CO2等离子体改性Pebax/PDMS/PSf复合膜的制备及CO2/N2分离性能
作者: 王玉杰, 杨芳芳, 李楠,刘轶群* 
单位: 中石化(北京)化工研究院有限公司, 北京 100013
关键词: CO2 等离子体改性; 浸涂法; CO2分离膜; PDMS; Pebax
DOI号: 10.16159/j.cnki.issn1007-8924.2026.03.001
分类号: TQ028.8
出版年,卷(期):页码: 2026, 46(3):1-12

摘要:

针对CO2分离膜涂覆过程中界面相容性差、易分层和表面缺陷等问题,采用CO2等离子体改性聚二甲基硅氧烷/聚砜(PDMS/PSf)膜表面,之后浸涂聚醚嵌段聚酰胺(Pebax-1657)溶液制备薄层复合(TFC)膜。优化了CO2等离子体处理功率、处理时间、Pebax溶液浓度及浸涂时间等条件,通过扫描电子显微镜(SEM)、接触角、原子力纳米红外(AFM-Nano-IR)、X射线光电子能谱(XPS)等表征手段,系统研究了制膜条件对膜结构与分离性能的影响。结果表明,CO2等离子体改性后,PDMS膜表面粗糙度增加,接触角降低(115.3°降至55.6°)。 AFM-Nano-IR和XPS表征证实,PDMS与Pebax分离层间界面处化学键合增强,显著提升了界面相容性。优化条件下制得的TFC膜CO2渗透率为598~624 GPU,CO2/N2理想选择性达44~56。CO2等离子体改性结合浸涂法制备Pebax/PDMS/PSf高性能薄层复合膜的工艺简便且易于放大,在CO2/N2气体分离中展现出良好的应用潜力。

 To address the challenges of poor interfacial compatibility, delamination tendency, and surface defects in CO2 separation membrane, a polydimethylsiloxane/polysulfone (PDMS/PSf) substrate membrane was modified using CO2 plasma treatment technology, followed by dip-coating with a polyether block amide (Pebax-1657) solution to prepare thin-film composite (TFC) membrane. By such as CO2 plasma treatment power, treatment time, Pebax solution concentration, and dipping time, combined with characterization techniques including scanning electron microscopy (SEM), contact angle analysis,atomic force microscopy-nano infrared spectroscopy (AFM-Nano-IR) and X-ray photoelectron spectroscopy (XPS)for evaluation, the effects of fabrication conditions on membrane structure and separation performance were systematically investigated. CO2 plasma modification significantly enhanced surface roughness and reduced contact angle (from 115.3° to 55.6°). AFM-Nano-IR and XPS confirmed strengthened chemical bonding at the interface between PDMS and Pebax selective layer, enhancing interfacial compatibility. The Pebax/PDMS/PSf membrane under optimized conditions exhibited a continuous and defect-free layer, achieving CO2 permeance of 598~624 GPU and CO2/N2 ideal selectivity of 44~56. The integration of CO2 plasma modification and dip-coating enables efficient fabrication of high-performance Pebax/PDMS/PSf TFC membrane with a simple and scalable process, demonstrating promising potential for industrial-scale CO2 separation membrane development. 


基金项目:

新材料重大专项项目资助(2026ZD0621900); 企业项目“二氧化碳分离膜研发”(322003)


作者简介:
第一作者简介: 王玉杰(1980-),女,河北保定人,高级工程师,博士,研究方向为气体分离膜材料、分离膜制备与应用.*通讯作者,E-mail:liuyq.bjhy@sinopec.com  

参考文献:

[1]中国政府网. “双碳”工作开局良好 实现目标须久久为功——国家发展改革委新闻发布会聚焦生态文明建设 [EB/OL]. 2022-09-22. https://www.gov.cn/xinwen/2022-09/22/content_5711174.htm.
[2]Esposito E, Clarizia G, Bernardo P, et al. Pebax/PAN hollow fiber membranes for CO2/CH4 separation [J]. Chem Eng Process-Process Intensif, 2015, 94: 53-61.
[3]Rahman M M, Filiz V, Shishatskiy S, et al. PEBAX with PEG functionalized POSS as nanocomposite membranes for CO2 separation [J]. J Membr Sci, 2013, 437: 286-297.
[4]Bouilloux A, Alex P. Material comprising a polyamide, a polymer having polyamide and polyether blocks and a functionalized polyolefin, and film and object obtained therefrom: US, 5,959,042 [P/OL]. 1999-09-28.
[5]Baker R W, Low B T. Gas separation membrane materials: A perspective [J]. Macromolecules, 2014, 47(20): 6999-7013.
[6]Liu M, Nothling M D, Webley P A, et al. Postcombustion carbon capture using thin-film composite membranes [J]. ACC Chem Res, 2019, 52(7): 1905-1914.
[7]谢尊虎, 曾凡伟, 肖建斌. 硅橡胶性能及其研究进展 [J]. 特种橡胶制品, 2011, 32(2): 69-72.
[8] 陈杰瑢. 低温等离子体处理聚酯 (PET) 表面润湿性与表面结构的研究 [J]. 高等学校化学学报, 1997, 18(3): 466-471.
[9]Selyanchyn O, Selyanchyn R, Fujikawa S. Critical role of the molecular interface in double-layered Pebax-1657/PDMS nanomembranes for highly efficient CO2/N2 gas separation [J]. ACS Appl Mater Interfaces, 2020, 12(29): 33196-33209.
[10]Ozdemir Y, Hasirci N, Serbetci K. Oxygen plasma modification of polyurethane membranes [J]. J Mater Sci: Mater Med, 2002, (13): 1147-1152.
[11]Barbier V, Tatoulian M, Li H, et al. Stable modification of PDMS surface properties by plasma polymerization application to the formation of double emulsions in microfluidic systems [J]. Langmuir, 2006, 22(12): 5230-5232.
[12]Fritz J L, Owenm J. Hydrophobic recovery of plasma-treated polydimethylsiloxane [J]. J Adhesion, 1995, 54(1/2/3/4):33-45.
[13]任煜, 邱夷平. 低温等离子体对高聚物材料表面改性处理时效性的研究进展 [J]. 材料导报, 2007, 21(1): 56-59.
[14]Markov D A, Lillie E M, Garbett S P, et al. Variation in diffusion of gases through PDMS due to plasma surface treatment and storage conditions [J]. Biomed Microdevices, 2014, 16: 91-96.
[15]Eddington D T, Puccinelli J P, Beebe D J. Thermal aging and reduced hydrophobic recovery of polydimethylsiloxane [J]. Sens Actuators B Chem, 2006, 114(1): 170-172.
[16]Morent R, De Geyter N, Leys C, et al. Study of the ageing behaviour of polymer films treated with a dielectric barrier discharge in air, helium and argon at medium pressure [J]. Surf Coat Technol, 2007, 201(18): 7847-7854.
[17]Hillborg H, Tomczak N, Olàh A, et al. Nanoscale hydrophobic recovery: A chemical force microscopy study of UV/ozone-treated cross-linked poly (dimethylsiloxane) [J]. Langmuir, 2004, 20(3): 785-794.
[18]Pal D, Neogi S, De S. Hydrophilic surface modification of polyacrylonitrile based membrane: Effect of low temperature radio frequency carbon dioxide plasma [J]. Polymer Bulletin, 2018, 75(8): 3567-3586.
[19]Bernardo P, Jansen J C, Bazzarelli F, et al. Gas transport properties of Pebax/room temperature ionic liquid gel membranes [J]. Sep Purif Technol, 2012, 97: 73-82.
[20]Pal D, Neogi S, De S. Improved antifouling characteristics of acrylonitrile co-polymer membrane by low temperature pulsed ammonia plasma in the treatment of oil-water emulsion [J]. Vacuum, 2016, 131: 293-304.
[21]Jiang X, Goh K, Wang R. Air plasma assisted spray coating of Pebax-1657 thin-film composite membranes for post-combustion CO2 capture [J]. J Membr Sci, 2022, 658: 120741.
[22]罗放. 基于AFM-IR的高分子聚合物添加剂定量检测新方法 [J]. 合成树脂与塑料,2024, 41(2): 30-33.
[23]Wang Z X, Sun W S, Zhang W H, et al. Construction of high-performance thin-film composite membrane for CO2 separation via interface engineering [J]. Sep Purif Technol, 2023, 322: 124348.
[24]Go Y K, Leal C. Polymer-lipid hybrid materials [J]. Chem Rev, 2021, 121(22): 13996-14030.
[25]Sun W S, Yin M J, Zhang W H, et al. Tailor-made microstructures lead to high-performance robust PEO membrane for CO2 capture via green fabrication technique [J]. Green Energy Environ, 2023, 8(5): 1389-1397.
[26]刘迪, 任吉中, 邓麦村. 聚醚共聚酰胺复合气体分离膜的制备与分离性能 [J]. 膜科学与技术, 2010, 30(3): 44-49.
[27]Liu L, Chakma A, Feng X. Preparation of hollow fiber poly(ether block amide)/polysulfone composite membranes for separation of carbon dioxide from nitrogen [J]. Chem Eng J, 2004, 105(1/2): 43-51.
[28]Scofield J M P, Gurr P A, Kim J, et al. Development of novel fluorinated additives for high performance CO2 separation thin-film composite membranes [J]. J Membr Sci, 2016, 499: 191-200.
[29]任晓灵, 任吉中, 邓麦村. 聚醚共聚酰胺多层复合气体分离膜的制备及其分离性能 [J]. 膜科学与技术, 2012, 32(2): 30-35.
[30]王颖, 任吉中, 徐徜徉, 等. 聚醚共聚酰胺-三醋酸甘油酯多层复合气体分离膜的制备及其分离性能 [J]. 膜科学与技术, 2014, 34(5): 27-32.
[31]Car A, Stropnik C, Yave W, et al. Pebax/polyethylene glycol blend thin film composite membranes for CO2 separation: Performance with mixed gases [J]. Sep Purif Technol, 2008, 62(1): 110-117.
[32]Selyanchyn R, Ariyoshi M, Fujikawa S. Thickness effect on CO2/N2 separation in double layer Pebax-1657/PDMS membranes [J]. Membranes, 2018, 8(4): 121.
[33]Li T, Pan Y, Peinemann K V, et al. Carbon dioxide selective mixed matrix composite membrane containing ZIF-7 nano-fillers [J]. J Membr Sci, 2013, 425: 235-242.
[34]Scofield J M P, Gurr P A, Kim J, et al. Blends of fluorinated additives with highly selective thin-film composite membranes to increase CO2 permeability for CO2/N2 gas separation applications [J]. Ind Eng Chem Res, 2016, 55(30): 8364-8372.
[35]Sutrisna P D, Hou J, Li H, et al. Improved operational stability of Pebax-based gas separation membranes with ZIF-8: A comparative study of flat sheet and composite hollow fibre membranes [J]. J Membr Sci, 2017, 524: 266-279. 


服务与反馈:
Download】【加入收藏

《膜科学与技术》编辑部 地址:北京市朝阳区北三环东路19号蓝星大厦 邮政编码:100029 电话:010-80492417/010-80485372 传真:010-80485372邮箱:mkxyjs@163.com

京公网安备11011302000819号