Source Jouranl of CSCD
Source Journal of Chinese Scientific and Technical Papers
Included as T2 Level in the High-Quality Science and Technology Journals in the Field of Environmental Science
Core Journal of RCCSE
Included in the CAS Content Collection
Included in the JST China
Indexed in World Journal Clout Index (WJCI) Report
YANG De-yu, HAO Qing-lan, ZHAO Chen-chen, YAN Ning-na, DOU Bao-juan. CATALYTIC DEGRADATION PERFORMANCE OF TOLUENE OVER CuxMn1-xCe0.75Zr0.25Oy[J]. ENVIRONMENTAL ENGINEERING , 2021, 39(1): 96-100. doi: 10.13205/j.hjgc.202101014
Citation: BAI Yongfeng, WANG Zhengrong, ZHAN Guoxiong, CHEN Zhen, LI Junhua. SIMULATION AND OPTIMIZATION OF CARBON CAPTURE IN COAL-FIRED FLUE GAS[J]. ENVIRONMENTAL ENGINEERING , 2023, 41(9): 61-71. doi: 10.13205/j.hjgc.202309008

SIMULATION AND OPTIMIZATION OF CARBON CAPTURE IN COAL-FIRED FLUE GAS

doi: 10.13205/j.hjgc.202309008
  • Received Date: 2023-04-03
    Available Online: 2023-11-15
  • A 10000 t/a amine-based carbon capture device was designed and constructed in a power plant, using blend amine solvent. Under the design conditions, the flue gas flow was 5877 Nm3/h, the solvent circulating flow was 37500 kg/h, the capture efficiency reached 97% above, and the CO2 output was not less than 1.39 t/h; the energy consumption for solvent regeneration decreased by 23%, compared with the traditional monoethanolamine (MEA) solvent. According to the engineering design parameters, the detailed carbon capture process was modelled, and the results reveal relative error was less than 3%, between the key parameters of the modelling and the engineering values. Furthermore, some energy-saving technologies were designed and investigated, including liquid-rich separation, interstage cooling and MVR flash. The effects of energy-saving process parameters were comprehensively explored, such as liquid-rich separation rate, interstage cooling rate and vacuum degree on energy consumption and benefits of the carbon capture system. The results showed that MVR technology could reduce the energy consumption of capture by 15.45%, and then the energy-saving effect was the best, the energy-saving effect of rich liquid diversion and interstage cooling was in a range of 2% to 4.5%. The energy-saving effect was further improved by the combined use of various technologies and optimization of operating parameters. Their energy-saving effect ranked as:interstage cooling+MVR heat pump technology>rich liquid shunt+MVR heat pump technology>energy-saving effect of interstage cooling+rich liquid shunt. The results of this study could provide some guidance for the process system design, energy saving and operation of flue gas carbon capture projects in coal-fired power plants.
