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Wang Q, Qian C, Xu N, Liu Q, Wang B, Zhang L, Fan L, Zhou R. Synthesis optimization and separation mechanism of ZSM-5 zeolite membranes for pervaporation dehydration of organic solvents. THE SCIENCE OF THE TOTAL ENVIRONMENT 2024; 929:172641. [PMID: 38670376 DOI: 10.1016/j.scitotenv.2024.172641] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Subscribe] [Scholar Register] [Received: 01/13/2024] [Revised: 03/31/2024] [Accepted: 04/18/2024] [Indexed: 04/28/2024]
Abstract
Pervaporation (PV), as an energy-efficient mixture separation technology, plays an important role in the chemical industry. In this work, no organic templates were needed to produce high-performance ZSM-5 membranes with an extremely low Si/Al ratio of 3.3 on α-Al2O3 tubular supports using 100 nm nanoseeds. The effects of preparation parameters on the crystalline phase structures, micromorphologies, and PV separation performance of ZSM-5 membranes were comprehensively investigated. The results revealed that the Si/Al ratio of gels significantly affected both the Si/Al ratio and the crystal orientation of the final ZSM-5 membrane. The optimized ZSM-5 membrane with a thickness of 1.8 μm was utilized to dehydrate various organic solvents via PV, and the influence of the operating parameters on PV dehydration performance was evaluated and is described herein. Furthermore, the permeation behaviors of single gases and PV were examined using permeate molecules within a similar size range to reveal the PV mechanism of the ZSM-5 membrane. The results demonstrated that gas permeation followed Knudsen diffusion, while PV permeation was decreased with decreases in the affinity of molecules, revealing an adsorption-diffusion mechanism that dominated PV dehydration through the ZSM-5 membrane. Moreover, the as-synthesized ZSM-5 membrane had good water permselectivity for water/acetone (e.g., total flux = 1.03 kg/(m2 h), α = 307) and for water/isopropanol (e.g., total flux = 1.49 kg/(m2 h), α = 1070) mixtures compared with other membranes reviewed in the literature. The synthesized ZSM-5 membrane also exhibited excellent reproducibility, high stability, and attractive PV separation performance, demonstrating its significant potential application in the PV dehydration of organic solvents.
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Affiliation(s)
- Qing Wang
- School of Energy, Materials and Chemical Engineering, Hefei University, Hefei 230601, China; State Key Laboratory of Materials-Oriented Chemical Engineering, College of Chemical Engineering, Nanjing Tech University, Nanjing 210009, China
| | - Cheng Qian
- School of Energy, Materials and Chemical Engineering, Hefei University, Hefei 230601, China
| | - Nong Xu
- School of Energy, Materials and Chemical Engineering, Hefei University, Hefei 230601, China; State Key Laboratory of Materials-Oriented Chemical Engineering, College of Chemical Engineering, Nanjing Tech University, Nanjing 210009, China.
| | - Qiao Liu
- School of Energy, Materials and Chemical Engineering, Hefei University, Hefei 230601, China
| | - Bin Wang
- State Key Laboratory of Materials-Oriented Chemical Engineering, College of Chemical Engineering, Nanjing Tech University, Nanjing 210009, China
| | - Lingyun Zhang
- School of Energy, Materials and Chemical Engineering, Hefei University, Hefei 230601, China
| | - Long Fan
- School of Energy, Materials and Chemical Engineering, Hefei University, Hefei 230601, China
| | - Rongfei Zhou
- State Key Laboratory of Materials-Oriented Chemical Engineering, College of Chemical Engineering, Nanjing Tech University, Nanjing 210009, China
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Qiao Y, Xu S, Wu Y, Zhang L, Xie L. Dehydration of Organic Solvents from Ternary Mixtures Containing Toluene/Methanol/Water by Pervaporation. MEMBRANES 2024; 14:139. [PMID: 38921506 PMCID: PMC11205444 DOI: 10.3390/membranes14060139] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Subscribe] [Scholar Register] [Received: 05/10/2024] [Revised: 06/01/2024] [Accepted: 06/07/2024] [Indexed: 06/27/2024]
Abstract
The separation of a toluene/methanol/water ternary mixture is a difficult task due to the toluene/water and toluene/methanol azeotropes. In this article, low-energy pervaporation is proposed for the separation of the ternary azeotrope toluene-methanol-water. This work investigates the effects of feed temperature, feed flow rate, and vacuum on pervaporation and compares the energy consumption of pervaporation with that of distillation. The results showed that at the optimized flow rate of 50 L/h and a permeate side vacuum of 60 kPa at 50 °C, the water and methanol content in the permeate was about 63.2 wt.% and 36.8 wt.%, respectively, the water/ methanol separation factor was 24.04, the permeate flux was 510.7 g/m2·h, the water content in the feed out was reduced from 2.5 wt.% to less than 0.66 wt.%, and the dehydration of toluene methanol could be realized. Without taking into account the energy consumption of pumps and other power equipment, pervaporation requires an energy consumption of 43.53 kW·h to treat 1 ton of raw material, while the energy consumption of distillation to treat 1 ton of raw material is about 261.5 kW·h. Compared to the existing distillation process, the pervaporation process consumes much less energy (about one-sixth of the energy consumption of distillation). There is almost no effect on the surface morphology and chemical composition of the membrane before and after use. The method provides an effective reference for the dehydration of organic solvents from ternary mixtures containing toluene/methanol/water.
