共查询到17条相似文献，搜索用时 468 毫秒
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采用三级隔离曝气生物滤池对炼油废水进行了生物氧化预处理。研究了水力停留时间、气水比对污染物去除效果的影响,同时分析了各级生物滤池的处理效果。当水力停留时间为7.95 h,气水比为8时,CODCr的平均去除率为90.3%,硫化物的平均去除率为99.3%。装置具有良好的抗冲击性能,当水力停留时间和进水中污染物浓度发生大幅变化时,仍能稳定运行且处理效果良好。 相似文献
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采用循环式生物曝气滤池工艺（CBAF）,对炼油碱性污水硫化物进行了预处理实验研究,初步探讨其去除机理。研究了不同水力停留时间（HRT）、溶解氧（DO）、pH等对污水中硫化物的影响。当水力停留时间为32h,溶解氧不小于2mg·L^-1,pH范围在5～8时,硫化物平均去除率达到99．5％,且循环式生物曝气滤池工艺处理效果好．运行稳定。 相似文献
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文章介绍了生物接触氧化法在国内外的研究现状,阐述了生物接触氧化法处理效果的影响因素,展望了生物接触氧化法研究和发展的方向.文中以高县县医院污水为例,选择水力停留时间这一项至关重要的参数进行试验.通过改变水力停留时间测试最终处理水质与水力停留时间的关系.结果表明:COD Cr及BOD5的去除率随水力停留时间的延长而逐渐增大.当水力停留时间大于4 h,出水COD Cr及BOD5均达到《医疗机构水污染物排放标准》GB 18466-2006的排放要求;验证了医院污水处理设备化的可行性.4 h为本试验条件下最为经济的水力停留时间,为设备设计提供了可选参数. 相似文献
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文章介绍了生物接触氧化法在国内外的研究现状,阐述了生物接触氧化法处理效果的影响因素,展望了生物接触氧化法研究和发展的方向．文中以高县县医院污水为例,选择水力停留时间这一项至关重要的参数进行试验．通过改变水力停留时间测试最终处理水质与水力停留时间的关系．结果表明：CODcr及BOD5的去除率随水力停留时间的延长而逐渐增大．当水力停留时间大于4h,出水CODcr及BOD5均达到《医疗机构水污染物排放标准》GB18466—2006的排放要求;验证了医院污水处理设备化的可行性．4h为本试验条件下最为经济的水力停留时间,为设备设计提供了可选参数． 相似文献
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研究了组合工艺(高温55℃UASB反应器一常温三相好氧生物流化床)对含盐偶氮染料活性嫩黄X-6G的去除能效。试验结果表明:在水温为55℃,运行周期120d,水力停留时间18h的条件下,此工艺对于CODCr为600～1 000mg/L,含盐量为25～35g/L,活性嫩黄X-6G的浓度为40～50mg/L的染料废水,染料及CODCr的去除率可达80%～90%。 相似文献
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本文在以复合式膜生物反应器系统为基础,以模拟城市污水为处理对象。通过运行条件优化研究,综合脱氮除磷效果及经济因素,将复合区水力停留时间控制在7h左右。此时系统总去除率为:CODcr≧96.28%、NH3-N≧97.54%、TN≧74.87%、TP≧74.34%,出水可以稳定保证在CODcr≦14.35mg/L、NH3-N≦0.74mg/L、TN≦9.02mg/L、TP≦1.05mg/L。效果较好。 相似文献
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向两级EGSB反应器中投加硅藻土,考察焦化废水中氨氮的去除效果及影响因素。结果表明,当硅藻土投加量为0.5 g/L或5 g/L,两级反应器进水量均为1 L/h,上升流速分别为3.2 m/h、2.9 m/h的条件时,水力停留时间为12 h,可使出水中氨氮浓度达到排放标准。 相似文献
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膜法SBR工艺对生活污水N、P降解的研究 总被引：3，自引：0，他引：3
研究了膜法SBR工艺在不同操作条件下对生活污水N、P的降解效果，当污泥浓度一定，水中DO达到3．5mg/L时，水质pH及无机C源是影响NH3－N降解的关键。当进水NH3－N浓度在50－105mg/L,COD浓度在120－260mg/L时，用Na2CO3调pH在8．0－8．4，运行工况为：进水－闲置段0．5h,曝气1．5h、沉降1h时，可使COD达标排放，NH3－N去除率在50－70％，且有最佳脱N效果。 相似文献
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朱蕾 《渭南师范学院学报》2014,29(19):34-38
在处理制革废水中常用SBR工艺,试验探讨了不同HRT、进水pH、COD负荷、NH3-N浓度、活性污泥浓度的运行参数,研究SBR工艺处理制革废水的最优运行参数．结果表明：SBR反应器在进水COD为1500～2000mg／L、NH3-N为150～250mg／L、pH为7．5、运行污泥浓度在3．0g／L左右、曝气时间为18h时COD去除率能达到95％左右,NH3-N去除率达到97％左右,其出水能够达到一级出水标准． 相似文献
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The feasibility and performance of nitrogen removal from municipal sewage were investigated through the completely autotrophic nitrogen removal over nitrite (CANON) process in a continuous reactor. CANON process was successfully started up with the transformation of nitrogen into gas by mass-balance analysis. For the synthetic waste-water (up to 480 mg NH4+-N/(L·d)), removal rates of the ammonia nitrogen and total nitrogen (TN) were about 80% and 55%, respectively, at 1.25 h hydraulic retention time (HRT). For the secondary effluent of municipal sewage, the effluent concentrations of NH4+-N and TN were below 5 mg/L and 9 mg/L, respectively. It is in accordance with the water quality standard for scenic environment with the reuse of urban recycling water (GB/T 18921-2002). 相似文献
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徐功娣 《上海大学学报(英文版)》2006,10(2):179-184
