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METHODS FOR ELECTROCHEMICAL DECHLORINATION OF ANOLYTE BRINE FROM NaCl ELECTROLYSIS

a technology of electrochemical dechlorination and anolyte brine, which is applied in the direction of polycrystalline material growth, separation process, treatment water, etc., can solve the problems of nacl solution sulfate, inability to electrochemically degrade sulfate, and gradual accumulation of sulfate, so as to achieve economic viability and environmental compatibility of nacl electrolysis

Inactive Publication Date: 2013-04-25
BAYER INTELLECTUAL PROPERTY GMBH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0011]The methods according to the invention may be used to remove dissolved chlorine, hypochlorite which is still present, chlorate and other reducible compounds such as for example nitrogen trichloride, without reaction products passing into the NaCl-containing solutions, whereby markedly smaller quantities of the NaCl-containing solution have to be worked-up, or removed and discarded. The economic viability and environmental compatibility of NaCl electrolysis performed using the methods according to the various embodiments of the invention are markedly improved.

Problems solved by technology

One disadvantage of using sodium bisulfite and similar sulfur-containing compounds for chemical dechlorination is that sulfate arises in the NaCl solution as a reaction product of the chemical reduction with bisulfite or sulfur-containing compounds.
However, the sulfate cannot be electrochemically degraded, such that it gradually accumulates in the NaCl-containing solution.
Modern high performance ion exchange membranes are damaged by relatively high concentrations of sulfates, however.
An excessively high concentration of sulfate in the brine brings about the formation of oxygen on the anode and reduces current efficiency, so impairing the economic viability of the electrolysis method.
Damage to the coating of the anode is likewise possible.
In this way, large amounts of sodium chloride are lost, which has a negative effect on the economic viability and environmental compatibility of the electrolysis method.
One disadvantage of such methods is that sulfate formation is not prevented, but rather an additional method step is necessary in order to remove sulfate from the brine.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

example 1

[0042]In the above-described cell, provided with a Nafion 982 ion-exchange membrane from DuPont de Nemours, the chlorine-containing, NaCl-depleted anolyte brine was passed at a volumetric flow rate of 1.0 l / h out of the NaCl electrolysis into the cathode compartment with a chlorine content of 422 mg / l. The cathode compartment was filled with graphite balls, the residual volume of the cathode compartment after deduction of the volume of graphite balls amounting to 160 ml. The residence time of the brine to be treated in the cathode compartment was 5.6 min. The voltage amounted to 132 V, and the current intensity to 0.8 A. The concentration of chlorine in the outflow of the cathode compartment was approx. 89 mg / l. The pH value of the anolyte brine was pH 4. A charge of 0.48 Ah / l of brine was introduced. The current density relative to the total surface area of the graphite balls used was 8.5 A / m2.

example 2

[0043]The chlorine-containing anolyte brine from another NaCl electrolysis with a corresponding chlorine content of 1522 mg / l and a pH value of 10 was introduced at 1.0 l / h into the above-described cell, provided with a Nafion 324 ion-exchange membrane from DuPont de Nemours. The cathode compartment was filled with graphite balls, the residual volume of the cathode compartment after deduction of the volume of graphite balls amounting to just 95 ml. The residence time of the NaCl brine to be reduced was 5.7 min. The cell voltage amounted to 2.33 V, and the current intensity to 1.5 A. The concentration of chlorine in the outflow of the cathode compartment was approx. 113 mg / l. The current density relative to the total surface area of the graphite balls used was 9.7 A / m2.

example 3

[0044]The chlorine-containing anolyte brine from an NaCl electrolysis with a corresponding chlorine content of 422 mg / l and a pH value of 4 was introduced at 1.1 l / h into the above-described cell, provided with a DUPONT Nafion 982 ion-exchange membrane. The cathode compartment was filled with graphite balls, the residual volume of the cathode compartment after deduction of the volume of graphite balls amounting to 95 ml. The residence time of the brine to be reduced in the cathode compartment was 5.3 min, The cell voltage amounted to 1.72 V, and the current intensity to 0.8 A. The concentration of chlorine in the outflow of the cathode compartment was less than 1 mg / l, The current density relative to the total surface area of the graphite balls used was 5.2 A / m2.

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PUM

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Abstract

Methods for the reductive post-treatment of NaCl-containing solutions, wherein such methods comprise: providing a NaCl-containing solution obtained from an anode side of an NaCl electrolysis cell, the solution comprising reducible components; and subjecting the solution to cathodic electrochemical reduction.

Description

BACKGROUND OF THE INVENTION[0001]Conventionally, membrane electrolysis methods are used, for example, for electrolyzing sodium chloride-containing solutions (see, e.g., Peter Schmittinger, CHLORINE, Wiley-VCH Verlag, 2000). A divided electrolysis cell can be used in this case, which divided cell consists of an anode compartment with an anode and a cathode compartment with a cathode. The anode and cathode compartments can be separated by an ion-exchange membrane. A sodium chloride-containing solution, also referred to hereinafter as brine, having a sodium chloride concentration of conventionally approx. 300 g / l, is introduced into the anode compartment of such a cell. The chloride ion in the brine is oxidized to yield chlorine on the anode, and the chlorine can then be conveyed out of the cell with the depleted sodium chloride-containing solution, also referred to herein as the anolyte brine, which can have a remaining sodiumchloride concentration of approx. 200 g / l.[0002]So that the...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C25B1/26
CPCC02F1/4676C02F1/722C25B1/26C25B1/46C25B15/08C02F2103/34
Inventor BULAN, ANDREASWEBER, RAINER
Owner BAYER INTELLECTUAL PROPERTY GMBH
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