Apparatus for manufacturing chlorine dioxide

• US 4,432,856 A
• Filed: 04/28/1981
• Issued: 02/21/1984
• Est. Priority Date: 05/13/1980
• Status: Expired due to Fees

• Current Assignee: Japan Carlit (Shanghai) Co. Ltd. (Carlit Holdings Co., Ltd.)
• Original Assignee: Japan Carlit (Shanghai) Co. Ltd. (Carlit Holdings Co., Ltd.)
• Inventors: Itai, Reiichi, Hirakata, Kaoru, Murakami, Katsuyuki, Shimoda, Shinichi, Ishizaka, Fumio
• Primary Examiner(s): Tung, T.
• Application Number:
  US06/258,545
• Time in Patent Office: 1,029 Days
• Field of Search: 204/232, 204/234-239, 204/255-258, 204/263-266, 204/275-278
• US Class Current: 204/237
• CPC Class Codes: C01B 11/022 Chlorine dioxide (ClO2)
• CPC Class Codes: C25B 1/26 Chlorine; Compounds thereof by simultaneous production of alkali metal hydroxides and chlorine, oxyacids or salts of chlorine C25B1/34
• CPC Class Codes: C25B 9/00 Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features

Abstract

Chlorine dioxide is produced by electrolysis of a solution of chlorite and by using a compact apparatus which provides continuously a uniform concentration of chlorine dioxide, which can be operated easily, which discharges a spent electrolyte that can be treated easily and which achieves highly efficient use of chlorite and high current efficiency.

Claims

1. An apparatus for producing chlorine dioxide by the electrolysis of a chlorite solution which comprises:

an electrolytic cell for producing chlorine dioxide by electrolysis of a solution of chlorite, said electrolytic cell including an anode compartment and a cathode compartment, said electrolytic cell including means for discharging anolyte from said anode compartment and means for discharging catholyte from said cathode compartment;

a supply tank having a first input for receiving an aqueous fresh chlorite solution, a first output for supplying a chlorite containing solution, a second input for receiving a mixture of chlorine dioxide and air and a second output for removing a mixture of chlorine dioxide and air from the system;

a stripping tank having a first output for supplying an anolyte to the anode compartment of said electrolytic cell, a first input coupled to the anode compartment of said electrolytic cell for receiving anolyte containing chlorine dioxide dissolved therein, a second input for receiving a mixture of chlorine dioxide and air, said stripping tank stripping some of said anolyte of chlorine dioxide by said air contained in said mixture supplied thereto, a second output for supplying anolyte containing dissolved chlorine dioxide to an auxiliary stripping tank, and a third output for supplying a mixture of chlorine dioxide and air to said supply tank;

said auxiliary stripping tank including a first input for receiving anolyte from said stripping tank, a second input for receiving fresh air, a first output for supplying a mixture of chlorine dioxide and air to said stripping tank, said auxiliary stripping tank stripping anolyte of chlorine dioxide dissolved therein by means of said fresh air supplied thereto, and a second output for discharging a part of the anolyte contained in said auxiliary stripping tank from the system;

a circulation tank coupled to the cathode compartment of said electrolytic cell and including a first input for receiving a first portion of said catholyte discharged from said cathode compartment, a second input for receiving a diluent to dilute the catholyte and to thereby control the alkali concentration of the catholyte in said circulation tank, a first output for supplying diluted catholyte to the cathode compartment of said electrolytic cell, and a second output for discharging a part of the catholyte contained in said circulation tank from the system;

means for supplying a second portion of the catholyte discharged from said cathode compartment to said first output of said stripping tank;

means for combining said second portion of said catholyte and said anolyte from said first output of said stripping tank to form a first mixture; and

means for combining said first mixture with said chlorite containing solution provided at said first output of said supply tank to thereby form a second mixture, and means for supplying said second mixture to said anode compartment of said electrolytic cell.

2. The apparatus of claim 1, wherein said electrolytic cell comprises a diaphragm electrolytic cell.

3. The apparatus of claim 2, wherein said diaphragm comprises a fluorocarbon cation exchange membrane.

4. The apparatus of claim 2, wherein said electrolytic cell comprises a bipolar diaphragm electrolyte cell.

5. The apparatus of claim 2, wherein said electrolytic cell comprises a unipolar diaphragm electrolytic cell.

6. The apparatus of claim 1 comprises a source of diluent coupled to said circulation tank for supplying said diluent consisting essentially of water.

