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501.
502.
一种新型的生物脱氮工艺——生物循环流化床(CFBBR)用于脱氮和除碳。系统由缺氧床(升流床)和好氧床(降流床)及其连接装置构成。进水由缺氧床底部进入,同来自好氧床的硝化液一起,在缺氧床内完成脱氮和除碳。研究了不同进水负荷,硝化液回流率200%~600%下的系统性能。从技术和经济角度考虑,400%硝化液回流率为最佳。最短水力停留时间2.5h(缺氧床0.8h,好氧床1.7h)和400%硝化液回流率下,TN和CODCr去除率和出水浓度分别为88%、95%和3.5mg/L、16mg/L。系统VSS低于1g/L,硝化率和反硝化率分别为0.026~0.1g/(g·d)和0.016~0.074g/(g·d)。 相似文献
503.
以粉煤灰为原料,采用水热合成法制备沸石,造粒后合成沸石填充至滤柱中. 研究了不同运行条件下合成沸石对污水中磷的净化与回收效果. 结果表明:合成沸石对模拟污水和城市生活污水经二级生化处理后的排放水中磷的去除能力相近,且在磷含量低的情况下后者高于前者;与造粒前相比,造粒后的合成沸石仍具有良好的固磷能力. 水力负荷明显影响滤柱中磷的去除效果,其在177.9 L/(m2·h)以下时,磷的去除效果较好. 此外,进水pH也明显影响合成沸石的除磷效果,当进水pH调至酸性或碱性范围时,合成沸石的除磷能力显著提高. 该滤柱能够长期有效地净化与回收污水中的磷,达到饱和时合成沸石的w(磷)达20.04 g/kg(以磷元素计),可实际应用于农田改良. 相似文献
504.
通过小试规模的移动床生物膜反应器(MBBR)处理陕西科技大学污水处理厂生活污水的实验研究,探讨了水力停留时间、冲击负荷、pH对反应器处理效果的影响。实验结果表明,在HRT为10 h,进水ρ(COD)为300 mg/L,ρ(NH3-N)为35 mg/L,填料体积填充率为35%,pH为7左右时,MBBR反应器对COD、TN的去除率分别为87.38%、68%。 相似文献
505.
506.
This study assesses the efficiency of various physico-chemical, biological and other tertiary methods for treating leachate.
An evaluation study on the treatability of the leachate from methane phase bed (MPB) reactor indicated that at an optimum
hydraulic retention time of 6 days, the efficiency of the reactor in terms of biological oxygen demand (BOD) and chemical
oxygen demand (COD) removal was 91.29 and 82.69%, respectively. Recycling of the treated leachate through the municipal solid
waste layers in the leachate recycling unit (LRU) resulted in a significant increase in the biodegradation of organics present
in the leachate. Optimum BOD and COD removal efficiencies were achieved at the third recycle; additional recycling of the
leachate did not produce any significant improvement. Physico-chemical treatment of the leachate demonstrated that alum and
lime (Option 2) were more economical than coagulants lime and MgCO3. A cost analysis of the economics of the various treatments revealed that the alternative treatment consisting of a MPB bed
followed by a LRU and aerated lagoon is the most cost-effective treatment. However, the alternative consisting of a MPB followed
by the LRU and a soil column, which is slightly more costly, would be the most appropriate treatment when adequate land is
readily available. 相似文献
507.
A review on numerous modeling approaches for effective, economical and ecological treatment wetlands 总被引:1,自引:0,他引:1
Constructed wetlands (CWs) for wastewater treatment have evolved substantially over the last decades and have been recognized as an effective means of "green technology" for wastewater treatment. This paper reviews the numerous modeling approaches ranging from simple first-order models to more complex dynamic models of treatment behaviour in CWs. The main objective of the modeling work is to better understand the process in CWs and optimize design criteria. A brief study in this review discusses the efforts taken to describe the process-based model for the efficient removal of pollutants in CWs. Obtaining better insights is essential to understand the hydraulic and biochemical processes in CWs. Currently, employed modeling approaches can be seen in two categories, i.e. "black-box models" and "process-based models". It is evident that future development in wetland technology will depend on improved scientific knowledge of internal treatment mechanisms. 相似文献
508.
509.
沉水植物与生态浮床组合对水产养殖污染控制的研究 总被引:4,自引:0,他引:4
通过2009年9月—2010年2月测定陆基围隔中水生植物种植密度、浮床水面覆盖率、水质状况、浮游藻类群落特征及水生生物生长状况,研究了沉水植物与植物浮床相结合的新型养殖水体净化模式对养虾塘污染原位净化及水质调控效果。结果表明,养虾塘第Ⅴ组围隔(单个围隔面积为3 m×3 m)内栽种苦草(Vallisneria natans)4.0 kg和轮叶黑藻(Hydrilla verticillata)3.0 kg,与种植312株常绿鸢尾(Iris hexagonus)的植物浮床组合,对养殖污染的控制效果较好,TN、TP、CODMn分别从3.41、0.32、14.34 mg.L-1降至0.79、0.02和11.96 mg.L-1;第Ⅴ组围隔内浮游藻类Margalef指数为4.00,Shannon-Wiener多样性指数为3.32,Pielou均匀度指数为0.76,显示养殖水体环境较稳定,水质相对较好。 相似文献
510.
A continuous fluidized bed bioreactor (FBBR) with nylon support particles was used to treat synthetic sulfide wastewater at different hydraulic retention time of 25, 50 and 75 min and upflow velocity of 14, 17 and 20 m/hr. The effects of upflow velocity, hydraulic retention time and reactor operation time on sulfide oxidation rate were studied using statistical model. Mixed culture obtained from the activated sludge, taken from tannery effluent treatment plant, was used as a source for microorganisms. The diameter and density of the nylon particles were 2-3 mm and 1140 kg/m3, respectively. Experiments were carried out in the reactor at a temperature of (30 ± 2)℃, at a fixed bed height of 16 cm after the formation of biofilm on the surface of support particles. Biofilm thickness reached (42 ± 3) μupm after 15 days from reactor start-up. The sulfide oxidation, sulfate and sulfur formation is examined at all hydraulic retention times and upflow velocities. The results indicated that almost 90%-92% sulfide oxidation was achieved at all hydraulic retention times. Statistical model could explain 94% of the variability and analysis of variance showed that upflow velocity and hydraulic retention time slightly affected the sulfide oxidation rate. The highest sulfide oxidation of 92% with 70% sulfur was obtained at hydraulic retention time of 75 min and upflow velocity of 14 m/hr. 相似文献