Electrochemical method, apparatus and system with improved production efficiency and CO
The present invention describes ways of increasing the production efficiency of a saline water electrolysis cell and of consuming CO 2 gas and sequestering it from the atmosphere. This is achieved by the introduction of CO 2 gas into the catholyte of the electrolysis, where reaction of the CO 2 with the hydroxide ions present in the catholyte reduces the pH of the catholyte, thereby increasing production efficiency of the electrolysis cell. The preceding reaction forms bicarbonate and/or carbonate, thus sequestering the reactant CO 2 gas from the atmosphere. The CO 2 gas may be introduced either directly into the cathode area of the electrolysis cell, or into the electrolyte prior to its introduction into the electrolysis cell. Corresponding apparatus is also provided.
1. A method of controlling an operation of an electrolysis cell to achieve an improved production efficiency of the electrolysis cell, the method comprising:
defining a production efficiency of the electrolysis cell as a quantity of a product produced per unit of time per watt of power used by the electrolysis cell, the product being selected from the group consisting of a gas formed at the cathode, a gas formed at the anode, acid, a carbonate, and a bicarbonate;
determining a dependence of the production efficiency as a function of a control variable of the electrolysis cell;
controlling the operation of the electrolysis cell, comprising:
introducing a CO 2 gas into an electrolyte of the electrolysis cell containing OH − ions at a rate resulting in a reduced pH level of the electrolyte, but not exceeding a rate leading to a total consumption of the OH − ions, the CO 2 gas reacting with the OH − ions to form one or more of the bicarbonate and carbonate;
varying the rate of introducing the CO 2 gas so as to achieve a value of the control variable corresponding to an improved predetermined production efficiency in accordance with said dependence;
and
operating the electrolysis cell under the improved predetermined production efficiency until an exit condition is met;
thereby improving the production efficiency of the electrolysis cell while sequestering the CO 2 gas.
2. The method of claim 1 , wherein the varying further comprises varying the rate of introducing the CO 2 gas so as to keep values of the control variable between a minimal and maximal thresholds.
3. The method of claim 1 , wherein the control variable is one or more of the following:
pH level of a catholyte in the cathode area inside the electrolysis cell;
PH level of a catholyte removed from the cathode area of the electrolysis cell;
pH level of the electrolyte of the electrolysis cell;
current of the electrolysis cell;
concentration of the CO 2 in a gas stream;
concentration of CO 2 in the catholyte;
concentration of CO 2 in the catholyte removed from the cathode area of the electrolysis cell; and
concentration of CO 2 in the electrolyte.
4. The method of claim 1 , wherein the introducing the CO 2 gas into the electrolyte comprises introducing the CO 2 gas into a catholyte in a cathode area of the electrolysis cell.
5. The method of claim 1 , wherein the introducing the CO 2 gas into the electrolyte comprises introducing the CO 2 gas into an electrolyte prior to introduction of the electrolyte into the electrolysis cell.
6. The method of claim 1 , wherein the operating comprises conducting saline water electrolysis, with saline water containing a salt dissolved in water, the dissolved salt being selected from the group of salts whose ions consist of:
ammonium, calcium, iron, magnesium, potassium, sodium, or copper cations; and
bicarbonate, carbonate, chloride, nitrate, phosphate, or sulfate anions.
7. The method of claim 1 , wherein the operating comprises conducting saline water electrolysis, with saline water containing a salt dissolved in water, the dissolved salt containing one or more of the following:
sodium sulfate; sodium nitrate; sodium phosphate, sodium carbonate; potassium sulfate; potassium nitrate; potassium phosphate; potassium carbonate.
8. The method of claim 1 , wherein the introducing comprises contacting the catholyte with a gas stream containing CO 2 .
9. The method of claim 1 , wherein the reduced pH level is from about pH=14 to about pH=7.
10. The method of claim 1 , wherein the reduced pH level is from about pH=11 to about pH=9.
11. The method of claim 1 , wherein the product is selected from the group consisting of H 2 , O 2 , Cl 2 , an acid, bicarbonate, carbonate.
12. The method of claim 1 , wherein:
the operating comprises conducting the electrolysis in the electrolysis cell having at least one ion-exchange membrane disposed between cathode and anode and defining a cathode area and an anode area; and
the introducing comprises introducing the CO 2 gas into the cathode area in close proximity to the cathode.
