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CO2 and CH4 permeation through T-type zeolite membranes:Effect of synthesis parameters and feed pressure

机译:T型沸石膜上的CO2和CH4渗透:合成参数和进料压力的影响

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In this paper,effects of synthesis parameters(synthesis temperature and time)and feed pressure on CO2 and CH4 gas permeances through zeolite T membranes were investigated.Experiments were carried out at three levels of synthesis temperature:100,120 and 140°C;synthesis time:15,30 and 50 h and two levels of feed pressure:1 and 5 bar.The gas permeances versus synthesis temperature first decreased with increasing synthesis temperature from 100 up to 120°C,then increased with further increasing the values of synthesis temperature.The same plots were acquired for gas permeances versus synthesis time.In the case of CO2/CH4 ideal selectivity,reverse trends were observed.This behavior was attributed to the dual effect of increasing synthesis temperature and time on gas permeance and ideal selectivity.More zeolites were deposited and larger crystals were formed at higher synthesis temperatures and times.Formation of larger crystals accelerated the rate of zeolite layer integration,which was responsible for gas separation,in one hand and reduced the density of deposited zeolite layer on the support,due to void increase,on the other hand.Gas permeances through the membranes were in the range of 10~(-11)to 10~(-6)(mol/m2 s Pa).In terms of maximizing the CO2/CH4 ideal selectivity,medium synthesis temperature and time(120°C and 30 h)and low feed pressure(1 bar)were selected.Maximum gas permeances were obtained at low levels of synthesis temperature and time(100°C,15 h)and high feed pressure(5 bar).Zeolite T membranes were found as good choices for the separation of CO2 from CH4.
机译:本文研究了合成参数(合成温度和时间)和进料压力对通过T型沸石膜渗透CO2和CH4气体的影响。在100、120和140°C的三种合成温度下进行了实验:合成时间: 15、30和50 h以及两个进料压力水平:1和5 bar。随着合成温度从100升高到120°C,气体渗透率与合成温度的关系首先下降,然后随着合成温度的值进一步上升。在CO2 / CH4理想选择性的情况下,观察到了相反的趋势,这种行为归因于合成温度和时间的增加对气体渗透率和理想选择性的双重影响。在较高的合成温度和时间下沉积并形成较大的晶体。较大的晶体形成加快了沸石层的整合速度,这是可以解决的。一方面不能进行气体分离,另一方面由于孔隙增加而降低了在载体上沉积的沸石层的密度。通过膜的气体渗透率在10〜(-11)到10〜( -6)(mol / m2 s Pa)。为了最大程度地提高CO2 / CH4的理想选择性,选择了中等合成温度和时间(120°C和30 h)和低进料压力(1 bar)。在低合成温度和时间(100°C,15 h)和高进料压力(5 bar)的条件下获得了沸石.T型沸石膜是从CH4分离CO2的良好选择。

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