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Hydrogen Production by Steam Reforming of Liquefied Natural Gas over Mesoporous Ni-Al<sub>2</sub>O<sub>3</sub> Catalysts Prepared by a Co-Precipitation Method: Effect of Ni/Al Atomic Ratio.
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- Catalysis Letters, 2009, v. 130, n. 3/4, p. 410, doi. 10.1007/s10562-009-0024-x
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Production of Middle Distillate from Synthesis Gas in a Dual-bed Reactor Through Hydrocracking of Wax Over Mesoporous Pd-Al<sub>2</sub>O<sub>3</sub> Composite Catalyst.
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- Catalysis Letters, 2009, v. 130, n. 1/2, p. 192, doi. 10.1007/s10562-009-9854-9
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Deactivation behaviors of hybrid Fischer-Tropsch catalysts in the production of middle distillate from synthesis gas in a dual-bed reactor.
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- Research on Chemical Intermediates, 2010, v. 36, n. 6/7, p. 685, doi. 10.1007/s11164-010-0170-1
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