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城市污水臭氧消毒宏观动力学探索 总被引:1,自引:0,他引:1
消毒是城市污水回用的必要环节。本文以某污水厂出水为研究对象,采用臭氧(O3)作为消毒剂,考查了臭氧在实验水中的溶解和衰减过程,不同通气量和不同pH值条件下臭氧对城市污水厂生化处理后出水中大肠菌群的消毒过程和消毒效果。实验结果显示,臭氧对水中大肠菌群的消毒速度快、消毒效果十分显著;通入水中的气量低于10l/h时,灭菌率随通气量的提高而提高;在水质偏酸性时,有利于臭氧的溶解和提高大肠菌群的去除率;通气量在5l/h—30l/h,处理时间在10min以内时实验条件下臭氧消毒宏观动力学方程为—logS=Kt,式中K=0.2385min^-1—0.4674min^-1。 相似文献
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以油田钻井废水为处理对象,采用基于臭氧的非均相催化氧化处理工艺,负载了MnO_2催化剂强化臭氧处理效果,实验对比分析单独臭氧化和非均相催化臭氧化的处理效果差异,确定最佳工艺参数条件。X射线衍射分析表明,过量浸渍法制备的催化剂中含有大量活性组分MnO_2,使非均相催化臭氧化去除钻井废水COD的效率提高了45.8%。经工艺优化后,确定非均相催化臭氧化处理钻井废水最佳条件为:催化剂加量50mg/L、反应pH值为11、反应温度20℃、臭氧浓度85mg/L、处理时间50min,此时废水COD最大去除率为83.1%。通过5次重复实验验证,催化剂和系统稳定性几乎不受影响,出水均达到GB 8978—1996《污水综合排放标准》一级标准。 相似文献
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《中国环境管理干部学院学报》2017,(6)
采用臭氧高级氧化技术对某染料废水进行处理,探究不同条件对染料废水COD以及色度的去除效果的影响,确定最佳工艺条件。在最佳条件下,采用单独臭氧、单独紫外、臭氧-紫外、臭氧-双氧水以及臭氧-铁炭五种氧化方法对染料废水进行处理。结果表明:臭氧氧化技术最佳条件为pH值=8,臭氧流量80 L/h,反应时间为2 h;采用最佳处理方案,采用臭氧-紫外高级氧化技术处理染料废水,其脱色率为98.3%,COD去除率为67.0%。 相似文献
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臭氧—紫外光化法处理含TNT、RDX和HMX废水的研究 总被引:1,自引:0,他引:1
本文应用光化反应原理,叙述用臭氧——紫外光氧化降解废水中的TNT、RDX和HMX的研究结果。比较了臭氧、紫外光单独处理和联合处理上述炸药废水的效果。通过对模拟废水和工业废水的静态和动态处理的扩大试验,提供了工业设计的基本参数。初步研究了臭氧的投加量、紫外光强度、光化塔高度及温度对处理效果的影响。 相似文献
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Antibiotic formulation effluent is well known for its important contribution to environmental pollution due to its fluctuating and recalcitrant nature. In the present study, the chemical treatability of penicillin formulation effluent (average filtered COD(o)=830 mg/l; average soluble COD(o)=615 mg/l; pH(o)=6.9) bearing the active substances penicillin Amoxicillin Trihydrate (C(16)H(19)N(3)O(5)S.3H(2)O) and the beta-lactamase inhibitor Potassium Clavulanate (C(8)H(8)KNO(5)) has been investigated. For this purpose, the penicillin formulation effluent was subjected to ozonation (applied ozone dose=2500 mg/(lxh)) at varying pH (2.5-12.0) and O(3)+H(2)O(2) (perozonation) at different initial H(2)O(2) concentrations (=2-40 mM) and pH 10.5. According to the experimental results, the overall Chemical Oxygen Demand (COD) removal efficiency varied between 10 and 56% for ozonation and 30% (no H(2)O(2)) and 83% (20 mM H(2)O(2)) for the O(3)+H(2)O(2) process. The addition of H(2)O(2) improved the COD removal rates considerably even at the lowest studied H(2)O(2) concentration. An optimum H(2)O(2) concentration of 20 mM existed at which the highest COD removal efficiency and abatement kinetics were obtained. The ozone absorption rate ranged between 53% (ozonation) and 68% (perozonation). An ozone input of 800 mg/l in 20 min was sufficient to achieve the highest BOD(5)/COD (biodegradability) ratio (=0.45) and BOD(5) value (109 mg/l) for the pre-treated penicillin formulation effluent. After the establishment of optimum ozonation and perozonation conditions, mixtures of synthetic domestic wastewater+raw, ozonated and perozonated penicillin formulation effluent were subjected to biological activated sludge treatment at a food-to-microorganisms (F/M) ratio of 0.23 mg COD/(mg MLSSxd), using a consortium of acclimated microorganisms. COD removal efficiencies of the activated sludge process were 71, 81 and 72% for pharmaceutical