  • [1]
    MASSON-DELMOTTE V,ZHAI P,PÖRTNER H,et al. Global Warming of 1.5℃[M/OL]. An IPCC Special Report:Summary for Policy makers; Intergovernmental Panel on Climate Change (IPCC):Geneva,2018.
    [2]
    习近平在第七十五届联合国大会一般性辩论上发表重要讲话[N/OL].新华网.[2020-09-22]. http://www.xinhuanet.com/politics/leaders/2020-09/22/c_1126527647.htm.
    [3]
    国务院新闻办公室. 强化应对气候变化行动:中国国家自主贡献[EB/OL].(2015-11-18) [2020-01-08]. http://www.scio.gov.cn/xwfbh/xwbfbh/wqfbh/35861/37265/xgzc37271/Document/1603661/1603661.htm.
    [4]
    于方,宋宝华. 二氧化碳捕集技术发展动态研究[J].中国环保产业, 2009(10):27-30.
    [5]
    康重庆,陈启鑫,夏清. 应用于电力系统的碳捕集技术及其带来的变革[J]. 电力系统自动化, 2010, 34(1):1-7.
    [6]
    科学技术部社会发展科技司,中国21世纪议程管理中心.应对气候变化国家研究进展报告2019[M]. 北京:科学出版社, 2019.
    [7]
    乌若思,苏文斌,郑松. 挑战全球气候变化:二氧化碳捕集与封存[M]. 北京:中国水利水电出版社, 2008:1-58.
    [8]
    LI K K, LEIGH W, FERON P, et al. Systematic study of aqueous monoethanolamine (MEA)-based CO2 capture process:techno-economic assessment of the MEA process and its improvements[J]. Applied Energy, 2016, 165:648-659.
    [9]
    OH S Y, KIM J K. Operational optimization for part-load performance of amine-based post-combustion CO2 capture processes[J]. Energy, 2018, 146:57-66.
    [10]
    THIRUVENKATACHARI R, SU S, AN H,et al. Post combustion CO2 capture by carbon fibre monolithicadsorbents[J].Progress in Energy and Combustion Science,2009(35):438-455.
    [11]
    MUCHAN P, NARKU-TETTEH J, SAIWAN C, et al. Effect of number of amine groups in aqueous polyamine solution on carbon dioxide (CO2) capture activities[J]. Separation and Purification Technology, 2017, 184:128-134.
    [12]
    XIAO S N, LIU H L, GAO H X, et al. Kinetics and mechanism study of homogeneous reaction of CO2 and blends of diethanolamine and monoethanolamine using the stopped-flow technique[J]. chemical engineering journal, 2017, 316:592-600.
    [13]
    JIANG G D, HUANG Q L, KENARSARI S D. A new mesoporous amine-TiO2 based pre-combustion CO2 capture technology[J]. Appl. Energy, 2015, (147):214-223.
    [14]
    方梦祥, 周旭萍, 王涛. 等. CO2化学吸收剂[J]. 化学进展, 2015, 27(12):1808-1814.
    [15]
    KELVIN O Y, MICHAEL O D, PATRICK T S, et al. Advances and emerging techniques for energy recovery during absorptive CO2 capture:a review of process and non-process integration-based strategies[J]. Renewable and Sustainable Energy Reviews, 2021,147, 1364-0321.
    [16]
    MAEDA K, OWADA M,KIMURA N,et al. CO2 fixation from the flue gas on coal-fired thermal power plant by microalgae[J]. Energy Convers Manage, 1995, 36(69):717-720.
    [17]
    OH S Y, BINNS M, CHO H, et al. Energy minimization of MEA-based CO2 capture process[J]. Applied Energy, 2016, 169:353-362.
    [18]
