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Simulation Experiments on Thermochemical Origin of High H_2S in Natural Gas

机译:天然气中高H_2S热化学成因的模拟实验

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摘要

Thermal simulation experiments on thermochemical sulfate reduction system of natural gas and magnesium sulphate were carried out using an autoclave in the presence of water. The products were characterized by some advanced analytical methods. Thermodynamics and reaction kinetics of thermochemical sulfate reduction processes had been investigated on the basis of the experimental data. The results showed that thermochemical sulfate reduction of natural gas with magnesium sulphate could proceed at 425℃-525℃ to produce magnesium oxide, carbon, hydrogen sulfide, and carbon dioxide as the main products. The reactions are thermochemically possible and high temperature is favored. Long-chain hydrocarbons more easily ther-modynamically participate in the reactions than short-chain hydrocarbons. According to the reaction model, the calculated activation energy for the reaction between natural gas and magnesium sulfate is about 78.975 kJ/mol.
机译:使用高压釜在水存在下,对天然气和硫酸镁的热化学硫酸盐还原系统进行了热模拟实验。产品通过一些先进的分析方法进行了表征。根据实验数据研究了热化学硫酸盐还原过程的热力学和反应动力学。结果表明,用硫酸镁对天然气进行热化学硫酸盐还原可在425℃-525℃下进行,以氧化镁,碳,硫化氢和二氧化碳为主要产物。该反应是热化学上可能的,并且高温是有利的。与短链烃相比,长链烃更容易在热力学上参与反应。根据反应模型,天然气和硫酸镁之间反应的活化能约为78.975 kJ / mol。

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