Sánchez-Laínez Javier, Ballester-Catalán Marcos, Javierre-Ortín Enrique, Téllez Carlos, Coronas Joaquín
Chemical and Environmental Engineering Department, Instituto de Nanociencia de Aragón (INA) and Instituto de Ciencia de Materiales de Aragón (ICMA), Universidad de Zaragoza-CSIC, 50018 Zaragoza, Spain.
Dalton Trans. 2020 Mar 3;49(9):2905-2913. doi: 10.1039/c9dt04424h.
This work shows the preparation of Pebax® 1041 films from solutions in DMAc and water-DMAc emulsions as alternatives to those prepared by extrusion that can be found in the literature. These membranes were tested in post-combustion CO2 capture, in the separation of a 15/85 (v/v) CO2/N2 mixture. Self-supported membranes of Pebax® 1041 were prepared by solvent evaporation and phase inversion. The characterization of these films defined the intrinsic properties of this polymer in terms of chemical structure, crystallinity, thermal stability and gas separation performance (a CO2 permeability of 30 Barrer with a CO2/N2 selectivity of 21 at 35 °C and 3 bar feed pressure). Supported Pebax® 1041 membranes were also developed to decrease the Pebax® thickness (in the 1.5-10 μm range), resulting in a higher permeance. These membranes were prepared by a phase inversion process consisting of the precipitation of a Pebax® 1041/DMAc solution in water and dispersing it to form a stable emulsion that was drop-cast on PSF asymmetric supports. Once dried, the polymer formed a dense continuous layer. The phase inversion methodology is "greener" than solvent evaporation since dimethylacetamide is not released as toxic vapour during membrane preparation. The amount drop-cast led to a different selective layer thickness, which was enhanced by the dispersion of MWCNTs in the polymer emulsion. The properties of the Pebax® selective layer were studied by thermogravimetry and by measuring the contact angle of the membrane surface, and the optimal CO2/N2 selectivity (22.6) was obtained with a CO2 permeance of 3.0 GPU.
这项工作展示了由二甲基乙酰胺(DMAc)溶液和水 - DMAc乳液制备Pebax® 1041薄膜,作为文献中可找到的通过挤出法制备薄膜的替代方法。这些膜用于燃烧后二氧化碳捕集测试,分离15/85(v/v)的二氧化碳/氮气混合物。通过溶剂蒸发和相转化制备了Pebax® 1041自支撑膜。这些薄膜的表征从化学结构、结晶度、热稳定性和气体分离性能方面定义了该聚合物的固有特性(在35°C和3巴进料压力下,二氧化碳渗透率为30巴雷尔,二氧化碳/氮气选择性为21)。还开发了支撑型Pebax® 1041膜以减小Pebax®的厚度(在1.5 - 10μm范围内),从而获得更高的渗透通量。这些膜通过相转化过程制备,该过程包括将Pebax® 1041/DMAc溶液在水中沉淀并分散形成稳定乳液,然后将其滴铸在聚砜(PSF)不对称支撑体上。干燥后,聚合物形成致密连续层。相转化方法比溶剂蒸发“更环保”,因为在膜制备过程中二甲基乙酰胺不会以有毒蒸汽形式释放。滴铸量导致选择性层厚度不同,通过在聚合物乳液中分散多壁碳纳米管(MWCNTs)可增强这一效果。通过热重分析和测量膜表面接触角研究了Pebax®选择性层的性能,在二氧化碳渗透通量为3.0 GPU时获得了最佳二氧化碳/氮气选择性(22.6)。