scholarly journals Preparation, Characterization and Catalytic Performance of Supported Titanium Silicalite-1 Zeolite Membrane Catalyst

2017 ◽  
Vol 32 (6) ◽  
pp. 631 ◽  
Author(s):  
GUO Yu ◽  
LI Dong-Xin ◽  
WU Hong-Mei ◽  
JIN Yu-Jia ◽  
ZHOU Li-Dai ◽  
...  
2018 ◽  
Vol 39 (2) ◽  
pp. 275-282 ◽  
Author(s):  
Li Chen ◽  
Teng Xue ◽  
Jian Ding ◽  
Hai Hong Wu ◽  
Kun Zhang ◽  
...  

2019 ◽  
Vol 209 ◽  
pp. 734-740 ◽  
Author(s):  
Jian Liu ◽  
Quan Yin ◽  
Huiping Zhang ◽  
Ying Yan ◽  
Zhengji Yi

Membranes ◽  
2020 ◽  
Vol 10 (3) ◽  
pp. 41
Author(s):  
Wenjuan Ding ◽  
Sitong Xiang ◽  
Fei Ye ◽  
Tian Gui ◽  
Yuqin Li ◽  
...  

Dense and good catalytic performance TS-1 zeolite membranes were rapidly prepared on porous mullite support by secondary hydrothermal synthesis. The properties of seed crystals were very important for the preparation of high-catalytic performance TS-1 zeolite membranes. Influences of seed crystals (Ti/Si ratios, size, morphology, and zeolites concentration of the seed suspension) on the growth and catalytic property of TS-1 zeolite membranes were investigated in details. High Ti/Si ratio, medium-size, and morphology of the seed crystals were critical for preparing the high-performance TS-1 zeolite membrane. Compared with the bi-layer TS-1 zeolite membrane (inner and outer of the mullite tube), the mono-layer TS-1 zeolite membrane had a better catalytic performance for Isopropanol IPA oxidation with H2O2. When the Ti/Si ratio, size, and morphology of the TS-1 zeolites were 0.030, 300 nm, ellipsoid, and the zeolites concentration of the seed suspension was 5%, the IPA conversion, and flux through the TS-1 zeolite membrane were 98.23% and 2.58 kg·m−2·h−1, respectively.


2019 ◽  
Vol 4 (5) ◽  
pp. 1618-1626
Author(s):  
Zongzhuang Han ◽  
Yun Shen ◽  
Xiaofei Qin ◽  
Fumin Wang ◽  
Xubin Zhang ◽  
...  

ACS Catalysis ◽  
2018 ◽  
Vol 8 (11) ◽  
pp. 10649-10657 ◽  
Author(s):  
Xiang Feng ◽  
Zhaoning Song ◽  
Yibin Liu ◽  
Xiaobo Chen ◽  
Xin Jin ◽  
...  

2018 ◽  
Vol 5 (8) ◽  
pp. 180587 ◽  
Author(s):  
Xiaotong Zhang ◽  
Ying Yan

Catalytic combustion of isopropanol in the structured fixed-bed reactor was investigated over Co–ZSM-5 zeolite membrane catalysts. Firstly, ZSM-5 zeolite membrane catalysts with different Si/Al ratios were coated onto the surface of stainless steel fibres via secondary growth method and wet lay-up paper-making method. Then, cobalt oxides were loaded onto the zeolite membranes by impregnation method. The performance of catalytic combustion of isopropanol was conducted over the prepared zeolite membrane catalysts, and the experimental results showed that the catalyst with infinite Si/Al ratio has the highest catalytic activity for the combustion with the lowest T 90 of isopropanol (285°C). Finally, the effects of bed structure, feed concentration, gas hourly space velocity and reaction temperature on the catalytic performance were investigated to analyse the kinetics of isopropanol over the catalyst with infinite Si/Al ratio in the structured fixed-bed reactor. The results showed that the longer residence time could cause higher reaction contact efficiency of isopropanol combustion. T 90 of isopropanol can be dramatically decreased by 105°C in the fixed-bed reactor packed with Co–ZSM-5 zeolite membrane catalysts, compared to the fixed-bed reactor packed with granular catalyst.


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