Tunable Thin Liquid/Gas Diffusion Layers for Electrolyzers
Abstract
A liquid/gas diffusion layer (LGDL) 112 for use in a proton exchange membrane electrolyzer cell 100 includes a planar body 120 having first and second surfaces 128, 130 that are separated by a body thickness 126. The body defines 120 a plurality of straight-through, non-interconnected, pores 122 extending through the body thickness 126, between the first and the second surfaces 128, 130. Each pore 122 has a peripheral rim shape 124, a throat area, and is separated from one another by a land length distance. The body has a porosity c that is calculated by dividing a total throat area of the plurality of pores A P by a total surface area of the surface around the pores A H , and where the porosity ratio e is between approximately 0.20 and approximately 0.80.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1 . A liquid/gas diffusion layer for use in a proton exchange membrane electrolyzer cell comprising:
a planar body having a first surface and a second surface that are separated by a thickness, said body defining a plurality of straight-through, non-interconnected, pores extending through the thickness, between the first surface and the second surface, with each pore having a peripheral rim shape, a throat area, and where each pore is separated from one another by a land length distance; and wherein said body has a porosity ratio that is calculated by dividing a total throat area of the plurality of pores by a total surface area of the first surface extending around the pores, and where the porosity ratio is between approximately 0.20 and approximately 0.80.
2 . The liquid/gas diffusion layer of claim 1 wherein the calculated porosity ratio is between approximately 0.25 and approximately 0.35.
3 . The liquid/gas diffusion layer of claim 2 wherein the calculated porosity ratio is between approximately 0.28 and approximately 0.32.
4 . The liquid/gas diffusion layer of claim 1 wherein the calculated porosity ratio is between approximately 0.65 and approximately 0.75.
5 . The liquid/gas diffusion layer of claim 4 wherein the calculated porosity ratio is between approximately 0.68 and approximately 0.72.
6 . The liquid/gas diffusion layer of claim 1 wherein the peripheral shape of each pore is circular and each pore has a diameter and the diameter is between approximately 10 μm and 800 μm.
7 . The liquid/gas diffusion layer of claim 6 wherein the diameter is between approximately 200 μm and 600 μm.
8 . The liquid/gas diffusion layer of claim 7 wherein the diameter is between approximately 350 μm and 450 μm.
9 . The liquid/gas diffusion layer of claim 1 wherein the peripheral rim shape of a pore is selected from the group consisting of circular, rectangular, square, and triangular.
10 . The liquid/gas diffusion layer of claim 9 wherein the peripheral shape of each pore is the same shape.
11 . The liquid/gas diffusion layer of claim 1 wherein the pores are uniformly distributed in a pattern.
12 . The liquid/gas diffusion layer of claim 1 wherein the thickness of said body is less than 200 μm.
13 . The liquid/gas diffusion layer of claim 12 wherein the thickness of said body is less than 30 μm.
14 . The liquid/gas diffusion layer of claim 13 wherein the thickness of said body is approximately 25.4 μm.
15 . The liquid/gas diffusion layer of claim 1 wherein said body is made of a titanium or titanium alloy material.
16 . The liquid/gas diffusion layer of claim 1 wherein, when the plurality of pores is filled with air and the first surface is level, a contact angle between a drop of water and the first surface measures between approximately 60 degrees and approximately 85 degrees.
17 . The liquid/gas diffusion layer of claim 1 wherein one of the first or the second surfaces is coated with a layer of catalyst material.
18 . The liquid/gas diffusion layer of claim 17 wherein the catalyst material layer is between approximately 3 nm and 20 nm thick.
19 . The liquid/gas diffusion layer of claim 18 wherein the catalyst material layer is approximately 15 nm thick.
20 . The liquid/gas diffusion layer of claim 17 wherein the catalyst material layer is Pt.
21 . The liquid/gas diffusion layer of claim 17 wherein the catalyst material layer is chosen from the group consisting of Ir, IrOx, and IrRuOx.
22 . A proton exchange membrane electrolyzer cell comprising:
an anode liquid/gas diffusion layer having a planar body having a first surface and a second surface that are separated by a thickness, said body defining a plurality of straight-through, non-interconnected, pores extending through the thickness, between the first surface and the second surface, with each pore having a peripheral shape, a throat area, and where each pore is separated from one another by a land length distance; and wherein said body has a porosity ratio that is calculated by dividing a total throat area of the plurality of pores by a total surface area of the first surface around the pores, and where the porosity ratio is between approximately 0.20 and approximately 0.80.
23 . The liquid/gas diffusion layer of claim 20 wherein the peripheral shape of each pore is circular and each pore has a diameter and the diameter is between approximately 10 μm and 800 μm.
24 . The liquid/gas diffusion layer of claim 20 wherein the peripheral shape of a pore is selected from the group consisting of circular, rectangular, square and triangular.
25 . The liquid/gas diffusion layer of claim 20 wherein the thickness of said body is less than 200 μm.
26 . The liquid/gas diffusion layer of claim 20 wherein one of the first or the second surfaces is coated with a layer of catalyst material.
27 . The liquid/gas diffusion layer of claim 26 wherein the catalyst material layer is Pt.
28 . The liquid/gas diffusion layer of claim 26 wherein the catalyst material layer is chosen from the group consisting of Ir, IrOx, and IrRuOx.Join the waitlist — get patent alerts
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