一种高效复合絮凝剂对多种废水的处理效果

用聚合氯化铝（PAC）和聚丙烯酰胺（PAM）复配成复合絮凝剂（PAC＋PAM）应用于污染河水、生活污水、工业废水和餐饮废水等6种废水的处理，结果表明。PAC、PAM、PAC＋PAM对污染河水的CODc。SS、浊度有显著降低作用，PAC＋PAM的净水效果明显优于PAC和PAM；PAC＋PAM对6种废水中COD的去除率为81．5％～90．4％，平均84．6％。对SS的去除率为81．9％～96．5％，平均88．9％，对浊度的去除率为91．3％-98．0％，平均95．1％；处理后悬浮物基本被絮凝沉降，水体变得较清澈透明，异味或臭味消除。说明本PAC＋PAM复合絮凝剂对各种废水均有良好的净水效果，具有重要的应用价值。     

混凝沉降法处理洗衣废水的实验研究

洗涤废水含有表面活性剂和磷酸盐物质，直接排入水体会造成水体的污染，增加给水处理厂的处理难度，甚至会引起水体富营养化。本实验是通过投加PAC和PAM絮凝沉降联合活性炭吸附来处理商业洗涤废水，以去除废水中的COD。实验表明：采用PAC PAM 活性炭工艺处理洗衣废水的效果较好，投药过程COD的去除率可以达到60％以上，经过活性炭过滤后，总的去除率可以达到86％。出水ODD可以降至在50mg／L左右。     

絮凝- 电气浮法处理乳化油废水

含乳化油废水由于表面活性剂的存在处理难度较大。通过絮凝——电气浮方法处理乳化油废水,确定絮凝及絮凝——电气浮所需的最佳絮凝剂用量;通过正交试验考察了pH值、电流密度、电极间距及气浮时间等操作参数的影响,得到絮凝一电气浮的最优操作条件为电流密度为20．83A／m^2,电极间距为1cm,pH值为7．4。在聚合硫酸铁投加量为50mg／L,电气浮30min时COD去除率可达95．2％。此方法对轴承厂废水的COD去除率可达75％,出水COD可降至91．9mg／L。结果表明用这种方法处理乳化油废水是可行的。     

HY1141和HY241菌产生的絮凝剂絮凝性能及水处理应用研究

从土壤中分离筛选得到絮凝剂产生菌HY1141和HY241，对高岭土悬浊液进行絮凝性能试验研究。试验结果表明：HY1141絮凝荆在ptt值为3．0时，絮凝率达到97．2％，HY241絮凝剂在pH值为4．0-7．0时，絮凝率在90％以上；絮凝剂的最佳投加量均为4mL／L，此时絮凝率分别达到98．2％和96．5％；HY1141和HY241絮凝剂所需CaCl2，最佳浓度分剐为0．5％和1．0％，此时絮凝率分刺为97．6％和96．8％；絮凝荆最佳静置时间分别为5min和10min。此外，两株菌所产絮凝刘对洪水和选矿废水都有一定的处理效果，且HY1141絮凝剂处理洪水效果较好，絮凝率为71．7％，COD去除率为81．8％；混合絮凝刺处理选矿废水效果较好，絮凝率为92．8％，COD去除率为96．0％。     

纳米级聚合氯化铝处理石化废水絮凝效果研究

采用自制的纳米级聚合氯化铝絮凝荆处理石大科技股份公司胜华炼油厂隔油池出水，以处理后水样的透光率作为混凝沉降效果的评价指标，并对絮凝剂投加量、搅拌速度、搅拌时间等影响混凝效果的因素进行了研究。试验表明，聚合氯化铝对石化废水的处理达到较为理想的效果，聚合氯化铝混凝处理石化废水的最佳条件为：纳米级聚合氯化铝投加量为15mg／L左右，慢速搅拌的搅拌速度为50～60rpm，快速搅拌的搅拌速度为190—225rpm，快速搅拌时间90s。慢速搅时间10min时效果最佳。使用Al-Ferron逐时络合比色法及XRD对絮凝荆进行了表征，结果证实样品中Alb含量可达到85％左右。     

聚合氯化铝与水解聚丙稀酰胺复合絮凝剂JX-3的制备及室内评价试验

在无机高分子絮凝剂聚合氯化铝(PAC)中引入有机高分子水解聚丙稀酰胺(PHP),制备出一种复合絮凝剂JX-3。PAC和PHP在其中可起到电性中和及絮凝桥架的的双重作用,使絮团紧密结合,提高絮凝效果,室内评价试验表明JX-3处理含轻油污水效果优于PAC和聚丙稀酰胺(PAM)。     

