Electrolysis cell and electrolysis tank
US-9506157-B2 · Nov 29, 2016 · US
US9273404B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9273404-B2 |
| Application number | US-201313772501-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 21, 2013 |
| Priority date | Mar 15, 2012 |
| Publication date | Mar 1, 2016 |
| Grant date | Mar 1, 2016 |
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Processes for electrolysis of alkali metal chlorides with oxygen-consuming electrodes having startup and shutdown conditions which prevent damage to the constituents of the electrolysis cell.
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The invention claimed is: 1. Process for chloralkali electrolysis with an electrolysis cell having an oxygen-consuming electrode, operated according to the finite gap arrangement, the electrolysis cell having at least one anode space with an anode and an anolyte comprising alkali metal chloride, an ion exchange membrane, a cathode space with an oxygen-consuming electrode as the cathode, comprising a silver-containing catalyst, and an electrolyte gap between oxygen-consuming electrode and membrane through which a catholyte having a content of alkali metal hydroxide of 7.5-10.5 mol/I flows, wherein the catholyte is circulated and application of electrolysis voltage between anode and cathode is preceded by adjustment of the volume flow rate and/or composition of the catholyte supplied to the gap to result in an aqueous solution of alkali metal hydroxide leaving the cathode gap having a content of chloride ions of at most 1000 ppm and the electrolysis voltage is applied after introduction of the anolyte and of an oxygenous gas into the cathode space. 2. Process according to claim 1 , wherein the electrolysis cell is a falling-film cell. 3. Process according to claim 1 , wherein the alkali metal hydroxide solution introduced in the catholyte feed prior to application of the electrolysis voltage has a content of alkali metal chlorate of at most 20 ppm. 4. Process according to claim 1 , wherein less than 240 minutes between commencement of the introduction of the catholyte and the application of the electrolysis voltage. 5. Process according to claim 1 , wherein a temperature difference between anolyte feed and catholyte drain of less than 20° C. is established after commencement of the introduction of the catholyte and anolyte. 6. Process according to claim 1 , wherein the alkali metal chloride is sodium chloride or potassium chloride. 7. Process for chloralkali electrolysis with an electrolysis cell having an oxygen-consuming electrode, the cell having at least one anode space with an anode and an anolyte comprising alkali metal chloride, an ion exchange membrane, a cathode space with an oxygen-consuming electrode with a silver-containing catalyst, and an electrolyte gap between oxygen-consuming electrode and membrane through which the catholyte flows, wherein chlorine is produced in the anode space during the electrolysis and at the end of the electrolysis operation, after the electrolysis voltage has been switched off, in a first step, the concentration of the alkali metal chloride solution removed from the anode space increases, then the anode space is flushed with fresh alkali metal chloride solution until the chlorine content of oxidation state 0 or greater than 0 in the anolyte is less than 10 ppm, then the anolyte temperature is lowered and then the anolyte is released from the anode space and, in a subsequent step, the introduction of the catholyte is ended and the catholyte is released from the electrolyte gap. 8. Process according to claim 7 , wherein the draining anolyte has an alkali metal chloride content of 2.2 to 4.8 mol/I. 9. Process according to claim 7 , wherein the electrolysis cell is a falling-film electrolysis cell. 10. Process according to claim 7 , wherein the electrolysis voltage is switched off after attainment of a chlorine content in the anolyte of <10 mg/I. 11. Process according to claim 7 , wherein that a positive pressure relative to the anode space of >10 mbar is maintained until the end of the emptying and flushing in the cathode space. 12. Process according to claim 7 , wherein, after shutdown and emptying of the electrolysis cell, the anode space is flushed repeatedly every 1 to 12 weeks with a dilute alkali metal chloride solution having an alkali metal chloride content of 2.2 to 4.8 mol/I, and the cathode space is flushed with an alkali metal hydroxide solution having an alkali metal chloride content of 4 to 10 mol/I. 13. Process according to claim 7 , wherein the alkali metal chloride is sodium chloride or potassium chloride.
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