化学活化法制取污泥衍生吸附剂的实验研究

用有机污泥按照一定的工艺制作污泥衍生吸附剂。结果表明，氯化锌作为化学活化剂在吸附剂的生成过程中起到了关键作用，热解温度是影响吸附剂性能的最主要因素，750℃是最佳热解温度。     

The effect of Na and Ca salts on MSWI bottom ash activation for reuse as a pozzolanic admixture

In this study the possibility of both chemical and combined chemical + thermal activation of municipal solid waste incinerator bottom ash was investigated. A number of chemical activators including Na₂SiO₃·9H₂O, NaOH, Na₂SO₄ and CaCl₂·2H₂O were individually added at varying concentrations to bottom ash/Portland cement mixtures having different bottom ash contents. The effect of the selected compounds was evaluated in terms of macroscopic properties including mechanical strength and composition of cementitious materials/water slurries. The results showed that Na-based activators were not capable of improving the characteristics of the cementitious products if compared to Portland cement under both normal and accelerated curing. Conversely, the use of calcium chloride at 40 °C-curing did promote the pozzolanic properties of bottom ash, leading to UCS values of 45.5 and 60.0 MPa after 10 and 20 days, respectively, as opposed to a value of 43.6 MPa obtained after 28 days for Portland cement under normal curing conditions.     

Determination of toxic elements in waters and sediments from River Subin in the Ashanti Region of Ghana

Waters and sediments of Subin River, which flows through the industrial and commercial areas of Kumasi in the Ashanti region of Ghana, were geochemically investigated to ascertain heavy metal pollution levels due to anthropogenic activities. The study shows preoccupying pollution levels that constitute a threat to public and ecological systems. The waters of Subin River are neutral to slightly basic, inferred from pH values of 6.89–7.65). Electric conductivity (EC) of the waters ranges from 822 to 1,821 μs/cm and the range of total dissolved solids (TDS) is from 409 to 913 mg/l. Toxic elements contents of sediments and waters from 10 sites along the river were analysed by instrumental neutron activation analysis (INAA), and Al, As, Cd, Cr, Cu and Zn were determined. The concentrations of Al, As, Cd, Cr, Cu and Zn in the waters range between 4.02–15.18, 0.007–0.16, 0.002–0.05, 0.001–0.019, 1.32–7.04 and 4.28–10.2 mg/l, respectively. The contamination factors (CF) computed for the elements indicate that with the exception of sampling site S10, the sediments are polluted with Cd. Chromium contamination in the sediments is observed at S6 and S7, where the CF values were 1.39 and 1.52, respectively. The pollution load indices (PLI) were low (<1) and ranged from 0.14 to 0.75, suggesting that the overall sediment column of the river is not polluted.     

Planar detonation structure for chain-branching kinetics with large activation energy and small initiation rate

The structure of the steady planar detonation wave is analyzed for three-step chain-branching kinetics consistent with hydrogen–air chemistry. The initiation and chain-branching steps are described by an Arrhenius rate. Both are thermally neutral, so that heat release is due to termination. The initiation rate is typically very low and very stiff. As a result, a small fraction of the reactant is consumed in the initiation region, which is very long but ends in an exponential chain-branching explosion. Next, the reactant is rapidly converted into chain-branching radicals, within a very thin zone, which ends when the concentration of the chain-branching radical reaches a peak, because of reactant depletion. Finally, the termination step consumes the chain-branching radicals and releases heat within a region thicker than the peak zone, but much thinner than the initiation region. The analysis is based upon two assumptions: that the chain-branching activation energy is high and that initiation is slow. The structure of the initiation and chain-branching zones is different for post-shock states within or outside the explosion region in the chain-branching diagram. In the former situation, chain-branching is already stronger than termination at the von Neumann point, and vice versa. In the no-explosion case, the initiation zone becomes very long, while the little chain-branching specie produced by initiation is directly converted into product by the termination step. Temperature increases slowly until reaching the explosion curve, when chain-branching becomes stronger than termination. The subsequent structure is similar to the explosion case.     

