US2717237A - Production of chlorine dioxide - Google Patents
Production of chlorine dioxide Download PDFInfo
- Publication number
- US2717237A US2717237A US295551A US29555152A US2717237A US 2717237 A US2717237 A US 2717237A US 295551 A US295551 A US 295551A US 29555152 A US29555152 A US 29555152A US 2717237 A US2717237 A US 2717237A
- Authority
- US
- United States
- Prior art keywords
- chlorite
- chlorine dioxide
- chlorine
- production
- electrolysis
- 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 - Lifetime
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
- 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
- This invention relates to an electrolytic process for the production of chlorine dioxide substantially free from chlorine.
- Chlorine dioxide is produced by a number of different processes, one of which is the electrolysis of an aqueous solution of a chlorite in the presence of a chloride.
- This process is subject to certain disadvantages when used for large scale production since, if the chlorite is fed to the electrolytic process in insufiicient quantities, or if the feed of chlorite is unexpectedly interrupted, there is a danger of the chlorite present in the electrolytic cell being exhausted so that chlorine is developed instead of chlorine dioxide. If the electrolysis takes this course, it may be disadvantageous or even hurtful for certain fields of applications, since chlorine dioxide is very often used to treat substances which are not stable. to chlorine.
- the present invention provides a process for the production of substantially chlorine-free chlorine dioxide by electrolysis of an aqueous solution of a chlorite, such as sodium chlorite, wherein the electrolysis is carried out in the presence of a water-soluble sulfate.
- a chlorite such as sodium chlorite
- the process of the invention has the advantage that substantially chlorine-free chlorine dioxide is produced while the electrolysis proceeds normally, and that if the feed of chlorite solution decreases or even stops, the evolution of chlorine dioxide simultaneously also de creases or stops, without any quantity of chlorine being evolved as the electrolysis proceeds.
- the process of the invention may be carried out in an electrolytic cell consisting substantially of a platinum 2,717,237 Patented Sept. 6, 1955 anode, a diaphragm and a lead cathode.
- the heat evolved in the anode compartment is preferably dissipated by a cooling device.
- the chlorine dioxide, developed in the anode compartment during electrolysis, is expelled and diluted by a controlled quantity of an inert gas, for instance air, which is introduced at the bottom of the anode by means of a distributor device.
- a feed solution containing controlled amounts of a chlorite and a sulfate is continuously introduced into the anode compartment by means of an automatic contrivance, while an appropriate quantity of caustic soda solution is discharged from the cathode compartment through an overflow.
- the desired concentration of chlorine dioxide is varied and adjusted by regulating the air supply within a predetermined range.
- Example 1 The anode compartment of an electrolytic cell is charged and subsequently fed at a rate of 25 ccs. per hour, with a solution containing per litre 200 grams of NaClOz and grams of NazSO4. A current of 1.251.4 amperes at a voltage of 6.15-6.25 volts is passed through the cell, and the air flow is 25 litres per hour. In this way a gas with a chlorine dioxide content of between 3.2 and 4.1 per cent by volume is obtained. The amount of chlorine dioxide thus formed is about 2.3-3 grams per hour. The content of C12, is between 0.04 and 0.09 per cent by volume.
- said chlorite is an alkali metal chlorite and said sulfate is an alkali metal sulfate.
Description
United States Patent PRODUCTION OF CHLORINE DIGXIDE Nikolaus Rempel, deceased, late of Leve'rkusen-Bayerwerk, Germany, by Erika G. Rempel, administratrix, Leverkusen-Bayerwerk, Germany, assignor to Farbenfabriken Bayer Aktiengesellschaft, Leverkusen, Germany No Drawing. Application June 25, 1952, Serial No. 295,551
4 Claims. (Cl. 204--101) This invention relates to an electrolytic process for the production of chlorine dioxide substantially free from chlorine.
