WO1996034999A1 - Extraction du bromure - Google Patents
Extraction du bromure Download PDFInfo
- Publication number
- WO1996034999A1 WO1996034999A1 PCT/US1995/005603 US9505603W WO9634999A1 WO 1996034999 A1 WO1996034999 A1 WO 1996034999A1 US 9505603 W US9505603 W US 9505603W WO 9634999 A1 WO9634999 A1 WO 9634999A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- brine
- electrolyser
- filter
- bromide
- sodium hypochlorite
- 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.)
- Ceased
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B15/00—Operating or servicing cells
- C25B15/08—Supplying or removing reactants or electrolytes; Regeneration of electrolytes
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B11/00—Oxides or oxyacids of halogens; Salts thereof
- C01B11/20—Oxygen compounds of bromine
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B7/00—Halogens; Halogen acids
- C01B7/09—Bromine; Hydrogen bromide
- C01B7/096—Bromine
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01D—COMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
- C01D3/00—Halides of sodium, potassium or alkali metals in general
- C01D3/14—Purification
- C01D3/16—Purification by precipitation or adsorption
-
- 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
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/467—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
- C02F1/4672—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation
- C02F1/4674—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation with halogen or compound of halogens, e.g. chlorine, bromine
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/24—Halogens or compounds thereof
- C25B1/26—Chlorine; Compounds thereof
Definitions
- the present invention relates to a method and apparatus for removing bromide from an electrolytic chlorination system. It is well known to produce sodium hypochlorite from sodium chloride brine by converting the brine to sodium hypochlorite in an electrolyser. Sodium hypochlorite is used to treat potable water. Unfortunately, if the brine includes traces of bromide, the electrolyser causes the conversion of the bromide by oxidation to bromate. It is desirable to produce bromate-free sodium hypochlorite for the treatment of potable water as experiments have indicated that bromate may be carcinogenic. It is an object of the present invention to provide a method and apparatus for removing bromide from an electrolytic chlorination system so as to obviate or mitigate the problem outlined above.
- a method for removing bromide from an electrolytic chlorination system in which brine is converted to sodium hypochlorite in an electrolyser, wherein the brine is fed to the electrolyser through a filter containing a medium capable of adsorbing bromine or hypobromous acid, and sodium hypochlorite is fed back from the electrolyser and mixed with the brine feed upstream of the filter to oxidize any bromide in the brine to bromine or hypobromous acid.
- the present invention also provides an electrolyser for converting brine to sodium hypochlorite, means for feeding brine to the electrolyser, a filter through which the brine is fed to the electrolyser, the filter being capable of adsorbing bromine or hypobromous acid, and means for mixing sodium hypochlorite from the electrolyser with the brine upstream of the filter such that bromide in the brine is oxidized to bromine or hypobromous acid.
- hydrochloric acid is mixed with the brine upstream of the filter to maintain a low pH and thereby ensure effective oxidation of the bromide.
- the illustrated electrolytic chlorination system comprises a salt saturator 1 in which brine is prepared.
- the saturator 1 may have a capacity of, for example, 15 cubic meters.
- Brine flows from the saturator 1 through a filter 2 to an electrolyser 3, the brine flow being maintained by a brine transfer pump 4.
- a flow rate through the pump 4 of 51.5 liters per hour may be established.
- the electrolyser 3 is of conventional form and is effective to oxidize the brine to sodium hypochlorite.
- the contents of the electrolyser are mixed with dilution water supplied through line 5 at a rate of 540 liters per hour, the resultant sodium hypochlorite being transferred to a product tank 6 with a capacity of 13 cubic meters.
- sodium hypochlorite from the product tank 6 is fed back through line 8 to a point upstream of the filter 2.
- the flow of hypochlorite is maintained by a hypochlorite transfer pump 9.
- Hydrochloric acid is also delivered to the brine flow upstream of the filter 2 via line 10, the flow of hydrochloric acid being maintained by a pump 11.
- the flow of sodium hypochlorite was 1 liter per hour and the flow of hydrochloric acid was 1 liter per hour.
- the supply of hydrochloric acid is controlled to maintain a low pH in the brine flow upstream of the filter 2. Typically the acidity will be controlled to approximately 4 pH.
- bromide in the brine flow is rapidly converted into bromine and hypobromous acid which is adsorbed by the filter 2.
- the filter is capable of adsorbing bromine or bromine released by the reduction of hypobromous acid, substantially no bromine compounds reach the electrolyser and accordingly substantially no bromate reaches the product tank 8.
