scholarly journals Membrane Performance of High-Silica CHA-Type Zeolite Membranes in Vapor Permeation for Dehydration of Hydrous 2-Propanol

2012 ◽  
Vol 44 ◽  
pp. 1048-1049 ◽  
Author(s):  
K. Sato ◽  
T. Kyotani ◽  
T. Kikuchi
2018 ◽  
Vol 199 ◽  
pp. 298-303 ◽  
Author(s):  
Satoshi Imasaka ◽  
Masaya Itakura ◽  
Kazuhiro Yano ◽  
Suguru Fujita ◽  
Masashi Okada ◽  
...  

2002 ◽  
Vol 752 ◽  
Author(s):  
Hidetoshi Kita

ABSTRACTZeolite Membranes Were Prepared On A Porous Ceramic Support By Hydrothermal Synthesis Using Conventional Heating System And Microwave Heating. Naa And T Type Zeolite Membranes Were Highly Selective For Permeating Water Preferentially With The High Permeation Flux, While Silicalite Membranes Exhibited Preferential Organic Compound Permeation From Water Such As Ethanol/Water. Nay And Nax Zeolite Membranes Showed A High Alcohol Selectivity For Several Feed Mixtures With Methanol Or Ethanol And A High Benzene Selectivity For Benzene/Cyclohexane And Benzene/N-Hexane Separation. The Performance Of The Zeolite Membranes Was The Most Favorable One For Pervaporation Membranes Which Have Been Published So Far And A Tubular Type Module Using A Type Zeolite Membrane For Dehydration Of Organic Liquids Has Been Put Into Industrial Operation. The Tubular Type Pervaporation And Vapor Permeation Module Can Produce 99.8 Wt% Ethanol From 600 L/H, 90 Wt% Ethanol Feed At 120 °C. For The Mass Production Of Zeolite Membrane A New Synthetic Method Using A Microwave Heating Is Also Proposed.


2012 ◽  
Vol 409-410 ◽  
pp. 82-95 ◽  
Author(s):  
Kiminori Sato ◽  
Kazunori Sugimoto ◽  
Naoto Shimotsuma ◽  
Tomohisa Kikuchi ◽  
Tomohiro Kyotani ◽  
...  

Membranes ◽  
2021 ◽  
Vol 11 (4) ◽  
pp. 249
Author(s):  
Yasuhisa Hasegawa ◽  
Chie Abe ◽  
Mayumi Natsui ◽  
Ayumi Ikeda

The polycrystalline CHA-type zeolite layer with Si/Al = 18 was formed on the porous α-Al2O3 tube in this study, and the gas permeation properties were determined using single-component H2, CO2, N2, CH4, n-C4H10, and SF6 at 303–473 K. The membrane showed permeation behavior, wherein the permeance reduced with the molecular size, attributed to the effect of molecular sieving. The separation performances were also determined using the equimolar mixtures of N2–SF6, CO2–N2, and CO2–CH4. As a result, the N2/SF6 and CO2/CH4 selectivities were as high as 710 and 240, respectively. However, the CO2/N2 selectivity was only 25. These results propose that the high-silica CHA-type zeolite membrane is suitable for the separation of CO2 from CH4 by the effect of molecular sieving.


2021 ◽  
Vol 319 ◽  
pp. 111044
Author(s):  
Xinluona Su ◽  
Yuta Nakasaka ◽  
Ren Moriwaki ◽  
Takuya Yoshikawa ◽  
Takao Masuda

2011 ◽  
Vol 143 (2-3) ◽  
pp. 270-276 ◽  
Author(s):  
Xiansen Li ◽  
Hidetoshi Kita ◽  
Hua Zhu ◽  
Zhenjia Zhang ◽  
Kazuhiro Tanaka ◽  
...  

2020 ◽  
Vol 15 (1) ◽  
pp. 122-132 ◽  
Author(s):  
Carolina Conde-Mejía ◽  
Arturo Jiménez-Gutiérrez

AbstractAfter the biomass pretreatment and fermentation processes, the purification step constitutes a major task in bioethanol production processes. The use of membranes provides an interesting choice to achieve high-purity bioethanol. Membrane separation processes are generally characterized by low energy requirements, but a high capital investment. Some major design aspects for membrane processes and their application to the ethanol dehydration problem are addressed in this work. The analysis includes pervaporation and vapor permeation methods, and considers using two types of membranes, A-type zeolite and amorphous silica membrane. The results identify the best combination of membrane separation method and type of membrane needed for bioethanol purification.


2008 ◽  
Vol 196 (1-2) ◽  
pp. 182-193 ◽  
Author(s):  
Belma Soydaş ◽  
Ali Çulfaz ◽  
Halil Kalipçilar

Desalination ◽  
2006 ◽  
Vol 200 (1-3) ◽  
pp. 66-67 ◽  
Author(s):  
Eser Dinçer ◽  
Ali Çulfaz ◽  
Halil Kalipçilar

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