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基于热力学分析的MAP法处理模拟氮磷废水研究 被引量:1
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作者 米海蓉 成功 +2 位作者 李士松 刘桂芳 丁学姣 《哈尔滨工程大学学报》 EI CAS CSCD 北大核心 2016年第11期1514-1519,共6页
磷酸氨镁(MAP)法处理氮磷废水过程中,NH_4^+-N和PO_4^(3-)-P的去除率无法反映影响MAP法的因素及沉淀物的生成过程。为解决此问题通过单因素实验以及热力学平衡计算的方法,对MAP法处理模拟氮磷废水中的氨氮和磷酸盐的影响因素进行了分析... 磷酸氨镁(MAP)法处理氮磷废水过程中,NH_4^+-N和PO_4^(3-)-P的去除率无法反映影响MAP法的因素及沉淀物的生成过程。为解决此问题通过单因素实验以及热力学平衡计算的方法,对MAP法处理模拟氮磷废水中的氨氮和磷酸盐的影响因素进行了分析和探讨。研究了初始氨氮浓度、p H值、摩尔比n(Mg)∶n(N)以及摩尔比n(P)∶n(N)条件,对NH_4^+-N和PO_4^(3-)-P去除率的影响以及不同条件各沉淀组分的变化。结果表明,在p H值为9~9.5,摩尔比n(Mg)∶n(N)∶n(P)为1∶1∶1条件下,MAP法的处理效果最优,NH_4^+-N去除率可达79.35%~93.76%,PO_4^(3-)-P去除率可达86.76%~95.43%,且MAP沉淀物中杂质较少;虽然增大摩尔比n(Mg)∶n(N)或摩尔比n(P)∶n(N)会分别提高PO_4^(3-)-P和NH_4^+-N去除率,但也会分别使NH_4^+-N和PO_4^(3-)-P残余量增大。 展开更多
关键词 酸氨镁 氮磷废水 热力学平衡 影响因素 摩尔比 去除率
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反硝化-水解酸化-厌氧-缺氧-MBR 工艺处理氮磷废水 被引量:1
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作者 王浩 王学华 +2 位作者 王国梁 高超 秦毅 《水处理技术》 CAS CSCD 北大核心 2014年第1期132-134,共3页
针对常州某工业园各企业生产废水的特点,对氮磷段废水采用分质收集处理。对高磷废水采用化学反应-混凝沉淀法;处理后废水与非磷段废水混合,采用反硝化-水解酸化-厌氧-缺氧-膜生物反应器进行处理。经过4个月的实际运行,结果表明,出水水... 针对常州某工业园各企业生产废水的特点,对氮磷段废水采用分质收集处理。对高磷废水采用化学反应-混凝沉淀法;处理后废水与非磷段废水混合,采用反硝化-水解酸化-厌氧-缺氧-膜生物反应器进行处理。经过4个月的实际运行,结果表明,出水水质达到GB 18918-2002中的一级A标准。 展开更多
关键词 氮磷废水 反硝化 水解酸化 厌氧 缺氧 膜生物反应器
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模拟生态湿地处理氮磷废水的实验研究 被引量:2
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作者 冯亚南 周海洋 王磊 《农业与技术》 2016年第20期9-10,共2页
随着人们环保意识的增强,污水处理一直是人们关注的热点。本文以植物净化污水技术进行了研究,利用水葫芦、香蒲、美人蕉3种湿地植物进行氮磷废水处理实验,经过实验得出3种植物中属美人蕉在氮磷废水处理中去除率较为稳定。
关键词 模拟生态湿地 氮磷废水 美人蕉
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某太阳能电池片生产氮磷废水“零排放”处理工程设计实例 被引量:2
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作者 郭庆 《水处理技术》 CAS CSCD 北大核心 2018年第4期136-139,共4页
针对某太阳能电池片技改项目中产生的氮磷废水,为实现"零排放",经处理后的废水全部回用于冷却循环系统补水。本工程实例采用"一级混凝+一级沉淀+二级混凝+二级沉淀+砂滤+碳滤+离子交换+超滤+三级反渗透"处理工艺,... 针对某太阳能电池片技改项目中产生的氮磷废水,为实现"零排放",经处理后的废水全部回用于冷却循环系统补水。本工程实例采用"一级混凝+一级沉淀+二级混凝+二级沉淀+砂滤+碳滤+离子交换+超滤+三级反渗透"处理工艺,处理后的产水满足城市污水再生利用工业用水水质(GB/T 19923-2005)标准。同时,产生的浓水进入二效蒸发系统进行蒸发,系统产生的污泥经污泥池浓缩后泵提至污泥压滤机进行脱水后外运处置。 展开更多
关键词 太阳能电池 含氟废水 氮磷废水 零排放 回用 混凝 反渗透
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联合沉淀法处理氮磷废水的试验研究 被引量:2
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作者 黄新毅 《科技信息》 2010年第21期J0014-J0015,共2页
本文在富含氮磷的废水中,通过MAP法与HAP法联合的方式对废水进行处理。分别考察了pH值和钙镁源添加量对MAP法和HAP法处理试验废水时对磷回收率的影响,并研究了MAP和HAP联合处理废水的效果以及处理后回收的沉淀物中磷的缓释性。结果表明:... 本文在富含氮磷的废水中,通过MAP法与HAP法联合的方式对废水进行处理。分别考察了pH值和钙镁源添加量对MAP法和HAP法处理试验废水时对磷回收率的影响,并研究了MAP和HAP联合处理废水的效果以及处理后回收的沉淀物中磷的缓释性。结果表明:MAP法最佳的反应条件为pH值为10.5,N:P:Mg为1:1:1.2;HAP法的最佳反应条件为pH值为9.5,P:Ca为1:1.6;MAP-HAP法相对于单纯使用MAP法和HAP法,磷回收率分别提高了15.03%和12.16%,且MAP-HAP法的回收率高于HAP-MAP法;在MAP-HAP法处理后得到的沉淀产物在前3次浸提中磷的释放量逐渐降低,证明其作为磷肥使用具有一定的缓释性能。 展开更多
关键词 氮磷废水 沉淀法 回收率 缓释性
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将含氮磷废水用于磷酸二铵尾洗的工艺改造
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作者 刘明高 沈维云 +5 位作者 杜万保 朱刚 王宗孝 黄翔翔 陈春雷 汪耀兴 《山东化工》 CAS 2017年第24期127-127,129,共2页
磷酸一铵生产过程中产生的含氮磷废水代替工艺水艺用于磷酸二铵尾洗,同时通过对尾气洗涤器简单的改造及优化工艺指标,确保尾气达标排放及产品质量的同时,回收利用氮、磷资源,减轻污水处理压力。
关键词 酸二铵 尾气洗涤 氮磷废水 改造
