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首页> 外文期刊>Adsorption >Pure and mixture adsorption equilibria of methane and nitrogen onto clinoptilolite: effects of Cs+ and Fe3+ exchanged cations on separation performance
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Pure and mixture adsorption equilibria of methane and nitrogen onto clinoptilolite: effects of Cs+ and Fe3+ exchanged cations on separation performance

机译:甲烷和氮的纯净和混合物吸附平衡到Clinoptilolite上:Cs +和Fe3 +交换阳离子对分离性能的影响

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摘要

Cation exchanged clinoptilolite has emerged as an adsorbent that may be used for the treatment of natural gas type mixtures containing excess amounts of nitrogen. In this study, natural clinoptilolite was modified through Fe3+ and Cs+ cation exchange. The resultant mineral phase and elemental composition were verified and the extra framework cation type, charge, and distribution is shown to have a profound effect on the observed adsorptive properties. Single gas adsorption isotherms were conducted at 15 degrees C and/or 30 degrees C for CH4 and N-2 using a microgravimetric adsorption analyser, and the ideal equimolar CH4/N-2 selectivity values were determined for the natural and modified clinoptilolites. Natural clinoptilolite presents selectivity values close to 1. However, we demonstrate that clinoptilolite cation-exchanged with Cs+ and Fe3+ cations is rendered preferentially adsorptive for CH4 over N-2 with a higher CH4/N-2 selectivity than many adsorbents reported in the literature. The experimental CH4-N-2 binary adsorption behavior was evaluated for the first time on raw clinoptilolite and was compared to the modified clinoptilolites with Cs+ and Fe3+ exchanged cations using the concentration pulse chromatographic technique. The experimental binary isotherms showed non-ideal behavior with competitive adsorption between CH4 and N-2. In most cases, the theoretical models could not adequately describe the experimental adsorption behavior. Within the temperature range studied of 15 degrees C and 30 degrees C, the binary CH4/N-2 separation factors range from 2.7 to 5.3, and 3.9 to 7.3 for Cs+ and Fe3+ exchanged clinoptilolite, respectively. These results are comparable or better than those found in literature for activated carbon which typically ranges from 2.1 to 5.5 and may serve as an alternative adsorbent for this type of separation which warrants further investigation.
机译:阳离子交换的Clinopholegolite作为吸附剂,可用于处理含有过量氮的天然气型混合物。在该研究中,通过Fe3 +和Cs +阳离子交换改性天然的Clinophitolite。已验证所得矿物相和元素组合物,并显示额外的框架阳离子型,电荷和分布对观察到的吸附性质具有深远的影响。使用微血管吸附分析仪以15摄氏度和/或30摄氏度进行单液吸附等温线,并测定理想的等摩尔CH4 / N-2选择性值,用于天然和改性的临床。天然的Clinopholegite呈现接近的选择性值。然而,我们证明与CS +和Fe3 +阳离子交换的Clinopholegolite优先对N-2的CH 4优先吸附,具有比文献中所报道的许多吸附剂更高的CH 4 / N-2选择性。在原始的Clinophoptogolite上首次评价实验性CH 4-N-2二元吸附行为,并使用浓度脉冲色谱技术与CS +和Fe3 +交换阳离子的改性临床凝固晶体进行比较。实验二进制等温物显示出在CH4和N-2之间具有竞争性吸附的非理想行为。在大多数情况下,理论模型无法充分描述实验吸附行为。在研究15℃和30摄氏度的温度范围内,二进制CH4 / N-2分离因子的分离因子分别为2.7〜5.3和3.9至7.3,分别用于CS +和Fe3 +交换的Clinophopholite。这些结果比活化碳的文献中的那些相当或更好,其通常为2.1-5.5,可用作这种分离的替代吸附剂,这是认证进一步调查的。

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