分散填料曝气塔多相流态分析与传氧性能表征

针对分散填料曝气塔中多相流的流态与传氧过程,实验了布气方式以及海绵和陶粒2种填料对于体系的气含率εg、流态以及气-液传质性能的影响。在表观气速U范围(0.01～0.18 m/s)内观察到81孔布气板(Φ1 mm)体系出现3个明显相区,孔数过少(25孔),或者孔间距较小(225孔)均没有明显过渡区,在湍流区(U>0.118 m/s)3种布气板的气含率没有明显差别。海绵填料体积分数εs<25%时体系的气含率没有明显变化,35%时气含率下降且过渡区提前出现。在非均相区,海绵填料明显提高了体系的传质系数KLa。陶粒填料降低了气含率,固含率对εg的影响差别不明显,同时降低了多相流体系的KLa,且随着固含率的增加KLa降低。对比多种操作条件,单位体积空气传氧能力KLa/εg无明显差别,但在81孔布气板的过渡区KLa/εg出现一个明显的极小区间,说明过渡区传氧效率较低。在特定的实验操作条件下,KLa/εg较为稳定,这为深入理解两种气泡群体的共存体系在传氧性能方面各自的权重,提供了重要的量化参考。     

Tylosin Sorption to Silty Clay Loam Soils,Swine Manure,and Sand

The objectives of this study were to assess sorption and desorption of tylosin, a macrolide antimicrobial chemical used in swine, cattle, and poultry production, in three silty clay loam soils of South Dakota and compare soil sorption to sand and manure sorption. The silty clay loam soils, from a toposequence in eastern South Dakota, standardized sand samples, and swine manure were used in 24-h batch sorption studies with tylosin concentrations ranging from 25 to 232 μ mole/L. Desorption from soil was conducted over a four-day period. Partition coefficients, based on the Freundlich isotherm (K _f ) or K _d values, were calculated. K _f values for the silty clay loams were similar, not influenced by landscape position, and averaged 1350 with isotherm slopes ranging from 0.85 to 0.93. K _f values for sand were dependent on solution/sand ratios and pH, ranging from 1.4 to 25.1. K _d values of manure were dependent on the solution type and ranged from 840 L/kg with urine to about 175 L/kg when sorbed from water. Desorption of tylosin from each soil over the four-day period was < 0.2% of the amount added. The soils' high K _f values and low desorption amounts suggest that once tylosin is in these soils, leaching to lower depths may not occur. However, this does not preclude runoff with soil eroded particles. If tylosin reaches a sand aquifer, through bypass flow or other mechanism(s), movement in the aquifer most likely would occur.     

不同工艺对含高浓度腐殖酸地下水处理的可行性

针对内蒙古农村地区高腐殖酸地下水的处理问题,分别对（pH调节）-PAC强化混凝、高锰酸钾预氧化／混凝、活性炭吸附／混凝、Fenton氧化等技术处理的可行性进行了研究,同时利用三维荧光和高效体积排阻色谱分析处理前后水中有机物的组成变化特征。有机分析结果显示,水中的有机物为腐殖酸类物质,分子量分别为1600和3500,腐殖酸类物质为水中色度的主要贡献者。原水PAC强化混凝、高锰酸钾预氧化／PAC混凝对有机物的去除效果不佳,处理前后水样DOC浓度无明显变化,而pH调节．PAC强化混凝、微米活性炭吸附和Fenton氧化均能有效去除有机物。将原水pH调节至6．5,经300mg／LPAC混凝后出水DOC降至5．99mg／L。活性炭投加量为0．6g／L时,DOC降至7．6mg／L,然后采用60mg／LPAC混凝出去高度分散而不易沉降的小颗粒活性炭。此外,当反应初始pH值为3,过氧化氢投加量为0．5％（v／v）,亚铁和双氧水摩尔比为0．05时,出水DOC降至5．6mg／L,氧化后有小分子有机物生成。     

Evaluation of the effect of different treatment methods on sugarcane vinasse remediation

Abstract

Sugarcane vinasse is a by-product obtained during ethanol production in sugar-ethanol plants. For each 1?L of ethanol produced approximately 11?L of vinasse are generated. As this residue is obtained in high amounts, it is used as fertilizer in sugarcane crops. However, despite being rich in nutrients, sugarcane vinasse is approximately one hundred times more polluting than domestic sewage, making it an environmental problem. Thus, the aim of the present study was to propose a treatment sequence for sugarcane vinasse and evaluate the possibility of energetic use of the generated sludge in the coagulation/flocculation stage. pH, conductivity, turbidity and decreases in UV/Vis absorption spectra were determined for each treatment step. In addition, the upper calorific value of the generated sludge was also determined, while ash (adsorption treatment) and catalyst (heterogeneous photocatalysis) characterizations were also carried out. At the end of the treatment, initial vinasse turbidity was reduced by 100% and pH and conductivity values were stabilized. The sludge presented a higher calorific value of approximately 3,000?kcal kg^?1 and the ash and catalyst displayed favorable characteristics to be applied to the sugarcane vinasse treatment stages.     