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磷酸铵镁法去除高氮磷比废水中磷的试验研究 被引量:5
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作者 周荣敏 雷延峰 武燕杰 《工业用水与废水》 CAS 2010年第6期32-34,共3页
采用磷酸铵镁法处理高氮磷比废水,正交试验结果表明对于氮磷物质的量之比为20的废水,在pH值为9.0~10.2时,镁磷物质的量之比是影响磷酸铵镁法除磷效果的主要因素。当pH值为9.5,反应时间为15 min,镁磷物质的量之比为1.3时,磷去除率可达97... 采用磷酸铵镁法处理高氮磷比废水,正交试验结果表明对于氮磷物质的量之比为20的废水,在pH值为9.0~10.2时,镁磷物质的量之比是影响磷酸铵镁法除磷效果的主要因素。当pH值为9.5,反应时间为15 min,镁磷物质的量之比为1.3时,磷去除率可达97%以上,且具有良好的适应性和稳定性;对于高氮磷比废水,在保证能达到预期的磷去除率情况下,通过降低所必须维持的pH值和镁磷物质的量之比来节约药剂成本是可行的。 展开更多
关键词 MAP法 废水 正交试验
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物化+生化工艺在高氮高磷制药废水处理中的应用 被引量:7
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作者 王白杨 吴星 +1 位作者 罗亚情 刘英辉 《工业水处理》 CAS CSCD 北大核心 2015年第12期93-95,共3页
某化工厂以化学合成法生产医药中间体,产生的废水中含有大量有机物及高浓度的氮磷,原有处理工艺处理废水后已不能达标排放。对存在问题进行分析研究,改进了原有工艺,采用MAP+ABR+A2/O工艺处理该制药废水。实际运行结果表明,工艺改进后... 某化工厂以化学合成法生产医药中间体,产生的废水中含有大量有机物及高浓度的氮磷,原有处理工艺处理废水后已不能达标排放。对存在问题进行分析研究,改进了原有工艺,采用MAP+ABR+A2/O工艺处理该制药废水。实际运行结果表明,工艺改进后出水各项指标均达到《化学合成类制药工业水污染物排放标准》(GB 21904—2008),可为高氮高磷制药废水处理提供参考与借鉴。 展开更多
关键词 制药废水 物化法 生化法
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对含氮磷生产工艺废水“零排放”技术的研究 被引量:1
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作者 黄军 杨英杰 《资源节约与环保》 2013年第9期44-44,共1页
随着节能社会和生态环境建设的不断深入,工业产生的废水处理,成为企业和环境部门保护环境的重要举措。据工程分析,废水主要污染因子为CODcr、氨氮、总磷。本文就"含氮磷废水零排放"技术进行了分析。
关键词 氮磷废水 零排放 技术
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MAP法处理高氮高磷制药废水的研究 被引量:4
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作者 吴星 邬容伟 +1 位作者 尹文静 西鹏 《江西化工》 2018年第3期114-117,共4页
对MAP法处理高氮高磷制药废水进行实验研究,探讨了反应物浓度、pH值、n(Mg):n(N)、n(N):n(P)和镁盐种类对MAP法脱氮除磷效果的影响。结果表明:当废水反应物浓度(以N计)1500mg/L,p H=9.0~9.5,n(Mg):n(N)=1.1~1.2,n(N):n(P)=0.95~1.0,反... 对MAP法处理高氮高磷制药废水进行实验研究,探讨了反应物浓度、pH值、n(Mg):n(N)、n(N):n(P)和镁盐种类对MAP法脱氮除磷效果的影响。结果表明:当废水反应物浓度(以N计)1500mg/L,p H=9.0~9.5,n(Mg):n(N)=1.1~1.2,n(N):n(P)=0.95~1.0,反应沉淀剂为MgCl_2·6H_2O,反应温度20℃,反应时间1h时,废水中氨氮、磷酸盐去除率可分别达96.7%、99.6%。 展开更多
关键词 制药废水 MAP 酸盐 去除率
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高含盐废水脱氮除磷技术研究 被引量:1
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作者 杨斌 《内蒙古煤炭经济》 2019年第24期199-199,共1页
本文论述了煤化工企业高含盐废水脱氮除磷技术研究及应用,研究了工业生产中高含盐废水脱氮除磷技术生化处理的新方式和途径。
关键词 高含盐废水技术 装置运行管理
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粉煤灰合成沸石脱氮除磷的应用及展望
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作者 肖聪 《当代化工》 CAS 2012年第10期1027-1029,共3页
介绍粉煤灰合成沸石在氮磷废水处理中的应用。指出了粉煤灰合成沸石在处理氮磷废水方面具有处理效果好、占地少、便于管理控制等优点。粉煤灰来源广泛,价格低廉,将粉煤灰合成沸石处理氮磷废水可以以废治废,具有广阔的发展前景。
关键词 粉煤灰 沸石 氮磷废水 展望
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磷酸铵镁结晶-沉淀反应器构建与流态模拟 被引量:3
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作者 李鹏 郝瑞霞 +2 位作者 李嘉雯 孙彤 武旭源 《中国环境科学》 EI CAS CSCD 北大核心 2020年第4期1523-1530,共8页
构建了套筒式机械搅拌磷酸铵镁结晶-斜板强化沉淀反应器用于处理高浓度氮磷废水,并回收磷酸铵镁晶体.考察了搅拌转速、水力停留时间以及颗粒碰撞总次数(GT值)对运行效果的影响,并利用计算流体动力学软件(Fluent18.1)对反应器流态进行了... 构建了套筒式机械搅拌磷酸铵镁结晶-斜板强化沉淀反应器用于处理高浓度氮磷废水,并回收磷酸铵镁晶体.考察了搅拌转速、水力停留时间以及颗粒碰撞总次数(GT值)对运行效果的影响,并利用计算流体动力学软件(Fluent18.1)对反应器流态进行了数值模拟,分析了反应器结构设计的合理性,为磷酸铵镁结晶-沉淀反应器设计及运行提供技术参考.结果表明,反应器在转速为250r/min、水力停留时间为0.375h、平均GT值范围在14000~20000之间时,氨氮的平均回收率为76.00%以上,磷的平均回收率为97.00%以上,晶体的平均粒径达到20.515μm,出水浊度一直稳定在2NTU以下.扫描电镜以及X射线衍射分析表明,沉淀物为纯净的磷酸铵镁.反应器内不同区域的水力分级明显:混合反应结晶区流态为湍流区,缓冲区和磷酸铵镁收集区流态为过渡区,固液分离区流态为层流区.反应器的流态特征表明,在适宜的运行参数下该反应器的结构设计满足晶体形成、生长与固液分离的水力需求. 展开更多
