Catalytic supercritical water gasification of primary paper sludge using a homogeneous and heterogeneous catalyst: Experimental vs thermodynamic equilibrium results
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文摘

Primary paper waste sludge (PWS) was gasified in supercritical water at 450 °C.

Addition of K2CO3 catalysed the water-gas shift reaction to yield 7.5 mol/kgPWS H2.

90% conversion of carbon to the gas phase achieved with Ni–Al2O3/SiO2 catalyst.

83% energy recovery achieved with Ni–Al2O3/SiO2 catalyst.

Gas product with HHV of 13.3 MJ/kgPWS achieved with Ni–Al2O3/SiO2 catalyst.

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