切割钢渣活化过硫酸盐降解偶氮类染料酸性红73

切割钢渣是钢铁生产过程中的固体废弃物,如何有效处理和利用这些废渣具有减少环境污染、实现废物资源化的重要意义.本文选择河北邢台钢铁厂中切割钢渣为过硫酸盐(PS)活化剂,活化过硫酸盐(PS)去除水相中偶氮染料酸性红73(AR73),实验表明,25 mg·L~(-1) AR73在15 min内,其降解率为99.9%,TOC矿化率达58.6%.同时考察了钢渣投入量、PS浓度、初始pH值等影响因素对AR73降解效率的影响:随着PS浓度、钢渣投入量的增加,AR73的降解速率也逐渐增加;在pH为3～9时,AR73均可被有效去除,酸性条件更有利于AR73的去除.活性自由基猝灭实验表明,酸性红73的降解是通过自由基和非自由基两种机制实现的,且钢渣可多次回收重复利用.钢渣活化PS技术,还可有效去除蒽醌类染料(活性蓝19),其去除率为99.9%,矿化率可达92.0%;同时该技术对某印染废水(COD_(Cr)=5625 mg·L~(-1))的去除率达49.9%.本文所构建的切割钢渣活化过硫酸盐(PS)技术可应用于偶氮印染废水的处理,实现"以废治废"的目标.     

Fe(Ⅱ)/K_2S_2O_8对水体中As(Ⅲ)的氧化研究

研究了Fe(Ⅱ)/K2S2O8对水体中As(Ⅲ)的氧化作用,以及pH值、Fe(Ⅱ)初始浓度等因素对氧化As(Ⅲ)的影响,并且采用分子探针法的竞争性实验鉴定了体系中产生的活性中间体,探讨了K2S2O8在Fe(Ⅱ)存在的条件下对As(Ⅲ)的氧化机理。     

活化赤泥吸附除磷及其机理的研究

以铝矿工业赤泥为原材料,采用酸活化、焙烧活化、热酸活化方法进行活化处理,得到除磷吸附剂,考察了pH值、反应时间和磷初始浓度等因素对除磷吸附剂吸附效果的影响.结果表明,活化赤泥具有较好的除磷能力,酸活化赤泥和焙烧活化赤泥对磷的饱和吸附量分别为155.2、144.2 mg·g-1.热酸活化赤泥除磷能力更强,其对磷的饱和吸附量可达202.9 mg·g～,经过热酸活化后的赤泥即使在pH值波动较大时也能很好处理高浓度含磷废水.溶液pH显著影响磷去除效果,在pH为7时得到最大去除量.     

Neutron activation method in the analysis of environmental objects

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Oxidation inhibition of sulfite in dual alkali FGD system

A laboratory-scale well-mixed thermostatic reactor with continuously blasting air was used to investigate the oxidation inhibition of sulfite in dual alkali flue gas desulfurization （FGD） system. The effects of operating parameters such as pH value and catalyst concentration on the oxidation were studied. Sodium thiosulfate was used in the system, and was found that it significantly inhabited the sulfite oxidation. In the absence of catalyst, sodium thiosulfate at 12.67 mmol/L had an inhibition efficiency of approximately 98%. While in the presence of catalyst, sodium thiosulfate at 26.72 mmol/L had an inhibition efficiency less than 85.0%. The oxidation reaction order of sulfite in the sodium thiosulfate was determined to be -1.90 and 4）.55 in the absence and presence of the catalyst, respectively. Apparent activation energy of oxidation inhibition was calculated to be 53.9 kJ/mol. Pilot tests showed that the consumption rate of thiosulfate agreed well with the laboratory-scale experimental results.     

Neutron activation analysis of ceramic tiles and its component and radon exhalation rate

IntroductionCeramic,consistofearthymaterialslikeclaykaolin ,limestoneandsandglass .Ceramicmaterialsarenonmetalic ,inorganiccompoundsprimaryoxides ,alsocarbides ,nitridesandsilicides .Twotypesofbondingmechanismsoccurinceramicmaterial ,ionicandcovalent.Theo…