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蒸汽活化对天然钙基吸收剂循环碳酸化捕获CO_2的影响 被引量:3

Effect of Steam Hydration on the Natural CaO-Based Sorbent for Cyclic CO_2 Capture
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摘要 为探明蒸汽活化对钙基CO_2吸收剂活性再生的影响规律,基于热天平系统研究了活化温度、蒸汽浓度、操作频率、碳酸化及蒸汽活化时间以及活化方法对天然钙基吸收剂CO_2捕获性能的影响.结果表明,300~400,℃对天然吸收剂活化效果最优;提高活化水蒸气浓度和频率有利于再生吸收剂碳捕获性能;短时间活化效果低于长时间活化工况;煅烧后水蒸气活化可大幅再生吸收剂活性,而在反应过程中通入蒸汽活化效果不佳;从捕获总量和活化效率考量,高频率短循环方式活化效果更佳. To study the steam reactivation of natural Ca-based sorbent,the influences of steam hydration temperature,steam concentration,hydration frequency,hydration duration and reactivation strategy on the cyclic carbonation/ calcination performance were investigated by using TGA.The results show that the hydration temperature of 300—400,℃ is superior to 500,℃ for natural sorbents reactivation.Carbonation conversion increases with the rise of steam concentration,hydration frequency and hydration duration.Steam hydration after every calcination could regenerate sorbent reactivity more remarkably than steam injection in carbonation and calcination process. Short cycle with high frequency hydration shows the best performance regarding the amount of CO2 capture and reactivation efficiency.
作者 荣鼐 樊宏韬 王勤辉 方廷勇 朱曙光 王晏平 王庚 Rong Nai1,Fan Hongtao2,Wang Qinhui2,Fang Tingyong1,Zhu Shuguang1,Wang Yanping1,Wang Geng1(1.Anhui Advanced Technology Research Institute of Green Building,Anhui Jianzhu University,Hefei 230601,China;2.State Key Laboratory of Clean Energy Utilization,Zhejiang University,Hangzhou 310027,Chin)
出处 《燃烧科学与技术》 EI CAS CSCD 北大核心 2018年第3期245-251,共7页 Journal of Combustion Science and Technology
基金 国家自然科学基金资助项目(51706002) 安徽省高校自然科学基金资助项目(KJ2016A148) 国家国际科技合作专项资助项目(2016YFE0102500) 国家重点研发计划资助项目(2017YFC0702900)
关键词 CO2捕获 钙基吸收剂 蒸汽活化 水合 再生 CO2 capture;Ca-based sorbent;steam reactivation;hydration;reactivation
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  • 1夏熙.二氧化锰的物理、化学性质与其电化学活性的相关(4)[J].电池,2006,36(3):195-198. 被引量:6
  • 2张洪流,陈明功.错流碟片式旋转超重力场强化氨水吸收燃煤烟气中CO_2的研究[J].煤炭学报,2007,32(7):748-752. 被引量:6
  • 3Abanades J C, Grasa G,Alonso M, et al. Cost structure of a postcombustion CO2 capture system using CaO [J]. Environ. Sci. Tehnol. , 2007,41 (15) :5 523-5 527.
  • 4Shimizu T,Hirama T,Hosoda H,et al. A twin fluid-bed reactor for removal of CO2 from combustion processes[ J]. Trans. I. Chem. E. , 1999,77( a1 ) :62-68.
  • 5Blarney J, Anthony, Wang J, et al. The calcium looping cycle for large-scale CO2 capture [ J ]. Progress in Energy and Combustion Science, 2010,36 : 260 - 279.
  • 6Wang J S, Anthoy E J, Abanades J C, et al. Clean and efficient use of petroleum coke for combustion and power generation [ J ]. Fuel, 2004,83(10) :1 341-1 348.
  • 7Lin S Y, Suzuki Y, Hatano H. Developing an innovative method HyPr-RING, to produce hydrogen from hydrocarbons [ J ]. Energy Conversion and Management,2002,43(9-12) :1 283-1 290.
  • 8Goldberg P, Chen Z Y, Connor W, et al. CO2 mineral sequestration studies in US [ A ]. Proceedings of 1 st National Conference on Carbon Sequestration[ C ]. Washington D C ,2001.
  • 9Wang J S,Anthony E J,Abanades J C. A simulation study for fluidized bed combustion of petroleum coke with CO2 capture [ A ]. Proceeding of 17^th International Fluidized Bed Combustion Conference [ C ]. Jacksonville, USA ,2003.
  • 10Li Y J,Zhao C S, Chen H C, et al. Modified CaO-based sorbent looping cycle for CO2 mitigation [ J ]. Fuel,2009,88 (4) :697-704.

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