关键词 高浓度氮磷废水 酸铵镁 结晶反应器 流态模拟
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Simultaneous removal of nitrogen and phosphorus from swine wastewater in a sequencing batch biofilm reactor 被引量:3
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作者 海热提 何一群 +1 位作者 王晓慧 李媛 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2015年第1期303-308,共6页
In this study, the performance of a sequencing batch biofilm reactor(SBBR) for removal of nitrogen and phosphorus from swine wastewater was evaluated. The replacement rate of wastewater was set at 12.5% throughout the... In this study, the performance of a sequencing batch biofilm reactor(SBBR) for removal of nitrogen and phosphorus from swine wastewater was evaluated. The replacement rate of wastewater was set at 12.5% throughout the experiment. The anaerobic and aerobic times were 3 h and 7 h, respectively, and the dissolved oxygen concentration of the aerobic phase was about 3.95 mg·L-1. The SBBR process demonstrated good performance in treating swine wastewater. The percentage removal of total chemical oxygen demand(COD), ammonia nitrogen(NH4+-N), total nitrogen(TN), and total phosphorus(TP) was 98.2%, 95.7%, 95.6%, and 96.2% at effluent concentrations of COD85.6 mg·L-1, NH4+-N 35.22 mg·L-1, TN 44.64 mg·L-1, and TP 1.13 mg·L-1, respectively. Simultaneous nitrification and denitrification phenomenon was observed. Further improvement in removal efficiency of NH4+-N and TN occurred at COD/TN ratio of 11:1, with effluent concentrations at NH4+-N 18.5 mg·L-1and TN 34 mg·L-1, while no such improvement in COD and TP removal was found. Microbial electron microscopy analysis showed that the filler surface was covered with a thick biofilm, forming an anaerobic–aerobic microenvironment and facilitating the removal of nitrogen, phosphorus and organic matters. A long-term experiment(15 weeks) showed that stable removal efficiency for N and P could be achieved in the SBBR system. 展开更多
关键词 Sequencing batch biofilm reactor Swine wastewater Simultaneous nitrogen and phosphorus REMOVAL
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Performance of Wuxi WWTP in China 被引量:1
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作者 WANGLin WANGLi JIANGYifeng: 《Journal of Ocean University of Qingdao》 2003年第2期224-229,共6页
In Wuxi Wastewater Treatment Plant, the Anaerobic, anoxic and oxic (A2/O) process was employed to remove the nitrogen and phosphorus, which exhibited the positive results of the high removal efficiency for phosphorus ... In Wuxi Wastewater Treatment Plant, the Anaerobic, anoxic and oxic (A2/O) process was employed to remove the nitrogen and phosphorus, which exhibited the positive results of the high removal efficiency for phosphorus with a range of 67.7% to 89.9% and an average value of 78.0. The effluent of phosphorus met the national discharge standard. The removal of TN was effected by both BOD variation of influent and wastewater temperature. TN removal was in the range of 28.5% to 55.8% with an average value of 39.4%. The energy cost was 0.15 kWh(m3d)-1 or 1.35 kWh(kgBOD@d)-1. The annual average sludge production was 46.3 m3d-1, the annual average dosage for the dewatering was 40 kg d-1 . 展开更多