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Affiliation(s)
| | - Shichang Xu
- Tianjin Key Laboratory of Membrane Science and Desalination Technology, State Key Laboratory of Chemical Engineering, School of Chemical Engineering and Technology, Tianjin University, Tianjin 300350, China; (Y.Q.); (Y.W.); (L.Z.)
| | | | | | - Lixin Xie
- Tianjin Key Laboratory of Membrane Science and Desalination Technology, State Key Laboratory of Chemical Engineering, School of Chemical Engineering and Technology, Tianjin University, Tianjin 300350, China; (Y.Q.); (Y.W.); (L.Z.)
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3
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Qadeer K, Al-Hinai A, Chuah LF, Sial NR, Al-Muhtaseb AH, Al Abri R, Qyyum MA, Lee M. Methanol production and purification via membrane-based technology: Recent advancements, challenges, and the way forward. CHEMOSPHERE 2023:139007. [PMID: 37253401 DOI: 10.1016/j.chemosphere.2023.139007] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Subscribe] [Scholar Register] [Received: 10/05/2022] [Revised: 05/08/2023] [Accepted: 05/21/2023] [Indexed: 06/01/2023]
Abstract
Industrail revolution on the back of fossil fuels has costed humanity higher temperatures on the planet due to ever-growing concentration of CO2 emissions in Earth's atmosphere. To tackle global warming demand for renewable energy sources continues to increase. Along renewables, there has been a growing interest in converting carbon dioxide to methanol, which can be used as a fuel or a feedstock for producing chemicals. The current review study provides a comprehensive overview of the recent advancements, challenges, and future prospects of methanol production and purification via membrane-based technology. Traditional downstream processes for methanol production, such as distillation and absorption, have several drawbacks, including high energy consumption and environmental concerns. In comparison to conventional technologies, membrane-based separation techniques have emerged as a promising alternative for producing and purifying methanol. The review highlights recent developments in membrane-based methanol production and purification technology, including using novel membrane materials such as ceramic, polymeric, and mixed matrix membranes. Additionally, integrating photocatalytic processes with membrane separation has been investigated to improve the conversion of carbon dioxide to methanol. Despite the potential benefits of membrane-based systems, several challenges need to be addressed. Membrane fouling and scaling are significant issues that can reduce the efficiency and lifespan of the membranes. Furthermore, the cost-effectiveness of membrane-based systems compared to traditional methods is a critical consideration that must be evaluated. In conclusion, the review provides insights into the current state of membrane-based technology for methanol production and purification and identifies areas for future research. The development of high-performance membranes and the optimization of membrane-based processes are crucial for improving the efficiency and cost-effectiveness of this technology and for advancing the goal of sustainable energy production.
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Affiliation(s)
- Kinza Qadeer
- School of Chemical Engineering, Yeungnam University, Gyeongsan, 712-749, South Korea
| | - Amer Al-Hinai
- Sustainable Energy Research Center (SERC) and Department of Electrical and Computer Engineering, College of Engineering, Sultan Qaboos University, Muscat, Oman.
| | - Lai Fatt Chuah
- Faculty of Maritime Studies, Universiti Malaysia Terengganu, Terengganu, Malaysia
| | - Noman Raza Sial
- School of Chemical Engineering, Yeungnam University, Gyeongsan, 712-749, South Korea
| | - Ala'a H Al-Muhtaseb
- Department of Petroleum and Chemical Engineering, College of Engineering, Sultan Qaboos University, Muscat, Oman
| | - Rashid Al Abri
- Sustainable Energy Research Center (SERC) and Department of Electrical and Computer Engineering, College of Engineering, Sultan Qaboos University, Muscat, Oman
| | - Muhammad Abdul Qyyum
- Department of Petroleum & Chemical Engineering, Sultan Qaboos University, Muscat, Oman.
| | - Moonyong Lee
- School of Chemical Engineering, Yeungnam University, Gyeongsan, 712-749, South Korea.