1Introduction Dyeingwastewaterisakindofindustrialwastewater whichisdifficulttotreat.Itcontainsnotonlyhigh concentrationsofbiggermolecules,e.g.,nitryland aminocompounds,butalsoalargeamountofheavy metals,whicharetoxiccompositionformostof micro organisms.The… 相似文献
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采用绿色水处理剂氧化镁处理氨氮废水,利用单因素优化分析法,对影响氧化镁处理效果的主要因素进行了研究,考察其对氧化镁处理效果的影响,确定最佳反应条件.在常温下(24℃)当氧化镁用量为2 g/L、曝气时间为2 h时氨氮去除率为99.6％,而时间再加长,用量增多,效果提升不明显.根据夏热冬冷的情况,取28℃和18℃两个温度进... 相似文献
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The characteristics of the start-up period of single-step autotrophic nitrogen removal process were investigated. The autotrophic nitrogen removal process used a sequencing batch reactor to treat wastewater of medium to low ammonia-nitrogen concentration, with dissolved oxygen （DO）, hydraulic retention time （HRT） and temperature controlled. The experimental conditions were temperature at （30±2） ℃, ammonia concentration of （60 to 120） mg/L, DO of （0.8 to 1.0） mg/L, pH from 7.8 to 8.5 and HRT of 24 h. The rates of nitrification and nitrogen removal turn out to be 77% and 40%, respectively, after a start up period going through three stages divided according to nitrite accumulation： sludge domestication, nitrifying bacteria selection and sludge adaptation, It is demonstrated that dissolved oxygen is critical to nitrite accumulation and elastic YJZH soft compound packing is superior to polyhedral hollow balls in helping the bacteria adhere to the membrane. 相似文献
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CAI Jing ZHENG Ping MAHMOOD Qaisar ISLAM Ejazul HU Bao-lan WU Dong-lei 《浙江大学学报(A卷英文版)》2007,8(7):1149-1156
The optimal operation conditions in an anoxic sulfide oxidizing (ASO) bioreactor were investigated. The maximal removal rates for sulfide and nitrate were found to be 4.18 kg/(m3·d) and 1.73 kg/(m3·d), respectively. The volumetrical volumetric loading rates (LRs) observed through decreasing hydraulic retention time (HRT) at fixed substrate concentration are higher than those by increasing substrate concentration at fixed HRT. The sulfide oxidation in ASO reactor was partially producing both sulfate and sulfur; but the amount of sulfate produced was approximately one third that of sulfur. The process was able to tolerate high sulfide concentration, as the sulfide removal percentage always remained near 99% when influent concentration was up to 580 mg/L. It tolerated relatively lower nitrate concentration because the removal percentage dropped to 85% when influent con- centration was increased above 110 mg/L. The process can tolerate shorter HRT but careful operation is needed. Nitrate conversion was more sensitive to HRT than sulfide conversion since the process performance deteriorated abruptly when HRT was decreased from 3.12 h to 2.88 h. In order to avoid nitrite accumulation in the reactor, the influent sulfide and nitrate concentrations should be kept at 280 mg/L and 67.5 mg/L respectively. Present biotechnology is useful for removing sulfides from sewers and crude oil. 相似文献
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利用两种生物膜技术处理高校生活污水进行了试验研究,结果表明,接触氧化法优于生物转盘法;在停留时间为4h,接触氧化法对CODCr和NH3-N的去除率分别为78.5%和75.6%,出水能达到《城市污水再生利用城市杂用水水质(》GB/T18920-2002)标准;随着气水比的增大,CODCr、NH3-N的去除率先增大后减小,其适宜的气水比为15∶1;出水CODCr浓度随CODCr容积负荷的增大而升高,合理的CODCr容积负荷为6～8kgCODCr/(m3.d). 相似文献