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The major units in the flow sheet involve a desulfurization unit, a steam reformer, a low temperature (LT) shift reactor, a methanation reactor, and a membrane separator unit.
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The fabricated system consists of three components; a pre-process unit, a rotating membrane separator and a magnetic separator.
The designed magnetic separator system consists of three components; a pre-process unit, a rotating membrane separator and a magnetic separator.
The effluent was extracted from the top layer of the broth by using a membrane separator.
For this study, a perfluorosulphonic acid membrane separator (Nafion® 117) was used.
In a membrane separator, hydrogen flow rates and partial pressures may vary along the flow directions on both sides of the separator.
This resulted in 33% enhancement in hydrogen recovery with multi-pass in comparison to single pass membrane separator.
Performance of a single and four collective membranes are tested in a single (without baffle) and multi-pass (with longitudinal baffles) membrane separator.
In current study self-supported dense PdAg membranes were used to study the hydrogen recovery in a multi-pass membrane separator.
The Li-ion battery using the PE-g-GMA membrane separator showed a better cycle life than that of the unmodified PE membrane separator, indicating that the surface hydrophilicity of the PE membrane separator improved the electrolyte holding capability between the electrodes in the Li-ion cell and prevented the electrolyte leakage.
In principle, these batteries are simple: They consist of two electrodes divided by a membrane "separator" and a liquid electrolyte that allows ions to glide back and forth between the electrodes.
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