Steam Reforming of Chloroform-Ethyl Acetate Mixture to Syngas over Ni-Cu Based Catalysts

Abstract

NiCuMoLaAl mixed oxide catalysts are prepared and applied in the steam reforming of chloroform-ethyl acetate (CHCl3-EA) mixture to syngas in the present work. The pre-introduction of Cl- ions using chloride salts as modifiers aims to improve the chlorine poisoning resistance. Catalytic tests show that KCl modification is obviously advantageous to increase the catalytic life. The destruction of catalyst structure induced by in situ produced HCl and carbon deposits that occurred on acidic sites are two key points for deactivation of reforming catalysts. The presence of Cl− ions gives rise to the formation of an Ni-Cu alloy, which exhibits a synergetic effect on catalyzing reforming along with metallic Ni crystals formed from excess nickel species, and giving an excellent catalytic stability. Less CHCl3 and more steam can also increase the catalytic stable time of KCl-modified NiCuMoLaAl reforming catalyst.

Salt-Supported Nickel Oxides for Boosted Hydrogen Production: The Critical Role of Halogen

“…The conversion rates of C 4 H 8 O 2 over these three catalysts were all above 90% at 500–700 °C (Figure e). Compared with the reported Ni-based catalysts, NiO/NaX catalysts possessed a relatively excellent low-temperature hydrogen production performance for C 4 H 8 O 2 reforming, − as shown in Figure f and Table S1. As seen in Figure d, the S H 2 of all three optimal catalysts rose with the increasing of the reaction temperature in the range of 500–650 °C.…”