TY - JOUR
T1 - Deactivation and Regeneration of Commercial SCR Catalysts Used in a 660 MW Coal-Fired Power Plant
AU - Zhang, Pei
AU - Wu, Si Ming
AU - Fang, Tuo Tuo
AU - Chen, Yan Ping
AU - Shi, Yao
AU - He, Yi
N1 - Publisher Copyright:
© 2017, Editorial Board of “Journal of Chemical Engineering of Chinese Universities”. All right reserved.
PY - 2017/10/1
Y1 - 2017/10/1
N2 - Used commercial SCR catalysts (30000 hours) obtained from a 660 MW coal-fired plant in Zhejiang Province (China) were examined by SEM, BET, NH3-TPD, XRF and XPS to investigate their deactivated and regeneration mechanisms. Fresh commercial SCR catalysts were chosen for comparison. The results indicate that depositions containing salts of alkali metals (K and Na) and compounds of arsenic and ammonium sulfate block pores of the catalyst, which decreases its BET surface. Moreover, the acidity of the SCR catalysts decreases due to the reaction of metal ions with activated acidic sites on the SCR catalyst surface. After catalyst regeneration with 0.5 mol·L-1 dilute sulphuric acid, the activity of denitration increases from 42.62% to 78.30% at 350℃. Regeneration by pickling can effectively remove alkali metals from the surface of the catalysts, which also has certain effects in the removal of arsenic and ammonium sulfate. In addition, the augment of acidity and the increase of chemical adsorption oxygen proportion were examined after pickling, which are found beneficial to increase activity of deactivated commercial SCR catalysts for denitration.
AB - Used commercial SCR catalysts (30000 hours) obtained from a 660 MW coal-fired plant in Zhejiang Province (China) were examined by SEM, BET, NH3-TPD, XRF and XPS to investigate their deactivated and regeneration mechanisms. Fresh commercial SCR catalysts were chosen for comparison. The results indicate that depositions containing salts of alkali metals (K and Na) and compounds of arsenic and ammonium sulfate block pores of the catalyst, which decreases its BET surface. Moreover, the acidity of the SCR catalysts decreases due to the reaction of metal ions with activated acidic sites on the SCR catalyst surface. After catalyst regeneration with 0.5 mol·L-1 dilute sulphuric acid, the activity of denitration increases from 42.62% to 78.30% at 350℃. Regeneration by pickling can effectively remove alkali metals from the surface of the catalysts, which also has certain effects in the removal of arsenic and ammonium sulfate. In addition, the augment of acidity and the increase of chemical adsorption oxygen proportion were examined after pickling, which are found beneficial to increase activity of deactivated commercial SCR catalysts for denitration.
KW - Coal-fired plant
KW - Deactivation mechanism
KW - Denitration catalysts
KW - Pickling regeneration
KW - SCR
UR - http://www.scopus.com/inward/record.url?scp=85033687093&partnerID=8YFLogxK
U2 - 10.3969/j.issn.1003-9015.2017.05.023
DO - 10.3969/j.issn.1003-9015.2017.05.023
M3 - 文章
AN - SCOPUS:85033687093
SN - 1003-9015
VL - 31
SP - 1186
EP - 1192
JO - Gao Xiao Hua Xue Gong Cheng Xue Bao/Journal of Chemical Engineering of Chinese Universities
JF - Gao Xiao Hua Xue Gong Cheng Xue Bao/Journal of Chemical Engineering of Chinese Universities
IS - 5
ER -