响应面法优化克浅十油田废水的混凝沉淀工艺

以克浅十污水处理站原水为研究对象,采用混凝沉淀工艺,探讨优选出的复配混凝剂投加量、助凝剂投加量及静置时间对原水中浊度和总铁去除效果的影响.应用Box-Behnken中心组合实验和响应面分析法,建立混凝剂对处理原水的二次多项式数学模型,确定了混凝沉淀去除原水浊度和总铁的优化工艺参数分别为:复配混凝剂投加量为152.15 mg/L、143.84 mg/L,助凝剂投加量为4.14 mg/L、4.32 mg/L,静置时间为11.77 min、11.22 min.在此工艺条件下回归方程得到的浊度和总铁的去除率预测值与实验值接近,且拟合性良好,误差介于3％～5％之间.通过均值内插法,对比浊度和总铁的多元二次回归方程,推导得出的2组最佳工艺条件均能满足浊度和总铁的去除要求.     

高浊度钼矿浮选废水的混凝沉淀

针对某钼矿选矿厂浮选废水,以PAC、PFS和FeCl3为凝聚剂,以APAM-A和APAM-N为絮凝剂,以H2SO4和NaOH为pH调整剂,研究了不同混凝剂、不同pH值和不同水力条件下废水处理后的浊度和COD.实验结果表明,在最佳水力条件下,原水pH不调整,以APAM-A为絮凝剂,以PAC为凝聚剂,其用量分别为15 g/t,750g/t时,处理后上清液浊度为25 NTU,COD小于30 mg/L.浮选废水经处理后回用于选矿浮选流程,大大改善了选矿指标.     

典型危险废物的工程力学特性

掌握填埋废物的工程力学特性是确保危险废物填埋堆体稳定性的重要前提条件,因此,针对6种典型危险废物的工程力学特性开展了调查研究.研究结果表明,污泥类危险废物的含水率和有机质含量远高于非污泥类危险废物,而前者的比重则显著低于后者.污泥类危险废物的渗透系数相对较小,比污染土壤和飞灰炉渣混合物的渗透系数小1个数量级,比滤池填料的渗透系数小2个数量级.不同危险废物的无侧限抗压强度排序为:飞灰炉渣混合物(314.3 kPa)和滤池填料(278.9 kPa)＞污染土壤(124.9 kPa)＞杭州氧气厂污泥(68.6 kPa)、锌铬污泥(71.4 kPa)、油泥(58.4 kPa).不同危险废物的粘聚力排序为:飞灰炉渣混合物(40.8 kPa)、滤池填料(31.1 kPa)＞污染土壤(20.9 kPa)＞杭州氧气厂污泥(1.94kPa)、锌铬污泥(3.10 kPa)、油泥(1.81 kPa).此外,不同危险废物的内摩擦角差异相对较小,其变化范围在18.8°～35.0°之间.综合分析可知,飞灰炉渣混合物和滤池填料的工程力学特性较好,而污泥类危险废物的工程力学特性则较差.     

强化混凝去除尖针杆藻

嘉陵江水系藻类暴发,水源水中的藻类在水厂前处理工艺中难以去除,造成该流域附近10余个水厂发生滤池堵塞现象,其中个别水厂滤池反冲洗周期由正常情况的24 h缩短至2~3 h,严重影响净水厂的正常运行,使得制水能力大幅降低。针对藻类(优势藻为硅藻中的针杆藻)暴发问题,通过对比PAFS、PAC和PFC3种混凝剂的除藻除浊效果,选取PAFS为最佳混凝剂;通过添加预氧化剂和助凝剂强化混凝除藻效果,其结果表明,使用助凝剂PDMDAAC的对PAFS的助凝效果最好,其余药剂结合PAFS的除藻效果为PPC>ClO2>PAM>H2O2>HCA-1,并将其应用到现有水厂,结果表明,0.6mg/L PDMDAAC+25 mg/L PAFS在水厂混凝沉淀,尖针杆藻含量降至49×104~55×104cells/L,其除藻率可达70%~75%,大大减轻了滤池的运行负荷,使得水厂运行恢复到正常水平。     

硅藻土强化混凝处理线路板含络合铜废水

采用硅藻土对聚合硫酸铁（PFS）、聚合氯化铝（PAC）的混凝能力进行强化,并用于线路板含络合铜废水中铜的去除。考察了硅藻土加入量、混凝剂加入量、pH、快速搅拌速率和沉淀时间等因素对除铜效果的影响,并与目前常用的硫化钠破络方法进行了对比。实验结果表明：硅藻土强化混凝的除铜效果明显好于单独投加PAC或PFS;PFS-硅藻土除铜效果好于PAC-硅藻土;在pH为8.0~9.0、硅藻土加入量为120 mg/L、PFS加入量为60 mg/L、快速搅拌速率为250 r/min的条件下,沉淀40 min后可使出水铜质量浓度低于0.30 mg/L,比传统破络工艺出水水质更稳定,成本更低。     

强化混凝法处理煤气冷凝水

以包头钢铁(集团)有限责任公司高炉煤气冷凝水为处理对象,采用强化混凝法进行静态混凝沉淀对比实验。实验结果表明,当聚合氯化铝加入量为20mg/L、高分子纳米除氯剂加入量为2.0mL/L时,处理后出水SS小于10mg/L,浊度小于10NTU,氯离子去除率在80%以上,而且对废水中的其他离子也有一定的去除效果,出水水质基本接近工业冷却循环水回用指标。