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Supercritical hydrogenation processes: Experimental results on the fluid phase behavior of binary and ternary mixtures of hydrogen,propane and tripalmitin
Affiliation:1. Departamento de Ingeniería Química, División de Ciencias Naturales y Exactas, Campus Guanajuato, Universidad de Guanajuato, Noria Alta S/N, Guanajuato, Gto. 36050, México.;2. Facultad de Química, Universidad Autónoma de Querétaro, Centro Universitario, Av. Cerro de las Campanas s/n Col. Las Campanas, Santiago de Querétaro, Qro. 76010, México.;1. School of Chemical & Environmental Engineering, China University of Mining and Technology (Beijing), Beijing 100083, China;2. Department of Chemical & Petroleum Engineering, University of Wyoming, Laramie, WY 82071, USA;3. School of Energy Resources, University of Wyoming, Laramie, WY 82071, USA
Abstract:The problems of low reaction rate and cistrans isomerization encountered in the gas–liquid catalyzed hydrogenation of vegetable oils can be overcome by using a supercritical fluid to bring the reactive mixture into a homogeneous phase. For that purpose, experimental phase equilibrium data on mixtures of high molecular weight substrates with hydrogen and a supercritical fluid are needed in order to evaluate optimum process conditions. In this work vapor–liquid and liquid–liquid equilibria in mixtures of hydrogen+propane+tripalmitin have been measured. A temperature region between 323 and 453 K, and pressures up to 15 MPa were covered.
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