7. The apparatus of claim 1 comprises a source of diluent coupled to said circulation tank for supplying said diluent consisting essentially of hydrochloric acid.

8. The apparatus of claim 1, further comprising means for maintaining the anolyte of said stripping tank at a temperature of between 10°

and 90°

C.

9. The apparatus of claim 1, further comprising means for maintaining the anode and cathode compartments of said electrolytic cell at substantially the same pressure.

10. The apparatus of claim 1, further comprising a vacuum producing means connected to the second output of said supply tank.

11. An apparatus for producing chlorine dioxide by the electrolysis of a chlorine solution which comprises:

a substantially enclosed substantially cylindrical reaction vessel having a bottom compartment, a middle compartment and a top compartment, and

an electrolytic cell located outside of said cylindrical reaction vessel for producing chlorine dioxide by electrolysis of a solution of chlorite, said electrolytic cell including an anode compartment, a cathode compartment, means for discharging anolyte from said anode compartment and means for discharging catholyte from said cathode compartment;

said upper compartment comprising a supply tank having a first input for receiving an aqueous fresh chlorite solution, a first output for supplying a chlorite containing solution, a second input for receiving a mixture of chlorine dioxide and air and a second output for removing a mixture of chlorine dioxde and air from said reaction vessel;

said middle compartment comprising a stripping tank having a first output for supplying an anolyte to the anode compartment of said electrolytic cell, a first input coupled to the anode compartment of said electrolytic cell for receiving anolyte containing chlorine dioxide dissolved therein, a second input for receiving a mixture of chlorine dioxide and air, said stripping tank stripping some of said anolyte of chlorine dioxide by said air contained in said mixture supplied thereto, a second output for supplying anolyte containing dissolved chlorine dioxide to an auxiliary stripping tank, and a third output for supplying a mixture of chlorine dioxide and air to said supply tank;

said bottom compartment comprising said auxiliary stripping tank including a first input for receiving anolyte from said stripping tank, a second input for receiving fresh air, a first output for supplying a mixture of chlorine dioxide and air to said stripping tank, said auxiliary stripping tank stripping anolyte of chlorine dioxide dissolved therein by means of said fresh air supplied thereto, and a second output for discharging a part of the anolyte contained in said auxiliary stripping tank from said cylindrical reaction vessel; and

a circulation tank coupled to the cathode compartment of said electrolytic cell and including a first input for receiving a first portion of said catholyte discharged from said cathode compartment, a second input for receiving a diluent to dilute the catholyte and to thereby control the alkali concentration of the catholyte in said circulation tank, a first output for supplying diluted catholyte to the cathode compartment of said electrolytic cell, and a second output for discharging a part of the catholyte contained in said circulation tank from said reaction vessel;

means for supplying a second portion of the catholyte discharged from said cathode compartment to said first output of said stripping tank;

means for combining said second portion of said catholyte and said anolyte from said first output of said stripping tank to form a first mixture; and

means for combining said first mixture with said chlorite containing solution provided at said first output of said supply tank to thereby form a second mixture, and means for supplying said second mixture to said anode compartment of said electrolytic cell.

12. The apparatus of claim 11 further comprising:

(a) means for dispersing the mixture of chlorine dioxide and air, which enters the supply tank through said second input, throughout the chlorite containing solution in said supply tank;

(b) means for dispersing the mixture of chlorine dioxide and air which enters the stripping tank through said second input throughout the anolyte in said stripping tank; and

(c) means for dispersing fresh air which enters the auxiliary stripping tank throughout the anolyte in said auxiliary stripping tank.

13. The apparatus of claim 12, wherein each of said dispersing means comprises a plate having an upper and a lower major surface, said plate having uniformly distributed perforations connecting said upper and lower major surfaces, said plate having substantially the same size and shape as the bottom surface of said tank and being substantially parallel to the bottom surface of said tank, wherein said mixture of chlorine dioxide and air or said fresh air is released into said tank below the lower major surface of said plate.

14. The apparatus of claim 11, wherein said circulation tank is in said bottom compartment of said reaction vessel.

15. The apparatus of claim 11 comprises a source of diluent coupled to said circulation tank for supplying said diluent consisting essentially of water.

16. The apparatus of claim 11 comprises a source of diluent coupled to said circulation tank for supplying said diluent consisting essentially of hydrochloric acid.