Ibrahim Suhaina Mohd, Yu Xin, Miyata Shigeru, Mishina Kengo, Salak Feridoun, Lawal Sulaiman Oladipo, Tsuru Toshinori, Sawamura Ken-Ichi
eSep Inc., Keihanna Open Innovation Center@Kyoto (KICK), Annex 320, 7-5-1, Seikadai, Seika-cho, Soraku-gun, Kyoto 619-0238, Japan.
Department of Chemical Engineering, Hiroshima University, 1-4-1 Kagamiyama, Higashihiroshima 739-8527, Japan.
Membranes (Basel). 2024 Jul 25;14(8):165. doi: 10.3390/membranes14080165.
The separation ability of bis(triethoxysilyl)ethane (BTESE) membranes for hydrogen (H) purification from hydrogen (H)/toluene (TOL) gas mixtures after a methylcyclohexane (MCH) dehydrogenation process was investigated via one-stage and two-stage membrane processes. This study revealed that BTESE membranes of varied pore sizes (0.4, 0.5, and 0.7 nm) in a one-stage configuration can manage to achieve a H purity ~99.9%. However, the TOL concentrations fell within a wide range, ranging from 280 to 5441 ppm. A primary goal of this research was to lower the TOL concentration in the permeate stream below 200 ppm. Hence, by applying the two-stage membrane, it was demonstrated that the TOL concentration in the permeate stream could be lowered below 200 ppm.
通过单级和两级膜工艺,研究了双(三乙氧基硅基)乙烷(BTESE)膜在甲基环己烷(MCH)脱氢过程后从氢气(H)/甲苯(TOL)气体混合物中提纯氢气(H)的分离能力。该研究表明,在单级配置中,不同孔径(0.4、0.5和0.7纳米)的BTESE膜能够实现氢气纯度约99.9%。然而,甲苯浓度范围较宽,从280至5441 ppm不等。本研究的一个主要目标是将渗透气流中的甲苯浓度降低至200 ppm以下。因此,通过应用两级膜,结果表明渗透气流中的甲苯浓度可降低至200 ppm以下。