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组合工艺处理扎染废水的研究 总被引:1,自引:0,他引:1
采用水解调节池-厌氧折流反应池-组合好氧装置-垂直流人工湿地工艺处理扎染废水.厌氧折流反应池、好氧装置的设计容积负荷分别为0.5 kgCOD_(Cr)/(m~3·d)和0.3 kgCOD_(Cr)/(m~3·d),人工湿地水力负荷为0.35 m~3/(m~2·d).运行结果显示,系统运行稳定,污染物去除效果明显,COD_(Cr)、NH_3-N、TN和色度平均去除率分别为77%、85%、70%和89%,出水水质达到GB 18918-2002-级B标准.生化反应段对COD_(Cr)和色度的去除贡献率较大,而人工湿地对氮的去除较为明显,对COD_(Cr)去除贡献率相对较小. 相似文献
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采用恒压浮动盖式ASBR处理啤酒废水的研究表明,在中温35 ℃、容积负荷为1.5~7 kgCOD_(Cr)/(m~3·d)、HRT为1 d的条件下,COD_(Cr)去除率高于80%,平均沼气产率为410 L/kg COD_(Cr),气体中甲烷含量为50%~70%.ASBR运行2个月后污泥实现颗粒化,成熟颗粒污泥的直径为1.5 mm,VSS/SS高达91%.试验期间甲酸的最大比产甲烷活性(SMA)达1.2 gCOD_(Cr)-CH_4/(gVSS·d),8 h后温度骤然升高至65 ℃,污泥变得松散,活性降低,但温度恢复正常后经过50天运行活性可完全恢复. 相似文献
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肌苷制药废水属于高浓度有机废水,采用ABR-UBF-CASS工艺对其进行处理,运行结果表明:在进水CODCr为2 300~6 400 mg/L的情况下,缓慢增加ABR、UBF和CASS反应器容积负荷,运行三个月,出水CODCr在300 mg/L以下,达到《污水综合排放标准》(GB 8978-1996)二级标准. 相似文献
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生产规模UASB反应器处理柠檬酸废水启动试验研究 总被引:4,自引:0,他引:4
本文论述了容积为786.4m~3的生产性UASB反应器中温条件下处理柠檬酸废水的启动过程.当反应器稳定运行时,容积负荷为7.5~10kgCOD/(m~3·d),水力停留时间为38~49h,COD平均去除率达85%,出水COD≤2500mg/L.采用农村沼气池厌氧污泥和好氧活性污泥作为种泥(接种量均为6kgVSS/m~3)均可培养出颗粒污泥,并可实现快速启动. 相似文献
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基于A/O工艺与泳动床工艺技术的联合,开发出A/O泳动床生物膜反应器.A/O泳动床系统表现出高效去除COD_(Cr)、NH_3-N和TN以及较好的抗负荷冲击能力.在HRT=12.5 h,回流比为300%,进水COD_(Cr)、NH_3-N平均浓度分别为343.4 mg/L、94.1 mg/L时,COD_(Cr)和NH3-N平均去除率分别为84.6%, 86.8%;COD_(Cr)的容积负荷与去除负荷现良好的线性关系,R~2=0.970 4;系统在较低的C/N下,TN平均去除率为70.8%. 相似文献
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研究火山岩滤料和普通砾石滤料净化受污染河水的能力。试验结果表明,在好氧条件下,两种滤料对COD_(Cr)的去除没有显著区别,在厌氧条件下,砾石滤池的出水COD_(Cr)高于火山岩滤池。若维持系统出水COD_(Cr)在50 mg/L左右,两种滤池最高COD_(Cr)容积负荷可达1.6 kgCOD_(Cr)/(m~3·d)。当两种滤池的COD_(Cr)容积负荷均低于0.8 kgCOD_(Cr)/(m~3·d),且反应器的好氧区长度与厌氧区长度比大于1:8时,系统氨氮的去除效率会明显提高。 相似文献
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畜禽养殖废水处理方法探讨 总被引:25,自引:2,他引:23
通过实验室模拟试验 ,探讨了混凝 脱氨 好氧生化处理养猪场废水的工艺。经石灰乳混凝沉淀 ,可去除废水中的大部分胶体物质和悬浮物 ,同时可去除一部分难降解物质 ;经脱氨使废水中氨氮低于 2 0 0mg/L ,有利于后续生化的顺利进行。当生化池活性污泥浓度在 350 0~ 4 50 0mg/L之间 ,CODCr容积负荷 <3 0kg/ (m3·d) ,NH3-N容积负荷 <0 2 2kg/ (m3·d)时 ,生化出水能够达到上海市提出的畜牧业排放标准 (CODCr≤ 4 0 0mg/L ,NH3-N≤ 10 0mg/L)。 相似文献
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基于黄姜废水处理工程运行实际,着重分析了pH值、温度、COD及容积负荷等因素对UASB反应器启动的影响。该工程利用预处理+厌氧+好氧+混凝、脱色组合工艺处理黄姜废水,在进水COD和色度分别达12000mg/L和600倍的情况下,出水COD和色度分别为110mg/L和50倍,COD去除率达99%。废水经处理后出水水质符合《皂素工业水污染排放标准》(GB20425-2006)。 相似文献
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Biological aerated filtration of municipal wastewater using a low-cost filtration media. 总被引:1,自引:0,他引:1
The main objective of this research was to demonstrate that selected natural lava stones can be successfully used for low-cost aerobic biofiltration of municipal wastewater. To demonstrate the procedure a pilot filter was built using 6 mm lava stones as support material. The filter depth was 3.0 m. Provided with sampling ports at different depths analysis of the wastewater could be made for COD, TSS, ammonia and nitrates nitrogen, pH, temperature and Kjeldahl nitrogen. Backwashing was performed every 72 hours. Total and dissolved COD and TSS behaved similarly with the organic load: The highest removal rates were observed with the lowest organic load of 0.8 kgCOD/m3 d. These removal rates decreased to a minimum value at organic loading rates of 1.5 kgCOD/m3 d and then remained without noticeable changes to the highest value of 3.5 kgCOD/m3 d. The highest total and dissolved COD removal values were 81 and 84%, respectively. For TSS the best removal value was 95%. Up to 75% ammonia removal was achieved at the lowest organic load of 0.8 kgCOD/m3 d. Ammonia removal decreased to 36% with a higher organic load of 1.6 kgCOD/m3 d. The Mean Cellular Retention (MCRT) time varied from 1 to 6 days with an average of 3.2 days. This fact proves that the MCRT depends on the backwashing frequency more than of any other factor involved. The bed volume decreased in about 5% after 300 days of operation. Microscopic observations showed that the small stones were rounder after 300 days and that the volume losses were caused when the edges of the stones were cut by the abrasion caused by backwashing. 相似文献
