Understanding Electrochemical energy storage and compression energy cost
The cost includes the compression and dispensing cost but not the cost of hydrogen production. The electrochemical configuration has the lowest dispensing cost, followed by the combined and mechanical configuration for both HRS sizes.
The cost includes the compression and dispensing cost but not the cost of hydrogen production. The electrochemical configuration has the lowest dispensing cost, followed by the combined and mechanical configuration for both HRS sizes.
• Develop and demonstrate an electrochemical hydrogen compressor (EHC) to address critical needs of lower cost, higher efficiency, and improved durability. Fabricate stack and cell components for 12,688 psi (875 bar) operation, and scale up membranes, membrane electrode assemblies (MEAs), and stack.
To calculate the full life cycle cost per kilowatt hour, the investment cost, maintenance cost, replacement cost, charging cost and recovery cost of the energy storage system are respectively analyzed. The calculation method provides a reference for the cost evaluation of the energy storage system.
In terms of hydrogen storage, two compression modes (mechanical and non-mechanical compressors) are generally used to increase volume density in which mechanical compressors with several classifications including reciprocating piston compressors, hydrogen diaphragm compressors and ionic liquid.
There are various compressor designs that can be used and ultimately the choice of compression technology, associated costs, energy use and resulting GHG emissions will depend on where in the supply chain it is used. The purpose of this ‘technical brief’ is to describe how to conduct technoeconomic.
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About Electrochemical energy storage and compression energy cost video introduction
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