共查询到19条相似文献,搜索用时 218 毫秒
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为了提高矿井水处理系统的处理能力,改善出水水质,降低运行费用,实现矿井水的资源化回用,对某矿高悬浮物矿井水处理工艺系统进行了改进研究。改进后的处理工艺采用"絮凝污泥回流强化助凝反应+高密度预沉淀+混凝反应+高效沉淀",部分出水采用石英砂滤罐进一步降低浊度后供给工人洗澡用水。首先通过对浊度为802 NTU的原水进行的混凝试验研究确定了2号PAC与PAM为最佳混凝剂和助凝剂,最佳投加量分别为140 mg/L、0.1 mg/L,出水浊度可降为2.3 NTU;在此基础上,为了进一步降低药剂投加量以降低水厂的运行费用,采用絮凝污泥回流强化助凝反应并完成高密度预沉淀后再进行混凝沉淀处理。结果表明:当絮凝污泥回流比为原水量的12%时,混凝反应时最佳投药量PAC、PAM分别为80 mg/L、0.1 mg/L,PAC投药量降低了43%,出水浊度可降为2.1 NTU。 相似文献
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设计开发了一种新型的集浓缩澄清为一体的综合池中试装置.以江苏某湖水作为试验原水,考察了速度梯度G、进水水力负荷、回流泥渣浓度、泥渣回流比及污泥固体负荷等因素对综合池出水浊度和排泥水含固率的影响.研究结果表明,在达到设计进水负荷及回流泥渣浓度的条件下,控制搅拌梯度在100~115 s~(-1),其出水浊度达到1~2 NTU,排泥水含固率为4.2%~3.9%,此时泥渣回流比为2.5∶1~3∶1.当进水负荷增大至原来的1.2倍时,改变速度梯度至105~120 s~(-1),也可达到最佳运行工况,此时浊度在1~2 NTU,但排泥水含固率减至3.1%~3.0%,泥渣回流比为2.5∶1~2.8∶1.这种新型的浓缩澄清中试装置具有良好的应用前景和工程推广价值. 相似文献
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将含粉末活性炭(PAC)的沉淀池排泥水回流至原水进水处,延长PAC在系统中的停留时间,考察系统对氨氮、有机物和浊度的去除效果及去除氨氮的影响因素.结果表明,在温度为21~25℃,投炭量为50 mg/L条件下,系统第7~8天运行稳定,对氨氮、UV254和CODMn的去除率分别为40%、45%和60%左右,出水浊度在1 NTU左右,活性炭泥的生物量为130 nmolP/g左右.当活性炭泥回流比为6%,原水CODMn不超过10 mg/L,Ph为7~8,浊度不超过180 NTU时,对氨氮去除效果最好,为40%~50%,可应对原水氨氮浓度小于1 mg/L的情况. 相似文献
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针对以黄河水为原水的给水厂污泥进行了混凝及优选比阻调理试验,结果表明:当进行给水厂污泥脱水技术改造方案设计时,可以不经过混凝处理,直接利用电厂粉煤灰作为比阻调理剂。细粉煤灰的最佳投加率为20%,粗粉煤灰的最佳投加率为30%,使污泥比阻由1013数量级降至1010数量级,改善了污泥脱水性能,所得滤饼含水率仅为40%~50%,易于剥离,能耗低,所得滤液的色度、浊度、CODMn均达到可直接回用标准。当进行技改工程设计时,建议选用带式压滤机或板框压滤机,既适应粉煤灰调理剂,又可节约投资。 相似文献
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洗浴废水处理工艺中混凝预处理的作用与效果研究 总被引:1,自引:0,他引:1
采用混凝沉淀—过滤—固定化生物活性炭—膜滤—UV 消毒工艺处理洗浴废水,整体试验结果比较理想,在物化处理过程中混凝环节至关重要。为此研究了混凝对浊度、LAS、COD_(Cr)、洗浴浴香的处理效果。研究结果表明:当投药量大于25mg/L 时,混凝沉淀可以把平均浊度为65NTU的原水降低到15NTU 以下,对 LAS、COD_(Cr)的去除率可达62%和50%以上,因此混凝是去除洗浴废水中悬浮物质、LAS 和有机污染物有效的物化处理单元;但是混凝不能有效地去除洗浴废水中的浴香。 相似文献
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为了总结长江上游高浊度原水处理工艺设计经验和修编《高浊度水给水设计规范》(CJJ40—91),对川渝地区数座城市的供水企业进行了调研。长江上游干流(含金沙江)及其支流的浊度每年有数十天在1 000 NTU以上,数天在3 000 NTU以上,并有上1万NTU的情况,属多沙高浊度水体。近20年设计的高浊度水给水工程多采用两级混凝沉淀工艺流程,运行效果良好。对多沙高浊度原水给水工程的取水、絮凝、沉淀和排泥的形式作了介绍。 相似文献
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《给水排水》2017,(6)
针对最新开发的带有新型絮凝装置的沉淀设备,在进水浊度及进水流量变化的条件下,考察其在连续运行下的净水效果。结果表明:当原水浊度低于50NTU时,最佳投药量在8~10mg/L,当原水浊度在50~100NTU时,最佳投药量在10~15mg/L,出水浊度均小于3NTU;设计流量下,设备排泥周期为9h;当进水流量分别为192m~3/d、240m~3/d、288m~3/d时,出水平均浊度分别为2.17NTU、2.07NTU、2.76NTU,出水平均UV_(254)为0.037cm~(-1)、0.037cm~(-1)、0.039cm~(-1),出水平均CODMn为1.47mg/L、1.54mg/L、1.54mg/L,表明设备抗冲击负荷能力强,处理效果好,运行稳定。 相似文献
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在常规处理条件下,对西南岷江地区突发性非多砂高浊水进行了原水特性的分析及絮凝优化试验。结果表明,采用单级絮凝、分级沉淀工艺,先投加PAC,60~120s后投加PAM,对高浊度原水有良好的去除效果。原水浊度为15000NTU时,投加200mg/LPAC、0.4~0.5mg/LPAM,静沉30min后,出水浊度为1.73~2.48NTU。 相似文献
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摘要:在常规处理条件下,对西南岷江地区突发性非多砂高浊水进行了原水特性的分析及絮凝优化试验。结果表明,采用单级絮凝、分级沉淀工艺,先投加PAc,60~120s后投加PAM,对高浊度原水有良好的去除效果。原水浊度为15000NTU时,投加200m∥LPAC、0.4-0.5mg/LPAM,静沉30min后,出水浊度为1.73-2.48NTU。 相似文献
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分析龙滩电站纳付堡水厂的水净化工艺选择适宜的搅拌试验条件,提高搅拌试验与实际混凝过程的相似性。结果表明,在进水浊度为34.2~47.9NTU,水温在0~15℃的条件下,最佳理论聚合铝投加量为14mg/L,此时沉淀池出水浊度可控制在3NTU左右,滤池出水可达1NTU以下。 相似文献
