Inorganic Chemicals Industry ›› 2023, Vol. 55 ›› Issue (4): 38-44.doi: 10.19964/j.issn.1006-4990.2022-0467

• Research & Development • Previous Articles     Next Articles

Study on preparation,evaluation and application of new low-carbon emission nano calcium hydroxide desulfurizer

YAO Yong1(), LI Shizhu1, ZHENG Dongchen2, ZENG Tinghua3, WU Zhichao1, YU Chi1, LIU Faqian2()   

  1. 1. Guangdong Energy Group Science and Technology Research Institute Co. ,Ltd. ,Guangzhou 510630,China
    2. School of Chemical Engineering and Technology,Sun Yat-sen University,Zhuhai 519082,China
    3. China Southern Power Grid Power Technology Co. ,Ltd. ,Guangzhou 510180,China
  • Received:2022-08-06 Online:2023-04-10 Published:2023-04-13

Abstract:

In the traditional limestone-gypsum wet flue gas desulfurization(FGD) process,the reaction of limestone and SO2 generate a large amount of CO2,which is not favorable to the realization of “carbon peaking” and “carbon neutralization”.By using cheap starting materials and in the presence of polyethyleneimine(PEI),a series of nanoscale Ca(OH)2 were prepared to replace traditional limestone for FGD process.The samples were characterized by SEM,XRD,BET,and FT-IR.The effects of Ca(OH)2 with different specific surface area and limestone on SO2 adsorption rate and desulfurization efficiency were studied in a simulated experimental device.The results showed that when the inlet SO2 concentration was 3 500 mg/Nm3,the desulfurization efficiency was increased from 93.05% of limestone to 99.31% of Ca(OH)2.The actual desulfurization effect of the new nano Ca(OH)2 desulfurizer was studied by using the wet desulfurization device of Shaoguan Power Plant Unit 1(600 MW).The results showed that the limestone could not meet the requirements of ultra-low emission by using high sulfur coal,but after adding part of Ca(OH)2(18.0%~22.5%),the ultra-low emission could be achieved(the outlet SO2 concentration was less than 35 mg/Nm3),and the desulfurization efficiency was all higher than 99%,thus improving the adaptability of FGD system to high sulfur coal.

Key words: nano calcium hydroxide, power plant desulfurization, polyethyleneimine, specific surface area

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