• Title/Summary/Keyword: Membrane for gas separation

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Microstructure and Pore Size Control of Silica Membrane for Gas Separation at Elevated Temperatures

  • Lee Kew-Ho;Sea Bongkuk;Lee Dong-Wook
    • Korean Membrane Journal
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    • v.7 no.1
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    • pp.42-50
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    • 2005
  • Among ceramic membranes developed to date, amorphous silica membranes are attractive for gas separation at elevated temperatures. Most of the silica membranes can be formed on a porous support by sol-gel or chemical vapor deposition (CVD) process. To improve gas permselectivity of the membrane, well-controlled pores having desired size and chemical affinity between permeates and membrane become important factors in the preparation of membranes. In this article, we review the literature and introduce our technologies on the microstructure to be solved and pore size control of silica membranes using sol-gel and CVD methods.

Carbon Molecular Sieve Membranes Dispersed with Nano Particles

  • H.Suda;Ha, K.raya
    • Proceedings of the Membrane Society of Korea Conference
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    • 2004.05a
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    • pp.183-186
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    • 2004
  • Nano particles-containing CMS membranes were prepared by pyrolysis of polyimides dispersed uniformly with precursors and their gas separation performances were examined, to elucidate the permeation mechanism and to further improve the gas separation performance. Consequently, it was suggested that the separation performance could be controlled by doping nano-particles in the CMS membranes, and that optimization of various factors, such as the size, content, and dispersion state of the nano particles would contribute for further improvement of the gas separation performance.

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Research and Development Trends of Polyimide Based Material for Gas Separation (기체분리용 폴리이미드 소재의 연구개발동향)

  • Kim, Deuk Ju;Nam, Sang Yong
    • Membrane Journal
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    • v.23 no.6
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    • pp.393-408
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    • 2013
  • Gas separation processes using polymeric membranes have been greatly developed during the last few decades due to high energy efficiency and economic advantages. To achieve optimum economic performance, gas separation membranes required high permeability and selectivity. So, a number of reports examining the various polymeric materials for gas separation membranes have been published. Among the studied materials, polyimide (PI), which exhibit high permselectivity for various gas pairs, high chemical resistance, thermal stability, and mechanical strength, have attracted much attention. This paper focuses on the basic principle of gas separation, preparation procedure of membrane along with the recent developments and research trends of PI based materials for gas separation.

Developmental Trend of Polyimide Membranes for Gas Separation (Polyimide계 기체분리막의 개발 동향)

  • Oh, Dae-Youn;Nam, Sang-Yong
    • Membrane Journal
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    • v.21 no.4
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    • pp.307-320
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    • 2011
  • Polymeric gas separation membrane is the fastest growing field in membrane separation process. Polymeric gas separation membrane process is competitive compare to cryogenic process and pressure swing adsorption process. Aromatic polymer materials such as polysulfones, polypheneylene oxides, polycarbonates and polyimides have been used for gas separation. Recently, glassy polymer likes polyimide in aromatic polymers has been developed for achievement of high selectivity and permeability coefficients. The accurate understanding on a type and structure of polymer material is very important, because the factor that polymer material affect gas separation property. In the study, trend and the development direction on synthesis and permeation properties of polyimide is confirmed.

Applications and a View of Gas Separation by Membranes in Japan (일본에서의 기체분리막의 현황 및 응용)

  • Nakagawa, Tsutomu
    • Membrane Journal
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    • v.4 no.1
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    • pp.9-29
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    • 1994
  • The development of separation technology is an important research subject as is clear from its role in the Japanese government's research and development program for basic technology for the next generation(1981~1990). Japan is poor not only in mineral resources but also in energy resources and if a sudden change occurs in oil producing facility or an accident occurs in a nuclear power plant, then energy policy must undergo changes and economic foundations may collapse. Japan has already experienced this. Although, oil prices are stable at present and Japan can import oil at low cost due to the yen appreciation, Japan needs to promote development work for any new energy crisis that may come in the future. This has been the motive for gas separation membrane development in Japan. The study of gas permeation through polymer membranes, which is the basis for membranes for gas separation, at Japanese universities began many years ago, but interest in membranes for gas separation was aroused mainly by the Government. The development of gas separation membranes in Japan started with membranes for oxygen separation on an industrial scale.

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Mathematical Modelling and Simulation of CO2 Removal from Natural Gas Using Hollow Fibre Membrane Modules

  • Gu, Boram
    • Korean Chemical Engineering Research
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    • v.60 no.1
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    • pp.51-61
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    • 2022
  • Gas separation via hollow fibre membrane modules (HFMM) is deemed to be a promising technology for natural gas sweetening, particularly for lowering the level of carbon dioxide (CO2) in natural gas, which can cause various problems during transportation and process operation. Separation performance via HFMM is affected by membrane properties, module specifications and operating conditions. In this study, a mathematical model for HFMM is developed, which can be used to assess the effects of the aforementioned variables on separation performance. Appropriate boundary conditions are imposed to resolve steady-state values of permeate variables and incorporated in the model equations via an iterative numerical procedure. The developed model is proven to be reliable via model validation against experimental data in the literature. Also, the model is capable of capturing axial variations of process variables as well as predicting key performance indicators. It can be extended to simulate a large-scale plant and identify an optimal process design and operating conditions for improved separation efficiency and reduced cost.

