Influence of AlCl3 and oxidant catalysts on hydrogen production from the supercritical water gasification of dewatered sewage sludge and model compounds

Hydrogen has attracted significant attention as a clean energy source. Supercritical water gasification (SCWG) technology can produce hydrogen-rich gas while also disposing of sludge. The hydrogen yield from the SCWG of sludge is greatly increased when catalyzed by AlCl 3 . In this paper, a combined catalyst based on AlCl 3 was proposed to further increase the hydrogen yield of SCWG of dewatered sewage sludge (DSS). Analysis of the products from catalytic gasified of DSS and its model compounds were used to propose a catalytic mechanism and reaction pathway of the catalytic SCWG of DSS. Among the combined catalysts used for the SCWG of DSS, 10 wt% AlCl 3 –H 2 O 2 (mass ratio 8:2) had the best hydrogen production effect, and the hydrogen yield reached 8.88 mol/kg organic matter. This was 14% higher than when catalyzed by 10 wt% AlCl 3 . During catalysis with AlCl 3 , Al 3+ reacted with OH − in water and precipitated as Al(OH) 3 , which produced an acidic environment in the liquid product. Al(OH) 3 dehydrated to form an AlO(OH) and deposited in the solid product. A small amount of H 2 O 2 promoted the steam reforming reaction of organic matter in DSS, which increased the hydrogen yield. H 2 O 2 further promoted the hydrogen yield in an acidic environment. The catalytic effect of AlCl 3 was unaffected by H 2 O 2 . The H + generated by AlCl 3 during catalysis promoted H 2 O 2 to further depolymerized organic matter (such as humic substances) in DSS, so that AlCl 3 –H 2 O 2 catalyzed the SCWG of DSS to further increase the hydrogen yield. The order of hydrogen yield catalyzed by AlCl 3 –H 2 O 2 was guaiacol  > humic acid > glycerol >  alanine  > glucose. Compared with AlCl 3 , AlCl 3 –H 2 O 2 reduced the hydrogen yield of glucose by nearly 20% and increased the hydrogen yield of humic acid by about 17% (25.81 mol/kg feed).