水体中苯胺光降解的实验研究

为了更好地了解苯胺类物质在环境中的化学行为,在自行设计的光化学反应器上进行模拟天然水体的苯胺光降解实验,用气相色谱法测定苯胺的残余质量浓度,考察了水体pH值、光强、反应时间、光敏化剂、水质等条件影响下苯胺的光降解效果和规律.3h内苯胺在3个不同体系中的降解效果从大到小依次是:去离子水模拟天然水体、加入光敏化物质的灭菌河水、未加光敏化物质的灭菌河水.pH值为5.0,Fe2 、过氧化氢、腐殖质存在时苯胺的光降解效果较好.     

应用质子变化滴定测量法监测氨氧化的化学计量关系

开发了一套监测批式废水生物处理系统质子变化的自动滴定测量装置.装置由批式反应器、数据自动采集与保存系统和药品自动投加系统组成.通过实际测量活性污泥氨氧化反应中氢离子产生量与氨消耗量的化学计量比值,考察自动滴定测量装置的测试精度.在1L的反应器中改变氨氮浓度(以N计)分别为1.67、3.33、8.33、16.66和30.00mg/L下实测比值与其理论值十分接近,相对误差在2.09%～6.34%之间;保持氨氮浓度16.66mg/L,在1、2、3和4L的反应器中实测比值相对误差在2.09%～-18.57%之间,随反应器体积增大而明显增大.反应器系统中的碳酸氢盐和氨盐缓冲体系,特别是在较大容积反应器中的滴定动态效应是导致测试误差的重要原因.研究成果为滴定测量方法在废水生物处理过程中监测质子变化提供了一种重要方法.     

重庆环境准入制度透视

2008年3月10日,重庆市政府印发了《重庆市工业项目环境准入规定》,标志着在全市正式建立了工业项目环境准入制度。3年多来,通过环境准入制度的严格实施,进一步规范了招商引资和建设项目的前期工作,促进了产业结构调整,优化了工业项目布局,提高了资源环境利用效率。3年多来,全市累计不予受理、不予审批不符合准入条     

从璧山之痛到“治污典范”——重庆璧南河治污攻坚战

14条受污染的次级河流肯定能治好,璧南河就是最好的例子!2010年9月29日,在全市主城区次级河流综合整治现场工作会上,璧南河污染治理经验被作为次级河流治污典范向全市推广。璧南河,璧山境内最大的次级河流,璧山的母亲河,主河道全长73千米,流域面积441平方千米,涉及璧山境内9个镇街,县域70%以上的经济总量分布在沿河流域。水黑如墨,臭不可闻,鱼虾绝迹曾经是其真实的写照,老百姓怨声载道。按照     

城市水循环中的微量污染物负荷

污水中不同的有机化合物,例如,药物、个人护理产品中的添加物、家用化学物质和工业化学等物质都对水生生态系统和人类健康带来了潜在威胁.这些污染物质的大部分在环境中含量非常低,范围在pg/L至ng/L间,因此,被称为微量污染物.这些微量污染物质对水生生态系统和人类健康的威胁表现在内分泌干扰作用、化学敏感作用,污染混合物的交互作用以及长期暴露下的慢性作用.     

Mobilities and leachabilities of heavy metals in sludge with humus soil

Chemical forms of Zn, Ni, Cu, and Pb in municipal sewage sludge were investigated by adding humus soil to sludge and by performing sequential extraction procedures. In the final sludge mixtures, Zn and Ni were mainly found in Fe/Mn oxide-bound (F3) and organic matter/sulfide-bound (F4) forms. For Zn, exchangeable (F1), carbonate-bound (F2), and F3 forms were transformed to F4 and residual forms (F5). For Ni, F1 and F2 forms were transformed to F1, F2, and F3 forms. Both Cu and Pb were strongly associated with the stable forms F4 and F5. For Cu, F2 and F3 forms were major contributors, while for Pb, F3 and F4 forms were major contributors to F5. Humus soil dosage and pH conditions in the sludge were strongly correlated with the forms of heavy metals. Five forms were used to evaluate metal mobilities in the initial and final sludge mixtures. The mobilities of the four heavy metals studied decreased after 28 days. The metal mobilities in the final sludge mixtures were ranked in the following order: Ni > Zn > Cu = Pb. Leaching tests showed that the mobilities of Zn and Ni in lower pH conditions (pH 4) were higher than those in higher pH conditions (pH 8).     

