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Moreover, a membrane obtained by deposition of palladium on the stainless-steel silicalite membrane was tested.
The thermal stability of the composite membrane was tested using TGA which showed that the decomposition temperature is as high as 400 °C.
A submerged type MF (micro filtration) membrane was tested for about two years in a pilot plant (200 m3/das) as a pre-treatment process to SWRO desalination.
A SrFeCo0.5O3 membrane was tested, and a blank run confirmed that it acted as a total oxidation catalyst, with no C2 products.
The membrane was tested in a commercial fuel cell test station at 100 °C with dry hydrogen and oxygen gas reactants using Pt/C electrodes.
Because only one batch of each membrane was tested in our study, it was not possible to determine if the differences in protein rejection between channel geometries were due to the membrane design or random manufacturing variation.
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Different compositions for the membrane were tested.
Predicted distances from DI and DIII to the membrane were tested by FRET32 (Fig. 4e).
Both the neo-Hookean membrane and the Skalak membrane are tested.
In this work, a VRFB with a polybenzimidazole (PBI) membrane is tested and compared with the Nafion system.
Four polydimethyl siloxane (PDMS) membranes and one polyoctylmethyl siloxane (POMS) membrane were tested for pervaporation and their separation performances were compared.
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