关键词 waste water treatment plant (WWTP) combined collection system organic load nutrient removal operation and management cost (O&M cost) ANAEROBIC anoxic and oxic (A^2/O)
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Removal of Nitrogen and Phosphorus from Animal and Municipal Wastewaters as Dittmarite 被引量:1
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作者 Asmare Atalay Brodie Whitehead +1 位作者 Oluwatomisin Oyewole Zatima Brown 《Journal of Environmental Science and Engineering(B)》 2017年第6期295-300,共6页
Phosphorus and nitrogen are known causes of eutrophication in rivers, lakes streams and estuaries. The sources of these nutrients are diverse and they include chemical fertilizers, CAFOs (Confmed Animal Feeding Opera... Phosphorus and nitrogen are known causes of eutrophication in rivers, lakes streams and estuaries. The sources of these nutrients are diverse and they include chemical fertilizers, CAFOs (Confmed Animal Feeding Operations), land application of animal and municipal as well as industrial wastewaters. Application of manure slurries to crop land beyond allowable limits could result in high levels of phosphorus and nitrogen in runoff that negatively impact aquatic animals. Municipal wastewater treatment plants are setup to remove these nutrients from domestic and industrial wastewater through a network of treatment processes. Controlling the discharge of phosphorus and nitrogen in wastewater is a key factor in preventing eutrophication. This paper presents work done to enhance a chemical precipitation process that removes over 90% of dissolved phosphorus and nearly 20% of dissolved nitrogen from both synthetic and municipal wastewaters. The objective of the study is to remove nitrogen and phosphorus from wastewater as dittmarite, a value-added mineral fertilizer found in nature. A laboratory procedure was developed that generated significant quantities of dittmarite from various wastewaters. Pure dittrnarite contains nitrogen, phosphorus and magnesium in approximate molar ratios of 1:1.2:1.2 that can support plant growth. It is produced as a wet precipitate from chemical reactions that occur in the wastewater treatment process; it can be dried for proper handling and utilization. Municipal wastewater treatment plants, high volume fish producers, CAFOs and individual rural homeowners could all benefit from this technology for on-site removal of nitrogen and phosphorus from produced wastewaters. 展开更多
关键词 Dittmarite PRECIPITATION WASTEWATER PILOT-SCALE
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Influencing Factors of Ammonium Nitrogen Removal by Composite Phosphate and Magnesium
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作者 闫立龙 李伟光 +1 位作者 李娟 贲岳 《Journal of Donghua University(English Edition)》 EI CAS 2007年第5期652-656,共5页
