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- W339417298 abstract "Results of pilot plant operation to upgrade Canadian oil sand bitumen and heavy oil are presented. Because it is not feasible to measure liquid and vapor compositions in the reactor directly, recourse must be made to computational methods. These involve estimating the equilibrium vaporization constant, K, for various components of the system using known or estimated values of their thermodynamic properties. Vapor-liquid equilibrium data were obtained from measurements in a hot separator downstream of the pilot plant reactor. This well-mixed separator, which was temperature controlled, was assumed to behave as a single stage contactor, and measurements of liquid and vapor flows and concentrations were taken at steady state conditions. Comparison of calculated values of liquid vaporization using a computer simulation with experimental data indicated that such computational methods will give reasonably accurate values for the degree of vaporization, considering the approximation and experimental errors involved, for a very heavy oil such as tar sand bitumen and its hydrocracked products." @default.
- W339417298 created "2016-06-24" @default.
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- W339417298 date "1978-01-01" @default.
- W339417298 modified "2023-09-23" @default.
- W339417298 title "Thermal hydrocracking of Athabasca bitumen: comparison of computer-simulated feed and product vaporization values with pilot plant data" @default.
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