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- W2022192190 abstract "ABSTRACT This paper describes TRITRICOMP [1], a three dimensional, three phase numerical model for simulating petroleum reservoirs where interphase mass transfers are significant. The model utilizes equations of standard volume conservation for water, oil, and gas, and mass conservation for vapor-liquid hydrocarbon. For reservoir oil systems at pressure below the bubble-pointpressure, PVT data are supposed to be functions of pressure, standard gas density, and a compositional parameter to reflect fluid composition changes resulting from contact between oil, liberated gas, gas-cap, and dry injection gas, in varying proportions. By tracking this time dependent parameter over the reservoir, fluid properties variations due to compositional variations are computed in the model with the aid of correlations obtained either from laboratory experiments, or from a fully compositional model with few cells, specifically designed for this purpose [2]. Special provisions are made to treat gas condensate systems below their dewpoint and reservoir oil systems above their bubble-point pressure (which is supposed to be time and space variable over the reservoir, and computed by the model). Comparative runs of a 2D reservoir, made with this new model, are checked against those made with a fully compositional model [3] on the one hand, and those made with a conventional black oil model [4] on the other hand. It is showed that both the new and fully compositional models provide similar results which are however different from those obtained with conventional black oil models. Moreover, this new TRITRICOMP simulator runs as fast as a conventional black oil model i.e. several times faster than a fully compositional model. INTRODUCTION Conventional three phase numerical models, as the TRITRI model [4], have been used for many years to simulate reservoir behaviour and appraise oil recovery performance. These so called black oil models are based on the assumption that reservoir oil is a solution of two components: stock-tank oil and gas at standard conditions. At a given reservoir temperature, the volume of gas dissolved in oil increases with pressure, according to a dissolved gas oil ratio curve, up to the bubble-point pressure. Reservoir oil properties are only temperature, pressure, and bubble-point pressure dependent. Reservoir gas is supposed to contain no stock-tank oil, and so is the same as the gas dissolved in reservoir oil." @default.
- W2022192190 created "2016-06-24" @default.
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- W2022192190 date "1980-10-21" @default.
- W2022192190 modified "2023-09-23" @default.
- W2022192190 title "Use of a Three-Dimensional Three-Phase Pseudo Compositional Model (TRITRICOMP) for Simulating Volatile Oil and Gas Condensate Reservoirs" @default.
- W2022192190 doi "https://doi.org/10.2118/182-1980-ms" @default.
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