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ADSORPTION INTEGRATION UNDER VARIABLE PRESSURE WITH AN ENERGY INSTALLATION FOR CO2 COOLING / DISPOSAL AND N2 PRODUCTION

机译:具有能量安装的可变压力下的吸附集成,用于二氧化碳的冷却/处置和氮气的产生

摘要

1. A method of generating energy, comprising: compressing a recycle exhaust gas in a main compressor to produce a compressed recycle exhaust gas, wherein the compressed recycle exhaust gas has a recycle temperature of from about 400 ° C to about 500 ° C and a recycle pressure of from about 1.0 MPa abs . (about 10 bar abs.) to about 3.0 MPa abs. (about 30 bar abs), while the recirculated exhaust gas contains at least about 70 vol. % N and at least about 10 vol. % СО; compression of the enriched air in the inlet compressor to produce a compressed oxidizer; passing the first part of the compressed recycle exhaust gas into the combustion chamber; stoichiometric combustion of the compressed oxidizer and fuel in the combustion chamber in the presence of the first part of the compressed recycle exhaust gas, thereby obtaining a discharge stream, where the first part of the compressed recycle exhaust gas acts as a diluent designed to reduce the temperature of the discharge stream; expanding the discharge sweat in the expander for at least partially driving the main compressor and generating recirculated exhaust gas; passing a second part of the recirculated exhaust gas into the short-cycle adsorption reactor containing adsorbent material; adsorption of CO on the adsorbent material at an adsorption temperature that differs from the recycling temperature by less than about 20 ° C, and at an adsorption pressure that differs from the recycle pressure by less than about 0.1 MPa (about 1 bar); extract stream Nc purity of approximately 95 vol. %, from the front end of the reactor, and the extracted stream
机译:1.一种产生能量的方法,包括:在主压缩机中压缩再循环废气以产生压缩的再循环废气,其中所述压缩的再循环废气具有约400℃至约500℃的再循环温度和循环压力约为1.0 MPa(绝对)。 (约10 bar abs。)至约3.0 MPa abs。 (约30 bar abs),而再循环废气中至少包含约70 vol。 %N和至少约10 vol。 %СО;在入口压缩机中压缩浓空气以产生压缩的氧化剂;使压缩的再循环废气的第一部分进入燃烧室;在压缩再循环废气的第一部分存在的情况下,燃烧室中压缩氧化剂和燃料的化学计量燃烧,从而获得排放流,其中压缩再循环废气的第一部分用作稀释剂,旨在减少二氧化碳的排放。排放物流的温度;使膨胀机中的排出汗液膨胀,以至少部分地驱动主压缩机并产生再循环废气;使再循环废气的第二部分进入含有吸附剂材料的短循环吸附反应器;在与再循环温度相差小于约20℃的吸附温度和与再循环压力相差小于约0.1MPa(约1巴)的吸附压力下,CO在吸附剂材料上的吸附;萃取液流的Nc纯度约为95 vol。 %,从反应器的前端,和提取的流

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