M. Abdolmajidi, Ali Hasani Jooshaghani, A. Cheraghi, A. Haghtalab
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引用次数: 0
摘要
例如,在气体净化框架中,烷醇胺捕获气态汽油中的二氧化碳和H2S是常规的。在这项研究中,我们首次使用了一个额外的Gibbs弹性模型(N_Wilson_NRF)来证明CO2在双组分CO2+MDEA和三组分MDEA+H2O+CO2框架中的可溶性。为了便于建模,探讨了不发生复合反应的全原子框架和CO2气体浸没气级的假设。采用作用系数策略(γ_φ法)和N-Wilson-NRF模型确定CO2的可溶性。双组分水- CO2模型的实验结果为1.38。对测度为6.912的水- co2 - mdea框架进行了改进。
Thermodynamic Modeling the Solubility of CO2 in the Binary and Three-Component Aqua System of Methyldiethanolamine (MDEA) Using the N-Wilson-NRF
Catching acidic gases, for example, CO2 and H2S from gaseous petrol by alkanolamines are regular in gas cleansing frameworks. In this study, for the first time we use an additional Gibbs argillic model (N_Wilson_NRF) for thermodynamic demonstration of CO2 dissolvability in the double part CO2+MDEA and three part MDEA+H2O+CO2 frameworks. The supposition an altogether atomic framework with no occurrence compound responses and immersed gas stage from the CO2 gas were explored for the point of having a convenient modelling. To decide the dissolvability of CO2 the action coefficient strategy (γ_φ Approach) and the N-Wilson-NRF model were utilized. The result was 1.38 from experimental emerge attain in the two-component water- CO2 modelling. For the three-parts, water-CO2-MDEA framework with the measure of 6.912, the improvement was created.
期刊介绍:
The aim of the Iranian Journal of Chemistry and Chemical Engineering is to foster the growth of educational, scientific and Industrial Research activities among chemists and chemical engineers and to provide a medium for mutual communication and relations between Iranian academia and the industry on the one hand, and the world the scientific community on the other.