wastewater containing synthetic domestic wastewater mixed with either raw, ozonated or perozonated formulation effluent, respectively. The ultimate COD value obtained after 24-h biotreatment of the synthetic domestic wastewater+pre-ozonated formulation effluent mixture was around 100 mg/l instead of 180 mg/l which was the final COD obtained for the wastewater mixture containing raw formulation effluent, indicating that pre-ozonation at least partially removed the non-biodegradable COD fraction of the formulation effluent. 相似文献
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依据溶解性对麻黄碱提取工艺废水中COD作了分类,该废水中的COD主要以溶解态存在并可大量酸析。 相似文献
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Although the application of complex integrated models to wastewater systems is useful, it is often difficult to implement and not always suitable for the design of new systems or for their rehabilitation. Integrated simple approaches that allow assessing the environmental performance of urban wastewater systems may be advantageous, especially during the initial phases of the system planning process. This paper presents an original, straightforward approach that can be used for planning, design and operation of urban wastewater systems. The INtegrated Simplified Approach (INSA) combines the concepts of performance indicators with mass balances and can be applied to wastewater systems as a management support tool, particularly in situations where there is lack of data, economic limitations or time constraints. The INSA was applied to the Algés-Alcantara wastewater system to evaluate its environmental performance and to simulate the individual or combined impact of the rehabilitation measures proposed, thus defining their priority. The results clearly indicate that, despite the investment already made upgrading the wastewater treatment plant (WWTP), the proposed interventions must be implemented to ensure an acceptable environmental performance of the system. In addition, the results demonstrate the significant pollution loads present in stormwater, frequently higher than the pollution loads discharged into receiving waters during dry weather. 相似文献
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采用“含有配制油基钻井液用主乳和油相的Winsor I微乳液+臭氧氧化”联合工艺对油基岩屑进行处理,Winsor I微乳液处理油基岩屑后的所得基础油和部分主乳进入平衡油相,可以用来配制油基钻井液,臭氧氧化对岩屑进行深度处理,进一步降低岩屑表面含油量。论文以处理后岩屑含油量为指标,系统优化了微乳液组成、微乳液清洗油基岩屑工艺和臭氧氧化工艺。实验结果建议微乳液组成为“脂肪醇聚氧乙烯醚硫酸钠+配制油基钻井液用主乳(2:1)”混合乳化剂浓度为6wt%,正戊醇浓度5 wt%,柴油浓度36 wt%,其他为盐水。推荐微乳液清洗条件为固液比1:5,室温下搅拌清洗60 min。此条件下岩屑含油量可以降低至1.41 wt%,微乳液重复使用4次后,岩屑含油量仍可以保持在2.0 wt%以下。臭氧氧化深度处理时,建议工艺条件为臭氧氧化时间40 min,清水pH=7,固液比1:5,臭氧流量5 mg/min,处理后岩屑含油量可降低至0.36wt%。 相似文献
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本文研究了混凝—催化臭氧化对垃圾渗滤液MBR出水COD、UV254和色度的去除效果及可生化性能的影响。在pH 11,FeCl3用量800 mg/L的优化条件下,COD、UV254和色度去除率分别为37.8%、61.9%和88.7%。混凝出水催化臭氧化结果表明,3%-Ce/AC催化臭氧化效率最好,COD去除率为33.6%,臭氧消耗系数为1.40 mgO3/mgCOD。经混凝—催化臭氧化处理后,MBR出水的COD、UV254及色度总去除率分别为58.7%、90.8%及98.7%,BOD5/COD从0.036提高到0.375,可生化性明显改善。 相似文献
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混凝沉降-生物膜法处理制革废水 总被引:8,自引:0,他引:8
采用混凝沉降-生物膜法处理蓝湿牛皮制革废水。工程实践证明:该法对废水COD和BOD的去除率可达94%以上,且对废水的脱色效果良好,是一种合理有效的处理皮革废水工艺路线。 相似文献
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混凝沉降法处理洗衣废水的实验研究 总被引:2,自引:1,他引:1
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。 相似文献