Gasification of humic acid in subcritical and supercritical water.
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Temperature, feed concentration, reaction time and catalyst affect H2 production.
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High H2 yield at 600 °C with 15 wt% humic acid, 15 wt% FeCl3 in 75 min at 24 MPa.
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H2 and total gas yields increased exponentially with rising FeCl3 concentration.
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FeCl3 promotes ring-opening reaction to accelerate humic acid degradation.
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