Chlorine dioxide is produced by a number of different processes, one of which is the electrolysis of an aqueous solution of a chlorite in the presence of a chloride. This process is subject to certain disadvantages when used for large scale production since, if the chlorite is fed to the electrolytic process in insufiicient quantities, or if the feed of chlorite is unexpectedly interrupted, there is a danger of the chlorite present in the electrolytic cell being exhausted so that chlorine is developed instead of chlorine dioxide. If the electrolysis takes this course, it may be disadvantageous or even hurtful for certain fields of applications, since chlorine dioxide is very often used to treat substances which are not stable. to chlorine.
It has now been found that practically chlorine-free chlorine-dioxide is obtained by electrolysis of an aqueous solution of a chlorite, such as an alkali metal chlorite, for instance, sodium chlorite, by carrying out the electrolysis in the presence of a water-soluble sulfate, such as an alkali metal sulfate.
Accordingly, the present invention provides a process for the production of substantially chlorine-free chlorine dioxide by electrolysis of an aqueous solution of a chlorite, such as sodium chlorite, wherein the electrolysis is carried out in the presence of a water-soluble sulfate.
The process of the invention has the advantage that substantially chlorine-free chlorine dioxide is produced while the electrolysis proceeds normally, and that if the feed of chlorite solution decreases or even stops, the evolution of chlorine dioxide simultaneously also de creases or stops, without any quantity of chlorine being evolved as the electrolysis proceeds.
The process of the invention may be carried out in an electrolytic cell consisting substantially of a platinum 2,717,237 Patented Sept. 6, 1955 anode, a diaphragm and a lead cathode. The heat evolved in the anode compartment is preferably dissipated by a cooling device. The chlorine dioxide, developed in the anode compartment during electrolysis, is expelled and diluted by a controlled quantity of an inert gas, for instance air, which is introduced at the bottom of the anode by means of a distributor device. A feed solution containing controlled amounts of a chlorite and a sulfate is continuously introduced into the anode compartment by means of an automatic contrivance, while an appropriate quantity of caustic soda solution is discharged from the cathode compartment through an overflow. The desired concentration of chlorine dioxide is varied and adjusted by regulating the air supply within a predetermined range.
The invention is further illustrated by the following example:
Example The anode compartment of an electrolytic cell is charged and subsequently fed at a rate of 25 ccs. per hour, with a solution containing per litre 200 grams of NaClOz and grams of NazSO4. A current of 1.251.4 amperes at a voltage of 6.15-6.25 volts is passed through the cell, and the air flow is 25 litres per hour. In this way a gas with a chlorine dioxide content of between 3.2 and 4.1 per cent by volume is obtained. The amount of chlorine dioxide thus formed is about 2.3-3 grams per hour. The content of C12, is between 0.04 and 0.09 per cent by volume.
What is claimed is:
1. In the process for the production of substantially chlorine-free chlorine dioxide by electrolysis of a chlorite, the improvement which comprises electrolyzing an aqueous solution of a chlorite in the presence of a water-soluble metal sulfate.
2. Improvement according to claim 1, in which said chlorite is an alkali metal chlorite and said sulfate is an alkali metal sulfate.
3. Improvement according to claim 2, in which said alkali metal chlorite is sodium chlorite and in which said alkali metal sulfate is sodium sulfate.
4. In the process for the production of substantially chlorine-free chlorine dioxide by electrolysis of a chlorite, the improvement which comprises electrolyzing an aqueous solution consisting essentially of 200 grams of sodium chlorite per liter in the presence of 80 grams of sodium sulfate per liter.