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Sub-nanometer scale tailoring of the microstructures of composite organosilica membranes for efficient pervaporation of toluene/n-heptane mixtures. J Memb Sci 2023. [DOI: 10.1016/j.memsci.2023.121469] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 02/09/2023]
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5
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Polotskaya G, Tian N, Faykov I, Goikhman M, Podeshvo I, Loretsyan N, Gofman I, Zolotovsky K, Pulyalina A. Novel Design of Co-Poly(Hydrazide Imide) and Its Complex with Cu(I) for Membrane Separation of Methanol/Dimethyl Carbonate Mixture. MEMBRANES 2023; 13:160. [PMID: 36837663 PMCID: PMC9963631 DOI: 10.3390/membranes13020160] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Figures] [Subscribe] [Scholar Register] [Received: 12/30/2022] [Revised: 01/24/2023] [Accepted: 01/25/2023] [Indexed: 06/18/2023]
Abstract
Poly(2,2'-biquinoline-6,6'-dicarbohydrazide)-co-(bistrimelliteimide)methylene-bisanthranylide (PHI) and its metal-polymer complex PHI-Cu(I) containing several types of functional groups (hydrazide, carboxyl, amide, and imide fragments) were synthesized to prepare two types of dense nonporous membranes. The study on morphology using scanning electron microscopy (SEM), measurements of mechanical, thermal, and transport properties of the membrane samples was carried out. The main mechanical properties of both membranes do not differ significantly, but the values of ultimate deformation differ palpably as a result of a non-uniform character of the deformation process for the PHI membrane. The thermal analysis based on the curves of thermogravimetric (TGA) and differential thermal (DTA) analyses of the PHI and PHI-Cu(I) membranes revealed peculiarities of the membrane structure. Transport properties were studied in pervaporation (PV) of methanol (MeOH) and dimethyl carbonate (DMC) mixtures including an azeotropic point. Intrinsic properties of the penetrant-membrane system were also determined. It was found that the total flux is higher through the PHI membrane, but the PHI-Cu(I) membrane exhibits a higher separation factor. Calculation of the pervaporation separation index (PSI) allowed to conclude that the PHI-Cu(I) membrane exhibits better transport properties as compared with the PHI membrane.
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Affiliation(s)
- Galina Polotskaya
- Institute of Macromolecular Compounds, Russian Academy of Sciences, Saint Petersburg 199004, Russia
- Institute of Chemistry, Saint Petersburg State University, Saint Petersburg 198504, Russia
| | - Nadezhda Tian
- Institute of Chemistry, Saint Petersburg State University, Saint Petersburg 198504, Russia
| | - Ilya Faykov
- Institute of Chemistry, Saint Petersburg State University, Saint Petersburg 198504, Russia
| | - Mikhail Goikhman
- Institute of Macromolecular Compounds, Russian Academy of Sciences, Saint Petersburg 199004, Russia
| | - Irina Podeshvo
- Institute of Macromolecular Compounds, Russian Academy of Sciences, Saint Petersburg 199004, Russia
| | - Nairi Loretsyan
- Institute of Macromolecular Compounds, Russian Academy of Sciences, Saint Petersburg 199004, Russia
| | - Iosif Gofman
- Institute of Macromolecular Compounds, Russian Academy of Sciences, Saint Petersburg 199004, Russia
| | - Konstantin Zolotovsky
- Institute of Chemistry, Saint Petersburg State University, Saint Petersburg 198504, Russia
| | - Alexandra Pulyalina
- Institute of Chemistry, Saint Petersburg State University, Saint Petersburg 198504, Russia
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Ikeda A, Matsuura W, Abe C, Lundin STB, Hasegawa Y. Evaluation of FAU-type Zeolite Membrane Stability in Transesterification Reaction Conditions. MEMBRANES 2023; 13:68. [PMID: 36676875 PMCID: PMC9867027 DOI: 10.3390/membranes13010068] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Figures] [Subscribe] [Scholar Register] [Received: 12/12/2022] [Revised: 12/23/2022] [Accepted: 12/28/2022] [Indexed: 06/17/2023]
Abstract
The transesterification conversion of methyl ether can be enhanced by the removal of the byproduct methanol using methanol permselective faujasite (FAU-type) zeolite membranes. However, the authors previously observed that the methanol flux during the transesterification reaction was lower than the predicted flux. Therefore, this study investigated the stability of FAU-type zeolite membranes in the presence of organic components associated with the transesterification reaction of methyl hexanoate and 1-hexanol. The stability was defined in terms of changes in methanol permeance and zeolite structure. The effect of reaction components (methanol, 1-hexanol, methyl hexanoate, and hexyl hexanoate) on the FAU-type zeolite structure and the methanol permeation performance of the FAU-type zeolite membranes were evaluated to find the component causing the lower methanol flux. From these results, two esters were found to adsorb strongly on the FAU-type zeolite. The methanol flux of the FAU-type zeolite membrane was examined after vapor exposure of each of the four reaction chemicals at 373 K for 8 h. In the case of methyl hexanoate and hexyl hexanoate vapor exposure, the methanol flux was reduced by about 75% compared to the initial flux of 15 kg m-2 h-1. These results indicated methanol permeation performance was inhibited by the adsorption of esters.
