carbonate, and the sulphate ions being removed, for example, by means of a weakly basic anion exchange resin in the Cl-form as described in Specification 1,036,560.ALSO:A resin-transferring ion exchange apparatus comprising a liquid-passing vessel, a regenerating vessel and a water-washing vessel is used in a process for producing sodium hydroxide from sea water. Sea water is fed into the liquid-passing vessel charged with ion exchange resin in the OH-form to give sodium hydroxide solution and ion exchange resin converted to the C1-form. This resin is transferred to the regenerating vessel and contacted in countercurrent with a slurry of calcium hydroxide the treated liquid being removed from the top of the regenerating vessel. The resin regenerated to the OH-form is passed to the waterwashing vessel, washed with water and recycled to the liquid-passing vessel. The regenerating vessel may be provided with a stirrer revolving around a shaft suspended from the top of the vessel; alternatively, the regenerating vessel may be of the movable bed type with an inlet and an outlet for liquid at its lower portion and a resin reservoir connected through a check valve to its upper portion, the resin in the C1-form being passed into the vessel through the upper portion, the slurry of calcium hydroxide being fed into the centre portion, water being fed through the lower portion, and treated liquid being withdrawn from the top of the vessel, the resin thus being regenerated by countercurrent contact with the slurry. The resin in the C1-form is preferably passed into the vessel intermittently at times when no water is being fed to the vessel.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP815462 | 1962-03-06 | ||
JP1961162 | 1962-05-17 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1036559A true GB1036559A (en) | 1966-07-20 |
Family
ID=26342616
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2986465A Expired GB1036559A (en) | 1962-03-06 | 1962-12-28 | Production of sodium hydroxide |
Country Status (2)
Country | Link |
---|---|
DE (1) | DE1467216B2 (en) |
GB (1) | GB1036559A (en) |
-
1962
- 1962-12-19 DE DE19621467216 patent/DE1467216B2/en active Pending
- 1962-12-28 GB GB2986465A patent/GB1036559A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
DE1467216A1 (en) | 1969-05-29 |
DE1467216B2 (en) | 1971-09-02 |
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