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Various CO x electrolyzer cell architectures are provided, including various flow field designs and gas diffusion layer designs that may be particularly useful in the context of CO x electrolyzer cells.
1 . A CO x electrolyzer system comprising:
a cathode inlet port;
a cathode outlet port; and
one or more CO x electrolyzer cells, each CO x electrolyzer cell including:
a corresponding cathode flow field,
a corresponding membrane electrode assembly (MEA) that includes a metal nanoparticle catalyst layer,
a corresponding cathode gas diffusion layer (GDL) interposed between the corresponding cathode flow field of that CO x electrolyzer cell and the corresponding MEA of that CO x electrolyzer cell, wherein:
the one or more CO x electrolyzer cells are configured to be connected with a voltage or current source so as to develop an electrical potential or current across the one or more CO x electrolyzer cells,
the corresponding cathode flow field of each CO x electrolyzer cell has one or more corresponding cathode channels that are each configured to receive a cathode fluid via the cathode inlet port and to direct at least some of that cathode fluid to the cathode outlet port,
the cathode inlet port is configured to receive gaseous CO x ,
the corresponding cathode channels of the corresponding cathode flow field of each CO x electrolyzer cell are in a corresponding side of the corresponding cathode flow field of that CO x electrolyzer cell that is in contact with the corresponding cathode GDL of that CO x electrolyzer cell,
each cathode channel of the one or more corresponding cathode channels of the corresponding cathode flow field of each CO x electrolyzer cell has a length of between 300 and 6000 mm, a cross-sectional area of between 0.15 and 6 square mm, and a width of between 0.5 and 2 mm, and
each cathode flow field is configured to develop a pressure drop across the cathode channels thereof that is between 1 psi and 50 psi under normal operating conditions of the CO x electrolyzer system.
2 . The CO x electrolyzer system of claim 1 , wherein each of the one or more corresponding cathode channels of the corresponding cathode flow field of each CO x electrolyzer cell follows a corresponding serpentine path with multiple longer segments thereof extending along parallel paths and shorter segments thereof spanning between opposing ends of adjacent longer segments thereof.
3 . The CO x electrolyzer system of claim 2 , wherein each cathode channel of the one or more corresponding cathode channels of the corresponding cathode flow field of each CO x electrolyzer cell has a length of between 1500 and 6000 mm.
4 . The CO x electrolyzer system of claim 2 , wherein there are multiple corresponding cathode channels in the corresponding cathode flow field of each CO x electrolyzer cell.
5 . The CO x electrolyzer system of claim 4 , wherein the multiple corresponding cathode channels of the corresponding cathode flow field of each CO x electrolyzer cell are arranged in an interleaved pattern in which each longer segment of each corresponding cathode channel is adjacent to at least one longer segment of another corresponding cathode channel.
6 . The CO x electrolyzer system of claim 5 , wherein:
the multiple corresponding cathode channels of the corresponding cathode flow field of each CO x electrolyzer cell include a first corresponding cathode channel and a second corresponding cathode channel,
the longer segments of the first corresponding cathode channel of the corresponding cathode flow field of that CO x electrolyzer cell that are adjacent to one another are separated by first corresponding peninsular walls,
the longer segments of the second corresponding cathode channel of the corresponding cathode flow field of that CO x electrolyzer cell that are adjacent to one another are separated by second corresponding peninsular walls,
each first corresponding peninsular wall, for at least part of its length, decreases in width as that first corresponding peninsular wall approaches the shorter segment of the corresponding first cathode channel of the corresponding cathode flow field of that CO x electrolyzer cell that spans between the two longer segments thereof that are separated by that first corresponding peninsular wall, and
each second corresponding peninsular wall, for at least part of its length, decreases in width as that corresponding second peninsular wall approaches the shorter segment of the corresponding second cathode channel of the corresponding cathode flow field of that CO x electrolyzer cell that spans between the two longer segments thereof that are separated by that second corresponding peninsular wall.