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Xing J, Qu Y, Su Z, Zhou M, Sun C, Wang Y, Cui P. Phase Equilibria and Mechanism Insights into the Separation of Isopropyl Acetate and Methanol by Deep Eutectic Solvents. Ind Eng Chem Res 2022. [DOI: 10.1021/acs.iecr.2c03488] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/23/2022]
Affiliation(s)
- Jiafu Xing
- College of Chemical Engineering, Qingdao University of Science and Technology, 53 Zhengzhou Road, Qingdao266042, P. R. China
| | - Yajuan Qu
- College of Chemical Engineering, Qingdao University of Science and Technology, 53 Zhengzhou Road, Qingdao266042, P. R. China
| | - Zihao Su
- College of Chemical Engineering, Qingdao University of Science and Technology, 53 Zhengzhou Road, Qingdao266042, P. R. China
| | - Mengjin Zhou
- College of Chemical Engineering, Qingdao University of Science and Technology, 53 Zhengzhou Road, Qingdao266042, P. R. China
| | - Chao Sun
- College of Chemical Engineering, Qingdao University of Science and Technology, 53 Zhengzhou Road, Qingdao266042, P. R. China
| | - Yinglong Wang
- College of Chemical Engineering, Qingdao University of Science and Technology, 53 Zhengzhou Road, Qingdao266042, P. R. China
| | - Peizhe Cui
- College of Chemical Engineering, Qingdao University of Science and Technology, 53 Zhengzhou Road, Qingdao266042, P. R. China
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Lu X, Huang J, Pinelo M, Chen G, Wan Y, Luo J. Modelling and optimization of pervaporation membrane modules: A critical review. J Memb Sci 2022. [DOI: 10.1016/j.memsci.2022.121084] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/05/2022]
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9
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Xing J, Liu X, Dai Y, Zhang Y, Su Z, Chen Z, Gao J, Wang Y, Cui P. Phase behavior and extraction mechanism of ethanol in alcohol ester mixture separated by deep eutectic solvents. J Mol Liq 2022. [DOI: 10.1016/j.molliq.2022.120694] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/06/2022]
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10
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Low-temperature cross-linking fabrication of sub-nanoporous SiC-based membranes for application to the pervaporation removal of methanol. J Memb Sci 2022. [DOI: 10.1016/j.memsci.2022.121008] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/17/2022]
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11
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Emerging membranes for separation of organic solvent mixtures by pervaporation or vapor permeation. Sep Purif Technol 2022. [DOI: 10.1016/j.seppur.2022.121729] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 01/25/2023]
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12
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Anggarini U, Yu L, Nagasawa H, Kanezashi M, Tsuru T. Structural transformation of the nickel coordination-induced subnanoporosity of aminosilica membranes for methanol-selective, high-flux pervaporation. J Memb Sci 2022. [DOI: 10.1016/j.memsci.2022.120613] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/15/2022]
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13
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Zhu H, Li R, Liu G, Pan Y, Li J, Wang Z, Guo Y, Liu G, Jin W. Efficient separation of methanol/dimethyl carbonate mixtures by UiO-66 MOF incorporated chitosan mixed-matrix membrane. J Memb Sci 2022. [DOI: 10.1016/j.memsci.2022.120473] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/18/2022]
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14
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Methanol/dimethyl carbonate separation using graphene oxide membrane via cationic control of molecular transport channels. J Memb Sci 2022. [DOI: 10.1016/j.memsci.2022.120457] [Citation(s) in RCA: 3] [Impact Index Per Article: 1.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/23/2022]
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15
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Yoon YH, Lively RP. Co-transport of water and p-xylene through carbon molecular sieve membranes. J Memb Sci 2022. [DOI: 10.1016/j.memsci.2022.120495] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/18/2022]
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16
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SUZ-4 zeolite membrane fabricated by dynamic hydrothermal crystallization for pervaporation separation of MeOH/MMA mixture. J Memb Sci 2022. [DOI: 10.1016/j.memsci.2021.119974] [Citation(s) in RCA: 3] [Impact Index Per Article: 1.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/19/2022]
