PERFORMANCE ENHANCEMENT VIA WATER MANAGEMENT IN ELECTROCHEMICAL CELLS
Techniques are provided for system operation and performance management of electrochemical cells. Electrochemical cells using polybenzimidazole (PBI) proton exchange membranes may be used. In certain embodiments, performance enhancements are achieved through water management via anode and/or cathode humidification, and reactant air injection.
1 . A method of operating an electrochemical cell in a hydrogen pumping mode, comprising:
applying an electrical potential between a first electrode and a second electrode of the cell;
wherein the first electrode has a higher electrical potential with respect to zero than the second electrode;
flowing electrical current through the cell to consume electrical power;
wherein the first and second electrodes have an acid doped polybenzimidazole membrane between them;
ionizing hydrogen at the first electrode;
evolving hydrogen at the second electrode; and
contacting the first electrode or the second electrode with H2O to decrease the electrical power consumed.
2 . The method of claim 1 , wherein a relative humidity of the hydrogen ionized at the first electrode is less than 0.1% prior to performing the step of contacting the first electrode or the second electrode with H2O to decrease the electrical power consumed.
3 . The method of claim 1 , wherein the step of contacting the first electrode or the second electrode with H2O to decrease the electrical power consumed comprises raising a relative humidity of the hydrogen ionized at the first electrode from less than 0.1% to greater than 0.1%.
4 . The method of claim 1 , wherein the step of contacting the first electrode or the second electrode with H2O to decrease the electrical power consumed comprises raising a relative humidity of the hydrogen ionized at the first electrode from less than 0.5% to greater than 0.5%.
5 . The method of claim 1 , wherein the step of contacting the first electrode or the second electrode with H2O to decrease the electrical power consumed comprises raising a relative humidity of the hydrogen ionized at the first electrode from less than 1.0% to greater than 1.0%.
6 . The method of claim 1 , wherein the electrical power consumed is decreased by a factor of at least 10%.
7 . The method of claim 1 , wherein the electrical power consumed is decreased by a factor of at least 50%.
8 . The method of claim 1 , wherein the electrical potential is maintained at less than 0.8 volts.
9 . The method of claim 1 , wherein the electrical potential is maintained at less than 0.6 volts.
10 . The method of claim 1 , wherein the electrical potential is maintained at less than 0.3 volts.
11 . The method of claim 1 , wherein the step of contacting the first electrode or the second electrode with H2O comprises contacting the cell with H2O vapor.
12 . The method of claim 1 , wherein the step of contacting the first electrode or the second electrode with H2O comprises humidifying a hydrogen source gas and contacting the first electrode with the hydrogen source gas.
13 . The method of claim 1 , wherein the step of contacting the first electrode or the second electrode with H2O comprises injecting oxygen into a hydrogen source gas and contacting the first electrode with the hydrogen source gas.
14 . The method of claim 1 , wherein the step of contacting the first electrode or the second electrode with H2O comprises:
injecting air into a hydrogen source gas to raise an air content of the hydrogen source gas to within the range of 1-6% on a molar basis; and
contacting the first electrode with the hydrogen source gas.
15 . The method of claim 1 , wherein the step of contacting the first electrode or the second electrode with H2O comprises replacing the electrical potential between the first and second electrodes with an electrical load, and then replacing the electrical load with the electrical potential.
16 . The method of claim 1 , further comprising;
measuring an electrical performance parameter of the cell;
generating a control signal when the electrical performance parameter exceeds a predetermined value;
wherein the step of contacting the first electrode or the second electrode with H2O to decrease the electrical power consumed is performed upon generation of the control signal.
17 . The method of claim 16 , wherein the performance parameter is the electrical potential between the first electrode and second electrode.
18 . The method of claim 16 , wherein the performance parameter is the electrical current flow through the cell.
19 . The method of claim 16 , wherein the performance parameter is the electrical power consumed by the cell.
20 . The method of claim 16 , wherein the performance parameter is a ratio of (electrical power consumed by the cell) to (hydrogen evolved at the second electrode).
21 . The method of claim 1 , wherein the cell is maintained at a temperature of at least 100 C.
22 . The method of claim 1 , wherein the cell is maintained at a temperature of at least 140 C.
23 . The method of claim 1 , wherein the membrane comprises phosphoric acid at a ratio of at least 20 moles phosphoric acid to polybenzimidazole repeating unit.