    FYTIANOS G, UCAR S, GRIMSTVEDT A, et al. Corrosion and degradation in MEA based post-combustion CO2 capture[J]. International Journal of Greenhouse Gas Control, 2016, 46:48-56.
    [19]
    LIU J, WANG S J, ZHAO B, et al. Absorption of CO2 in aqueous ammonia[J]. Energy Procedia, 2009, 1(1):933-940.
    [20]
    KNUUTILA H, SVENDSEN H F, ANTTILA M. CO2 capture from coal-fi red power plants based on sodium carbonate slurry:a systems feasibility and sensitivity study[J]. International journal of greenhouse gas control, 2009(3):143-151.
    [21]
    WANG R J, LIU S S, LI Q W, et al. CO2 capture performance and mechanism of blended amine solvents regulated by N-methyl cyclohexyamine[J]. Energy, 2021, 215(Part B):119209.
    [22]
    IDEM R, GELOWITZ D, TONTIWACHWUTHIKUL P. Evaluation of the performance of various amine-based solvents in an optimized multipurpose technology development pilot plant[J]. Energy Procedia, 2009, 1:1543-1548.
    [23]
    YU K, CURCIC I, GABRIEL J, et al. Recent advances in CO2 capture and utilization[J]. Chem Sus Chem, 2008, 1:893-899.
    [24]
    安山龙, 汪黎东, 于松华. 相变溶剂捕集CO2技术的研究进展[J]. 化工环保, 2017, (1):31-37.
    [25]
    BLANCHARD L A, DAN H, BECKMAN E J, et al. Green processing using ionic liquids and CO2[J]. Nature, 1999, 399(6731):28-29.
    [26]
    樊丽华,聂阳,梁英华. 离子液体吸收CO2的研究进展[J]. 化工环保, 2010, 30(2):136-140.
    [27]
    ZHANG X, FU K, LIANG Z, et al. Experimental studies of regeneration heat duty for CO2 desorption from diethylenetriamine (DETA) solution in a stripper column packed with dixon ring random packing[J]. Fuel, 2014, 136:261-267.
    [28]
    KOTHANDARAMAN A, NORD L, BOLLAND O, et al. Comparison of solvents for post-combustion capture of CO2 by chemical absorption[J].Energy Procedia,2009(1):1373-1380.
    [29]
    杜云贵, 辜敏, 刘涛. 捕集二氧化碳气体的复合胺及复合胺吸收剂:重庆,CN102218254A[P]. 2011-10-19.
    [30]
    白亚开. 基于乙醇胺法与氨水法碳捕集能耗特性分析与系统优化[D]. 保定:华北电力大学, 2015:66.
    [31]
    郭宇红. 燃煤电厂碳捕集技术及节能优化研究进展[J]. 山西电力, 2021(6):46-49.
    [32]
    KIM H, HWANG S J, LEE K S. Novel shortcut estimation method for regeneration energy of amine solvents in an absorption-based carbon capture process[J]. Environmental Science & Technology, 2015, 49(3):1478-1485.
    [32]
    YU C H, HUANG C H, TAN C S. A review of CO2 capture by absorption and desorption[J]. Aerosol and Air Quality Research, 2012, 12(5):745-769.
    [33]
    RAZA A, GHOLAMI R, REZAEE R, et al. Significant aspects of carbon capture and storage:a review[J]. Petroleum, 2019,5(4):335-340.
    [34]
    van den BROEK M, HOEFNAGELS R, RUBIN E,et al. Effects of technological learning on future cost and performance of power plants with CO2 capture[J]. Progress in Energy and Combustion Science, 2099, 35(1):457-480.
  • Relative Articles

