The PEM water electrolyzer uses PEM to conduct protons, isolates the gas on both sides of the electrode. And it avoids the shortcomings associated with AWE’s use of strong alkaline liquid electrolytes. The PEM water electrolyzer uses PEM as the electrolyte and pure water as the reactant. In addition, the hydrogen permeability of PEM is low, the purity of the hydrogen produced is high, and only water vapor needs to removed; the electrolyzer adopts a zero-spacing structure and has a low ohmic resistance. The overall efficiency of the electrolysis process is significantly improved, and the volume is more compact. The pressure regulation range is large, and the hydrogen output pressure can reach several megapascals, adapting to the rapidly changing renewable energy power input. Therefore, PEM electrolysis of water for hydrogen production is a promising green hydrogen production technology path.
It should also note that the bottleneck of PEM electrolysis for hydrogen production lies in cost and life. In the cost of the electrolytic cell, the bipolar plate accounts for about 48%. And the membrane electrode accounts for about 10%. The current international advanced level of PEM is: the performance of a single cell is 2A cm–[email protected] The total platinum catalyst loading is 2~3mg/cm², the stable operation time is 60,000~80,000 h, and the hydrogen production cost is about 1 kg. Hydrogen $3.7. Research on reducing the cost of PEM electrolyzers focuses on core components such as catalysts, PEM-based membrane electrodes, gas diffusion layers, and bipolar plates.
Since the anode of the PEM electrolyzer is in a strongly acidic environment (pH ≈ 2) and the electrolysis voltage is 1.4~2.0V, most non-precious metals will corrode and may combine with the sulfonate ions in the PEM. Thereby reducing the ability of the PEM to conduct protons. The electrocatalyst research of PEM electrolyzer is mainly about Ir, Ru and other noble metals/oxides and their binary and ternary alloys/mixed oxides, supported catalysts with titanium material as carrier.
According to the technical planning target, the total loading of platinum group catalysts on the membrane electrode should be reduced to 0.125 mg/cm². While the current anode iridium catalyst loading is in the order of 1 mg/cm². And the cathode Pt/C catalyst Pt loading is about 0.4 ~0.6mg/cm². The Ir0.7Ru0.3Ox catalyst prepared by the Italian research team can achieve an electrolytic cell performance of 3.2A cm–[email protected] when the total anode catalyst loading is 1.5mg/cm².
The Ir0.38/WxTi1-xO2 catalyst prepared by Giner’s research team has a full-cell performance of 2A cm-[email protected] when the Ir loading is 0.4 mg/cm². And the Ir content is only 1/5 of the traditional electrode. The electrocatalytic oxygen evolution activity of Ru is higher than that of Ir, but the stability is poor; the activity and stability of the catalyst can be improved by forming a stable alloy with Ir. The Ir0.6Sn0.4 catalyst prepared by the Dalian Institute of Chemical Physics. Chinese Academy of Sciences has a performance of 2A [email protected] in the full electrolytic cell test; IrSn can form a stable solid solution structure. And the process of forming an alloy with Sn improves The dispersibility of Ir helps to reduce the Ir load.
The National Renewable Energy Laboratory of the United States and Giner have jointly developed a variety of metal-organic framework (MOF) material catalysts. And the price is only 1/20 of the traditional catalysts. Among them, the overpotential of Co-MOF-GO catalyst at 0.01A/cm² It is 1.644V (vs. RHE) and outperforms traditional Ir catalysts in half-cell decay experiments, but full-cell tests have not yet carry out.
Limited by the requirements of the acidic environment, high anode potential, and good electrical conductivity of PEM water electrolysis for hydrogen production. The research and development of non-precious metal catalysts or non-metal catalysts is relatively difficult. Ir is dominant. A better way to reduce the cost of hydrogen production and reduce the amount of precious metal catalysts in the future is to develop ultra-low loading or ordered membrane electrodes.
(2) Diaphragm material
In terms of PEM, currently commonly used products include DuPont Na-fion series membrane, Dow Chemical Dow series membrane, Asahi Glass Co., Ltd. Flemion series membrane, Asahi Kasei Co., Ltd. Aciplex-S series membrane, Tokuyama Chemical Co., Ltd. Neosepta-F and so on. The DSMTM membrane developed by Giner has been produced on a large scale. Compared with Nafion membrane, it has better mechanical properties and thinner thickness. It has good dimensional stability during power fluctuation and start-up and shutdown. The application performance of the actual electrolytic cell is better.
In order to further improve the performance of PEM and reduce the cost, on the one hand, the enhanced composite scheme can be used to improve the mechanical properties of PEM, which is beneficial to reduce the thickness of the membrane. On the other hand, the membrane resistance and electrolytic energy can reduce by increasing the ionic conductivity of the membrane. It is beneficial to improve the overall performance of the electrolytic cell. Domestic PEM products have entered the trial stage.
