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31.
根据国家环保总局发布的"高污染、高环境风险"产品名录(2009年),无机盐产品高氯酸钾属于高环境风险的产品,其生产存在较大风险。高氯酸钾项目在生产过程中的环境风险主要来源于强酸、强碱、有毒有害、易燃易爆等原辅材料、产品,运输、贮存和使用过程产生的燃爆、泄漏、贮运风险以及工艺废气治理措施失效等环节。识别项目产生的环境风险主要包括爆炸风险、泄漏风险、危险化学品贮运风险及氯气直排风险,并从生产管理、生产工艺及贮运等方面提出相应的防范措施。 相似文献
32.
F. Gallardo‐Lara M. Azcón A. Polo 《Journal of environmental science and health. Part. B》2013,48(5):623-643
Abstract Land disposal of olive oil wastewater using it as a soil amendment requires a knowledge of the effects that its application may produce on the status of the mineral nutrients in the plant‐soil system. A pot experiment using calcareous soil was performed in a growth chamber to examine the effects of olive oil wastewater on the availability and postharvest soil extractability of K, Mg and Mn. The experiment included 6 treatments: two rates of olive oil wastewater, two mineral fertilizer treatments containing K (which supplied K in amounts equivalent to the K supplied by the olive oil wastewater treatments), a K‐free mineral fertilizer treatment, and a control. The pots were sown with ryegrass as the test plant, harvesting 3 times at intervals of one month. Olive oil wastewater has demonstrated a considerable capacity for supplying K that can be assimilated by the plant, tending in fact to surpass the mineral potassium fertilizer tested. The application of olive oil wastewater tends to reduce the concentration of Mg in the plant, similarly to the effect of adding mineral potassium fertilizer. An enhancement of Mn availability takes place in the soil amended with olive oil wastewater, which on occasion has produced Mn concentrations in plant that could be considered phytotoxic or at least excessive. After harvesting, we observed an increase in the amount of exchangeable K in soil with added industrial wastewater. However, these increases are lower than those in soil treated with mineral potassium fertilizer. The levels of exchangeable, carbonate‐bound, organic‐bound and residual Mg in soil were higher in treatments incorporating olive oil wastewater than in those with added mineral K, with the opposite tendency occurring in the amount of Fe‐Mn oxides‐bound Mg in soil. Treatments based on olive oil wastewater, especially in high doses, increased the amount of exchangeable and carbonate‐bound Mn in soil, in comparison with treatments adding mineral fertilizers with or without K. In contrast, the addition of industrial wastewater caused a drop in the amount of Fe‐Mn oxides‐bound and organic‐bound Mn in soil. 相似文献
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以地水中的氯代烃污染物三氯乙烯(TCE)为目标污染物,以过硫酸钾溶液为氧化剂,探讨了不同条件下过硫酸钾对TCE的去除效果。实验结果表明,在40℃,过硫酸钾初始浓度为2.43 g/L条件下,反应2 h后,TCE的去除率就可达到96.8%;过硫酸钾对TCE的去除符合一级反应动力学方程,速率常数(K)为1.3364 h-1,半衰期(t1/2)为0.51 h;过硫酸钾对TCE的去除速率在pH为中性附近时最大,其后无论pH升高或降低去除速率均减小;受温度和pH影响较明显,并且反应温度越高,受pH的影响越明显;随离子强度的增加而减小;反应活化能为119.6 kJ/mol;过硫酸钾溶于水生成过硫酸根离子(S2O28-),S2O28-会进一步生成硫酸根自由基(SO4-.),在碱性条件下,SO4-.与OH-反应会进一步生成羟基自由基(.OH)。过硫酸钾对于TCE的去除主要源自SO4-.和.OH的强氧化性。 相似文献
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36.
用蒽醌生产中的废硫酸制备硫酸钾 总被引:2,自引:0,他引:2
研究了以蒽醌生产中的废硫酸为原料,通过缔合,置换,解缔等步骤,制备硫酸钾的最佳工艺条件。在最佳条件下,可使废硫酸中H2SO4的质量分数从23%降至0.60%,废硫酸成盐率为89.01%,硫酸钾纯度为95.85%。 相似文献
37.
利用碱性过硫酸钾消解紫外分光光度法,探讨了消解时间和消解温度对空白吸光值的影响,认为增加消解时间可以降低空白吸光值,而提高消解温度对空白吸光值的影响不大;对于某些样品中总氮含量低于氨氮含量的现象,将碱性过硫酸钾装入小试管,再放入装有水样的比色管中,虽然能够减少氨气形式逸出的氮含量,但回收率较低;连续流动和流动注射-盐酸萘乙二胺分光光度法,在以后的修订中应增加过硫酸钾含氮量以及镉柱还原能力大小的界定. 相似文献
38.
采用Fe3O4活化过硫酸盐(PS)同步去除水中的NOR (诺氟沙星)和Pb (II).探讨了Fe3O4投加量、PS浓度、初始pH值和Pb (II)浓度对NOR降解的影响.结果表明,NOR的降解符合伪一级反应动力学,在温度为30℃、NOR初始浓度为5.0mg/L、Pb (II)浓度为1.0mg/L、Fe3O4投加量为2.0g/L、PS浓度为1.5mmol/L、初始pH值为7.0的条件下,反应120min后,NOR降解率达90.2%,Pb (II)去除率为99.5%.自由基淬灭实验证实,硫酸根自由基(SO4-·)是NOR降解的主要自由基.通过LC-MS分析结果推测了NOR可能的降解路径和中间产物.Fe3O4活化PS高级氧化工艺可作为一种同步去除有机污染物和重金属的工艺. 相似文献
39.
Oxidation of aniline by persulfate in aqueous solutions was investigated and the reaction kinetic rates under different temperature, persulfate concentration and pH conditions were examined in batch experiments. The results showed that, the aniline degradation followed pseudo first-order reaction model. Aniline degradation rate increased with increasing temperature or persulfate concentration. In the pH range of 3 to 11, a low aniline degradation rate was obtained at strong acid system (pH 3), while a high degradation rate was achieved at strong alkalinity (pH 11). Maximum aniline degradation occurred at pH 7 when the solution was in a weak level of acid and alkalinity (pH 5, 7 and 9). Produced intermediates during the oxidation process were identified using liquid chromatography-mass spectrometry technology. And nitrobenzene, 4-4’-diaminodiphenyl and 1-hydroxy-1,2-diphenylhydrazine have been identified as the major intermediates of aniline oxidation by persulfate and the degradation mechanism of aniline was also tentatively proposed. 相似文献
40.