13. The method of claim 1 , wherein:
the operating comprises conducting the electrolysis in the electrolysis cell having a cation exchange membrane and an anion exchange membrane disposed in the electrolysis cell between cathode and anode and defining a cathode area, an anode area, and a central area therebetween; and
the introducing comprises introducing the CO 2 gas into one or more of the cathode area and the central area.
14. The method of claim 1 , wherein the CO 2 gas is derived from one or more of the following: the atmosphere; a waste stream; biomass; soil; the ocean; a fossil source.
15. The method of claim 1 , wherein the production efficiency of the electrolysis cell is increased up to about 30%.
16. An apparatus for controlling an operation of an electrolysis cell for achieving an improved production efficiency of the electrolysis cell, the apparatus comprising:
a means for obtaining a dependence of a production efficiency of the electrolysis cell as a function of a control variable of the electrolysis cell, the production efficiency being defined as a quantity of a product produced per unit of time per watt of power used by the electrolysis cell, the product being selected from the group consisting of a gas formed at a cathode, a gas formed at an anode, an acid, a carbonate, and a bicarbonate;
a means for introducing CO 2 gas into an electrolyte of the electrolysis cell containing OH − ions at a rate resulting in a reduced pH level of the electrolyte, but not exceeding a rate leading to total consumption of the OH − ions, the CO 2 gas reacting with the OH − ions to form one or more of the bicarbonate and carbonate;
a means for varying the rate of introducing the CO 2 gas so as to achieve a value of the control variable corresponding to an improved predetermined production efficiency in accordance with said dependence;
and
a means for operating the electrolysis cell under the improved predetermined efficiency until an exit condition is met;
thereby improving the production efficiency of the electrolysis cell while sequestering the CO 2 gas.
17. The apparatus of claim 16 , wherein the means for varying are further configured to vary the rate of introducing the CO 2 gas so as to keep values of the control variable between a minimal and maximal thresholds.
18. The apparatus of claim 16 , wherein the means for introducing comprises one of the following:
a means for introducing the CO 2 gas into a catholyte in a cathode area of the electrolysis cell;
a means for introducing the CO 2 gas into the electrolyte prior to introduction of the electrolyte into the electrolysis cell.
19. The apparatus of claim 16 , wherein the electrolysis cell contains saline water having a salt dissolved therein, the salt being selected from the group of salts whose ions consist of:
ammonium, calcium, iron, magnesium, potassium, sodium, or copper cations; and
bicarbonate, carbonate, chloride, nitrate, phosphate, or sulfate anions.
20. The apparatus of claim 16 , wherein the electrolysis cell contains saline water having a salt dissolved therein, the salt containing one or more of the following:
sodium sulfate; sodium nitrate; sodium phosphate, sodium carbonate; potassium sulfate; potassium nitrate; potassium phosphate; potassium carbonate.
21. The apparatus of claim 16 , wherein the reduced pH level is one of the following:
from about pH=14 to about pH=7;
from about pH=12 to about pH=8;
from about pH=11 to about pH=9;
from about pH=10 to about pH=7.
22. The apparatus of claim 16 , wherein the product is selected from the group consisting of H 2 , O 2 , Cl 2 , an acid, bicarbonate, and carbonate.
23. The apparatus of claim 16 , wherein:
the electrolysis cell has at least one ion-exchange membrane disposed between the cathode and the anode and defining a cathode area and an anode area respectively; and
the means for introducing is configured to introduce the CO 2 gas into the cathode area in close proximity to the cathode.
24. The apparatus of claim 16 , wherein the production efficiency of the electrolysis cell is increased up to about 30%.
25. An electrolysis cell with an improved production efficiency and sequestration of the CO 2 gas, configured to:
obtain a dependence of a production efficiency of the electrolysis cell as a function of a control variable of the electrolysis cell, the production efficiency being defined as a quantity of a product produced per unit of time per watt of power used by the electrolysis cell, the product being selected from the group consisting of a gas formed at the cathode, a gas formed at the anode, acid, a carbonate, and a bicarbonate;
introduce a CO 2 gas into an electrolyte of the electrolysis cell containing OH − ions at a rate resulting in a reduced pH level of the electrolyte, but not exceeding a rate leading to total consumption of the OH − ions, the CO 2 gas reacting with the OH − ions to form one or more of the bicarbonate and carbonate;
and
vary the rate of introducing the CO 2 gas so as to achieve a value of the control variable corresponding to an improved predetermined production efficiency in accordance with said dependence;
thereby improving the production efficiency of the electrolysis cell while sequestering the CO 2 gas.