模拟生物反应器加速产甲烷过程研究

渗滤液原液回灌易导致填埋垃圾产甲烷过程的滞后,从而对甲烷收集利用产生不利影响。通过3根实验室模拟生物反应器,研究了原液回灌(C1)、渗滤液好氧预处理后回灌(C2)和原液回灌+垃圾层上部通风曝气(C3)3种填埋方式下的填埋气产气规律。结果表明,C1甲烷浓度经历短暂上升,达到19.5%后开始逐渐降低,产甲烷速率和产甲烷总量均很低;C2甲烷浓度逐渐上升,在第121天时甲烷浓度达到50%,产甲烷最高速率和产甲烷总量分别为0.31 L/(kg·d)和25.2 L/kg。在停止上部垃圾层通风曝气后,C3甲烷浓度迅速上升,在81 d时甲烷浓度便达到50%以上,最大产甲烷速率和产甲烷总量分别为0.22 L/(kg·d)和16.0 L/kg。对各模拟柱填埋气可回收性评价结果表明,C3填埋气可回收利用比例最高,C2略低,C1在实验期间内则无可回收利用气体产生。     

热解吸对污染土壤中不同形态汞的去除作用

选取贵州省万山矿区的汞污染土壤样品进行不同形态汞的热解吸去除行为研究。研究了热解吸过程中∑Hg的去除效果及动力学,以及温度和时间对污染土壤中不同形态汞的去除作用。结果表明,热解吸修复技术可有效去除土壤中的汞,土壤中∑Hg的热解吸过程符合二级动力学方程。固定热解吸时间在10 min时,随着热解吸温度的升高,土壤中水溶态汞、盐酸溶态汞和碱溶态汞含量呈现先下降后上升再下降的趋势,王水溶汞和盐酸溶态汞始终呈现下降趋势,说明不同形态的汞之间发生了转化。热解吸温度为250℃时,随着热解吸时间的增加,环境风险大的水溶态汞、盐酸溶态汞、碱溶态汞和硝酸溶态汞的去除率大幅增加,土壤的有机质损失较少,说明在低温下,延长热解吸时间,对生物毒性强的形态汞有良好的修复效果,且此温度下处理后的土壤更容易恢复农田耕作。     

改性啤酒酵母及柑橘皮凝胶小球对铜的吸附性能

为有效去除污水中的铜离子并实现资源有效的利用,以啤酒酵母和柑橘皮为原料制备海藻酸钙固定啤酒酵母菌小球(SCA)、海藻酸钙固定柑橘皮小球(OPCA)及海藻酸钙固定柑橘皮及啤酒酵母菌复合小球(OPSCA),研究了其对铜离子的吸附和解吸性能。研究结果表明,3种吸附剂对铜离子吸附的最佳pH值为5.0,吸附量的大小顺序为:OPSCAOPCASCA。吸附动力学数据符合准二级动力学模型。吸附过程被内扩散步骤和外扩散步骤共同控制。Langmuir等温吸附模型能较好地模拟3种吸附剂的吸附数据,SCA、OPCA及OPSCA的理论最大吸附量分别为33.49、40.80和61.69 mg/g。3种吸附剂可利用0.1 mol/L的盐酸解吸再生,可循环使用3次以上。     

