变压吸附
天然气
氢
吸附
压缩天然气
燃料气
氢燃料
巴(单位)
化学
膜技术
氢气净化器
工艺工程
膜
材料科学
化学工程
废物管理
制氢
工程类
物理
有机化学
气象学
燃烧
生物化学
作者
Werner Liemberger,Markus Groß,Martin Miltner,Michael Harasek
标识
DOI:10.1016/j.jclepro.2017.08.012
摘要
The current work presents a process that separates hydrogen from mixtures with natural gas transported in the natural gas grid. The aim is to achieve hydrogen at fuel cell quality (99.97% (v/v) according to ISO 14687-2:2012). Due to gas grid regulations in Austria the hydrogen content is limited to a maximum of 4% (v/v). In a hybrid approach based on membrane separation and pressure swing adsorption (PSA) the supplied high pressure hydrogen – natural gas mixture (up to 120 bar) is pre-enriched by membrane technology and further upgraded to the required quality by PSA. The majority of the feed gas is kept at grid pressure, which ensures a high energetic efficiency. The remaining components, separated by PSA, are re-compressed and returned to the grid. Beside the technological feasibility, the influence of various process parameters (e.g. stage-cut, permeate conditions, PSA hydrogen recovery) is analysed. Based on the results, the required amount of energy of 0.8–1.5 kWh/m3 (fuel-cell quality hydrogen at 25.81 bar(a)) is calculated for the so called HylyPure® process.
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