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首页> 外文期刊>Fluid Phase Equilibria >A robust multiphase isenthalpic flash model for water/solvent/hydrocarbon systems at high pressures and elevated temperatures
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A robust multiphase isenthalpic flash model for water/solvent/hydrocarbon systems at high pressures and elevated temperatures

机译:用于水/溶剂/碳氢化合物系统的鲁棒多相型闪光模型,高压和升高的温度

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摘要

Based on the assumption that only the presence of water and solvent is considered in the aqueous phase, a robust and pragmatic water-associated isenthalpic flash (WAIF) model has been developed to perform multiphase isenthalpic flash calculations for water/solvent/hydrocarbon mixtures at high pressures and elevated temperatures. More specifically, the phase boundary diagram in enthalpy-temperature (H-T) space is constructed first for a given water/solvent/hydrocarbon system at a specified pressure. Then, the phase transition enthalpies and temperatures are determined from the H-T diagram, and thus one-, two-, or three-phase isenthalpic flash calculations can be conducted directly without resorting to stability test for a given system at a specified enthalpy and pressure. In addition, a recursive method has been proposed to initialize the temperature so that the energy conservation equation and material balance equation can be solved simultaneously to overcome the convergence difficulties. The newly proposed isenthalpic flash model has been compared with the water-free isenthalpic flash (WFIF) model and conventional three-phase isenthalpic flash (CTIF) model through three case studies. The WAIF model is found to handle the narrow-boiling constraints effectively and accurately. Furthermore, as for Water/C3H8/C16H34 mixture and Water/CO2/C16H34 mixture, a good agreement is achieved between the WFIF model and the WAIF model as the solubility of solvents (i.e., C3H8 and CO2) in the aqueous phase is quite small. With respect to Water/dimethyl ether (DME)/C16H34 mixture, however, the WAIF model is found to more accurately predict the phase behaviour of water/solvent/hydrocarbon mixtures than the WFIF model since the solubility of DME in the aqueous phase cannot be neglected. The case studies demonstrate that the newly developed water-associated isenthalpic flash model for water/solvent/hydrocarbon systems is robust efficient, and accurate. (C) 2019 Elsevier B.V. All rights
机译:基于仅在水相中考虑水和溶剂的存在,已经开发出稳健和务实的水相关的型闪光(WAIF)模型,以对高处进行水/溶剂/烃混合物进行多相型闪光灯计算压力和升高的温度。更具体地,焓 - 温度(H-T)空间中的相位边界图首先在特定的压力下为给定的水/溶剂/烃系统构成。然后,从H-T图确定相转变焓和温度,因此可以直接进行一次,两个或三相等焓闪光计算,而不诉诸于指定的焓和压力的给定系统的稳定性测试。另外,已经提出了一种递归方法来初始化温度,从而可以同时解决节能方程和材料平衡方程以克服收敛困难。通过三种案例研究将新提出的Isenthalpic Flash模型与无水型闪光灯(WFIF)模型和常规的三相型号闪光(CTIF)模型进行了比较。发现WAIF模型有效准确地处理窄沸点约束。此外,对于水/ C3H8 / C16H34混合物和水/ CO2 / C16H34混合物,在WFIF模型和WAIF模型之间实现了良好的一致性,因为溶剂(即,C3H8和CO2)在水相中的溶解度非常小。然而,对于水/二甲醚(DME)/ C 16H34混合物,发现沃夫米模型更精确地预测水/溶剂/烃混合物的相行为,因为DME在水相中的溶解度不能是被忽视了。案例研究表明,新开发的水/溶剂/烃系统的水相关的型闪光模型是稳健的,高效,准确。 (c)2019 Elsevier B.V.所有权利

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