TiO_2/PTh/Fe_3O_4催化剂制备及光催化与磁回收性能

以聚噻吩磁性微珠PTh/Fe3O4(PF)为载体,采用低温水热法(170℃,pH=7±0.2)在其表面负载TiO2,制备了壳/壳/核结构的磁载光催化剂TiO2/PTh/Fe3O4(TPTF)。用透射电子显微镜(TEM)、X射线衍射仪(XRD)、傅里叶红外分光光度计(FT-IR)、振动样品磁强计(VSM)对催化剂的形貌、物相组成、表面性质、磁学性质进行了表征。以苯酚为模拟污染物,评价其光催化活性;通过自制的磁回收装置,考察其磁回收特性。结果表明,TiO2晶粒大小在4~6 nm之间,具有混晶结构(锐钛矿型占93.6%,金红石型占6.4%);当nTiO2∶n噻吩单体∶nFe3O4=75∶2.5∶1时,TPTF的催化活性最佳;P25、纯TiO2、TPTF(nTiO2∶n噻吩单体:nFe3O4=75∶2.5∶1)和TiO2/Fe3O4(TF)光催化降解苯酚的速率常数分别是0.0371、0.0302、0.0253和0.0106 min-1;TPTF循环使用5次,其反应速率常数、饱和磁化强度以及磁回收率为0.0205 min-1、1.59emu/g和89.3%,比第1次的0.0253 min-1、1.85 emu/g和94.7%略有降低。     

基于正交实验的颗粒移动床烟气脱硫工艺参数优化

石灰石颗粒移动床脱硫工艺参数是影响脱硫效率和操作压降变化的重要因素,考虑到工艺参数对脱硫过程的影响,基于正交实验方法,通过直观分析和方差分析得到喷淋密度、空床气速、SO2浓度、烟气温度和床层下移速度对脱硫效率影响程度的主次顺序和脱硫效率与各因素之间的关系,并且分析了各因素对脱硫效率的影响规律。研究发现,各因素对脱硫效率的影响程度依次是空床气速>喷淋密度>SO2浓度>烟气温度>床层下移速度。喷淋密度对脱硫效率的影响高度显著,呈正相关;空床气速对脱硫效率的影响高度显著,呈负相关;SO2浓度和烟气温度对脱硫效率有影响但不显著,呈负相关。床层下移速度与脱硫效率呈正相关。     

铋电极差分脉冲伏安法测定水中痕量2,4-二硝基苯肼

以自制铋电极作为工作电极,建立了铋电极差分脉冲伏安法测定2,4-二硝基苯肼的分析方法。实验结果表明：以0.1 mol/L NaOH+0.1 mol/L KCl混合溶液（pH=13.0）配制测定底液,在扫描速率为100 mV/s的条件下,2,4-二硝基苯肼于-0.53 V处产生灵敏的氧化峰;在2,4-二硝基苯肼浓度为3.0×10-8~1.0×10-5 mol/L范围内,空白和试样的氧化峰电流强度差值与对应2,4-二硝基苯肼浓度的对数呈良好的线性关系,检出限达8.37×10-9 mol/L;将该方法应用于工业废水中痕量2,4-二硝基苯肼的检测,回收率为95.6%~103.1%,相对标准偏差小于3%。     

Statistical analysis of sudden chemical leakage accidents reported in China between 2006 and 2011

According to the data from authoritative sources, 1,400 sudden leakage accidents occurred in China during 2006 to 2011 were investigated, in which, 666 accidents were used for statistical characteristic abstracted with no or little damage. The research results were as follows: (1) Time fluctuation: the yearly number of sudden leakage accidents is shown to be decreasing from 2006 to 2010, and a slightly increase in 2011. Sudden leakage accidents occur mainly in summer, and more than half of the accidents occur from May to September. (2) Regional distribution: the accidents are highly concentrated in the coastal area, in which accidents result from small and medium-sized enterprises more easily than that of the larger ones. (3) Pollutants: hazardous chemicals are up to 95 % of sudden leakage accidents. (4) Steps: transportation represents almost half of the accidents, followed by production, usage, storage, and discard. (5) Pollution and casualties: it is easy to cause environmental pollution and casualties. (6) Causes: more than half of the cases were caused by human factor, followed by management reason, and equipment failure. However, sudden chemical leakage may also be caused by high temperature, rain, wet road, and terrain. (7) The results of principal component analysis: five factors are extracted by the principal component analysis, including pollution, casualties, regional distribution, steps, and month. According to the analysis of the accident, the characteristics, causes, and damages of the sudden leakage accident will be investigated. Therefore, advices for prevention and rescue should be acquired.     

