北京科技大学学报
北京科技大學學報
북경과기대학학보
JOURNAL OF UNIVERSITY OF SCIENCE AND TECHNOLOGY BEIJING
2014年
2期
235-240
,共6页
刘应书%王海鸿%张辉%范菲%刘文海
劉應書%王海鴻%張輝%範菲%劉文海
류응서%왕해홍%장휘%범비%류문해
烟气%脱硫%活性炭%催化作用%反应速率%二氧化硫
煙氣%脫硫%活性炭%催化作用%反應速率%二氧化硫
연기%탈류%활성탄%최화작용%반응속솔%이양화류
flue gases%desulfurization%activated carbon%catalysis%reaction rate%sulfur dioxide
针对活性炭烟气脱硫过程,以吸附质浓度沿床层分布曲线实验为基础,对活性炭脱除SO2的催化反应速率的影响因素进行了探讨.研究发现SO2质量浓度和CO2体积分数对活性炭催化反应速率有显著影响. SO2质量浓度对活性炭催化反应速率影响最大,随着SO2质量浓度升高催化反应速率将显著增加,但高SO2质量浓度下催化反应速率将不再增加;体积分数在15%以内的CO2对催化反应速率呈线性抑制,使得活性炭催化反应速率降低约30%;烟气线速度在0.14~0.3 m·s-1之间变化时对催化反应速率的影响效果不大。
針對活性炭煙氣脫硫過程,以吸附質濃度沿床層分佈麯線實驗為基礎,對活性炭脫除SO2的催化反應速率的影響因素進行瞭探討.研究髮現SO2質量濃度和CO2體積分數對活性炭催化反應速率有顯著影響. SO2質量濃度對活性炭催化反應速率影響最大,隨著SO2質量濃度升高催化反應速率將顯著增加,但高SO2質量濃度下催化反應速率將不再增加;體積分數在15%以內的CO2對催化反應速率呈線性抑製,使得活性炭催化反應速率降低約30%;煙氣線速度在0.14~0.3 m·s-1之間變化時對催化反應速率的影響效果不大。
침대활성탄연기탈류과정,이흡부질농도연상층분포곡선실험위기출,대활성탄탈제SO2적최화반응속솔적영향인소진행료탐토.연구발현SO2질량농도화CO2체적분수대활성탄최화반응속솔유현저영향. SO2질량농도대활성탄최화반응속솔영향최대,수착SO2질량농도승고최화반응속솔장현저증가,단고SO2질량농도하최화반응속솔장불재증가;체적분수재15%이내적CO2대최화반응속솔정선성억제,사득활성탄최화반응속솔강저약30%;연기선속도재0.14~0.3 m·s-1지간변화시대최화반응속솔적영향효과불대。
According to flue gas desulfurization processes with activated carbon, several factors affecting the catalytic reaction rate of activated carbon for flue gas desulfurization were investigated on the basis of the experiment of adsorbate concentration curves along the bed. It is found that SO2 concentration and CO2 volume fraction have significant influences on the catalytic reaction rate, and SO2 concentration is the primary factor. With increasing SO2 concentration, the catalytic reaction rate increases significantly, but it does not increase at high SO2 concentration. While the CO2 volume fraction increases from 0 to 15%, the catalytic reaction rate decreases by 30% linearly, indicating that CO2 plays a linear inhibition role in the catalytic reaction. The flue gas velocity between 0.14 m·s-1 and 0.3 m·s-1 has no significant effect on the catalytic reaction rate.