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本文研究了pH值、温度、曝气时间、茵投入量(体积比)、溶解氧、水力停留时间、进水碳氮比、冲击负荷等影响因素对氨氮去除率的影响,对项目参数进行了优化。研究结果如下:在高效菌处理氨氮废水时,为了得到较好的去除效果,pH值应控制在7.0到8.O之间;温度应控制在25℃到35℃之间;曝气时间应保持在5h到6h之间;茵投入量(体积比)应保持在0.004到0.006之间;溶解氧浓度应保持在2mg/L到3mg/L之间:水力停留时间为16h.高效茵对污水中氨氮的去除效果最佳。 相似文献
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接种了高效菌种A、B的驯化污泥在前期的生物滤床系统中体现了良好的铬(Ⅵ)去除效率,为了解决系统放大后污泥再生与使用周期等问题,对污泥的铬(Ⅵ)吸附容量进行了测定,测定项目包括一次连续吸附总量、营养添加前后吸附容量的变化等。以铬(Ⅵ)质量浓度为100mg/L的废水进行实验,得到该污泥吸附最佳时间为40min,此时污泥对铬的吸附能力为污泥自身干重的14 94%。一次连续吸附总量为27~28mg/g干污泥。营养液的加入使得污泥吸附能力提高了29 68%。 相似文献
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Upflow anaerobic sludge blanket (UASB) methane fermentation treatment of cow manure that was subjected to screw pressing, thermal treatment and subsequent solid-liquid separation was studied. Conducting batch scale tests at temperatures between 140 and 180 degrees C, the optimal temperature for sludge settling and the color suppression was found to be between 160-170 degrees C. UASB treatment was carried out with a supernatant obtained from the thermal treatment at the optimal conditions (170 degrees C for 30 minutes) and polymer-dosed solid-liquid separation. In the UASB treatment with a COD(Cr) loading of 11.7 kg/m3/d and water temperature of 32.2 degrees C, the COD(Cr) level dropped from 16,360 mg/L in raw water to 3,940 mg/L in treated water (COD(Cr), removal rate of 75.9%), and the methane production rate per COD(Cr) was 0.187 Nm3/kg. Using wastewater thermal-treated at the optimal conditions, also a methane fermentation treatment with a continuously stirred tank reactor (CSTR) was conducted (COD(Cr) in raw water: 38,000 mg/L, hydraulic retention time (HRT): 20 days, 35 degrees C). At the COD(Cr) loading of 1.9 kg/m3/d, the methane production rate per COD(Cr), was 0.153 Nm3/kg. This result shows that UASB treatment using thermal pre-treatment provides a COD(Cr), loading of four times or more and a methane production rate of 1.3 times higher than the CSTR treatment. 相似文献
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In a bioelectrochemical system, the energy content in dissolved organic matter can be used to power the production of hydrogen peroxide (H(2)O(2)), which is a potentially useful chemical at wastewater treatment plants. H(2)O(2) can be produced by the cathodic reduction of oxygen. We investigated four types of gas-diffusion electrodes (GDEs) for this purpose. A GDE made of carbon nanoparticles bound with 30% polytetrafluoroethylene (PTFE) (wt./wt.C) to a carbon fiber paper performed best and catalyzed H(2)O(2) production from oxygen in air with a coulombic efficiency of 95.1%. We coupled the GDE to biological anodes in two bioelectrochemical reactors. When the anodes were fed with synthetic wastewater containing acetate they generated a current of up to ~0.4 mA/mL total anode compartment volume. H(2)O(2) concentrations of ~0.2 and ~0.5% could be produced in 5 mL catholyte in 9 and 21 h, respectively. When the anodes were fed with real wastewater, the generated current was ~0.1 mA/mL and only 84 mg/L of H(2)O(2) was produced. 相似文献
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以周公宅水库流域污染源的调查数据为依据,运用排污系数法和GIS的空间分区统计法,引入负荷污染密度概念,研究了流域污染量及其构成、负荷空间分布和污染治理措施。结果表明,农业面源和生活污染源为流域主要污染源,主要沿周公宅水库环形分布。流域CODCr入河量为599.5 t/a,氨氮为18.6 t/a,总氮为91.9 t/a,总磷为3.2 t/a。水库流域内CODCr、氨氮、总氮、总磷污染负荷污染密度分布比较相似。CODCr污染密度主要集中在5.282~4.287 t/km2,氨氮在0.190~0.121 t/km2,总氮在0.830~0.380 t/km2,总磷在0.038~0.014 t/km2。 相似文献