- Appropriate materials for the filter 2 are activated carbon zeolites and insoluble reducing agents, for example calcium sulphite.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Water Treatment By Sorption (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
Priority Applications (6)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB9421964A GB2283484B (en) | 1993-11-03 | 1994-10-28 | Bromide removal |
| MX9708504A MX9708504A (es) | 1995-05-04 | 1995-05-04 | Remocion de bromuro. |
| CA002220112A CA2220112C (fr) | 1993-11-03 | 1995-05-04 | Extraction du bromure |
| PCT/US1995/005603 WO1996034999A1 (fr) | 1993-11-03 | 1995-05-04 | Extraction du bromure |
| US08/973,078 US6428677B1 (en) | 1995-05-04 | 1995-05-04 | Bromide removal |
| AU24351/95A AU702950B2 (en) | 1995-05-04 | 1995-05-04 | Bromide removal |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB939322625A GB9322625D0 (en) | 1993-11-03 | 1993-11-03 | Bromide removal |
| CA002220112A CA2220112C (fr) | 1993-11-03 | 1995-05-04 | Extraction du bromure |
| PCT/US1995/005603 WO1996034999A1 (fr) | 1993-11-03 | 1995-05-04 | Extraction du bromure |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO1996034999A1 true WO1996034999A1 (fr) | 1996-11-07 |
Family
ID=27170521
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/US1995/005603 Ceased WO1996034999A1 (fr) | 1993-11-03 | 1995-05-04 | Extraction du bromure |
Country Status (3)
| Country | Link |
|---|---|
| CA (1) | CA2220112C (fr) |
| GB (1) | GB2283484B (fr) |
| WO (1) | WO1996034999A1 (fr) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113753861A (zh) * | 2021-09-29 | 2021-12-07 | 山东海王化工股份有限公司 | 碱法吸收提溴与无隔膜电解相结合生产溴酸钠的方法 |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2348195A (en) * | 1999-03-24 | 2000-09-27 | Ion Enterprises Ltd | Fluid treatment |
| DE50102673D1 (de) * | 2001-05-16 | 2004-07-29 | Va Tech Wabag Deutschland Gmbh | Verfahren und Vorrichtung zur Entfernung von Bromid aus Wasser |
| DE102008041164B4 (de) | 2008-08-11 | 2011-01-13 | Werthmann, Christine, Dr. | Verfahren zur Aufbereitung von Wasser |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB867790A (en) * | 1958-04-03 | 1961-05-10 | Donald Edward Ferris | Method and apparatus for producing hypochlorite of soda in an electrolytic cell |
| US3909377A (en) * | 1971-12-14 | 1975-09-30 | Rhone Poulenc Sa | Purification of a chloride solution |
| FR2388597A1 (fr) * | 1977-04-27 | 1978-11-24 | Sorapec | Procede d'electrolyse |
-
1994
- 1994-10-28 GB GB9421964A patent/GB2283484B/en not_active Expired - Fee Related
-
1995
- 1995-05-04 CA CA002220112A patent/CA2220112C/fr not_active Expired - Fee Related
- 1995-05-04 WO PCT/US1995/005603 patent/WO1996034999A1/fr not_active Ceased
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB867790A (en) * | 1958-04-03 | 1961-05-10 | Donald Edward Ferris | Method and apparatus for producing hypochlorite of soda in an electrolytic cell |
| US3909377A (en) * | 1971-12-14 | 1975-09-30 | Rhone Poulenc Sa | Purification of a chloride solution |
| FR2388597A1 (fr) * | 1977-04-27 | 1978-11-24 | Sorapec | Procede d'electrolyse |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113753861A (zh) * | 2021-09-29 | 2021-12-07 | 山东海王化工股份有限公司 | 碱法吸收提溴与无隔膜电解相结合生产溴酸钠的方法 |
| CN113753861B (zh) * | 2021-09-29 | 2022-10-18 | 山东海王化工股份有限公司 | 碱法吸收提溴与无隔膜电解相结合生产溴酸钠的方法 |
Also Published As
| Publication number | Publication date |
|---|---|
| CA2220112A1 (fr) | 1996-11-07 |
| CA2220112C (fr) | 2007-02-27 |
| GB2283484A (en) | 1995-05-10 |
| GB9421964D0 (en) | 1994-12-21 |
| GB2283484B (en) | 1997-07-30 |
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