Underlying core-shell colloidal nanostructure for Beta zeolite membrane formation

Author(s):  
Puyam S. Singh ◽  
Vinod K. Aswal ◽  
Wilhelm Schwieger
2011 ◽  
Vol 166 (1) ◽  
pp. 205-208 ◽  
Author(s):  
M. Torres ◽  
M. Gutiérrez ◽  
V. Mugica ◽  
M. Romero ◽  
L. López

2020 ◽  
Vol 45 (33) ◽  
pp. 16409-16420 ◽  
Author(s):  
Shiyao Wang ◽  
Bo He ◽  
Ren Tian ◽  
Xu Wu ◽  
Xia An ◽  
...  

2007 ◽  
Vol 21 (10) ◽  
pp. 841-848 ◽  
Author(s):  
N. Kuanchertchoo ◽  
R. Suwanpreedee ◽  
S. Kulprathipanja ◽  
P. Aungkavattana ◽  
D. Atong ◽  
...  

2014 ◽  
Vol 86 (5) ◽  
pp. 775-783 ◽  
Author(s):  
Yanping Chen ◽  
Yiming Xu ◽  
Dang-guo Cheng ◽  
Yingcai Chen ◽  
Fengqiu Chen ◽  
...  

AbstractThe present study focuses on synthesis of SAPO-34 zeolite membrane on the surface of CuO–ZnO–Al2O3 (CZA) catalyst particles to form CZA@SAPO-34 core@shell structured catalyst. In contrast to the traditional support of porous alumina, CZA catalyst particles have a relatively brittle surface, which leads to a big challenge to coat SAPO-34 zeolite membrane on their surface. Moreover, the hydrothermal synthesis of SAPO-34 zeolite membrane is carried out under weakly alkaline condition at 200 °C for hours, which causes part of the surface of CZA to be fragmented. To overcome these shortcomings, the intermediate layer of alumina is introduced to the surface of the CZA particles and acts as a barrier to the high-temperature hydrothermal and alkaline condition. It also takes as a transition to enhance SAPO-34 zeolite seeds adherence to the surface of CZA particles. With the help of an alumina layer, a continuous and dense zeolite membrane has been obtained on the surface of CZA particles. The prepared core@shell structured catalyst has better selectivity in CO hydrogenation for producing light hydrocarbons because of the synergetic effects between the membrane and core catalyst.


2014 ◽  
Vol 50 (64) ◽  
pp. 8834-8837 ◽  
Author(s):  
Yanting Tang ◽  
Xiufeng Liu ◽  
Shifeng Nai ◽  
Baoquan Zhang

The preferentially (h0l)-oriented beta zeolite membrane was prepared on the porous α-Al2O3 support by secondary growth of a beta seed layer in the absence of organic templates.


2000 ◽  
Vol 164 (1-2) ◽  
pp. 257-275 ◽  
Author(s):  
Joseph Lik Hang Chau ◽  
Carlos Tellez ◽  
King Lun Yeung ◽  
Kachun Ho

2012 ◽  
Vol 608-609 ◽  
pp. 1463-1466 ◽  
Author(s):  
Guo Lin Shao ◽  
Chun Ling Yu ◽  
Ying Huan Fu ◽  
Hong Yi Dai ◽  
Li Ping Zhang

Beta zeolite membrane was prepared on the surface of α-Al2O3support tube with large pore by the way of secondary growth. Different seeding techniques, such as ultrasonic surge, self-assembling and dip-coating, were investigated, and the results indicated that the best one was dip-coating method for the support with large pore. The prepared membrane was characterized by SEM and XRD. It was proved that the beta zeolite membrane prepared by the way of secondary growth is continuous, dense and defect-free.


2022 ◽  
Vol 8 (1) ◽  
pp. 10-16
Author(s):  
R. Brovko ◽  
L. Mushinskii ◽  
V. Doluda

The continuous depletion of hydrocarbon sources contributes to a wide study of the use of biorenewable raw materials to obtain synthetic hydrocarbons from them. Isopropyl alcohol is traditionally produced by chemical hydration of propylene, however, with the development of biotechnology, broad prospects have opened for its production by fermentation of glucose-containing substrates obtained from agricultural and forestry waste. This way, isopropyl alcohol can also be considered as a bio-renewable raw material and it can be widely used for the production of chemical synthesis products, including hydrocarbons. One of the possible ways of processing isopropyl alcohol is the catalytic transformation of alcohols on zeolites and zeotypes of various natures with the formation of hydrocarbons. Currently, zeolite H-ZSM-5 and zeotype SAPO-34 are the most frequently used catalysts for the transformation of alcohols into hydrocarbons, however, their rapid deactivation due to the formation of a carbon residue remains an unresolved problem. The formation of core-shell structures with H-ZSM-5 zeolite in center and an outer shell consist of H-Beta zeolite with large pores can reduce the deactivation of zeolite because of increase in reagents diffusion rate. In this article is devoted to synthesis of ZSM-5/Beta sample with a core-shell structure, as well as a study of its catalytic and physicochemical properties. To form the H-ZSM-5 zeolite, a colloidal solution of tetrapropylammonium hydroxide, a colloidal solution of silicon oxide, aluminum oxide, sodium hydroxide of distilled water was used. The colloidal solution was placed in an autoclave, heated to 140 °C and kept at this temperature for 48 hours, after which the crystals formed were centrifuged, washed with distilled water and kept in a 1M solution of ammonium nitrate for a day. Then, to form the H-Beta layer, H-ZSM-5 was suspended in a colloidal solution consisting of tetraethylammonium hydroxide, tetraethylammonium chloride, a colloidal solution of silicon oxide, sodium hydroxide, sodium chloride and distilled water. The suspension was placed in an autoclave and kept at a temperature of 140 °C for 48 hours, followed by centrifugation, washing in distilled water, suspended in a 1M solution of ammonium nitrate, with repeated washing with distilled water, drying and calcining at 600 °C. Testing of the synthesized of H-ZSM-5/Beta zeolite sample showed a significant decrease in the rate of deactivation compared to the synthesized sample of H-ZSM-5; it is also necessary to note a slight increase in the fraction of liquid hydrocarbons for the sample H-ZSM-5/Beta.


2021 ◽  
pp. 119452
Author(s):  
Yanwei Yang ◽  
Nanke Ma ◽  
Xiaoke Wu ◽  
Xiaofei Lu ◽  
Zhengchi Yin ◽  
...  

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