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Hydrogen production by supercritical water gasification (SCWG) of valine as a model for protein was examined in a fixed-bed reactor at 28 MPa. The effect of reaction temperature (500–710 °C), type of catalyst (AC, Ni–Y/AC, Ni–Pt/AC, and Ni–Pd/AC), and LHSV (24–72 h−1) on the extent of gasification and gas composition was investigated. Total gas yield increased with increasing temperature up to 710 °C...
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