24 . The method of claim 1 , wherein the membrane comprises phosphoric acid at a ratio of at least 32 moles phosphoric acid to polybenzimidazole repeating unit.
25 . The method of claim 1 , wherein the membrane comprises phosphoric acid at a ratio of at least 40 moles phosphoric acid to polybenzimidazole repeating unit.
26 . The method of claim 1 , wherein the membrane is prepared by a sol-gel process.
27 . The method of claim 1 , wherein the membrane has a proton conductivity of at least 0.1 S/cm.
28 . The method of claim 1 , wherein the membrane has a proton conductivity of at least 0.2 S/cm.
29 . A method of operating an electrochemical cell in a hydrogen pumping mode, comprising:
applying an electrical potential between a first electrode and a second electrode of the cell;
wherein the first electrode has a higher electrical potential with respect to zero than the second electrode;
flowing electrical current through the cell to consume electrical power;
wherein the first and second electrodes have an acid doped polybenzimidazole membrane between them;
ionizing hydrogen at the first electrode;
evolving a hydrogen output flow at the second electrode;
wherein the cell has a ratio of (electrical power consumed) to (hydrogen output flow); and
contacting the first electrode or the second electrode with H2O to decrease the ratio of (electrical power consumed) to (hydrogen output flow).
30 . A method of operating an electrochemical cell in a hydrogen pumping mode, comprising:
applying an electrical potential between a first electrode and a second electrode of the cell;
wherein the first electrode has a higher electrical potential with respect to zero than the second electrode;
flowing electrical current through the cell to consume electrical power;
wherein the first and second electrodes have an acid doped polybenzimidazole membrane between them;
ionizing hydrogen at the first electrode;
evolving a hydrogen output flow at the second electrode; and
contacting the first electrode or the second electrode with H2O to maintain the hydrogen output flow while decreasing the electrical potential between the first electrode and second electrode.
31 . A method of operating an electrochemical cell in a hydrogen pumping mode, comprising:
applying an electrical potential between a first electrode and a second electrode of the cell;
wherein the first electrode has a higher electrical potential with respect to zero than the second electrode;
flowing electrical current through the cell to consume electrical power;
wherein the first and second electrodes have a proton exchange membrane between them;
ionizing hydrogen at the first electrode;
evolving hydrogen at the second electrode; and
contacting the first electrode or the second electrode with H2O to decrease the electrical power consumed.
32 . The method of claim 31 , wherein a relative humidity of the hydrogen ionized at the first electrode is less than 1% prior to performing the step of contacting the first electrode or the second electrode with H2O to decrease the electrical power consumed.
33 . The method of claim 31 , wherein the electrical power consumed is decreased by a factor of at least 10%.
34 . The method of claim 31 , wherein the electrical power consumed is decreased by a factor of at least 50%.
35 . The method of claim 31 , wherein the step of contacting the first electrode or the second electrode with H2 0 comprises humidifying a hydrogen source gas and contacting the first electrode with the hydrogen source gas.
36 . The method of claim 31 , wherein the step of contacting the first electrode or the second electrode with H2O comprises injecting oxygen into a hydrogen source gas and contacting the first electrode with the hydrogen source gas.
37 . The method of claim 31 , wherein the step of contacting the first electrode or the second electrode with H2O comprises:
injecting air into a hydrogen source gas to raise an air content of the hydrogen source gas to within the range of 1-6% on a molar basis; and
contacting the first electrode with the hydrogen source gas.
38 . The method of claim 31 , wherein the step of contacting the first electrode or the second electrode with H2O comprises replacing the electrical potential between the first and second electrodes with an electrical load, and then replacing the electrical load with the electrical potential.
39 . The method of claim 31 , further comprising;
measuring an electrical performance parameter of the cell;
generating a control signal when the electrical performance parameter exceeds a predetermined value;
wherein the step of contacting the first electrode or the second electrode with H2O to decrease the electrical power consumed is performed upon generation of the control signal.
40 . The method of claim 39 , wherein the performance parameter is the electrical potential between the first electrode and second electrode.
41 . The method of claim 39 , wherein the performance parameter is the electrical current flow through the cell.
42 . The method of claim 39 , wherein the performance parameter is the electrical power consumed by the cell.
43 . The method of claim 39 , wherein the performance parameter is a ratio of (electrical power consumed by the cell) to (hydrogen evolved at the second electrode).