7 . The CO x electrolyzer system of claim 4 , wherein:
endmost longer segments of each corresponding cathode channel of each corresponding cathode flow field of each CO x electrolyzer cell each include a corresponding first endmost segment and a corresponding second endmost segment, and
the multiple corresponding cathode channels of each corresponding cathode flow field of each CO x electrolyzer cell are arranged in a side-by-side pattern in which the first corresponding endmost segment of one of the corresponding cathode channels in each pair of adjacent corresponding cathode channels of each corresponding cathode flow field of each CO x electrolyzer cell is adjacent to the second corresponding endmost segment of the other of the corresponding cathode channels of that pair of adjacent corresponding cathode channels.
8 . The CO x electrolyzer system of claim 2 , wherein the shorter segments are arcuate.
9 . The CO x electrolyzer system of claim 1 , wherein there are multiple corresponding cathode channels of the corresponding cathode flow field of each CO x electrolyzer cell arranged in a linear array, each corresponding cathode channel spanning between one side of the corresponding cathode flow field of that CO x electrolyzer cell and an opposing side of the corresponding cathode flow field of that CO x electrolyzer cell.
10 . The CO x electrolyzer system of claim 1 , wherein:
there are a plurality of cathode channels in a first cathode flow field of the one or more cathode flow fields;
the cathode channels in the first cathode flow field are parallel channels;
the cathode channels in a first group of the cathode channels in the first cathode flow field have first ends that are each connected with a corresponding inlet branch channel that extends in a first direction that is transverse to the parallel channels,
the cathode channels in the first group of the cathode channels in the first cathode flow field have second ends that are each connected with a corresponding outlet branch channel that extends in the first direction,
the first group of the cathode channels has two outermost cathode channels,
an inlet passage extends from a fluidic inlet port in the first cathode flow field to the inlet branch passage and connects with the inlet branch passage at a location proximate to where one of the outermost cathode channels of the first group connects with the inlet branch passage, and
an outlet passage extends from a fluidic outlet port in the first cathode flow field to the outlet branch passage and connects with the outlet branch passage at a location proximate to where the other of the outermost cathode channels of the first group connects with the outlet branch passage.
11 . The CO x electrolyzer of claim 1 , wherein:
each corresponding cathode channel of the corresponding cathode flow field of each CO x electrolyzer cell has two corresponding interior bottom edges that are spaced apart from, and in a direction perpendicular to, a corresponding side of the corresponding cathode flow field of that CO x electrolyzer cell that is in contact with the corresponding cathode GDL of that CO x electrolyzer cell, and
each corresponding interior bottom edge is rounded.
12 . A CO x electrolyzer system comprising:
a cathode inlet port;
a cathode outlet port; and
one or more CO x electrolyzer cells, each CO x electrolyzer cell including:
a corresponding cathode flow field,
a corresponding membrane electrode assembly (MEA) that includes a metal nanoparticle catalyst layer,
a corresponding cathode gas diffusion layer (GDL) interposed between the corresponding cathode flow field of that CO x electrolyzer cell and the corresponding MEA of that CO x electrolyzer cell, wherein:
the one or more CO x electrolyzer cells are configured to be connected with a voltage or current source so as to develop an electrical potential or current across the one or more CO x electrolyzer cells,
the corresponding cathode flow field of each CO x electrolyzer cell has one or more corresponding cathode channels that are each configured to receive a cathode fluid via the cathode inlet port and to direct at least some of that cathode fluid to the cathode outlet port,
the cathode inlet port is configured to receive gaseous CO x ,
the corresponding cathode channels of the corresponding cathode flow field of each CO x electrolyzer cell are in a corresponding side of the corresponding cathode flow field of that CO x electrolyzer cell that is in contact with the corresponding cathode GDL of that CO x electrolyzer cell, and
each cathode flow field is configured to develop a pressure drop across the cathode channels thereof that is between 1 psi and 50 psi under normal operating conditions of the CO x electrolyzer system.
