广东电力
廣東電力
엄동전력
GUANGDONG ELECTRIC POWER
2014年
11期
41-46
,共6页
碳捕集技术%燃煤烟气%N-甲基环己胺%甲基咪唑离子液体
碳捕集技術%燃煤煙氣%N-甲基環己胺%甲基咪唑離子液體
탄포집기술%연매연기%N-갑기배기알%갑기미서리자액체
CO2 capture%coal-fired flue gas%N-methylcyclohexylamine%imidazolium based ionic liquids
为了提高碳捕集技术吸收效率、降低再生能耗、避免二次污染,提出一种利用 N-甲基环己胺 MCA水溶液及甲基咪唑离子液体混合吸收二氧化碳(CO2)的方法以实现燃煤电厂烟气碳减排,并分别开展了基于 MCA水溶液·1-丁基-3-甲基咪唑四硼氟酸盐[Bmim][BF4]体系和MCA水溶液·1-丁基-3-甲基咪唑醋酸盐[Bmim][OAc]体系的CO2吸收及再生性能实验。实验结果表明,10%MCA+10%H2 O+[Bmim][OAc]体系的吸收容量为0.369,吸收速率为5.83 g/(kg·min),优于工业常压吸收剂30%MEA水溶液;再生性能相较于10%MCA溶液明显改善。
為瞭提高碳捕集技術吸收效率、降低再生能耗、避免二次汙染,提齣一種利用 N-甲基環己胺 MCA水溶液及甲基咪唑離子液體混閤吸收二氧化碳(CO2)的方法以實現燃煤電廠煙氣碳減排,併分彆開展瞭基于 MCA水溶液·1-丁基-3-甲基咪唑四硼氟痠鹽[Bmim][BF4]體繫和MCA水溶液·1-丁基-3-甲基咪唑醋痠鹽[Bmim][OAc]體繫的CO2吸收及再生性能實驗。實驗結果錶明,10%MCA+10%H2 O+[Bmim][OAc]體繫的吸收容量為0.369,吸收速率為5.83 g/(kg·min),優于工業常壓吸收劑30%MEA水溶液;再生性能相較于10%MCA溶液明顯改善。
위료제고탄포집기술흡수효솔、강저재생능모、피면이차오염,제출일충이용 N-갑기배기알 MCA수용액급갑기미서리자액체혼합흡수이양화탄(CO2)적방법이실현연매전엄연기탄감배,병분별개전료기우 MCA수용액·1-정기-3-갑기미서사붕불산염[Bmim][BF4]체계화MCA수용액·1-정기-3-갑기미서작산염[Bmim][OAc]체계적CO2흡수급재생성능실험。실험결과표명,10%MCA+10%H2 O+[Bmim][OAc]체계적흡수용량위0.369,흡수속솔위5.83 g/(kg·min),우우공업상압흡수제30%MEA수용액;재생성능상교우10%MCA용액명현개선。
In order to improve absorption rate of CO2 capture technology,reduce regeneration energy consumption and a-void secondary pollution,a kind of method for absorbing CO2 by using blends of N-methylcyclohexylamine(MCA)and imid-azolium based ionic liquids so as to realize flue gas CO2 emission in coal-fired power plant. Tests on CO2 absorption and re-generation performance based on 1-buty1-3-methylimidazolium tetrafluoroborate-based system([Bmim][BF4])and 1-buty1-3-methylimizazaolium acetate([Bmim][OAc])system were developed. Results indicated that CO2 absorption capacity of 10%MCA+10%H2 O+[Bmim][OAc]system was 0.369 and absorption rate was 5.83 g/(kg ·min)which was superior to that of 30% MEA system. In addition,regeneration performance of this system was obviously improved compared with 1 0% MCA system.