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排放提标、节能降耗是目前企业污水处理新工艺研究的重点.连续流分段进水生物脱氮工艺(CSFBNR),具有高效深度脱氮、节约碳源、减少能耗、减少污泥产生量等诸多优点.分析了连续流分段进水生物脱氮工艺的控制要点及其影响因素,并且探讨了该工艺在节能降耗方面的作用. 相似文献
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新型分段进水生物脱氮反应器启动策略研究 总被引:1,自引:0,他引:1
研究了基于多段进水工艺原理开发的新型分段进水生物脱氮反应器的2种启动模式(模式一为先调整适当HRT,再根据分段配水比进水,模式二根据分段配水比直接配比,然后逐步调整HRT)下的最优启动调控策略。结果表明,在2种模式下,出水SS的质量浓度和TCOD分别均能低于30 mg.L-1和50 mg.L-1,浊度平均去除率均在80%以上,无显著差异。模式一由单一进水口改成分段进水后,平均出水氨氮的质量浓度由11.93 mg.L-1上升至19.51 mg.L-1,平均TN去除率由18.43%上升至49.25%;而模式二的氮素污染物去除性能较稳定,平均氨氮和TN去除率分别为66.15%和54.71%。模式一的污泥含量增长速度要快于模式二,但3个曝气区的污泥含量增长并不均衡,不利于整体反应器的启动驯化。总体而言,新型分段进水生物脱氮反应器建议采用模式二进行启动。 相似文献
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《工业用水与废水》2018,(6)
以考察分段进水一体化工艺脱氮的影响因素及脱氮能力为目的,研究了进水流量比(厌氧区∶缺氧区)、好氧区溶解氧(DO)浓度、水力停留时间(HRT)(固定厌氧区和缺氧区进水流量比为3∶1)对工艺的同步硝化反硝化(SND)的影响,同时运用动力学模型对工艺的脱氮能力进行了模拟分析。试验结果表明:厌氧区和缺氧区进水量比为3∶1时,总氮去除率最高,平均去除率在86%以上;好氧区DO质量浓度约为2.0 mg/L时,总氮去除率最高,平均去除率在85%以上;保持厌氧区和缺氧区进水流量比为3∶1, HRT为12 h时,总氮去除率最高,平均去除率在86%左右;对脱氮动力学进行了研究,反硝化速率方程为R=-1.87×10-3X,总氮降解常数为1.87×10-3 h-1。 相似文献
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采用混合反应器模拟氧化沟运行方式,探讨氧化沟不同好氧缺氧分区对脱氮除磷效果的影响。结果表明,在分点曝气氧化沟系统中氧传质推动力大,溶氧效率高,在相同的供氧条件下,其一个循环的好氧区比分段曝气系统好氧区长,但是分点曝气系统有机物耗氧多,DO浪费大,而分段曝气溶氧效率低,但DO的有效利用率(用于脱氮除磷)高,二者硝化能力相当,NH4+-N去除率分别为96.68%和97.03%,硝化菌活性分别为4.65、4.66 mg.g-1.h-1。在好氧区和缺氧区比例相同的条件下,分区越多,有机物被好氧异养菌利用的越多,脱氮除磷效果越差。分区减少,可以有效地增加反硝化菌对碳源的利用,对提高脱氮效果更有利。在同样的供氧条件下,分段曝气单个A/O分区长,反硝化菌和聚磷菌对碳源利用多,脱氮除磷效果优于分点曝气,在满足硝化的前提下,缺氧区和好氧区比例越大,碳源被利用的越完全,对脱氮除磷越有利,DO的有效利用率也越高,此时越接近于前置缺氧-好氧(A/O)工艺。 相似文献
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针对受控生态生保系统(CELSS)中生活废水(含卫生废水和尿液废水)的水质特点,采用厌氧、好氧两级MBfR工艺,完成CELSS特征性生活废水的微生物转化处理,以达到循环回用作植物营养液的水质要求。本文研究了水力停留时间(HRT)、尿液强度对该工艺有机物去除及氮素转换效率的影响。试验结果表明,当HRT≥1 d时,HRT对该系统TOC的去除效率无明显影响,其去除效率大于90%,出水TOC的浓度低于15 mg/L; HRT=1 d时,好氧反应器全程硝化能力达到最高,其容积负荷为0.418 kg N/(m3·d);而HRT≥2 d时,能获得相对更为稳定的氮素转换效率。工艺系统最高能处理1/5尿液强度的生活废水,该条件下,系统TOC的去除率达94.3%,出水TOC浓度低于20 mg/L;系统氮素的全程硝化效率为90.6%,且反应器容积负荷较高为0.409 kg N/(m3·d)。本文构建的两级MBfR工艺能较好地实现CELSS中特征性生活废水的有机物去除和氮素的有效转换,研究结果可为CELSS中生活废水微生物处理系统的设计和运行提供参考。 相似文献
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Ronald R Navarro Rosvic C Navarro Catalino G Alfafara Rex B Demafelis Kenji Tatsumi 《Journal of chemical technology and biotechnology (Oxford, Oxfordshire : 1986)》2005,80(10):1125-1130
Organic matter (chemical oxygen demand, COD) removal with decolorization in waste distillery slops and copper removal in a semiconductor industry wastewater were achieved in a single step mixing and precipitation/coagulation treatment system. The process utilized the complementary properties of the positively charged copper ions in semiconductor wastewater and net negative charge of melanoidin (organic chromophoric pollutant) in distillery slops to mutually neutralize each other. Copper ions served as coagulant for slops and melanoidin served as precipitant for copper. The volumetric ratio of the wastewater and pH were optimized to attain maximum