(3) Membrane electrode
The anode of PEM electrolyzed water needs to be resistant to acid environment corrosion, high potential corrosion resistance. And should have a suitable hole structure to allow gas and water to pass through. Limited by the reaction conditions of PEM water electrolysis, membrane electrode materials (such as carbon materials) commonly used in PEM fuel cells cannot be used for water electrolysis anodes. 3M company has developed a nanostructured thin film (NSTF) electrode. The anode and cathode use Ir and Pt catalysts respectively, and the loading is 0.25mg/cm2.
It can work stably in an acidic environment and high potential conditions, and the rod-like array structure on the surface is conducive to improving Surface dispersibility of catalysts. Proton uses direct spray deposition to reduce catalyst agglomeration. Pt/C and Ir with a loading of 0.1 mg/cm2 and IrO2 with a loading of 0.1 mg/cm2 are deposited on the Nafion117 membrane. The application performance of a single electrolytic cell is comparable to traditional high. The catalyst loading electrolyzer is similar (1.8A cm–[email protected]) and works stably for 500h at 2.3V.
Improving the performance of the current collector can also improve the performance of the electrolyzer. A research team from the University of Tennessee used template-assisted chemical etching to fabricate small holes with a diameter of less than 1 mm on a titanium sheet. And the thickness of the anode current collector was only 25.4 μm. The related current collector used in the PEM water electrolysis cathode, and the electrolytic performance was 2A cm–[email protected] The cathode Pt catalyst loading is only 0.086m/cm².
(4) Bipolar plate
The bipolar plate and flow field account for a large proportion of the cost of the electrolytic cell. And reducing the cost of the bipolar plate is the key to controlling the cost of the electrolytic cell. In the harsh working environment of the anode of the PEM electrolytic cell. If the bipolar plate is corroded, metal ions will be leached out, which will then contaminate the PEM.
Therefore, the commonly used bipolar plate protection measure is to prepare a layer of anti-corrosion coating on the surface. Letten-meier et al. prepared a Ti layer on a stainless steel bipolar plate by vacuum plasma spraying to prevent corrosion. And then prepared a Pt layer by magnetron sputtering to prevent the decrease in conductivity caused by Ti oxidation; Further studies found that the Pt coating was Switching to a lower-priced Nb coating can maintain similar cell performance. And the cell can run stably for more than 1000h.
The research team of the University of Tennessee used additive manufacturing technology to make a stainless steel material flow field with a thickness of 1mm on the cathode bipolar plate, and directly deposit a mesh gas diffusion layer with a thickness of 0.15mm on it. The cathode impedance of the single cell Very small, the battery performance is as high as 2A cm–[email protected] But the surface is still gold-plated to improve stability. In addition, the Oak Ridge National Laboratory of the United States, the Korea Institute of Science and Technology and other institutions have also carried out serial research and development of bipolar plates for PEM electrolyzers.
(5) Electrolyzer stability
In 2003, Proton completed the continuous operation test of PEM electrolyzer (>60,000 h). And the decay rate was only 4 μV/h. The technical goal of 2030 proposed by the European Fuel Cell and Hydrogen Energy Association requires that the life of the electrolyzer reach 90,000 hours. And the decay rate under continuous working conditions is stable at 0.4~15μV/h. Many research teams have focused on exploring the attenuation mechanism of various components in the PEM electrolytic cell.
And it found that the shedding of catalysts and membranes, changes in water flow, and corrosion of water supply pipelines will lead to an increase in ohmic impedance. The destruction of the membrane electrode structure will induce gas permeation on both sides. Contributing to reduced hydrogen purity, temperature/pressure changes, current density, and power duty cycling can also affect component decay rates. The Dalian Institute of Chemical Physics, Chinese Academy of Sciences conducted a 7800h decay test on the PEM electrolyzer. It found that the pollution mainly came from the water source and metal ions of the unit components; completed the analysis of the influence of water supply and current density changes on the performance of the PEM electrolyzer.
French researchers built a 46kW electrolyzer model to predict how it would work under power fluctuations. At higher temperatures and lower pressures, the electrolyzer was most efficient and could better adapt to power fluctuations.
In terms of promotion and application, my country’s PEM water electrolysis hydrogen production technology is undergoing a stage change from laboratory research and development to marketization and large-scale application. And demonstration projects are gradually being constructed. Such as the megawatt-level hydrogen energy demonstration of State Grid Anhui Electric Power Co., Ltd. They will complete the project and put into operation by the end of 2021.
The PEM Water Electrolysis Hydrogen Production Joint Laboratory jointly established by the Dalian Institute of Chemical Physics of the Chinese Academy of Sciences and Sungrow Co., Ltd.. It aims at key issues in the industrialization of PEM water electrolysis technology. Such as the activity and stability of inexpensive catalysts, membrane permeability, membrane Conduct research on electrode structure, etc.; For bipolar plates, diffusion layers, etc., develop cheap anti-corrosion coating technology under high current density and high voltage conditions. And focus on improving electrolysis efficiency and reducing overall costs.