References Cited in the file of this patent UNITED STATES PATENTS 2,163,793 Logan June 27, 1939
Claims (1)
1. IN THE PROCESS FOR THE PRODUCTION OF SUBSTANTIALLY CHLORINE-FREE CHLORINE DIOXIDE BY ELECTROLYSIS OF A CHLORITE, THE IMPROVEMENT WHICH COMPRISES ELECTROLYZING AN QUEOUS SOLUTION OF A CHLORITE IN THE PRESENCE OF A WATER-SOLUBLE METAL SULFATE.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US295551A US2717237A (en) | 1952-06-25 | 1952-06-25 | Production of chlorine dioxide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US295551A US2717237A (en) | 1952-06-25 | 1952-06-25 | Production of chlorine dioxide |
Publications (1)
Publication Number | Publication Date |
---|---|
US2717237A true US2717237A (en) | 1955-09-06 |
Family
ID=23138186
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US295551A Expired - Lifetime US2717237A (en) | 1952-06-25 | 1952-06-25 | Production of chlorine dioxide |
Country Status (1)
Country | Link |
---|---|
US (1) | US2717237A (en) |
Cited By (26)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3109789A (en) * | 1960-07-27 | 1963-11-05 | Hooker Chemical Corp | Preparation of phosphine |
DE3118795A1 (en) * | 1980-05-13 | 1982-03-11 | The Japan Carlit Co., Ltd., Tokyo | "METHOD AND DEVICE FOR PRODUCING CHLORDIOXIDE" |
US4426263A (en) | 1981-04-23 | 1984-01-17 | Diamond Shamrock Corporation | Method and electrocatalyst for making chlorine dioxide |
US4731169A (en) * | 1986-10-29 | 1988-03-15 | Tenneco Canada Inc. | Selective removal of chlorine from solutions of chlorine dioxide and chlorine |
US5041196A (en) * | 1989-12-26 | 1991-08-20 | Olin Corporation | Electrochemical method for producing chlorine dioxide solutions |
US5084149A (en) * | 1989-12-26 | 1992-01-28 | Olin Corporation | Electrolytic process for producing chlorine dioxide |
US5089095A (en) * | 1990-03-30 | 1992-02-18 | Olin Corporation | Electrochemical process for producing chlorine dioxide from chloric acid |
US5092970A (en) * | 1989-12-20 | 1992-03-03 | Olin Corporation | Electrochemical process for producing chlorine dioxide solutions from chlorites |
US5106465A (en) * | 1989-12-20 | 1992-04-21 | Olin Corporation | Electrochemical process for producing chlorine dioxide solutions from chlorites |
US5108560A (en) * | 1990-03-30 | 1992-04-28 | Olin Corporation | Electrochemical process for production of chloric acid from hypochlorous acid |
US5158658A (en) * | 1990-10-31 | 1992-10-27 | Olin Corporation | Electrochemical chlorine dioxide generator |
US5167777A (en) * | 1990-10-30 | 1992-12-01 | Olin Corporation | Process and apparatus for the removal of oxyhalide species from aqueous solutions |
US5294319A (en) * | 1989-12-26 | 1994-03-15 | Olin Corporation | High surface area electrode structures for electrochemical processes |
US5965004A (en) * | 1996-03-13 | 1999-10-12 | Sterling Pulp Chemicals, Ltd. | Chlorine dioxide generation for water treatment |
US6203688B1 (en) | 1997-10-17 | 2001-03-20 | Sterling Pulp Chemicals, Ltd. | Electrolytic process for producing chlorine dioxide |
US6274009B1 (en) | 1999-09-03 | 2001-08-14 | International Dioxide Inc. | Generator for generating chlorine dioxide under vacuum eduction in a single pass |
US6306281B1 (en) | 1999-11-30 | 2001-10-23 | Joseph Matthew Kelley | Electrolytic process for the generation of stable solutions of chlorine dioxide |
US20030082095A1 (en) * | 2001-10-22 | 2003-05-01 | Halox Technologies, Inc. | Electrolytic process and apparatus |
US20040071627A1 (en) * | 2002-09-30 | 2004-04-15 | Halox Technologies, Inc. | System and process for producing halogen oxides |
US6740223B2 (en) | 2001-06-22 | 2004-05-25 | Superior Plus Inc. | Electrolytic process for the production of chlorine dioxide |
