Electrolytic cell and system for treating water
A water treatment system is disclosed having electrolytic cell for liberating hydrogen from a base solution. The base solution may be a solution of brine for generating sodium hypochlorite, or potable water to be oxidized. The cell has first and second opposing electrode endplates held apart from each other by a pair of supports such that the supports enclose opposing sides of the endplates to form a cell chamber. One or more inner electrode plates are spaced apart from each other in the cell chamber in between the first and second electrode plates. The supports are configured to electrically isolate the first and second electrode plates and the inner electrode plates from each other. The first and second electrode plates are configured to receive opposite polarity charges that passively charge the inner electrode plates via conduction from the base solution to form a chemical reaction in the base solution as the base solution passes through the cell chamber.
1. A system for liberating hydrogen from a base solution, comprising:
a first electrolytic cell;
the first electrolytic cell having an input for receiving the base solution;
the first electrolytic cell comprising a cell chamber in communication with the input, the cell chamber defined by an anode plate at one end and a cathode plate at a second end;
wherein the base solution is received in the cell chamber such that the base solution is in contact with the anode plate and cathode plate to create an electrolytic conversion to generate a modified solution comprising sodium hypochlorite by liberating hydrogen from the base solution;
the first electrolytic cell having an output in communication with a first junction forming a first bifurcated line and a second bifurcated line;
wherein the first bifurcated line directs flow into a return line coupled to the input;
wherein the first junction is configured such that the modified solution is passively directed out the first bifurcated line while the liberated hydrogen is passively directed out the second bifurcated line to remove liberated hydrogen from the modified solution; and
wherein a pressure differential between the modified solution in the return line and the modified solution in the first electrolytic cell generates a positive upward flow through the first electrolytic cell.
2. A system as recited in claim 1 , wherein the return line is coupled to the input to circulate at least a portion of the modified solution back into the first electrolytic cell.
3. A system as recited in claim 2 , further comprising:
a second electrolytic cell in fluid communication with the first electrolytic cell; and
wherein the return line is bifurcated at a second junction to direct at least a portion of the modified solution through a third line coupled to an input of the second electrolytic cell.
4. A system as recited in claim 3 , wherein the modified solution leading into the second electrolytic cell is substantially free of liberated hydrogen.
5. A system as recited in claim 1 , wherein a density differential between the modified solution and the liberated hydrogen passively drives the liberated hydrogen out the second line.
6. A system as recited in claim 3 :
wherein the return line comprises a pipe having a first diameter; and
wherein the third line comprises a pipe having a smaller diameter than the return line to create a differential in pressure across the return and third lines.
7. A system as recite in claim 1 , further comprising:
a rectifier coupled to the first electrolytic cell;
the rectifier configured to supply a constant current to the first electrolytic cell such that the current across the first electrolytic cell is controlled via the content of the base solution passing through the first electrolytic cell.
8. A system as recited in claim 7 , wherein:
the base solution comprises brine; and
wherein the first electrolytic cell is configured to generate sodium hypochlorite from the brine solution.
9. A system as recited in claim 8 , further comprising:
a brine supply coupled to the input of the first electrolytic cell; and
a pump configured to feed the base solution into the first electrolytic cell; wherein the pump is further configured to incrementally adjust the flow rate of brine in the base solution to control the current across the electrolytic cell.
10. A system as recited in claim 1 :
wherein the first electrolytic cell is oriented vertically: and
wherein the base solution travels upward through the electrolytic cell against gravity.
11. A method for liberating hydrogen from a base solution, comprising:
directing the base solution through an inlet of an electrolytic cell;
the electrolytic cell comprising a cell chamber in communication with the input, the cell chamber defined by an anode plate at one end and a cathode plate at a second end;
receiving the base solution in to the sell chamber such that the base solution is in contact with the anode plate and cathode plate:
supplying a current to the anode plate and cathode plate of the electrolytic cell to separate hydrogen from the base solution to create a mixture of liberated hydrogen and a modified solution of sodium hypochlorite;
directing the liberated hydrogen and modified solution through a first junction having a first line and a second line; and
passively separating the liberated hydrogen from the modified solution by directing the modified solution into the first line and the liberated hydrogen into the second line;
wherein the first line is coupled to the inlet of the cell to return at least a portion of the modified solution back into the electrolytic cell;
wherein a pressure differential between the modified solution in the first line and the modified solution in the electrolytic cell generates a positive upward flow through the electrolytic cell.
12. A method as recited in claim 11 , wherein a density differential between the liberated hydrogen and the modified solution directs the liberated hydrogen into the second line.
13. A method as recited in claim 11 , further comprising:
directing at least a portion of the modified solution in the first line back into the electrolytic cell.
14. A method as recited in claim 11 , further comprising:
directing at least a portion of the modified solution through a third line leading to a second electrolytic cell.
15. A system as recited in claim 1 , further comprising:
a temperature sensor located outside the cell chamber in the return line.
16. A system as recited in claim 1 , further comprising:
a level sensor located outside the cell chamber in the return line.
17. A system as recited in claim 2 , wherein the re-circulated portion of the modified solution is fed directly into the electrolytic cell without any dilution of said modified solution.
18. A method as recited in claim 11 , further comprising:
measuring the temperature of the modified solution at a location within the first line.
19. A method as recited in claim 18 , further comprising:
measuring the level of the modified solution at a location within the first line.
20. A method as recited in claim 13 , wherein the portion of the modified solution is fed directly into the electrolytic cell without any dilution of said modified solution.
21. A system as recited in claim 1 :
wherein the pressure differential between the cell chamber and return line is at least 10%.
22. A method as recited in claim 11 :
wherein the pressure differential between the cell chamber and return line is at least 10%.