共查询到19条相似文献,搜索用时 687 毫秒
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用磷酸铵镁制备废水处理中氨氮吸附剂的研究 总被引:1,自引:0,他引:1
化学沉淀法不但去除废水手的氨氮效果较好,而且可以回收再利用氨氮,但因沉淀剂价格昂贵导致处理成本较高。对化学沉淀法所产生的磷酸铵镁焙烧后的产物作为废水处理中氨氮吸附剂进行研究,结果表明,采用磷酸铵镁焙烧回用法可以去除废水中的氨氮。磷酸铵镁的最佳焙烧条件为100℃,2h,在该条件下磷酸铵镁由晶态变为非晶态。当原水的pH为10,焙烧产物用量为2g/L时,吸附30min氨氮去除率可达89.9%。研究表明,氨氮的吸附符合Langmuir吸附等温式。 相似文献
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大量氮磷营养物质排入海湾,引起了富营养化、赤潮等一系列海洋污染问题,污海水中氮磷处理技术研究已引起人们的重视。磷酸铵镁化学沉淀法具有可同时脱除氨氮和磷酸盐,但还未应用于低浓度氨氮废水的处理,尤其是污海水中氨氮的处理。本文采用磷酸铵镁(MAP)化学沉淀法对污海水中氨氮进行处理实验研究,利用污海水中大量存在的Mg2+,以Na2HPO4作为沉淀剂,探讨了初始反应体系pH值、PO43?/NH4+投配比、反应时间等因素对氨氮脱除效果的影响。结合沉淀结晶物XRD和SEM分析,确定了MAP沉淀法处理污海水中氨氮的最佳反应条件:初始反应体系pH值为9.5~10.5,PO43?/NH4+投配比为1.1/1,反应时间为40 min。实验结果表明,在最佳反应条件下,随着氨氮初始浓度的增大,氨氮去除率逐渐增大,当进水氨氮浓度为12 mg/L时,氨氮去除率达到42.80%。 相似文献
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Wenxiu Zhang Anthony Lau 《Journal of chemical technology and biotechnology (Oxford, Oxfordshire : 1986)》2007,82(6):598-602
Composting can provide a viable alternative for poultry manure management in the Fraser Valley of British Columbia, Canada. However, it has a high potential for ammonia emission because of the high nitrogen content of poultry litter. The objective of this study was to reduce ammonia emission by precipitating ammonia into struvite before it can volatilize from the composting matrix. Nitrogen transformation occurs during composting, but struvite formation can help to conserve nitrogen, and does not allow a large amount of nitrogen to be released into the environment as ammonia or nitrate, because ammonium‐nitrogen becomes bound in struvite. It would also be possible to remove phosphorus from the manure. A laboratory‐scale experiment was conducted to examine the feasibility of struvite formation during poultry manure composting. Magnesium and phosphate salts were supplemented to create favorable conditions to form struvite. Results indicated that ammonia emission was reduced by 40% to 84%, while the nitrogen retention in compost was enhanced. The struvite formed in compost was confirmed by means of X‐ray diffraction; and scanning electron microscopy with energy dispersive X‐ray spectroscopy. Copyright © 2007 Society of Chemical Industry 相似文献
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准东煤作为优质动力煤,高含量的Na和Ca导致沾污结渣成为制约其大范围工业应用的因素。选取准东五彩湾煤作为研究对象,使用富磷鸟粪石作为添加剂,分别对500℃下处理后的原煤灰和混合煤灰(掺入质量分数为5%的鸟粪石)进行同步热分析;在管式炉中以空气气氛对原煤和混合煤在不同温度下进行燃烧实验;通过 X射线荧光光谱分析仪(XRF)、X射线衍射分析仪(XRD)、电感耦合等离子体发射光谱仪(ICP-OES)对收集灰分进行分析;并通过热力学软件FactSage对实验结果加以验证。结果表明:鸟粪石添加剂对Na和Ca的释放规律影响较大,大量的Na和Ca在燃烧过程中以磷酸复盐的形式聚集在混合煤灰中,Ca的低温共熔物未能生成;在1000℃之前鸟粪石添加剂对Na和Ca的捕集效果较好,温度上升后有所下降。 相似文献
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药剂成本过高是阻碍磷酸铵镁结晶技术推广应用的关键难题之一。通过改变结晶反应的初始条件,采用廉价氧化镁为镁盐,有效回收废水中的氨氮。研究结果表明,起始pH为2时,氧化镁为镁盐时,废水氨氮去除效率达到90%以上;采用Mg2+:NH4+:PO43- 摩尔比为1:1:1,煅烧温度在200~400℃时,氨氮回收率超过82%;XRD和FTIR分析结果表明,不同温度条件下,氧化镁的晶体结构出现畸变,导致Mg O键键长出现变化,红外光谱出现红移及蓝移现象,而Mg O键键长的变化与沉氨效率存在直接的相关性。 相似文献
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Bin Lu Jingcheng Xu Ming Zhang Weihai Pang Li Xie 《Korean Journal of Chemical Engineering》2017,34(11):2879-2885
Phosphorus is the crucial factor causing eutrophication in the aquatic ecology. The high phosphorus loading in water bodies may result from the direct disposal of untreated wastewater. In this study, a fluidized bed reactor (FBR) was specially developed to remove and recover phosphorus effectively and efficiently via struvite crystallization. Different physiochemical and hydraulic conditions, including hydraulic retention time (HRT), pH, and molar ratios of Mg : P, N : P and Ca : Mg, were explored to optimize the performance of this improved FBR. For the continuous operating trials, promising removal and recovery efficiencies were achieved at the phosphorus concentration of 25.0 mg/L: >90% of phosphorus could be removed under the optimum condition (pH=9, HRT=12 h, Mg : P=1.25 and N : P=7.5). Increasing the recycle flow rate and prolonging the contact time could also enhance the FBR efficiency. The crystal products obtained in FBR were analyzed in terms of composition and structure. Results indicated that almost pure struvite (>99%) was achieved at low calcium concentrations, which could be considered as a high quality fertilizer. 相似文献
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This paper focuses on struvite (MgNH4PO4·6H2O) crystallization in controlled supersaturation. Struvite can be used as a slow-release fertilizer. Crystallization experiments were conducted using supersaturated solutions. The secondary focus of this paper is the design of a struvite recovery system in fed-batch-controlled supersaturation mode. The design and commissioning of fed-batch struvite crystallization included the determination of operating supersaturation of struvite crystallization, suitable seed materials and the composition of feed solution. Determination of operating supersaturation of struvite crystallization was conducted by two steps including thermodynamic simulation using gPROMS2 (process simulation software) along with a set of batch experiments. Investigation of suitable seed materials was also conducted using set of batch experiments. Two types of seed materials including quartz sand and struvite seeds were used in the investigation of seed materials. Composition of feed solution included the investigation of struvite solution chemistry using PHREEQC3 thermodynamic modeling package. Based on the previously investigated design approach, struvite crystallization in fed-batch system was conducted using a 44-L of reactor with 15-L of initial reactant volume. 相似文献