It is necessary to adjust reaction pH when a single kind of PO4^3- is used as phosphorus source to remove NH4^+- N in a chemical precipitation process. However, this tedious step could be avoided in experiments that ... It is necessary to adjust reaction pH when a single kind of PO4^3- is used as phosphorus source to remove NH4^+- N in a chemical precipitation process. However, this tedious step could be avoided in experiments that use the buffering effect of the composite phosphate and employ PO4^3- and HPO4^2- as phosphorus sources, pH was controlled by properly changing the proportion of PO4^3- to HPO4^2-. The influences of pH, material proportion and different addition modes of magnesium on NH4^+-N removal efficiency were investigated, with NH4^3--N concentration in influent being 200 mg/L. It showed that the ratio of HPO4^2- : PO4^3- was concerned with phosphorus and NH4^+-N removal. Under the condition that the total amount of phosphate is definite, the removal efficiency of NH4^+-N decreased with the enhancement of HPO4^2- concentration, while the efficiency of phosphorus increased. When increasing PO4^3- concentration, it benefited the removal of NH4^+-N, but the remaining phosphorus was high. The results showed that NH4^+-N concentration decreased from the initial 200 mg/L to 39.14 mg/L with the remaining PO4^3- at 5.14 mg/L if the ratio of HPO4^2- : PO4^3- remained at 1:3. 展开更多
关键词 wastewater treatment phosphorus source ammonium nitrogen NH4^+-N) chemical precipitation magnesium-ammonium-phosphate (MAP)
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Removal of Nitrogen and Phosphorus from Saline Wastewater Using Up-Flow Sludge Blanket Filtration Process
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作者 Saud Bali Al-Shammari Abualbashar Shahalam Abdulallah Abusam 《Journal of Environmental Science and Engineering(B)》 2015年第7期347-353,共7页
There is recent trend of providing additional treatment of wastewater beyond tertiary level. The purpose is to refine water to a quality that is safe for reuse for unrestricted irrigation and other non potable uses. F... There is recent trend of providing additional treatment of wastewater beyond tertiary level. The purpose is to refine water to a quality that is safe for reuse for unrestricted irrigation and other non potable uses. For this purpose, Kuwait has built and operated an advanced wastewater treatment plant with capacity of 500,000 m3·dl. This plant providing treatment beyond tertiary utilizes the process of Ultra Filtration (UF) and Reverse Osmosis (RO). The reject water of this unit contains high concentration of total nitrogen and total phosphate. Safe disposal of this water into the environment or possible reuse needs substantial reduction of these chemicals. In this study, a bench scale up-flow sludge blanket filtration system was investigated. The system operated with an average Hydraulic-Retention Time (HRT) of 19 h, whereas, sludge age varied within the range of 14 days to 16.5 days. The results show that the average removal efficiencies of the system for Biological Oxygen Demand (BOD), Chemical Oxygen Demand (COD) were over 86% and 82% respectively. The phosphate and nitrogen's average removal were found to be 50% and 45% respectively. 展开更多
关键词 Wastewater treatment SLUDGE SALINE NITRATE phosphate.
