Electrochemical system for purifying drinking water and purification method
An electrochemical and drinking water technology, applied in the electrochemical system and purification field of drinking water, can solve the problems of decreased electrochemical activity, low utilization efficiency, heavy metal pollution, etc. The effect of promoting oxidation
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Embodiment 1
[0068] Example 1: Construction of an electrochemical system for drinking water purification
[0069] A 5mm thick polypropylene (PP) plate is used as the shell of the electrochemical system (length 240mm, width 140mm, height 250mm), in which the anode chamber 2 is 80mm long, 130mm wide, and 250mm high, with an effective volume of 2.6L, and the cathode chamber 4 is 140mm long and 130mm wide. The height is 250mm, and the effective volume is 4.5L. The partition wall between the anode chamber 2 and the cathode chamber 4 is provided with a diaphragm, the diaphragm adopts a proton exchange membrane (Nafion 117, 140mm, width 80mm), and the lower end of the diaphragm is 20mm from the bottom of the shell. A water-permeable membrane 12 and a gas-permeable membrane 13 are arranged on the upper part of the partition, wherein the water-permeable membrane 12 is fixed in the plastic card slot by laser microporous concave rubber, and the gas-permeable membrane is made of polytetrafluoroethylen...
Embodiment 2
[0070] Example 2: Operation of the electrochemical system and purification of drinking water
[0071] Using the electrochemical system constructed in Example 1, prepare 2.5 L of electrolyte solution (2% NaCl), inject it into the anode chamber, and seal the anode chamber. Use a three-way pipe to connect the electrochemical system to the drinking water pipeline, open the clean water outlet valve of the electrochemical system, the water flow switch detects the water flow and activates the external power supply through the automatic controller. During the operation, the static flow rate and continuous flow were tested. Under the conditions, the change of the cathode potential under different applied voltages.
[0072] The results show that the cathode potential of the electrochemical system can be maintained at -1.4V (VS Ag / AgCl) at a static flow rate with an external voltage of 0.5V. Under continuous flow, the cathode potential can be maintained between -1.0V - -1.5V (VS Ag / AgCl...
Embodiment 3
[0075] Embodiment 3: long-term operation of electrochemical system and its backwashing operation
[0076]The electrochemical system of Example 1 was used, connected to the drinking water pipeline for long-term operation, and the cathode potential change of the electrochemical system under different flow rates and different applied voltages, as well as the consumption of anolyte and anode loss under long-term operation were observed. The results show that the cathode potential can be maintained in the range of -1.0V - -1.5V (VS Ag / AgCl) by adjusting different applied voltages at different flow rates, especially under intermittent operation, the automatic controller can be controlled by the cathode potential The control interval completes the opening and closing of the external power supply. During operation, it was found that magnesium anodic oxidation not only generates electrons to reduce heavy metals through the cathode and produce hydrogen, but also self-oxidation and hydro...
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