US20050034997A1 (en) * | 2003-08-12 | 2005-02-17 | Halox Technologies, Inc. | Electrolytic process for generating chlorine dioxide |
US20050163700A1 (en) * | 2002-09-30 | 2005-07-28 | Dimascio Felice | System and process for producing halogen oxides |
WO2011086579A1 (en) | 2010-01-18 | 2011-07-21 | Prophylaxis | Process for producing stable and pure liquid form of chlorine dioxide |
US10046990B2 (en) | 2011-06-06 | 2018-08-14 | Ecolab Usa Inc. | Electrolytic method of generating chloride dioxide with improved theoretical yield |
US10814358B2 (en) | 2017-02-09 | 2020-10-27 | Karcher North America, Inc. | Floor cleaning device with disinfection capabilities |
ES2887610A1 (en) * | 2020-06-22 | 2021-12-23 | Cecotec Res And Development | SELF-MOVING CLEANING APPARATUS WITH SURFACE DISINFECTION MEANS (Machine-translation by Google Translate, not legally binding) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2163793A (en) * | 1937-06-08 | 1939-06-27 | Mathieson Alkall Works Inc | Production of chlorine dioxide |
-
1952
- 1952-06-25 US US295551A patent/US2717237A/en not_active Expired - Lifetime
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2163793A (en) * | 1937-06-08 | 1939-06-27 | Mathieson Alkall Works Inc | Production of chlorine dioxide |
Cited By (32)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3109789A (en) * | 1960-07-27 | 1963-11-05 | Hooker Chemical Corp | Preparation of phosphine |
DE3118795A1 (en) * | 1980-05-13 | 1982-03-11 | The Japan Carlit Co., Ltd., Tokyo | "METHOD AND DEVICE FOR PRODUCING CHLORDIOXIDE" |
US4426263A (en) | 1981-04-23 | 1984-01-17 | Diamond Shamrock Corporation | Method and electrocatalyst for making chlorine dioxide |
US4731169A (en) * | 1986-10-29 | 1988-03-15 | Tenneco Canada Inc. | Selective removal of chlorine from solutions of chlorine dioxide and chlorine |
US5092970A (en) * | 1989-12-20 | 1992-03-03 | Olin Corporation | Electrochemical process for producing chlorine dioxide solutions from chlorites |
US5106465A (en) * | 1989-12-20 | 1992-04-21 | Olin Corporation | Electrochemical process for producing chlorine dioxide solutions from chlorites |
US5041196A (en) * | 1989-12-26 | 1991-08-20 | Olin Corporation | Electrochemical method for producing chlorine dioxide solutions |
US5084149A (en) * | 1989-12-26 | 1992-01-28 | Olin Corporation | Electrolytic process for producing chlorine dioxide |
US5294319A (en) * | 1989-12-26 | 1994-03-15 | Olin Corporation | High surface area electrode structures for electrochemical processes |
US5298280A (en) * | 1989-12-26 | 1994-03-29 | Olin Corporation | Process for producing an electrode by electroless deposition |
US5089095A (en) * | 1990-03-30 | 1992-02-18 | Olin Corporation | Electrochemical process for producing chlorine dioxide from chloric acid |
US5108560A (en) * | 1990-03-30 | 1992-04-28 | Olin Corporation | Electrochemical process for production of chloric acid from hypochlorous acid |
US5167777A (en) * | 1990-10-30 | 1992-12-01 | Olin Corporation | Process and apparatus for the removal of oxyhalide species from aqueous solutions |
US5158658A (en) * | 1990-10-31 | 1992-10-27 | Olin Corporation | Electrochemical chlorine dioxide generator |
US5965004A (en) * | 1996-03-13 | 1999-10-12 | Sterling Pulp Chemicals, Ltd. | Chlorine dioxide generation for water treatment |
US6203688B1 (en) | 1997-10-17 | 2001-03-20 | Sterling Pulp Chemicals, Ltd. | Electrolytic process for producing chlorine dioxide |
US6274009B1 (en) | 1999-09-03 | 2001-08-14 | International Dioxide Inc. | Generator for generating chlorine dioxide under vacuum eduction in a single pass |
US6881320B1 (en) | 1999-09-03 | 2005-04-19 | International Dioxide, Inc. | Generator for generating chlorine dioxide under vacuum eduction in a single pass |