高黏度压裂废液絮凝处理实验

压裂废液的高黏度导致其流动性差,投加的PAC、PAM等常规处理剂在废液中很难扩散,传质作用慢,造成絮凝沉淀时间长,絮体虚浮、泥量体积比大,处理效果差。投加膨润土可改善高黏度压裂废液絮凝处理效果,缩短沉降时间。实验表明:最佳处理条件为膨润土加量800¹ 000 mg/L,PAC加量2001 000 mg/L,PAC加量200³00 mg/L.,投加膨润土后搅拌1300 mg/L.,投加膨润土后搅拌1² min;混凝处理后悬浮固体去除率97.5%,石油类去除率88.6%,污泥体积减少50%以上,沉降时间缩短90%。     

壳聚糖/碱铝复配絮凝剂在炼油污水处理中的应用

研究了壳聚糖(CHI)／碱铝(PAC)复配絮凝剂对炼油污水的处理效果，考察了pH值、搅拌时间、沉降时间对炼油污水处理效果的影响，并将之与聚丙烯酰胺(GD-112)／PAC复配絮凝剂对炼油污水处理的效果进行对比。结果表明，CHI／PAC复配絮凝剂在复配比为1：5，pH为7，搅拌10min且沉降10min时处理效果最好，具有适应性广、投加量少、浮渣少、毒性低等特点。     

CM-3絮凝剂的室内研制及在含油污水处理中的应用

介绍复合高分子絮凝剂CM─3的研制。CM─3是以无机高分子聚合铝（PAC）、有机高分子改性聚丙烯酰胺（APAM）为主，添加少量的硫酸根离子及破乳剂复配而成的。经室内实验研究确定了适合的PAM分子量、改性PAM的胺甲基化度、PAM与PAC的比例以及其他组分的添加量，并与PAC比较进行了室内及现场应用试验，结果表明CM─3投药量为20～30mg／L时，炼油厂含油污水处理后的水质符合GB8978─88的标准。     

吉林油田稠油热采污水处理絮凝剂实验研究＊

在含油污水水质分析的基础上,采用烧杯实验和分光光度法研究絮凝剂的絮凝效果。筛选出以无机絮凝剂硫酸铝与两性高分子聚合物CE-3090的复配体系,同时研究了影响絮凝效果的因素并探究了其影响机理。结果表明:在温度为40℃,pH为7.72,170 r/min时高速搅拌1 min,然后50 r/min低速搅拌5 min,硫酸铝的加量为90 mg/L、CE-3090的加量为0.5 mg/L,絮凝沉降30 min后其絮凝效果较好。实验证明:该复配处理剂处理含油污水后,含油量和杂质含量都达到了SY/T 5329-94《碎屑岩油藏注水水质推荐指标及分析方法》油田污水回注的要求。     

稠油区块含油污泥化学清洗方法研究

以稠油区块含油污泥为研究对象,确定了一种化学清洗方法,使稠油含油污泥清洗后油类含量≤2%。研究了化学清洗过程中固液比、搅拌速度、搅拌时间、加热温度等工艺技术参数对化学清洗效果的影响。通过化学清洗性能评价表明,采用两段化学清洗对稠油含油污泥中油类组分清洗效果最优,其中第一段清洗最优参数为实验温度80℃;固液比1∶4;药剂投加量为SH3.2%,SC 0.8%;搅拌速度250 r/min;搅拌时间30 min。第二段清洗最优参数为实验温度60℃;固液比1∶4,;药剂投加量为EP1.0%,三乙醇胺油酸皂1.0%,SE 1.5%;搅拌速度150 r/min;搅拌时间90 min。     

C_8-SBA-15新型介孔涂层SPME-HPLC联用测定水样中的芘

以辛基键合SBA-15为固相微萃取（SPME）的吸附涂层,考察了吸附和解吸时间、萃取温度、搅拌速率对SPME效率的影响。该方法的线性范围为3.0—320μg/L,检出限为0.5μg/L,依据此方法测定了环境水样中芘,具有灵敏度高和精密度好的特点。     

