Titlebook: Electrochemical Cell Design; Ralph E. White Book 1984 Plenum Press, New York 1984 Chlor.chemical engineering.extraction.water

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Overview: 978-1-4612-9723-9978-1-4613-2795-0

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https://doi.org/10.1007/978-3-030-27486-3e maintenance requirements. The major components of the electrolyzer assembly are shown schematically in figure 1, the electrolyzer pack being built up from alternate anode and cathode sub-assemblies each separated by a sheet of ion exchange membrane and the entire pack sandwiched between end plates

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Physical Principles of Sensing,hat cells which are currently available commercially can support viable processes for $1.00 lb. chemicals in the 100 molecular weight range. Higher value compounds can be very profitable. For lower value compounds, the same equation can be used to drive cell design towards an acceptable financial re

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Simulation in Force Spectroscopy,to small-scale production. In this investigation it is shown that with air cathodes instead of ordinary planar nickel cathodes in a chlor-alkali process as much as 1 MWh/ton chlorine produced or 30 MWh/yr-m. of electrode area could be gained. It is concluded that because of technical and economical