    [1]YAO Haiqian, GUO Xinchao, FU Fengman, YANG Hao, GUO Xiang, ZHANG Fanghong. Mn-Fe-Ce/GAC CATALYZED OZONE OXIDATION TECHNOLOGY FOR ANILINE WASTEWATER[J]. ENVIRONMENTAL ENGINEERING , 2024, 42(5): 28-34. doi: 10.13205/j.hjgc.202405004
    [2]LI Ru, LI Xiaokang, FENG Yan, WANG Xueyan, XING Qianyun. DEGRADATION OF XYLENE BY DBD PLASMA IN COLLABORATION WITH Mn-TiO2/γ-Al2O3 CATALYST[J]. ENVIRONMENTAL ENGINEERING , 2024, 42(4): 157-166. doi: 10.13205/j.hjgc.202404019
    [3]WANG Chengcheng, LI Qian, ZHAO Shuguang, SONG Leshan, LIU Hua, ZHANG Ying, LIU Si. PREPARATION AND ELECTRO-CATALYTIC PERFORMANCE OF LEAD-ANTIMONY ELECTRODE WITH A TIN-ANTIMONY INTERMEDIATE LAYER[J]. ENVIRONMENTAL ENGINEERING , 2024, 42(3): 92-98. doi: 10.13205/j.hjgc.202403011
    [4]LI Haicheng, CHENG Cheng, CHEN Zhenglin, YANG Lixia, LUO Shenglian. SULFIDE ION DOPING PROMOTES EFFICIENT PHOTOCATALYTIC DEGRADATION OF TOLUENE BY WO3 NANOWIRES[J]. ENVIRONMENTAL ENGINEERING , 2024, 42(9): 201-210. doi: 10.13205/j.hjgc.202409019
    [5]WU Xinming, AN Hao, ZHAO Junyu, OU Zixuan, HAO Liangshan, LI Chao. PREPARATION OF Fe/Mn-PAC CATALYSTS AND DEGRADATION OF REACTIVE BRILLIANT BLUE KN-R BY CATALYTIC OZONATION[J]. ENVIRONMENTAL ENGINEERING , 2023, 41(4): 32-39. doi: 10.13205/j.hjgc.202304005
    [6]YANG Jiani, ZHAO Baowei, YANG Maoying, SUO Jinmiao, ZHU Zhengyu, DENG Aiqin. PREPARATION OF Fe/C CATALYST BASED ON FERRIC CITRATE AND ITS ACTIVATION PERFORMANCE ON PEROXYDISULFATE TO DEGRADE SULFADIAZINE[J]. ENVIRONMENTAL ENGINEERING , 2023, 41(7): 116-123,251. doi: 10.13205/j.hjgc.202307016
    [7]ZHAO Ying, LIU Qingliang, WANG Shuo, SUN Zhiqiang, MA Jun. MECHANISM OF PEROVSKITE LaBO3 CATALYZED PEROXYACETIC ACID DEGRADATION OF BISPHENOL A IN WATER[J]. ENVIRONMENTAL ENGINEERING , 2023, 41(12): 1-10. doi: 10.13205/j.hjgc.202312001
    [8]LIU Dong, QI Junwen, XU Zunzhu, ZHANG Jiwen, JIN Xiaoxian, LI Jiansheng. ADSORPTION PERFORMANCE OF TOLUENE ON HYDROPHOBIC MODIFIED MOLECULAR SIEVES UNDER HIGH HUMIDITY[J]. ENVIRONMENTAL ENGINEERING , 2023, 41(2): 66-72,81. doi: 10.13205/j.hjgc.202302010
    [9]FENG Chao, XIONG Gaoyan, WANG Yunxia, PAN Yuan, LIU Yunqi. SYNTHESIS OF CuO-Cu1.5Mn1.5O4 COMPOSITE OXIDE BY USING A BIMETALLIC ORGANIC FRAMEWORK FOR CATALYTIC PROPANE TOTAL OXIDATION[J]. ENVIRONMENTAL ENGINEERING , 2022, 40(8): 69-77. doi: 10.13205/j.hjgc.202208009
    [10]ZHANG Shicheng, LI Simin, ZHU Jia. DEGRADATION OF METHYL ORANGE BY CuO/g-C3N4 ACTIVATED PEROXODISULFATE[J]. ENVIRONMENTAL ENGINEERING , 2022, 40(10): 40-48. doi: 10.13205/j.hjgc.202210006
    [11]SHANG Xiao-han, ZHU Xiao-biao. HETEROGENEOUS FENTON DEGRADATION OF BENZOTRIAZOLE IN WATER BY Fe/Cu/ZEOLITE CATALYST AT NEUTRAL pH VALUE[J]. ENVIRONMENTAL ENGINEERING , 2021, 39(2): 10-15. doi: 10.13205/j.hjgc.202102002
    [12]ZHANG Kai, YANG Shi-chao, LUO Min, WU Yan-heng, YU Su-ying. PREPARATION OF NANO-SHEET ZSM-5 ZEOLITE AND ITS ADSORPTION PROPERTIES FOR INDOOR ENVIRONMENT VOCs[J]. ENVIRONMENTAL ENGINEERING , 2020, 38(1): 60-64,74. doi: 10.13205/j.hjgc.202001009
  • Cited by