炼油废水回用于循环冷却水系统深度处理技术

为解决水资源紧缺问题,提高工业水资源的利用率,减少污水排放,采用臭氧催化氧化—活性炭吸附—石灰软化的工艺组合,深度处理炼油厂中二级处理达标排放的污水,探讨最佳工艺参数的选择,进行二级出水回用于循环冷却水的试验研究。试验表明:在臭氧氧化接触时间为40min,活性炭柱吸附通水流量为2L/h,石灰乳投加量0.32g/L、碳酸钠溶液0.06～0.10g/L、石灰软化搅拌15～20min,能使整套工艺达到最佳处理效果。小试阶段COD、氨氮、总硬度及总碱度的去除率分别达到96.00%、44.49%、64.61%、67.85%,硫酸根和氯离子均有所下降,通过整套工艺深度处理后,所得中水可作为循环冷却系统补充水。     

饮用矿泉水中微量钡的测定方法

采用硫酸钡比浊法测定饮用矿泉水中微量的钡。结果如下：１＋１０硫酸用量以５ｍＬ为最佳;标准曲线相关系数达极显著水准;回收率９５—１０７％;变异系数６４８％;最佳比浊时间为停止搅拌后３０ｍｉｎ内     

花生壳对Cr（Ⅵ）的等温吸附模型研究

在花生壳吸附剂量为1.0g、pH2.0、温度30℃、振荡速度140r/min、吸附时间360min条件下,实验研究了不同初始浓度（50 mg/L、75 mg/L、100 mg/L、125 mg/L、150 mg/L）的Cr（Ⅵ）溶液等温吸附曲线。研究结果表明,Langmuir等温吸附模型符合得更好;该吸附是一个优先吸附过程;最大饱和吸附量为6.25mg/g。     

Fed-batch and batch operating mode analysis of a stirred anaerobic sequencing reactor with self-immobilized biomass treating low-strength wastewater

This work presents an analysis of a stirred anaerobic sequencing discontinuous reactor with different substrate feeding strategies resulting in batch, fed-batch/batch and fed-batch operating modes. The reactor, containing granulated biomass, was fed with approximately 2.0L of synthetic domestic wastewater with Chemical Oxygen Demand of nearly 500 mg/L per cycle and operated at 30 degrees C and 50 rpm. Three feeding strategies with a total cycle time of 6 h, including 30-min settling, were adopted: batch mode with a fill cycle of 6 min, a fed-batch/batch mode with fill cycles of 60, 120 and 240 min and fed-batch mode with a fill cycle of 320 min. The system attained average non-filtered and filtered substrate removal efficiency of 78 and 84%, respectively, for all operating conditions, presenting good stability, solid retention and no granule break-up. A first order kinetic model with a residual organic matter concentration was proposed to analyze the influence of the feeding strategy on the performance during a cycle and bicarbonate alkalinity and total volatile acids concentration profiles were also quantified in order to verify the transient stability behavior.     

Recovery of phosphate from calcinated bone by dissolution in hydrochloric acid solutions

In this study, the optimum conditions of dissolution of calcinated bone in HCl solutions with different concentrations are investigated. Recovery of phosphate from calcinated bone by dissolution with hydrochloric acid solutions was investigated in a batch reactor, it was observed that a 32% hydrochloric acid solution can dissolve the calcinated bone effectively. Using the Taguchi fractional design method, it was found that the optimum process conditions, at which 67.2% P₂O₅ dissolution was reached, were as follows: Reaction temperature: 318 K, solid-to-liquid ratio: 1/5 (g ml⁻¹), acid concentrations:32 (% w/v), stirring speed:400 min⁻¹ and reaction time: 60 min.     

Aerobic treatment of palm oil mill effluent

In this study treatment of palm oil mill effluent (POME) was investigated using aerobic oxidation based on an activated sludge process. The effects of sludge volume index, scum index and mixed liquor suspended solids during the acclimatizing phase and biomass build-up phase were investigated in order to ascertain the reactor stability. The efficiency of the activated sludge process was evaluated by treating anaerobically digested and diluted raw POME obtained from Golden Hope Plantations, Malaysia. The treatment of POME was carried out at a fixed biomass concentration of 3900+/-200mg/L, whereas the corresponding sludge volume index was found to be around 105+/-5mL/g. The initial studies on the efficiency of the activated sludge reactor were carried out using diluted raw POME for varying the hydraulic retention time, viz: 18, 24, 30 and 36h and influent COD concentration, viz: 1000, 2000, 3000, 4000 and 5000mg/L, respectively. The results showed that at the end of 36h of hydraulic retention time for the above said influent COD, the COD removal efficiencies were found to be 83%, 72%, 64%, 54% and 42% whereas at 24h hydraulic retention time they were 57%, 45%, 38%, 30% and 27%, respectively. The effectiveness of aerobic oxidation was also compared between anaerobically digested and diluted raw POME having corresponding CODs of 3908 and 3925mg/L, for varying hydraulic retention time, viz: 18, 24, 30, 36, 42, 48, 54 and 60h. The dissolved oxygen concentration and pH in the activated sludge reactor were found to be 1.8-2.2mg/L and 7-8.5, respectively. The scum index was found to rise from 0.5% to 1.9% during the acclimatizing phase and biomass build-up phase.     

