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Data concerning adsorption equilibria of carbon dioxide nitrogen and oxygen over a zeolite molecular sieve 13X for the modelling of carbon dioxide capture from gaseous mixtures by adsorptive processes

机译:关于分子筛13X上二氧化碳氮和氧的吸附平衡的数据用于模拟通过吸附过程从气态混合物中捕获二氧化碳

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摘要

Experimental adsorption isotherms of carbon dioxide, nitrogen and oxygen at 293, 313 and 333 K over a zeolite molecular sieve 13X Grace are presented. The data were used in the simulations of the hybrid VSA-membrane process for carbon dioxide capture from flue gas as presented in a related article entitled “The performance of a hybrid VSA-membrane process for the capture of CO from flue gas” . A representative sample of ZSM 13X Grace (149.7 mg) was prepared using the Microscal Spinning Riffler. Adsorption equilibria were determined by a gravimetric method, which uses a microbalance IGA003, Hiden Isochema Ltd., UK at temperatures of 293, 313 and 333 K. Every adsorption isotherm was started at 0 bar. For CO the equilibrium concentration reaches 3.755-4.857 mol kg at the maximum pressure of 1 bar. In the case of N and O the equilibrium concentration reaches, respectively, 0.721-1.255 mol kg and 0.299-0.531 mol kg at the maximum pressure of 5 bar. Data may be reused in any adsorptive CO /N /O separation process which uses ZMS 13X as an adsorbent.
机译:给出了在13X Grace沸石分子筛上293、313和333 K的二氧化碳,氮气和氧气的实验吸附等温线。数据被用于模拟VSA膜工艺从烟气中捕获二氧化碳,如相关文章“混合VSA膜工艺从烟气中捕获CO的性能”中所述。使用Microscal Spinning Riffler制备ZSM 13X Grace的代表性样品(149.7 mg)。吸附平衡是通过重量分析法测定的,该方法使用的微量天平IGA003,Hiden Isochema Ltd.,UK,温度为293、313和333K。每个吸附等温线均始于0 bar。对于CO,在1 bar的最大压力下,平衡浓度达到3.755-4.857 mol kg。在N和O的情况下,最大压力为5 bar时,平衡浓度分别达到0.721-1.255 mol kg和0.299-0.531 mol kg。可以在任何使用ZMS 13X作为吸附剂的吸附性CO / N / O分离过程中重复使用数据。

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