US6306281B1 (en) | 1999-11-30 | 2001-10-23 | Joseph Matthew Kelley | Electrolytic process for the generation of stable solutions of chlorine dioxide |
US6740223B2 (en) | 2001-06-22 | 2004-05-25 | Superior Plus Inc. | Electrolytic process for the production of chlorine dioxide |
US6869517B2 (en) | 2001-10-22 | 2005-03-22 | Halox Technologies, Inc. | Electrolytic process and apparatus |
US20030082095A1 (en) * | 2001-10-22 | 2003-05-01 | Halox Technologies, Inc. | Electrolytic process and apparatus |
US20040071627A1 (en) * | 2002-09-30 | 2004-04-15 | Halox Technologies, Inc. | System and process for producing halogen oxides |
US6913741B2 (en) | 2002-09-30 | 2005-07-05 | Halox Technologies, Inc. | System and process for producing halogen oxides |
US20050163700A1 (en) * | 2002-09-30 | 2005-07-28 | Dimascio Felice | System and process for producing halogen oxides |
US7241435B2 (en) | 2002-09-30 | 2007-07-10 | Halox Technologies, Inc. | System and process for producing halogen oxides |
US20050034997A1 (en) * | 2003-08-12 | 2005-02-17 | Halox Technologies, Inc. | Electrolytic process for generating chlorine dioxide |
US7179363B2 (en) | 2003-08-12 | 2007-02-20 | Halox Technologies, Inc. | Electrolytic process for generating chlorine dioxide |
WO2011086579A1 (en) | 2010-01-18 | 2011-07-21 | Prophylaxis | Process for producing stable and pure liquid form of chlorine dioxide |
US10046990B2 (en) | 2011-06-06 | 2018-08-14 | Ecolab Usa Inc. | Electrolytic method of generating chloride dioxide with improved theoretical yield |
US10814358B2 (en) | 2017-02-09 | 2020-10-27 | Karcher North America, Inc. | Floor cleaning device with disinfection capabilities |
ES2887610A1 (en) * | 2020-06-22 | 2021-12-23 | Cecotec Res And Development | SELF-MOVING CLEANING APPARATUS WITH SURFACE DISINFECTION MEANS (Machine-translation by Google Translate, not legally binding) |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2717237A (en) | Production of chlorine dioxide | |
US3773634A (en) | Control of an olyte-catholyte concentrations in membrane cells | |
EP0544686B1 (en) | Chlorine dioxide generation from chloric acid | |
GB1049756A (en) | Electrochemical process for the production of olefin oxide | |
GB1185507A (en) | Improvements in or relating to Methods of and Device for Manufacturing Alkaline Chlorates, Notably Sodium Chlorate, by an Electrolytic Process. | |
US3959095A (en) | Method of operating a three compartment electrolytic cell for the production of alkali metal hydroxides | |
JPWO2018131493A1 (en) | Method for producing ammonium persulfate | |
PL82400B1 (en) | ||
US3723266A (en) | Catholyte recirculation in diaphragm chlor-alkali cells | |
GB845511A (en) | Improvements relating to the production of metal hydroxides | |
US2209681A (en) | Electrolysis of ammonium chloride | |
US2569329A (en) | Operation in electrolytic alkali chlorine cells | |
US2823177A (en) | Method and apparatus for lowering the chlorate content of alkali metal hydroxides | |
US3240687A (en) | Process for the manufacture of watersoluble basic aluminum compounds | |
US3785943A (en) | Electrolysis of magnesium chloride | |
US802205A (en) | Process of producing chlorates and bichromates. | |
US1126627A (en) | Process for electrolyzing alkali-chlorid solution. | |
US3553088A (en) | Method of producing alkali metal chlorate | |
GB1247563A (en) | Operating electrolytic cells and treatment of brine | |
US2118904A (en) | Process for the manufacture of chloro-amines | |
US3364127A (en) | Method for producing caustic soda and chlorine by means of electrolysis of sea water or other similar saltish water | |
JPS6240432B2 (en) | ||
US2810685A (en) | Electrolytic preparation of manganese | |
US2024242A (en) | Apparatus for producing anhydrous magnesium chloride | |
US3551309A (en) | Process for electrolysis of alkali metal chloride |