丙烷
沸石
模拟移动床
乙烯
吸附
烯烃纤维
空气分离
变压吸附
巴(单位)
化学工程
材料科学
色谱法
化学
分析化学(期刊)
有机化学
催化作用
氧气
气象学
工程类
物理
作者
Rute Seabra,Vanessa F. D. Martins,Ana M. Ribeiro,Alı́rio E. Rodrigues,Alexandre Ferreira
标识
DOI:10.1016/j.ces.2020.116006
摘要
In this work, binderfree zeolite 13X monoliths were tested as a new promising material for high purity ethylene production from olefin/paraffin mixtures by gas-SMB technology. To characterize the adsorbent and its potential for the target separation, the equilibrium isotherms of ethane, ethylene, and propane were measured gravimetrically, in a temperature range from 323 K to 423 K, and pressure up to 7 bar. Dynamic studies were performed at 373 K and 1.5 bar in the gas-SMB bench-scale unit. For the experiment with 0.48/0.52 ethane/ethylene (molar based) feed composition, an ethylene purity of 97.7% was obtained, with a recovery above 90% and productivity of 16.9 kgC2H4∙h-1∙mbed-3. Furthermore, the mathematical SMB model and the regions of separation were determined based on experimental data. This work experimentally demonstrated it is possible to produce high purity grade ethylene with a high recovery using binderfree zeolite 13X monoliths as adsorbent and propane as desorbent.
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