13 . The CO x electrolyzer system of claim 12 , wherein the CO x electrolyzer system is configured to operate, under normal operating conditions, such that CO x -containing gas is supplied to each cathode flow field at a rate of between 2 standard cubic centimeters per minute (sccm) per square centimeter of active flow cathode flow field area and 21 sccm per square centimeter of active flow cathode flow field area and at an inlet pressure at the cathode inlet port of between 50 psi and 400 psi.
14 . The CO x electrolyzer system of claim 12 , wherein each of the one or more corresponding cathode channels of the corresponding cathode flow field of each CO x electrolyzer cell follows a corresponding serpentine path with multiple longer segments thereof extending along parallel paths and shorter segments thereof spanning between opposing ends of adjacent longer segments thereof.
15 . The CO x electrolyzer system of claim 14 , wherein:
the one or more corresponding cathode channels of the corresponding cathode flow field of each CO x electrolyzer cell includes multiple corresponding cathode channels,
endmost longer segments of each corresponding cathode channel of each corresponding cathode flow field of each CO x electrolyzer cell include a corresponding first endmost segment and a corresponding second endmost segment, and
the multiple corresponding cathode channels of each corresponding cathode flow field of each CO x electrolyzer cell are arranged in a side-by-side pattern in which the corresponding first endmost segment of one of the corresponding cathode channels in each pair of adjacent corresponding cathode channels of each corresponding cathode flow field of each CO x electrolyzer cell is adjacent to the corresponding second endmost segment of the other of the corresponding cathode channels of that pair of adjacent corresponding cathode channels.
16 . The CO x electrolyzer system of claim 14 , wherein the shorter segments are arcuate.
17 . The CO x electrolyzer system of claim 12 , wherein the one or more corresponding cathode channels of the corresponding cathode flow field of each CO x electrolyzer cell includes multiple corresponding cathode channels and the multiple corresponding cathode channels of the corresponding cathode flow field of each CO x electrolyzer cell are arranged in an interleaved pattern in which each longer segment of each corresponding cathode channel is adjacent to at least one longer segment of another corresponding cathode channel.
18 . The CO x electrolyzer system of claim 17 , wherein:
the multiple corresponding cathode channels of the corresponding cathode flow field of each CO x electrolyzer cell include a first corresponding cathode channel and a second corresponding cathode channel,
the longer segments of the first corresponding cathode channel of the corresponding cathode flow field of that CO x electrolyzer cell that are adjacent to one another are separated by first corresponding peninsular walls,
the longer segments of the second corresponding cathode channel of the corresponding cathode flow field of that CO x electrolyzer cell that are adjacent to one another are separated by second corresponding peninsular walls,
each first corresponding peninsular wall, for at least part of its length, decreases in width as that first corresponding peninsular wall approaches the shorter segment of the corresponding first cathode channel of the corresponding cathode flow field of that CO x electrolyzer cell that spans between the two longer segments thereof that are separated by that first corresponding peninsular wall, and
each second corresponding peninsular wall, for at least part of its length, decreases in width as that corresponding second peninsular wall approaches the shorter segment of the corresponding second cathode channel of the corresponding cathode flow field of that CO x electrolyzer cell that spans between the two longer segments thereof that are separated by that second corresponding peninsular wall.
19 . The CO x electrolyzer system of claim 12 , wherein there are multiple corresponding cathode channels of the corresponding cathode flow field of each CO x electrolyzer cell arranged in a linear array, each corresponding cathode channel spanning between one side of the corresponding cathode flow field of that CO x electrolyzer cell and an opposing side of the corresponding cathode flow field of that CO x electrolyzer cell.
20 . The CO x electrolyzer of claim 12 , wherein:
each corresponding cathode channel of the corresponding cathode flow field of each CO x electrolyzer cell has two corresponding interior bottom edges that are spaced apart from, and in a direction perpendicular to, a corresponding side of the corresponding cathode flow field of that CO x electrolyzer cell that is in contact with the corresponding cathode GDL of that CO x electrolyzer cell, and
each corresponding interior bottom edge is rounded.