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17
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Dong G, Zhang Y, Sato T, Nagasawa H, Kanezashi M, Tsuru T. Reverse osmosis and pervaporation of organic liquids using organosilica membranes: Performance analysis and predictions. AIChE J 2022. [DOI: 10.1002/aic.17585] [Citation(s) in RCA: 2] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/12/2022]
Affiliation(s)
- Guanying Dong
- School of Chemical Engineering Zhengzhou University Zhengzhou China
| | - Yatao Zhang
- School of Chemical Engineering Zhengzhou University Zhengzhou China
| | - Takaaki Sato
- Department of Chemical Engineering Hiroshima University Hiroshima Japan
| | - Hiroki Nagasawa
- Department of Chemical Engineering Hiroshima University Hiroshima Japan
| | | | - Toshinori Tsuru
- Department of Chemical Engineering Hiroshima University Hiroshima Japan
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18
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Enhancing dehydration performance of isopropanol for flexible hybrid silica composite membranes with spray-coated active layer on polymers. Sep Purif Technol 2022. [DOI: 10.1016/j.seppur.2021.120230] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/19/2022]
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Gu L, Zhang Z, Yang S, Liu X, Zhang M, Gao L, Xiao G. Chitosan‐Modified Polyvinyl Alcohol Membrane High Performance in Biodiesel/Methanol Pervaporation Separation. ChemistrySelect 2021. [DOI: 10.1002/slct.202102763] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/12/2022]
Affiliation(s)
- Liuyu Gu
- School of Chemistry and Chemical Engineering Southeast University 2 Dongnandaxue Rd. China
| | - Zongqi Zhang
- School of Chemistry and Chemical Engineering Southeast University 2 Dongnandaxue Rd. China
| | - Su Yang
- School of Chemistry and Chemical Engineering Southeast University 2 Dongnandaxue Rd. China
| | - Xueping Liu
- School of Chemistry and Chemical Engineering Southeast University 2 Dongnandaxue Rd. China
| | - Mengting Zhang
- School of Chemistry and Chemical Engineering Southeast University 2 Dongnandaxue Rd. China
| | - Lijing Gao
- School of Chemistry and Chemical Engineering Southeast University 2 Dongnandaxue Rd. China
| | - Guomin Xiao
- School of Chemistry and Chemical Engineering Southeast University 2 Dongnandaxue Rd. China
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20
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The hybrid RDWC–pervaporation with series–parallel arrangement and heat integration for ETBE production. Sep Purif Technol 2021. [DOI: 10.1016/j.seppur.2021.118695] [Citation(s) in RCA: 3] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/22/2022]
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21
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Raza W, Jianhua Y, Wang J, Saulat H, Wang L, Lu J, Zhang Y. A selective organosilica membrane for ethyl acetate dehydration by pervaporation. J Appl Polym Sci 2021. [DOI: 10.1002/app.50942] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 01/17/2023]
Affiliation(s)
- Waseem Raza
- State Key Laboratory of Fine Chemicals Dalian University of Technology Dalian China
| | - Yang Jianhua
- State Key Laboratory of Fine Chemicals Dalian University of Technology Dalian China
- Panjin Institute of Industrial Technology Dalian University of Technology Panjin China
| | - Jiaxuan Wang
- State Key Laboratory of Fine Chemicals Dalian University of Technology Dalian China
| | - Hammad Saulat
- State Key Laboratory of Fine Chemicals Dalian University of Technology Dalian China
| | - Lei Wang
- State Key Laboratory of Fine Chemicals Dalian University of Technology Dalian China
| | - Jingming Lu
- State Key Laboratory of Fine Chemicals Dalian University of Technology Dalian China
| | - Yan Zhang
- State Key Laboratory of Fine Chemicals Dalian University of Technology Dalian China
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22
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Liu C, Dong G, Tsuru T, Matsuyama H. Organic solvent reverse osmosis membranes for organic liquid mixture separation: A review. J Memb Sci 2021. [DOI: 10.1016/j.memsci.2020.118882] [Citation(s) in RCA: 26] [Impact Index Per Article: 8.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 01/28/2023]
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