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Immersed membrane systems, and those with in-line coagulation, have been extensively applied in drinking water systems. Sedimentation is usually replaced by membrane processes in both systems. In these systems, voluminous flocculent aggregates formed during coagulation could be potential foulants. When raw waters with high turbidity are introduced, particle loadings to membrane due to coagulation pretreatment are enormous and thus could increase fouling. In general, during the rainy season, the turbidity of the Han River water, which supplies drinking water for the City of Seoul, Korea, is more than a hundred times higher than usual. Therefore, effects of floc on membrane fouling were investigated with highly turbid waters. Two turbidity concentrations, 40 and 200 NTU, were formulated by the addition of kaolin (used as a natural particle surrogate) to the Han River raw water. The results showed that the flux decline behaviours of the highly turbid waters were different from those of natural raw water. Coagulation pretreatment was very effective at reducing membrane fouling. Flocculent aggregates showed a negative effect on the flux decline but a positive effect on the membrane cleaning efficiency. 相似文献
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The removal of particulate organic material in the first step of wastewater treatment may result in significant savings of reactor volume and energy at wastewater treatment plants, because the organic loading to pursuing unit operations can be reduced. This article describes experiments into the possibility of using turbidity measurements as a tool to quantify the concentration of particles in raw wastewater and, based on the result, assess the organic polymer requirement. A feed forward polymer dosing strategy based on a fixed polymer to influent-turbidity ratio was developed and tested. The experimental work confirms that turbidity measurements can be used to quantify particulate COD. For the investigated wastewater (both untreated and flocculated samples) a linear relationship was found in a wide range of particulate COD (100-900 mg O2 x l(-1)) and turbidity (50-450 NTU). On-line turbidity measurements showed that the particle concentrations in the tested municipal wastewater varied significantly. During dry weather conditions the turbidity fluctuated from 100 to 400 NTU, while in rainy periods fluctuations of 100 to >1,000 NTU were measured. The tested turbidity-related polymer dosing method could be used to create different, constant levels of particle removal, despite large particle concentration variations in the influent. Moreover, it resulted in higher removal efficiencies and a more stable operation compared to the dosing of fixed polymer dose per unit of volume. 相似文献
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臭氧与活性炭深度处理微污染原水试验研究 总被引:4,自引:0,他引:4
采用"预臭氧氧化 常规处理 GAC/O3-BAC深度处理"工艺针对南方某市微污染原水进行中试研究.结果表明:预臭氧能明显提高浊度、有机物和THMFP的去除效果,在此条件下常规出水浊度平均值<O.1 NTU,与无预处理相比,CODMn去除率提高17.52%,氯消毒后CHCl3浓度降低86.4%;O3-BAC工艺对有机物、CHCl3的去除效果和吸附寿命均优于GAC工艺,但生物膜的脱落会影响浊度的去除效果;随着炭床厚度增加,GAC滤池中,CODMn呈线性降低,而BAC滤池中,上部500~1 000 mm厚度内,CODMn快速降低并稳定在一定的水平上. 相似文献
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