removal of organic matter and copper. The optimum volumetric ratio for the evaluated semiconductor wastewater to distillery slops was found to be 2–3 with an equilibrium pH of around pH 6. At optimum conditions, average removals of COD and copper were 86% and 92%, respectively, in an actual and undiluted system. Decolorization efficiency using the diluted distillery slops was 89%. The process can be considered an effective pretreatment procedure for simultaneous gross removal of copper and color/COD, particularly in highly concentrated waste streams. Copyright © 2005 Society of Chemical Industry 相似文献
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UASB处理纤维素乙醇废水的启动运行研究 总被引:1,自引:0,他引:1
以厌氧UASB反应器处理纤维乙醇废水为研究对象,探讨分析了UASB的启动和稳定运行过程。结果表明,采用城市污水处理厂的厌氧消化污泥作为接种污泥,在COD有效容积负荷为0.33~1.11 kgCOD/(m3·d)的条件下,UASB反应器成功启动,COD的去除率达到70%以上。启动初期,出水pH会明显高于进水,污泥呈先减少后增加的趋势,当增加进水SO42-浓度到7 250 mg/L,COD/SO42-比值2.7∶1时,会导致纤维素乙醇废水UASB处理系统的崩溃。UASB反应器运行稳定后,污泥浓度增至30~40 g/L,MLVSS/MLSS比值也达到90%左右,在HRT为14~41 h,回流比3∶1~13∶1,有效容积负荷3.45~14.67 kg COD/(m3·d)的条件下,对纤维乙醇生产废水均能保持90%以上的COD去除率,出水COD小于1 000 mg/L。 相似文献
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Successive concentration and purification of simulated nickel-electroplating rinsing wastewater was carried out by integrating membrane process with electrodeionization. The concentrate compartments were filled with ion exchange resins to enhance the separation. The concentrate stream of the primary EDI procedure was operated in closed circuit circulation. The influence of the volumetric ratio of resins in concentrate compartments on the separation was examined. It was found that the best performance could be achieved when anion to cation resin ratio of 6∶4 was adopted. With feed Ni2+ concentration of 50 mg·L-1 and pH of 4.25,the Ni2+ concentration of effluent dilute stream could reach 2.78 mg·L-1 while that of the effluent concentrate stream was as high as 11171 mg·L-1,which gave a concentration ratio of higher than 220. The effluent dilute stream of the primary EDI was then sent to the second EDI stack for deep desalting. Dilute product with resistivity of 1.6—2.0 MΩ·cm was then obtained,which could be recovered as pure water for electroplating. The membrane process integrated with EDI could find its potent role for zero emission and resource reuse of heavy metal wastewater. 相似文献
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在水力学直径为1.00 mm的方形T型微通道内,采用质量分数为40%的N-甲基二乙醇胺(MDEA)吸收含有体积分数为0.12%的H2S混合气体。实验发现,在微通道内可以获得很高的H2S脱除效率,在气液体积比为200∶1时,其脱除效率可以达到99.5%。在微通道内的H2S传质过程中,H2S传质的阻力主要集中在气侧,而且气侧体积传质系数随着气体和液体表观速率的增加而增加。提出了在过渡区的二相流型中,气侧体积传质系数的量纲一经验关联式,其计算值和实验值吻合得很好。通过比较发现,微通道比其他传统设备的气侧体积传质系数高出1—2个数量级。 相似文献
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皂化P204微乳液膜处理含锌废水的研究 总被引:3,自引:0,他引:3
研究以皂化P204为载体的微乳液膜配方及其稳定性.采用P204/Span80/煤油/NaOH微乳体系萃取废水中Zn^2+,考察了P204与煤油和Span80的质量比、NaOH的浓度、乳水比、外水相pH值、油相重复使用次数等因素对Zn^2+萃取率的影响.结果表明,当P204与煤油的质量比为1:2.5,P204与Span80的质量比为1:1,NaOH浓度为1.5mol/L,乳水比为1:4(体积比),废水pH值为5.5时,萃取10min,P204/煤油/NaOH微乳液膜对Zn^2+萃取率可达99.72%,P204/Span80/煤油/NaOH微乳液膜对Zn^2+萃取率可达99.98%,微乳液膜不仅稳定性好、萃取效率高,而且工艺简单、膜相可自动破乳、油相可重复使用. 相似文献