Temperature and feed strategy effects on sulfate and organic matter removal in an AnSBB

The objective of this work was to analyze the interaction effects between temperature, feed strategy and COD/[SO(4)(2-)] levels, maintaining the same ratio, on sulfate and organic matter removal efficiency from a synthetic wastewater. This work is thus a continuation of Archilha et al. (2010) who studied the effect of feed strategy at 30 °C using different COD/[SO(4)(2-)] ratios and levels. A 3.7-L anaerobic sequencing batch reactor with recirculation of the liquid phase and which contained immobilized biomass on polyurethane foam (AnSBBR) was used to treat 2.0 L synthetic wastewater in 8 h cycles. The temperatures of 15, 22.5 and 30 °C with two feed strategies were assessed: (a) batch and (b) batch followed by fed-batch. In strategy (a) the reactor was fed in 10 min with 2 L wastewater containing sulfate and carbon sources. In strategy (b) 1.2 L wastewater (containing only the sulfate source) was fed during the first 10 min of the cycle and the remaining 0.8 L (containing only the carbon source) in 240 min. Based on COD/[SO(4)(2-)] = 1 and on the organic matter (0.5 and 1.5 gCOD/L) and sulfate (0.5 and 1.5 gSO(4)(2-)/L) concentrations, the sulfate and organic matter loading rates applied were 1.5 and 4.5 g/L.d, i.e., same COD/[SO(4)(2-)] ratio (=1) but different levels (1.5/1.5 and 4.5/4.5 gCOD/gSO(4)(2-)). When reactor feed was 1.5 gCOD/L.d and 1.5 gSO(4)(2-)/L.d, gradual feeding (strategy b) showed to favor sulfate and organic matter removal in the investigated temperature range, indicating improved utilization of the electron donor for sulfate reduction. Sulfate removal efficiencies were 87.9; 86.3 and 84.4%, and organic matter removal efficiencies 95.2; 86.5 and 80.8% at operation temperatures of 30; 22.5 and 15 °C, respectively. On the other hand, when feeding was 4.5 gCOD/L.d and 4.5 gSO(4)(2-)/L.d, gradual feeding did not favor sulfate removal, indicating that gradual feeding of the electron donor did not improve sulfate reduction.     

Management strategy impacts on ammonia volatilization from swine manure

Ammonia emitted from manure can have detrimental effects on health, environmental quality, and fertilizer value. The objective of this study was to measure the potential for reduction in ammonia volatilization from swine (Sus scrofa domestica) manure by temperature control, stirring, addition of nitrogen binder (Mohave yucca, Yucca schidigera Roezl ex Ortgies) or urease inhibitor [N-(n-butyl) thiophosphoric triamide (NBPT)], segregation of urine from feces, and pH modification. Swine manure [total solids (TS) = 7.6-11.2%, total Kjeldahl nitrogen (TKN) = 3.3-6.2 g/L, ammonium nitrogen NH(+)(4)-N = 1.0-3.3 g/L] was stored for 24, 48, 72, or 96 h in 2-L polyvinyl chloride vessels. The manure was analyzed to determine pre- and post-storage concentrations of TS and volatile solids (VS), TKN, and NH(+)(4)-N. The concentration of accumulated ammonia N in the vessel headspace (HSAN), post-storage, was measured using grab sample tubes. Headspace NH(3) concentrations were reduced 99.3% by segregation of urine from feces (P < 0.0001). Stirring and NBPT (152 microL/L) increased HSAN concentration (119 and 140%, respectively). Headspace NH(3) concentration increased by 2.7 mg/m(3) for every 1 degree C increase in temperature over 35 degrees C. Slurry NH(+)(4)-N concentrations were reduced by segregation (78.3%) and acidification to pH 5.3 (9.4%), and increased with stirring (4.8%) and increasing temperature (0.06 g/L per 1 degree C increase in temperature over 35 degrees C). Temperature control, urine-feces segregation, and acidification of swine manure are strategies with potential to reduce or slow NH(+)(4)-N formation and NH(3) volatilization.