Giordano Lorena, Roizard Denis, Bounaceur Roda, Favre Eric
Laboratoire Réactions et Génie des Procédés (LRGP) (UMR 7274), Université de Lorraine, France.
Data Brief. 2016 Oct 26;9:776-780. doi: 10.1016/j.dib.2016.10.019. eCollection 2016 Dec.
The article describes data concerning the separation performances of polymeric hollow-fiber membranes. The data were obtained using a model for simulating gas separation, described in the research article entitled "Interplay of inlet temperature and humidity on energy penalty for CO post-combustion capture: rigorous analysis and simulation of a single stage gas permeation process" (L. Giordano, D. Roizard, R. Bounaceur, E. Favre, 2016) [1]. The data were used to validate the model by comparison with literature results. Considering a membrane system based on feed compression only, data from the model proposed and that from literature were compared with respect to the molar composition of permeate stream, the membrane area and specific energy requirement, varying the feed pressure and the CO separation degree.
本文描述了有关聚合物中空纤维膜分离性能的数据。这些数据是使用一个模拟气体分离的模型获得的,该模型在题为《入口温度和湿度对燃烧后二氧化碳捕集能量损失的相互作用:单级气体渗透过程的严格分析与模拟》(L. 乔达诺、D. 罗伊扎德、R. 布纳瑟尔、E. 法夫尔,2016年)[1]的研究文章中有描述。通过与文献结果进行比较,这些数据被用于验证该模型。仅考虑基于进料压缩的膜系统,将所提出模型的数据和文献数据就渗透物流的摩尔组成、膜面积和比能量需求进行了比较,同时改变进料压力和二氧化碳分离程度。