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采用52.5 L的A2O试验装置处理实际生活污水,研究了A2O工艺在处理低C/N比生活污水时的脱氮除磷特性,并探讨了如何通过强化缺氧吸磷来提高系统的脱氮除磷效率。试验结果表明:在厌氧/缺氧/好氧体积比为1/1/2、HRT为8 h、污泥回流比为70%、内回流比为300%的工况下处理C/N为7.89的生活污水,TN和SOP去除率分别能够达到85.4%和93.3%,系统中存在反硝化除磷,缺氧吸磷占总吸磷量的25.3%。同样的运行条件下处理C/N为4.20的生活污水时,SOP去除几乎不受影响,但TN去除率降低至62.2%,平均出水TN浓度也超过20 mg8226;L-1。维持厌氧区体积不变,增大缺氧区体积,使得缺氧/好氧体积比为5/8时,TN去除率可上升到70.7%,缺氧吸磷占总吸磷量的55.2%。同时改变内回流比的试验表明250%的内回流比能最大程度地强化反硝化除磷的作用,此时TN去除率可提高至77.3%。强化A2O工艺中的反硝化除磷,能克服碳源不足对脱氮除磷的影响,显著提高低C/N比污水的脱氮除磷效率。 相似文献
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高膨胀率高质量蛭石粉体研制 -I. 热膨胀机理初探 总被引:5,自引:2,他引:5
利用高温X射线衍射和热重-差热分析技术对蛭石在加热过程中膨胀及相应的结构变化进行了研究. 与XRD谱图相联系,结合蛭石的颜色与膨胀率进行统计分析,将蛭石矿物分为黄色蛭石、深黄色蛭石和深绿色蛭石,发现在相同加热条件下其水化程度和膨胀率之间存在确定的关系,同时又表现出不同的微观结构特征. 在膨胀机理研究的基础上,进一步分析了不同蛭石在不同温度下的膨胀率与结构变化的规律,得出了层间水是影响蛭石体积膨胀率的主要因素,结构水的脱出则主要引起层间距离的变化,这为加工生产高膨胀率、高质量的蛭石提供了重要的依据. 相似文献
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利用高温X射线衍射和热重-差热分析技术对蛭石在加热过程中膨胀及相应的结构变化进行了研究.与XRD谱图相联系,结合蛭石的颜色与膨胀率进行统计分析,将蛭石矿物分为黄色蛭石、深黄色蛭石和深绿色蛭石,发现在相同加热条件下其水化程度和膨胀率之间存在确定的关系,同时又表现出不同的微观结构特征.在膨胀机理研究的基础上,进一步分析了不同蛭石在不同温度下的膨胀率与结构变化的规律,得出了层间水是影响蛭石体积膨胀率的主要因素,结构水的脱出则主要引起层间距离的变化,这为加工生产高膨胀率、高质量的蛭石提供了重要的依据. 相似文献
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Chen‐hong Zhao Yong‐zhen Peng Shu‐ying Wang Akio Takigawa 《Journal of chemical technology and biotechnology (Oxford, Oxfordshire : 1986)》2008,83(12):1587-1595
BACKGROUND: UniFed SBR is a novel process that can achieve high levels of nitrogen and phosphorus removal simultaneously in a simple single SBR tank. In this study, effects of influent C/N ratio, influent C/P ratio and volumetric exchange ratio on biological phosphorus removal in UniFed SBR process were investigated in a lab‐scale UniFed apparatus treating real domestic wastewater. RESULTS: The results showed that phosphorus removal efficiency increased as C/N ratio increased from 27% at 2.8 to 88% at 5.7. For C/N ratios 6.5 and above, complete phosphorus removal could be achieved. When C/N ratios and volumetric exchange ratio were fixed at 6 and 33%, respectively, phosphorus removal efficiency remained at 100% for C/P ratios higher than 33; effluent phosphate concentration was below the detection limit. For C/P ratios lower than 33, phosphorus removal efficiency decreased linearly with C/P ratio. Under the same influent C/N ratio and C/P ratio, the following factors all contributed to better phosphorus removal performance: greater volumetric exchange ratio; more organic substrate for PAOs to utilize, less inhibition by NOx? of phosphorus release during the feed/decant period; more PHB synthesized; and more aerobic phosphate uptake. CONCLUSION: High influent C/N ratio, high C/P ratio and high volumetric exchange ratio were beneficial to phosphorus removal in this process. Copyright © 2008 Society of Chemical Industry 相似文献