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作 者:孙春宝[1] 周北海[1] 段旭琴[1] 邢奕[1] 窦源东[2]
机构地区:[1]北京科技大学土木与环境工程学院,北京100083 [2]山东省科学院能源所山东天力干燥设备有限公司,济南250014
出 处:《北京科技大学学报》2007年第3期256-260,共5页Journal of University of Science and Technology Beijing
基 金:北京市教育委员会共建项目建设计划资助项目(No.XK100080432)
摘 要:利用DSD酸生产过程产生的铁泥,研制出既能用作常规冶金原料,又能用于处理DSD酸氧化废水的水处理用海绵铁.研究表明:在配碳量27%、反应温度1160℃、反应时间16min的情况下,以铁泥为原料制备的常规海绵铁的金属化率可达90%以上;用于处理DSD酸氧化废水的海绵铁适宜配碳量为29%,用制备出的海绵铁处理DSD酸氧化废水,在pH值3~5、反应时间40min时,出水的CODCr去除率可达68%、色度的去除率达90%、可生化性指标BOD/COD提高到0.425.海绵铁中所含C,Fe3C和其他一些杂质元素,这些元素能与铁在水中形成无数微小原电池产生大量[H],[OH]和[Fe^2+],从而氧化还原废水中的有机物,达到污染物降解和提高废水可生化性的目的.海绵铁的微孔结构非常发达,使其具有比表面积大、活性高的特点.是一种替代常规铁屑的理想材料.The sponge iron making with iron sludge produced during DSD acid-making can be used for not only general metallurgy but also iron-carbon bed to treat DSD acid oxidation wastewater. It is pointed out that under the condition of the temperature of 1 120℃, the reaction time of 16 min and the carbon content of 27 %, the metal transformation rate of sponge iron used for general metallurgy is up to 90 %. But the optimal carbon content is 29 % for iron sponge to treat DSD acid oxidation wastewater. Under condition of the wastewater' s pH value of 3 to 5 and the reaction time of 40 min, the removal rates of CODCr and color are 68 % and 90 %, respectively. The BOD/COD ratio is up to 0.425 when DSD oxidation acid water is treated with sponge iron. As Fe3C and other materials contained in sponge iron formed so innumerable micro-batteries between iron and other elements to oxidate and deoxidize the organics in wastewater, the pollutants became degradable and the biodegradation of wastewater was promoted. The micro-sponge-shape of sponge iron is so developed that its special surface area is greater and its activity is higher, so it is the best alternative of general iron powder.
关 键 词:铁泥 海绵铁 铁碳床 DSD酸 DSD酸氧化废水
分 类 号:X703[环境科学与工程—环境工程] TF591[冶金工程—钢铁冶金]
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