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CO_2 RECOVERY PILOT PLANT

机译：CO_2回收飞行员

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The pilot plant in this study was using the recycle separation process adopted the absorption and stripping. Recovery of CO_2, one of the main parameters, was experimented at different temperatures and flow rates of flue gas and absorbent, Monoethanolamine (MEA). When the temperature of flue gas was increased by 10□ from 30□ to 40□, CO_2 recovery ratio was decreased by around 5%. When the flow rate of flue gas was increased to 690m~3/hr, equivalent to 120% of design value of pilot plant, CO_2 recovery ratio was decreased by around 15%. CO_2 recovery ratio was maintained stably at both 15wt% and 25wt% of MEA concentration over 2.5m~3/hr of MEA flow rate.
机译：本研究中的试验工厂使用回收分离过程采用了吸收和汽提。回收CO_2，其中一个主要参数之一，是在烟气和吸收剂，单乙醇胺（MEA）的不同温度和流速的不同温度和流速。当烟道气的温度从30℃增加10℃时，CO_2回收率下降约5％。当烟道气的流速增加至690m〜3 / hr时，相当于试验厂的120％的设计值，CO_2回收率减少了约15％。 CO_2回收率在15wt％和25wt％的MEA流速下稳定地保持在15wt％和25wt％的MEA浓度。

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