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首页> 外文期刊>Chemical Engineering and Processing >Carbon-rich solvent regeneration in solvent-based post-combustion CO2 capture process (PCCC): Process intensification by megasonics
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Carbon-rich solvent regeneration in solvent-based post-combustion CO2 capture process (PCCC): Process intensification by megasonics

机译:富含溶剂的溶剂溶剂再生在溶剂的后燃烧二氧化碳捕获过程(PCCC)中:摩中的过程强化

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摘要

Global greenhouse gas emanations from fossil-fuel combusting for power-generation alone contribute 9.795 gigatonnes (Gt) in 2014. There is a tremendous focus on global carbon capture researchers to cut down these emissions significantly. Chemical absorption is widely used and the use of monoethanolamine (MEA) was generally preferred. However, MEA solutions were not without problems. For example, equipment deterioration due to O-2 presence, high energy for solvent-regeneration, solvent degradation and formation of undesired harmful by-products inhibits the solvent's cyclic capacity. To address these issues megasonics-assisted (1 MHz tank-type) solvent regeneration process had been investigated experimentally. The results revealed that low regeneration temperature (< 45 degrees C), less condenser duty, the potential for sensible heat saving, no reboiler is required facilitates capital and maintenance saving, no significant colour change after regeneration and loss of absorption capacity after regeneration was 3.7 times lower than the conventional. In addition, similar regeneration energy (20.20 KJ/mol CO2) but with 3.5 times lower nominal power input than the conventional regeneration method. Furthermore, physicochemical characterization of the solvent before and after absorption and regeneration followed by C-13 NMR spectra analysis was also discussed.
机译:2014年,来自化石燃料燃烧的全球温室气体燃烧燃烧电力发电贡献了9.795年Gigatonnes(GT)。在全球碳捕获研究人员上有一个巨大的重点是显着减少这些排放。广泛使用化学吸收,通常优选使用单乙醇胺(MEA)。然而,MEA解决方案并非没有问题。例如,由于O-2存在的设备劣化,用于溶剂再生的高能量,溶剂降解和不需要的有害副产物的形成抑制了溶剂的循环能力。为了解决这些问题,通过实验研究了巨大的辅助(1 MHz Tank-Type)溶剂再生过程。结果表明,低再生温度(<45℃),较少的冷凝器占性能,可清热的可能性,无需再沸器,便于资本和维护,再生后没有显着的颜色变化,再生后的吸收能力损失为3.7时间低于常规。此外,类似的再生能量(20.20kJ / mol CO2),但具有比常规再生方法更低的标称功率输入的3.5倍。此外,还讨论了吸收和再生之后的溶剂和再生后的溶剂的物理化学表征,其次是C-13 NMR光谱分析。

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