A comparison of Al2O3 and SiO2 supported Ni-based catalysts in their performance for the dry reforming of methane

Rh promoted and ZrO2/Al2O3 supported Ni/Co based catalysts: High activity for CO2 reforming, steam–CO2 reforming and oxy–CO2 reforming of CH4

Steam reforming of acetic acid over cobalt catalysts: Effects of Zr, Mg and K addition

Methane dry reforming over activated carbon supported Ni-catalysts prepared by solid phase synthesis

CO2 reforming of CH4: Effect of Gd as promoter for Ni supported over MCM-41 as catalyst

Preparation of porous Al2O3 by template method and its application in Ni-based catalyst for CH4/CO2 reforming to produce syngas

In a toluene-water mixture, toluene disproportionation can occur under very gentle conditions if enhanced by a hydraulic cavitation field. Using a single factor approach, the effects of toluene concentration, ethanol and H2O2 addition, final reaction temperature, and pH on toluene conversion and yields of products in the organic phase were investigated. The optimal reaction conditions for p-xylene (PX), an objective product, were 12.5% (v/v) concentration of toluene and ethanol, final reaction temperature of 50 °C, pH of 9, and a H2O2 addition of 2.5% (v/v). Under such conditions, the toluene conversion reached 19.66%, and yields of benzene, alkyl cycloalkanes, and alkyl aromatic hydrocarbons were 2.70%, 2.64%, and 14.32%, respectively. Particularly, yields of PX, o-xylene (OX), and ethylbenzene were 8.56%, 4.06%, and 1.70%, respectively. A reaction mechanism was proposed and validated via both UV spectroscopy of the aqueous-phase products and material balance for the process.

Hydrodynamic cavitation for the enhancement of toluene disproportionation; study of the products distribution

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Preparation of porous Al2O3 by template method and its application in Ni-based catalyst for CH4/CO2 reforming to produce syngas

Hydrodynamic cavitation for the enhancement of toluene disproportionation; study of the products distribution