黄酒行业工业废水COD与BOD_5相关性研究

对黄酒厂各工序产生废水及各酒厂产生综合性废水及其处理后的排放水进行ＣＯＤ、ＢＯＤ５的测定，对两者的相关性进行研究，同时对两种回归方程作方差分析及相关系数的显著性检验．回归方程的建立对酒厂污染源监测分析、环境管理具有实际意义．     

改性沸石对焦化废水中COD的去除研究

本文研究了沸石经NaCl、NaOH、HDTMA(溴化十六烷基三甲胺)改性后对焦化废水中的COD的去除效果.比较得出HDTMA改性沸石对COD的去除能力较好,而且废水的色度明显减小.接着进一步研究了该废水处理过程中的影响因素,包括吸附时间、烘干温度、改性剂HDTMA的浓度、pH值等.结果表明,HDTMA改性沸石处理焦化废水可使其COD的浓度降低至150mg/L以下,这到污水综合排放二级标准.     

浅谈混凝沉淀在炼油污水中的应用

随着国家对环保的重视，为确保处理效果，混凝沉淀技术在一些炼油污水中得到应用，并取得了较好的效果。     

Abating whey organic load through ethanol and lactic acid production by kefir

Abstract

The extent to which selected ethanol and lactic acid production bioprocesses contribute to whey waste abatement was examined. Alcoholic fermentation of whey was carried out by kefir cells immobilized on grape stalks, delignified cellulosic materials, or brewer's spent grains. Lactic acid fermentation was also performed by free kefir cells with or without addition of brewer's spent grains as promoting material. Since whey fermentation rate is affected by the lactose uptake rate, ¹⁴C-labeled lactose was used to study the fermentation ability of kefir. The highest reductions in biochemical oxygen demand and chemical oxygen demand of whey, about 68% and 52%, respectively, were achieved by lactic acid fermentation in 6 h at 37 °C and pH 5.5, in the presence of 120 g brewer's spent grains. Additionally, at the same conditions, the highest ¹⁴C-labeled lactose uptake rate by kefir and consequently the highest alcoholic fermentation rate were also recorded. However, greater reductions in biochemical oxygen demand and chemical oxygen demand of whey are required prior to final disposal.     

铁镍改性膨润土对废水中有机污染物的吸附性能研究

以钠基膨润土为原料,制备了铁镍无机改性土和铁镍有机复合改性土,并应用于造纸废水的处理,探讨了改性土用量、废水pH值、搅拌时间等因素对COD去除率的影响,通过正交实验对实验条件进行了优化.结果表明:铁镍有机复合改性土和铁镍元机改性土对废水的处理效果明显好于原土;膨润土的用量、废水的pH对COD的去除率影响较大;对于铁镍无机改性土,吸附剂用量为12g/L,溶液pH=2,吸附时间为10 min时,对废水中COD的去除率为54.06%;对于铁镍有机复合改性土,吸附剂用量为14g/L,溶液pH=3,吸附时间为20 min时,对废水中COD的去除率为70.10%.     

The removal of lignin and phenol from paper mill effluents by electrocoagulation

This study aims to investigate the treatment of paper mill effluents using electrocoagulation. Removal of lignin, phenol, chemical oxygen demand (COD) and biological oxygen demand (BOD) from paper mill effluents was investigated at various current intensities by using different electrodes (Al and Fe) and at various electrolysis times (1.0, 2.5, 5.0 and 7.5min). It was observed that the experiments carried out at 12V, an electrolysis time of 2min and a current intensity of 77.13mA were sufficient for the removal of these pollutants with each electrode. The removal capacities of the process using an Al electrode were 80% of lignin, 98% of phenol, 70% of BOD, and 75% of COD after 7.5min. Using an Fe electrode the removal capacities were 92%, 93%, 80% and 55%, respectively. In addition, it was found that removal of lignin, phenol, BOD and COD increased with increasing current intensity. In the experiments carried out at different current intensities, higher removal can be explained through a decrease in intra-resistance of solution and consequently an increase at the transfer speed of organic species to electrodes. It was also found that Al electrode performs higher efficiency than Fe electrode except for COD removal. However, the time required for removal of BOD was more than that of COD. The results suggest that electrocoagulation could be considered as an effective alternative to paper mill effluents treatment.     

不同加碱量下爆破制浆的源强试验研究

为了解爆破制浆的排污情况和废水处理的可行性,以烧碱和石灰作投加药剂,进行了不同加碱量条件下爆破制浆产生源强的试验研究,以确定最佳的加碱量和适宜的黑液提取率.研究表明,在加碱量相同的情况下,采用常规爆破浆样,浆样性能较好;在保持吨粗干浆产生的COD一致时,投加价格低廉的石灰,既能降低生产成本,又便于后续的废水处理;工程调试运行结果表明,控制吨粗干浆的石灰投加量为25～30 kg时,黑液提取率超过80%,最终出水COD<100 mg/L.     

聚硅酸氯化铝处理皂素废水的研究

制备了聚硅酸氯化铝(PASC)絮凝剂,并用其进行了皂素废水处理实验。考察了絮凝剂投加量、pH值、搅拌速度对COD和浊度去除率的影响。结果表明,当絮凝剂投加量为9～13.5 mg/L、pH值5～7、搅拌速度150～250 r/min时,COD和浊度去除效果较好。最佳工艺条件为：絮凝剂投加量11.25 mg/L、pH值6、搅拌速度200 r/min。此时,COD去除率为93.7％,浊度去除率为97.5％。PASC的絮凝性能明显优于PAC。     

絮凝法处理含水溶性膦配体TPPTS废水

以Al-Fe混凝荆、聚丙烯酰胺（PAM）、十六烷基三甲基溴化铵（CTAB）为助凝剂,考察了水溶性膦配体间磺酸钠基三苯基膦（TPPTS）废水中化学耗氧量（COD）的去除率,以此来间接考察TPPTS的去除效果。结果表明,助凝剂的添加能提高COD的去除率。获得了化学耗氧量COD 1000～1500mg／L废水除膦的优化条件：pH=5．5,Al-Fe、CTAB、PAM的投加量分别为300mg／L、67mg／L和21mg／L时,COD去除率达92．9％。     

两相UASB反应器处理含高浓度硫酸盐黑液

两相UASB反应器处理含高浓度硫酸盐黑液,酸化相为8.87L的普通升流式反应器,甲烷相为28.75L的UASB反应器,系统温度(35±1)℃。当酸化相进水COD为(6.771～11.057)g/L,SO42-为(5.648～8.669)g/L,pH值为5.5时,整个系统COD去除率平均值为74.42%;系统对负荷的冲击有较强的耐受能力。