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通过溶液共混法制备了聚乙烯基胺(PVAm)/聚乙二醇(PEG)和PVAm/聚N-乙烯基-γ-氨基丁酸钠(PVSA)共混聚合物.分别以这两种共混聚合物为分离层,以聚醚砜超滤膜为支撑层制备了用于分离CO2的固定载体复合膜.研究了共混组成对膜结构和性能的影响,结果表明共混可以改善固定载体膜的透过分离性能.PEG质量含量为10%的PVAm/PEG共混膜具有整体最优的透过分离性能,当温度为25℃、压力为125kPa时,纯CO2渗透速率为4.34×10-9cm3(STP)8226;cm-28226;s-18226;Pa-1,CO2/CH4理想分离因子为63.5;对PVAm/PVSA共混膜,PVSA质量含量为33.3%的膜具有最高的CO2/CH4理想分离因子,而PVSA质量含量为50%的膜具有最高纯CO2渗透速率. 相似文献
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反渗透(RO)膜分离技术由于具有高效、低耗和产水水质高等优点,已成为现阶段解决水资源短缺的有效手段。进一步提高RO膜的选择透过性能有利于降低产水成本和提高产水质量,因此制备高选择透过性能的RO膜一直是膜领域研究的重点。从优化界面聚合工艺、优化基膜及开发新型制膜工艺三方面对近年来改善RO膜选择透过性能的研究进行了综述。通过优化界面聚合工艺和开发新型制膜工艺可以直接改变分离层的结构和性质,通过调节基膜的孔径、孔隙率及亲疏水性可以影响分离层的结构,从而改善RO膜的性能。最后对制备高选择透过性能的反渗透膜的研究方向与发展前景进行了总结与展望。 相似文献
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Amine-functionalized mesoporous silica was prepared by using lauric acid and N-stearoyl-l-glutamic acid as structure directing agents via the SN+-I mechanism and applied to CO2 adsorption at room temperature. With γ-aminopropyltriethoxysilane as co-structure directing agent and due to the direct electrostatic interaction with anionic surfactant, most of the amino groups were uniformly distributed at the inner surface of pores and the performance was stable. The amine-functionalized mesoporous silica was characterized by Fourier transform infrared spectrometer, X-ray diffraction, nitrogen physisorption and thermogravimetric analysis. The CO2 adsorption capacity was measured by digital recording balance. At the room temperature and under the atmospheric pres-sure, the adsorption capacity of LAA-AMS-0.2 for CO2 and N2 is 1.40 mmol•g1 and 0.03 mmol•g1, respectively, indicating high separation coefficient of CO2/N2. 相似文献
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双胍基化聚乙烯胺改性制备抗生物污染反渗透膜 总被引:1,自引:0,他引:1
反渗透作为一种高效、低能耗的膜分离技术,在使用过程中极易受到生物污染的侵袭,造成膜性能不可逆下降。制备具有杀菌功能的反渗透膜可以有效缓解膜生物污染问题。采用二次界面聚合法,将合成的双胍基化聚乙烯胺(PVAm G)阳离子聚合物引入到初生反渗透膜表面,制备出具有杀菌功能的PVAm G改性反渗透膜。结果表明,改性后膜表面的微观形貌和润湿性变化不大,在中性条件下膜表面荷正电。PVAm G改性膜在不降低膜选择透过性能的同时,有效提高了抗生物污染性能。PVAm G改性膜与枯草杆菌和大肠杆菌连续接触4次后,膜面细菌死亡率每次均接近99.9%,表明PVAm G改性膜具有持久的广谱杀菌性。 相似文献
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1 INTRODUCTION
Hydrogen evolution reaction is an important reaction to produce high purity hydrogen for use in applications such as fertilizers (synthesis of ammonia),food (hydrogenation of fats and oils),petrochemical industry(hydrocracking of petroleum), metallurgical industry (reducing agent in the metallurgical and semiconductors industries) and alkaline production. The main operating cost of the process is the cost of electricity. 相似文献