作者: J.P. Van Der Sluijs , C.A. Hendriks , K. Blok
DOI: 10.1016/0196-8904(92)90040-4
关键词: Power station 、 Membrane 、 Materials science 、 Flue gas 、 Synthetic membrane 、 Waste management 、 Gas separation 、 Permeation 、 Carbon dioxide 、 Tonne 、 Fuel Technology 、 Renewable Energy, Sustainability and the Environment 、 Energy Engineering and Power Technology 、 Nuclear Energy and Engineering
摘要: Abstract The feasibility of polymer membranes for the recovery CO 2 from flue gases a power plant is examined. With computer program based on cross flow permeation model membranes, several parameters are optimized to obtain lowest specific mitigation costs. gas separation commercially available, minimum attainable costs calculated be US$48 per tonne avoided (at 50% purity, 75% recovery). When restrictions posed purity (95%) and degree (90%), this figure much higher: US$71 avoided. Cost reduction possibilities perspectives discussed. Our analyses shows that with selectivity at least 200 required make serious competitor other techniques.