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Nitrogen and Phosphorus Removal from Agricultural Wastewater Using Constructed Rhizofiltration in Durban, South Africa
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作者 Mathews Simon Mthembu 《Journal of Agricultural Science and Technology(A)》 2012年第10期1142-1148,共7页
Constructed rhizofiltration is a relatively new technology and has potential in agricultural wastewater treatment. It has been reported to reduce heavy metals in wastewater but no substantive work has been reported ab... Constructed rhizofiltration is a relatively new technology and has potential in agricultural wastewater treatment. It has been reported to reduce heavy metals in wastewater but no substantive work has been reported about its ability to remove nitrogen and phosphorus, particularly in agricultural wastewater. If this technology's worth in nutrient removal from wastewater can be proved, it can save time as well as reducing wastewater treatment cost. Influent and effluent nitrogen and phosphate concentrations in the constructed rhizofiltration were measured and it was found that there was a significant difference between the two water samples (P = 0.01). It was also found that more nitrogen and phosphate were retained by planted region (P = 0.01) compared to unplanted (P = 0.02), demonstrating high removal efficiency in the planted region than in the unplanted region. Eighty six percent (86%) removal efficiency of phosphorus was achieved at some points in the planted region while 71% was achieved for nitrogen. These results indicate that constructed rhizofiltration systems, if properly constructed and planted with macrophytes and maintained, can be used for nitrogen and phosphorus removal in wastewater and thus could be used as an alternative technology for agricultural wastewater treatment. 展开更多
关键词 Constructed rhizofiltration wastewater treatment NUTRIENTS agricultural wastewater MACROPHYTES phosphorus andnitrogen removal.
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水解酸化-MUCT组合工艺处理畜禽养殖废水试验 被引量:2
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作者 蔡秀萍 王杏龙 《黑龙江畜牧兽医(下半月)》 北大核心 2017年第7期69-71,共3页
为了提高废水处理效能,试验采用水解酸化-改进型厌氧-缺氧-好氧(MUCT)组合工艺处理畜禽废水,即在MUCT工艺前增加了水解酸化处理,将二沉池的污泥部分回流至水解酸化池。结果表明:当进水固体悬浮物(SS)为1 000~2 500 mg/L、化学需氧量(COD... 为了提高废水处理效能,试验采用水解酸化-改进型厌氧-缺氧-好氧(MUCT)组合工艺处理畜禽废水,即在MUCT工艺前增加了水解酸化处理,将二沉池的污泥部分回流至水解酸化池。结果表明:当进水固体悬浮物(SS)为1 000~2 500 mg/L、化学需氧量(CODcr)为2 500~5 000 mg/L、氨氮(NH_4^+-N)为230~370 mg/L、总氮(TN)为150~400 mg/L、总磷(TP)为25~60 mg/L时,SS、CODcr、NH_4^+-N、TN、TP处理率分别达93.12%、94.82%、95.43%、92.79%、87.58%,出水水质达到国家畜禽养殖业污染物排放标准。说明该组合工艺对畜禽养殖废水处理效果优于传统MUCT工艺。 展开更多
关键词 水解酸化 改进型厌氧-缺氧-好氧(MUCT) 组合工艺 畜禽废水
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