Effects of bromide and iodide ions on the formation of disinfection by-products during ozonation and subsequent chlorination of water containing biological source matters

This study aims to investigate the influence of the coexistence of halogen ions (bromide/iodide) and biological source matters on the speciation and yield of trihalomethanes (THMs), haloacetic acids (HAAs), and N-nitrosodimethylamine (NDMA) during the ozonation and subsequent chlorination of water. The results show that the concentrations of brominated THMs and iodinated THMs increased with increasing bromide and iodide concentration. These results may be attributed to the higher reactivity of hypobromous acid and hypoiodous acid generated from the ozonation and subsequent chlorination in the presence of bromide or iodide ions. The presence of bromide increased the species of brominated HAAs. There was a shift from chlorinated HAAs to brominated HAAs after increasing the concentration of bromide. The effect of iodide on HAA formation was more complex than bromide. For most samples, the concentration of total HAAs (T-HAAs) increased to the maximum and then decreased with increasing iodide concentration. The components of the organic precursors also significantly influenced the formation of brominated and iodinated disinfection by-products (Br-DBPs and I-DBPs). Humic acids produced more CHBr₃ (596.60 μg/L) than other organic materials. Microcystis aeruginosa cells produced the most tribromoacetic acid (TBAA, 84.16 μg/L). Furthermore, the yield of NDMA decreased with increasing bromide concentration, indicating that the formation of NDMA was inhibited by the high concentration of bromide.     

催化铁与生物法耦合除磷工艺特性

为了研究催化铁与生物耦合后对生物除磷特性的影响,实验采用人工配水用厌氧／好氧间歇流式富集培养聚磷微生物。对比发现,催化铁与生物耦合组中厌氧末段ORP降低了约60mV,pH值小幅度的上升（≤0．3）,整个培养过程中铁离子的浓度开始快速增加,之后趋于稳定（约40mgFe／gMLSS）。对好氧末段污泥SVI值比较发现,耦合工艺污泥沉降性能得到改善。除磷曲线比较发现,耦合组中厌氧末段磷的释放量下降,而好氧阶段磷的吸收速率增加;胞内聚合物提取表明,耦合组厌氧末段聚磷菌细胞内PHA含量有提高,好氧末段糖原含量有下降。磷形态提取分析表明,耦合组好氧末段污泥中无机态PO3 4-- P含量更高。低浓度铁离子可以起到与生物耦合同步除磷的目的,本工艺长期运行未发现耦合体系中催化铁对除磷的抑制作用。     

用于磷吸附的载铁（β-FeOOH）沸石制备及特性

以天然沸石为载体,采用FeCl3水解法制备用于磷吸附的载铁沸石（β-FeOOH-Z）,优化β-FeOOH-Z的制备条件,包括FeCl,溶液浓度、负载pH值、负载时间、负载温度和烘干温度,并利用x射线衍射（XRD）和傅里叶变换红外光谱（FTIR）对β-FeOOH-Z及其磷吸附特性进行分析。结果表明,β-FeOOH-Z的优化制备条件为：FeCl3溶液浓度1mol／L、负载pH值6、负载时间24h、负载温度25℃和烘干温度60℃。优化制备条件下,100-120目沸石的载铁量为100．2mg／g,铁的负载率为18％,其磷吸附量为7．68mg／g,比天然沸石提高79．6％。XRD分析结果表明,β-FeOOH-Z中的杂质元素较天然沸石减少,并有效负载β-FeOOH;制备条件对β-FeOOH-Z的成分有较大影响,FeCl,溶液浓度较低、负载温度和烘干温度过高均使β-FeOOH-Z中含有α-Fe2O3,并导致其磷吸附效率降低。FTIR分析结果表明,β-FeOOH-Z的表面羟基在其吸附磷过程中起重要作用,羟基与磷酸根离子的配位交换是β-FeOOH-Z吸附磷的主要作用机制。