Preparation and coagulation efficiency of polyaluminium ferric silicate chloride composite coagulant from wastewater of high-purity graphite production

The aim of the present work was to produce a polyaluminium ferric silicate chloride (PAFSiC) coagulant from acidic and alkaline wastewater of purifying graphite by roasting, and subsequently to evaluate coagulation efficiency of the reagent by treating surface water from the Yellow River as well as municipal wastewater in comparison with the conventional coagulant polyaluminium chloride (PAC). The PAFSiC coagulant was prepared by co-polymerization. The effects of (Al+Fe)/Si molar ratio, OH/(Al+Fe) molar ratio (i.e., value), coagulant dosage and pH value of test suspension on the coagulation behavior of FAFSiC and the stability of the PAFSiC were also examined. Results showed that PAFSiC performed more efficiently than PAC in removing turbidity, chemical oxygen demand (COD), and total phosphate (TP). The PAFSiC with a value of 2.0 and (Al+Fe)/Si ratio of 5 (PAFSiC 2.0/5) showed excellent coagulation effect for both turbidity and COD, while PAFSiC 1.0/5 was the best for TP. The optimum coagulation pH range of PAFSiC 2.0/5 was 5.0–9.0, slightly wider than that of PAC (6.0–8.0). The process can be easily incorporated into high-purity graphite production plants, thereby reducing wastewater pollution and producing a valuable coagulant.     

Chemical cleaning of fouled PVC membrane during ultrafiltration of algal-rich water

Cleaning of hollow-fibre polyvinyl chloride (PVC) membrane with di erent chemical reagents after ultrafiltration of algal-rich water was investigated. Among the tested cleaning reagents (NaOH, HCl, EDTA, and NaClO), 100 mg/L NaClO exhibited the best performance (88.4% 1.1%) in removing the irreversible fouling resistance. This might be attributed to the fact that NaClO could eliminate almost all the major foulants such as carbohydrate-like and protein-like materials on the membrane surface, as confirmed by Fourier transform infrared spectroscopy analysis. However, negligible irreversible resistance (1.5% 1.0%) was obtained when the membrane was cleaning by 500 mg/L NaOH for 1.0 hr, although the NaOH solution could also desorb a portion of the major foulants from the fouled PVC membrane. Scanning electronic microscopy and atomic force microscopy analyses demonstrated that 500 mg/L NaOH could change the structure of the residual foulants on the membrane, making them more tightly attached to the membrane surface. This phenomenon might be responsible for the negligible membrane permeability restoration after NaOH cleaning. On the other hand, the microscopic analyses reflected that NaClO could e ectively remove the foulants accumulated on the membrane surface.     

Modeling assessment for ammonium nitrogen recovery from wastewater by chemical precipitation

Chemical precipitation to form magnesium ammonium phosphate (MAP) is an effective technology for recovering ammonium nitrogen (NH4 +-N). In the present research, we investigated the thermodynamic modeling of the PHREEQC program for NH4 +-N recovery to evaluate the effect of reaction factors on MAP precipitation. The case study of NH4 +-N recovery from coking wastewater was conducted to provide a comparison. Response surface methodology (RSM) was applied to assist in understanding the relative significance of reaction factors and the interactive effects of solution conditions. Thermodynamic modeling indicated that the saturation index (SI) of MAP followed a polynomial function of pH. The SI of MAP increased logarithmically with the Mg2+/NH4 + molar ratio (Mg/N) and the initial NH4 +-N concentration (CN), respectively, while it decreased with an increase in Ca2+/NH4 + and CO3 2??/NH4 + molar ratios (Ca/N and CO3 2??/N), respectively. The trends for NH4 +-N removal at different pH and Mg/N levels were similar to the thermodynamic modeling predictions. The RSM analysis indicated that the factors including pH, Mg/N, CN, Ca/N, (Mg/N) (CO3 2??/N), (pH)2, (Mg/N)2, and (CN)2 were significant. Response surface plots were useful for understanding the interaction effects on NH4 +-N recovery.