摘要
设计了一种催化还原法脱硫化氢并副产硫磺的系统,并针对该系统研究了混合气体温度、氧气流量、通入氧气位置(进口与脱硫装置顶部端盖的距离)及初始H2S体积分数对H2S脱除率的影响。结果表明:该系统的H2S脱除率在98%以上,随着混合气体温度的升高、氧气流量的增加或通入氧气位置与脱硫装置顶部端盖距离的增加,H2S脱除率呈先增加后减小的趋势;随着初始H2S体积分数的增加,H2S脱除率略有下降,故选择合适的混合气体温度、氧气流量、通入氧气位置及初始H2S体积分数,可显著提高该系统的H2S脱除率。
A catalytic reduction system was devised to remove hydrogen sulfide and the sulfur-related by-product of this system.The effects of the mixed gas temperature,oxygen flow rate,oxygen inlet position(the distance between the oxygen inlet and the top cover of the desulfurization unit)and volume fraction of initial H2S on the removal rate of H2S were studied.The results show that the removal rate of H2S in the system is over 98%.With the increase in the gas temperature,the oxygen flow rate or the distance between the oxygen inlet and the top cover of desulfurization unit,the H2S removal rate increases at first and then decreases;with the increase in the volume fraction of initial H2S,the H2S removal rate slightly decreases.Therefore,the optimal combinations of the mixed gas temperature,oxygen flow rate,oxygen inlet position and the volume fraction of initial H2S can significantly improve the H2S removal rate of the system.
作者
沈冰燕
于海龙
刘恩海
霍爱玺
王奕雅
孙运兰
朱宝忠
SHEN Bingyan;YU Hailong;LIU Enhai;HUO Aixi;WANG Yiya;SUN Yunlan;ZHU Baozhong(School of Petroleum Engineering, Changzhou University, 213164 Changzhou, China)
出处
《煤炭转化》
CAS
CSCD
北大核心
2020年第4期72-78,共7页
Coal Conversion
基金
江苏省研究生科研与实践创新计划项目(SJCX19_0667)
河南省自然科学基金资助项目(182300410133).
关键词
铁基催化剂
催化还原法
H2S
脱除率
干法脱硫
iron based catalyst
catalytic reduction
hydrogen sulfide
removal rate
dry desulfurization