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锰铈脱硝催化剂的制备及其再生性能研究
引用本文:樊恩亚,卫平波,眭国荣,陈朗,徐凌,谢慧,沈树宝,祝社民.锰铈脱硝催化剂的制备及其再生性能研究[J].环境科学与技术,2012(9):40-44.
作者姓名:樊恩亚  卫平波  眭国荣  陈朗  徐凌  谢慧  沈树宝  祝社民
作者单位:中石化扬子石化分公司;南京工业大学材料科学与工程学院;江苏华尔润集团有限公司;南京工业大学制药与生命科学学院
基金项目:国家自然科学基金项目(50872052)
摘    要:采用等体积浸渍法制备了一系列Mn-Ce-Ox复合氧化物脱硝催化剂用于NH3选择性催化还原(NH3-SCR)NO。考察了Mn/Ce摩尔比、焙烧温度、H2O和SO2对Mn-Ce-Ox复合氧化物脱硝催化剂活性的影响及催化剂中毒再生性能。结果表明:当NH3:NO=1:1,空速为5 000 h-1,550℃焙烧制得的Mn/Ce摩尔比为5∶1的Mn-Ce-Ox复合脱硝催化剂活性最佳,活性温度窗口为100~260℃,在此温度区间内催化剂活性大于90%。200℃时,Mn-Ce-Ox复合催化剂活性最高为97.84%;在10%(V/V)H2O蒸汽和300×10-6SO2共存条件下,200℃时,催化剂活性在开始反应2.5 h内迅速下降至53%左右,并在之后的6 h内没有明显变化;中毒催化剂经常温水洗再生处理、质量分数为3%的硝酸溶液再生处理和550℃焙烧2 h再生处理后200℃活性均能恢复到90%以上,其中中毒催化剂经质量分数为3%硝酸处理后活性恢复率最高。

关 键 词:选择性催化还原  Mn-Ce-Ox复合脱硝催化剂  脱硝  再生

Preparation of Mn-Ce-O_x Denitration Catalyst and Its Regeneration Performance
FAN En-ya,WEI Ping-bo,SUI Guo-rong,CHEN Lang,XU Ling,XIE Hui,SHEN Shu-bao,ZHU She-min.Preparation of Mn-Ce-O_x Denitration Catalyst and Its Regeneration Performance[J].Environmental Science and Technology,2012(9):40-44.
Authors:FAN En-ya  WEI Ping-bo  SUI Guo-rong  CHEN Lang  XU Ling  XIE Hui  SHEN Shu-bao  ZHU She-min
Institution:1.SINOPEC Yangtze Petrochemical Company,Nanjing 210009,China; 2.School of Material Science and Engineering,Nanjing University of Technology,Nanjing 210009,China; 3.Jiangsu Farun Group Company Ltd,Suzhou 215000,China;4.School of Life Science and Pharmaceutical Engineering,Nanjing University of Technology,Nanjing 210009,China)
Abstract:Mn-Ce-Ox denitration catalysts were prepared by isovolumetric impregnation method and tested for selective catalytic reduction(SCR) of NO with ammonia.Influences of different Mn/Ce molar ratio and calcinations temperature,H2O and SO2 on NO conversion of the catalyst and its regenerative performance were investigated.Results showed that the conditions of NH3:NO 1:1,space velocity 5 000 h-1,the catalyst of molar ratio of Mn/Ce 5:1 calcinated by 550 ℃ showed higher NO conversion and the activity achieved more than 90% in 100~260 ℃ and the most high activity could achieve 97.84% at 200 ℃.The activity of the catalyst was declined to 53% in 2.5h after the action and not changed evidently in the next 6h within 10%(V/V) H2O steam and 300×10-6 SO2 at 200 ℃.NO conversion of the deactivation catalyst dealt with water or 3(wt)% nitric acid and calcinated by 550 ℃ could recover more than 90% at 200 ℃,among which the activation was the best when treated by 3(wt)% nitric acid.
Keywords:selective catalytic reduction(SCR)  Mn-Ce-Ox complex catalyst  De-NO  regeneration
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