Influence of the synthesis conditions and growth environment on MFI zeolite film orientation

2002 ◽  
Vol 54 (1-2) ◽  
pp. 63-77 ◽  
Author(s):  
Sau Man Lai ◽  
Louisa Tak Yin Au ◽  
King Lun Yeung
2007 ◽  
Vol 19 (17) ◽  
pp. 4120-4122 ◽  
Author(s):  
Watcharop Chaikittisilp ◽  
Mark E. Davis ◽  
Tatsuya Okubo

2015 ◽  
Vol 217 ◽  
pp. 71-80 ◽  
Author(s):  
Lin-Yi Huang ◽  
Yuan-Chung Hao ◽  
WenChyuan ChangJean ◽  
Mei-Jhu Wang ◽  
Anthony S.T. Chiang ◽  
...  

Materials ◽  
2020 ◽  
Vol 13 (20) ◽  
pp. 4595
Author(s):  
Shang-Tien Tsai ◽  
Wen-Chyuan ChangJean ◽  
Lin-Yi Huang ◽  
Tseng-Chang Tsai

MFI zeolite film coated on AA6061 alloy was prepared from fumed silica modified with/without n-octyldecyltrimethoxysilane (ODS) by means of dry gel conversion (DGC) method. The DGC-grown MFI zeolite film could form a strong barrier to protect AA6061 surface against the corrosion from NaCl solution. By using fumed silica as a starting material, the hydrophilicity and anti-corrosion capability of the MFI zeolite film declined with increasing humidity in the DGC synthesis. By silanization with ODS, the surface hydrophobicity of the MFI zeolite film increased, leading to substantial enhancement in anti-corrosion capability. On the other hand, MFI film grown from ODS-modified fumed silica exhibited low hydrophilicity and a much improved anti-corrosion protection property by four orders of magnitude, even stronger than the ODS post-treated MFI film. The strong anti-corrosion capability is attributed to the “thick layer” surface hydrophobicity of zeolite crystal.


2018 ◽  
Vol 53 (sup1) ◽  
pp. 34-38 ◽  
Author(s):  
Shang-Tien Tsai ◽  
Wen-Chyuan ChangJean ◽  
Pei-Hsiun Chao ◽  
Shang-Yuan Fu ◽  
Tseng-Chang Tsai

CrystEngComm ◽  
2018 ◽  
Vol 20 (32) ◽  
pp. 4531-4535 ◽  
Author(s):  
Yong Peng ◽  
Ruilan Xu ◽  
Xinde Jiang ◽  
Sheng Xu ◽  
Zhengbao Wang

The formation of a close-packed oriented MFI zeolite film through thermal processing created a strong covalent linkage between the seed layer and the substrate.


2011 ◽  
Vol 32 (1-2) ◽  
pp. 217-223 ◽  
Author(s):  
Xianming LI ◽  
Zhengbao WANG ◽  
Jie ZHENG ◽  
Shiqun SHAO ◽  
Yinchao WANG ◽  
...  

2020 ◽  
pp. 1-18
Author(s):  
Yu.V. Bilokopytov ◽  
◽  
S.L. Melnykova ◽  
N.Yu. Khimach ◽  
◽  
...  

CO2 is a harmful greenhouse gas, a product of chemical emissions, the combustion of fossil fuels and car exhausts, and it is a widely available source of carbon. The review considers various ways of hydrogenation of carbon dioxide into components of motor fuels - methanol, dimethyl ether, ethanol, hydrocarbons - in the presence of heterogeneous catalysts. At each route of conversion of CO2 (into oxygenates or hydrocarbons) the first stage is the formation of CO by the reverse water gas shift (rWGS) reaction, which must be taken into account when catalysts of process are choosing. The influence of chemical nature, specific surface area, particle size and interaction between catalyst components, as well as the method of its production on the CO2 conversion processes is analyzed. It is noted that the main active components of CO2 conversion into methanol are copper atoms and ions which interact with the oxide components of the catalyst. There is a positive effect of other metals oxides additives with strong basic centers on the surface on the activity of the traditional copper-zinc-aluminum oxide catalyst for the synthesis of methanol from the synthesis gas. The most active catalysts for the synthesis of DME from CO2 and H2 are bifunctional. These catalysts contain both a methanol synthesis catalyst and a dehydrating component, such as mesoporous zeolites with acid centers of weak and medium strength, evenly distributed on the surface. The synthesis of gasoline hydrocarbons (≥ C5) is carried out through the formation of CO or CH3OH and DME as intermediates on multifunctional catalysts, which also contain zeolites. Hydrogenation of CO2 into ethanol can be considered as an alternative to the synthesis of ethanol through the hydration of ethylene. High activation energy of carbon dioxide, harsh synthesis conditions as well as high selectivity for hydrocarbons, in particular methane remains the main problems. Further increase of selectivity and efficiency of carbon dioxide hydrogenation processes involves the use of nanocatalysts taking into account the mechanism of CO2 conversion reactions, development of methods for removing excess water as a by-product from the reaction zone and increasing catalyst stability over time.


2015 ◽  
Vol 37 (4) ◽  
pp. 402-407
Author(s):  
S.V. Zhil’tsova ◽  
◽  
V.M. Mikhal’chuk ◽  
N.G. Leonova ◽  
R.I. Lyga ◽  
...  

2017 ◽  
Vol 58 (8) ◽  
pp. 1543-1552
Author(s):  
N.I. Fainer ◽  
◽  
R.V. Pushkarev ◽  
V.A. Shestakov ◽  
A.K. Gutakovsky ◽  
...  

Sign in / Sign up

Export Citation Format

Share Document