A Numerical Analysis of Direct Contact Membrane Distillation for Hollow Fiber Membrane (기체분리용 고분자 멤브레인의 최근 개발 동향)

  • Kim, Tae-Heon;Jeong, Jung-Chae;Park, Jong-Man;Woo, Chang-Hwa
    • Membrane Journal
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    • v.20 no.4
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    • pp.267-277
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    • 2010
  • Gas separation membranes have been developed for decades in various areas to replace the conventional processes. Membrane processes for gas separation have many advantages of energy saving, compact size, and easy scale-up. Nowadays, gas separation processes is widely spreaded in nitrogen generating system, hydrogen generating system, membrane dryer, on board inert gas generating system, natural gas purification, biogas purification and fuel cells. Carbon dioxide separation process using membrane would be a strong candidate of carbon dioxide capturing process. In order to broaden the scope of application of gas separation membranes, development of new materials which can overcome the borderline of Robeson's plot should be necessary, so that many researchers and companies are trying to develop the new materials like polymers containing cardo and spiro group and PIMs (polymers for intrinsic microporosity).

Study on the Separation of CO2 from Flue Gas Using Polysulfone Hollow Fiber Membrane (폴리설폰 중공사막을 이용한 연소 배기가스 중 이산화탄소 분리에 관한 연구)

  • Kim, Seongcheon;Chun, Jeonghyeon;Chun, Youngnam
    • Journal of Korean Society of Environmental Engineers
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    • v.36 no.2
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    • pp.147-152
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    • 2014
  • In this research, polysulfone hollow fiber membrane was used to recover $CO_2$ which is one of greenhouse gases from flue gas stream being emitted after the combustion of fossil fuels. The prerequisite requirement is to design the membrane process producing high-purity $CO_2$ from flue gas. For separation of $CO_2$, a membrane module and flue gas containing 10% carbon dioxide was used. The effects of operating conditions such as pressure, temperature, feed gas composition and multi-stage membrane on separation performance were examined at various stage cuts. Higher operating pressure and temperature increased carbon dioxide concentration and recovery ratio in permeate. Recovery ratio and separation efficiency increased if a higher content of $CO_2$ injection gas composition. Three-stage membrane system was producing a 95% $CO_2$ with 90% recovery from flue gas. The separation efficiency of three-stage membrane system was higher than one-stage system.

Research Trend of Membrane Technology for Separation of Carbon Dioxide from Flue Gas (온실기체 분리회수를 위한 막분리기술 연구 동향)

  • 김정훈;임지원;이수복
    • Membrane Journal
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    • v.12 no.3
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    • pp.121-142
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    • 2002
  • The $CO_2$ emission is the largest contribute for the green house effect. Among the existing chemical separation processes, the membrane separation technology is(/will be) the most potential process for $CO_2$, separation from flue gas. Based on the solution-diffusion theory and physical properties of carbon dioxide/nitrogen and the permeation data in the literature, the relationships between physico-chemical structures of polymeric membrane materials and the perm-selectivities for $CO_2$/$N_2$ gases were described in detail. The progress of membrane module and process development was introduced briefly. Finally, the worldwide research activity including South Korea's for carbon dioxide separation by membrane technology were introduced through the survey of papers and technical reports published.

Development of High Pressure Membrane-Based Associated Gas Separation System for DME Synthesis (DME 합성을 위한 고압 유휴가스 분리용 Membrane 시스템 개발)

  • Kim, Hackeun;Bae, Myongwon;Lee, Sangjin;Ha, Seongyong;Lee, Chungseop;Mo, Yonggi
    • Transactions of the Korean hydrogen and new energy society
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    • v.26 no.1
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    • pp.45-53
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    • 2015
  • The objective of this study is to develop a gas pro-treatment system for DME synthesis, wherein this system separates $CO_2$ from Flaring gas as Membrane, in order to save raw material ($CH_4$) cost of DME. In this study, hollow fiber membrane is developed, which is able to separate high-pressure gas, supported by polysulfone and coated with amorphous fluorinated polymer. Throughout the evaluation of the membrane's separation characteristics, the membrane is applied to this system. The membrane is designed by 2 stages for over 90% removal rate of $CO_2$ and over 90% recovery rate of $CH_4$. The bench scale of pro-treatment system is developed as $25Nm^3/hr$.