金属尾矿作水泥混合材活性试验研究

选取烧失量低于10%,SO3含量低于3%,SiO2、Al2O3含量较高,适于作水泥混合材的6种金属尾矿进行水泥混合材活性试验研究.6种金属尾矿分别按10%、15%、20%、25%、30%与熟料、石膏进行配比.试验结果表明:6种金属尾矿不同掺配比活性试验的R28在68.72%～76.54%之间,高于活性混合材R28为62%的判定指标,由此可认为此6种尾矿均属于活性混合材,可单独用作水泥活性混合材;6种金属尾矿掺配比在小于30%的范围内,水泥安定性、凝结时间等性能指标均符合普通硅酸盐水泥要求;6种金属尾矿掺配比在小于30%的范围内其强度均满足32.5R等级水泥强度要求;尾矿掺配比为10%时,6种金属尾矿除3号尾矿外,均满足42.5R等级水泥强度要求.符合要求的金属尾矿用作水泥混合材,将扩大水泥混合材来源,降低水泥粉磨能耗和成本,实现尾矿的资源化和水泥工业的可持续发展.     

预处理钢渣粉煤灰作水泥混合材的研究

介绍了对钢渣和粉煤灰进行预处理，并将预处理后的粉灰和钢渣的混合料与水泥进行复合强度试验研究，分析了混合料在预处理过程中的活性变化规律，研究了预处理混合料与水泥复全增强的机理。     

铸造水玻璃废砂作水泥混合材的试验研究

为了解决铸造企业水玻璃废砂大量排放而带来的堆场困难和环境污染的问题,拓宽水玻璃废砂资源化再利用范围,研究了利用水玻璃废砂作为混合材生产水泥的可行性。试验结果表明,当白砂（处于铸模内侧,经受过高温,溃散性差）或混合砂（铸模内、外侧砂同比例混合）掺量小于10％时,可生产42．5普通硅酸盐水泥,而且该水泥的其他各项性能指标均符合水泥的国家标准要求。     

基于酸浸焚烧污泥灰中的磷释放及蓝铁矿生成

酸浸焚烧污泥灰(ISSA)是一种湿化学法提取磷(P)的工艺,因其操作简单、损耗低而被广泛应用.以烘干污泥为对照,通过考察不同温度(600～900℃)下ISSA中的磷形态和矿物相转变,研究了H₂SO₄和HCl作为提取液的酸浓度、酸浸时间和液固比对ISSA样品释磷性能以及对Ca、Al、Mg、Fe等关键金属元素浸出行为的影响,最终通过酸浸、阳离子交换树脂(CER)纯化和沉淀三步反应得到磷回收产物.结果表明:ISSA样品磷的形态以非磷灰石态无机磷(NAIP)为主,且部分NAIP会随着焚烧温度的升高转变为磷灰石态无机磷(AP);同时,污泥样品经两种提取液酸浸后,金属元素Ca、Al、Mg释出量最多,其中Ca、Mg元素的浸出量随焚烧温度的升高变化不大,而Al的浸出量随焚烧温度的升高急剧降低;相比其他焚烧温度,800℃条件下ISSA释磷性能更好,且H₂SO₄酸浸释磷性能优于HCl酸浸,当H₂SO₄浓度为0.10mol/L、液固比为150mL/g、酸浸时间为150min时释...     

Simultaneous removal of ammonium and phosphate by zeolite synthesized from coal fly ash as influenced by acid treatment

Zeolite synthesized from fly ash （ZFA） without modification is not efficient for the purification of NH4＋ and phosphate at low concentrations that occur in real effluents, despite the high potential removal capacity. To develop an effective technique to enhance the removal efficiency of ammonium and phosphate at low concentrations, ZFA was modified with acid treatment and the simultaneous removal of ammonium and phosphate in a wide range of concentration was investigated. It was seen that when compared with untreated ZFA, only the treatment by 0.01 mol/L of H2SO4 significantly improved the removal efficiency of ammonium at low initial concentrations. The behavior was well explained by the pH effect. Treatment by more concentrated H2SO4 led to the deterioration of the ZFA structure and a decrease in the cation exchange capacity. Treatment by 0.01 mol/L H2SO4 improved the removal efficiency of phosphate by ZFA at all initial P concentrations, while the treatment by concentrated H2SO4 （≥0.9 mol/L） resulted in a limited maximum phosphate immobilization capacity （PIC）. It was concluded that through a previous mild acid treatment （e.g. 0.01 mol/L of H2SO4）, ZFA can be used in the simultaneous removal of NH4＋ and P at low concentrations simulating real effluent.