首页> 外文会议>International Symposium on Supercritical Fluids Tome 1: Natural Products, Process amp; Equipment Development; 20030428-20030430; Versailles; FR >THERMODYNAMIC MODELLING OF THE ABSORPTION OF ACID GAS IN A MIXED SOLVENT BY ELECTROLYTE NRTL EQUATION: NEW EQUIPMENT AND MEASURING
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THERMODYNAMIC MODELLING OF THE ABSORPTION OF ACID GAS IN A MIXED SOLVENT BY ELECTROLYTE NRTL EQUATION: NEW EQUIPMENT AND MEASURING

机译:电解质NRTL方程在混合溶剂中吸收酸性气体的热力学模型:新设备和测量

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A new process of gas sweetening based on the absorption of acid gas (CO_2 & H_2S) by mixing chemical solvents (aqueous diethanolamine) and physical solvents (methanol) is being developed at IFP in partnership with TFE. No literature data in representative temperature range concerning the vapour-liquid equilibrium of these systems can be found. Therefore, we developed a new experimental apparatus to measure the vapour-liquid equilibrium of these systems for pressures up to 100 bar and temperatures up to 120℃. There is no much literature concerning the modelling of these kind of systems therefore this aspect is also treated.
机译:IFP与TFE合作开发了一种通过混合化学溶剂(二乙醇胺水溶液)和物理溶剂(甲醇)吸收酸性气体(CO_2和H_2S)进行气体脱硫的新工艺。在有关这些系统的气液平衡的代表性温度范围内,没有找到文献数据。因此,我们开发了一种新的实验设备来测量这些系统在压力高达100 bar和温度高达120℃时的气液平衡。关于这类系统建模的文献不多,因此也要考虑这一方面。

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