A phase model for the gas–liquid equilibria in the ammonia–carbon dioxide–water–urea system in chemical equilibrium at urea synthesis conditions. II. Experimental verification

S. Lemkowitz, Eric Vet, P. Berg
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引用次数: 4

Abstract

Bubble- and critical-points in the ammonia–carbon dioxide plane and ammonia–urea system are presented as well as bubble-points in the carbon dioxide–urea system. In order to confirm the form of a previously presented phase model a large number of bubble- and dew-points were measured at various ammonia–carbon dioxide–water–urea compositions (including those most important to the urea industry) in the range of 140 ⩽ T ⩽ 200°C and 15 < P < 400 atm. All of the measurements were carried out under conditions of complete chemical equilibrium. The results are in agreement with the ternary phase model presented in a previous article.
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尿素合成条件下氨-二氧化碳-水-尿素化学平衡气液平衡的相模型。2实验验证
给出了氨-二氧化碳平面和氨-尿素系统的气泡点和临界点,以及二氧化碳-尿素系统的气泡点。为了确认先前提出的相模型的形式,在140°C≤T≤200°C和15 < P < 400 atm范围内,测量了大量的氨-二氧化碳-水-尿素组成(包括对尿素工业最重要的组成)的气泡点和露点。所有的测量都是在完全化学平衡的条件下进行的。结果与前一篇文章中提出的三元相模型一致。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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