    Periodical cited type(7)

    1. 黄威翔,高川作,吴波,陈坦,杨婷,张冰. 基于STIRPAT模型的广西碳达峰路径. 环境科学. 2025(02): 682-695 .
    2. 姜江. 水泥工业碳排放的影响因素量化研究. 环境科学与管理. 2025(02): 52-55+88 .
    3. 王思琪. 基于GDIM的京津冀公共建筑碳排放影响因素分析. 上海节能. 2025(03): 404-413 .
    4. 李菲菲,徐绘薇,崔金栋. 基于STIRPAT模型的吉林省石化行业碳排放影响因素研究. 综合智慧能源. 2024(08): 12-19 .
    5. 李艳芳,张蒙悯,吴桂君,蒋嘉伟,方芳. 河北省建筑业碳排放脱钩及影响因素研究. 河北企业. 2024(09): 59-63 .
    6. 吴永江. 基于LMDI模型的高铁客运站碳排放关键驱动因素研究. 铁道建筑技术. 2024(09): 29-31+64 .
    7. 高立兵. 基于LMDI的甘肃省工业碳排放现状及影响因子分解研究. 科技创新与生产力. 2024(10): 67-70 .

    Other cited types(27)

  • Created with Highcharts 5.0.7Amount of accessChart context menuAbstract Views, HTML Views, PDF Downloads StatisticsAbstract ViewsHTML ViewsPDF Downloads2024-052024-062024-072024-082024-092024-102024-112024-122025-012025-022025-032025-04010203040
    Created with Highcharts 5.0.7Chart context menuAccess Class DistributionFULLTEXT: 28.0 %FULLTEXT: 28.0 %META: 71.0 %META: 71.0 %PDF: 1.0 %PDF: 1.0 %FULLTEXTMETAPDF
    Created with Highcharts 5.0.7Chart context menuAccess Area Distribution其他: 10.8 %其他: 10.8 %China: 0.3 %China: 0.3 %[]: 0.3 %[]: 0.3 %临汾: 0.1 %临汾: 0.1 %北京: 1.6 %北京: 1.6 %南宁: 0.1 %南宁: 0.1 %南昌: 0.1 %南昌: 0.1 %南通: 0.4 %南通: 0.4 %卡拉奇: 0.3 %卡拉奇: 0.3 %台州: 0.1 %台州: 0.1 %咸阳: 0.1 %咸阳: 0.1 %哈尔滨: 0.1 %哈尔滨: 0.1 %嘉兴: 0.1 %嘉兴: 0.1 %太原: 0.9 %太原: 0.9 %宣城: 0.1 %宣城: 0.1 %常德: 0.1 %常德: 0.1 %广州: 0.7 %广州: 0.7 %张家口: 0.4 %张家口: 0.4 %成都: 0.3 %成都: 0.3 %扬州: 0.3 %扬州: 0.3 %昆明: 0.4 %昆明: 0.4 %晋城: 0.3 %晋城: 0.3 %朝阳: 0.1 %朝阳: 0.1 %杭州: 0.4 %杭州: 0.4 %武汉: 0.1 %武汉: 0.1 %济源: 0.3 %济源: 0.3 %湖州: 0.6 %湖州: 0.6 %漯河: 0.1 %漯河: 0.1 %芒廷维尤: 72.0 %芒廷维尤: 72.0 %芝加哥: 0.6 %芝加哥: 0.6 %苏州: 0.1 %苏州: 0.1 %衢州: 0.1 %衢州: 0.1 %西宁: 3.4 %西宁: 3.4 %贵阳: 0.1 %贵阳: 0.1 %运城: 1.3 %运城: 1.3 %遵义: 0.1 %遵义: 0.1 %邯郸: 0.1 %邯郸: 0.1 %郑州: 0.4 %郑州: 0.4 %重庆: 0.1 %重庆: 0.1 %长沙: 0.3 %长沙: 0.3 %长治: 0.1 %长治: 0.1 %青岛: 0.4 %青岛: 0.4 %其他China[]临汾北京南宁南昌南通卡拉奇台州咸阳哈尔滨嘉兴太原宣城常德广州张家口成都扬州昆明晋城朝阳杭州武汉济源湖州漯河芒廷维尤芝加哥苏州衢州西宁贵阳运城遵义邯郸郑州重庆长沙长治青岛

Catalog

    通讯作者: 陈斌, bchen63@163.com
    • 1. 

      沈阳化工大学材料科学与工程学院 沈阳 110142

    1. 本站搜索
    2. 百度学术搜索
    3. 万方数据库搜索
    4. CNKI搜索

    Article Metrics

    Article views (250) PDF downloads(10) Cited by(34)
    Proportional views
    Related

    /

    DownLoad:  Full-Size Img  PowerPoint
    Return
    Return