高氨氮化工废水MBBR—AMBBR—MBBR组合工艺处理

采用移动床生物膜反应器（MBBR）—厌氧移动床生物膜反应器（AMBBR）—MBBR组合工艺处理高氨氮化工废水。反应器采用几何构型优化、比表面积大的新型YD-25生物载体和DNF-203硝化细菌,实现了同步硝化和反硝化,强化了脱氮能力。采用投加菌种和排泥的方式,经27 d的驯化培养即完成了反应器的挂膜启动。试验结果表明：最佳操作条件为HRT 8 d、MBBR中DO 3 mg/L、进水pH 8.0;在进水COD 2 840~7 437 mg/L、ρ（氨氮）92~179 mg/L、TN 148~258 mg/L、pH 6~8的条件下,出水指标均值为COD 352 mg/L、ρ（氨氮）21.2 mg/L、TN 36 mg/L、pH 7.4,满足排放要求。     

固定床三维电极反应器深度处理炼油废水

以不锈钢板为阴阳主电极,以柱状活性炭为感应粒子电极,构建固定床三维电极反应器, 并用其深度处理炼油废水。考察了施加电压、水力停留时间、废水pH和曝气量对COD去除效果的影响。实验结果表明,在施加电压10 V、水力停留时间60 min、废水pH=7.0、曝气量120 L/h的优化工艺条件下,处理后出水的COD=27.1 mg/L,满足“超滤—反渗透”单元对进水COD的要求（COD<30.0 mg/L）。     

干化床和芦苇床稳定污泥过程中的腐殖化特征

通过现场实验,考查污泥干化床和污泥干化芦苇床稳定污泥过程中的腐殖质变化特征,重点分析了污泥腐殖化率和污泥腐殖化指数的变化情况。系统运行了3年,包括前2年的污泥负荷期和第3年的自然稳定期,检测分析在第3年进行。实验结果表明,污泥腐殖质含量历月变化不大,基本在1．1％～2．1％范围;总体上污泥的腐殖化率具有上升趋势,同一时间样品芦苇床中污泥的腐殖化率略高于干化床;污泥腐殖化指数呈上升趋势,但芦苇床略低于传统于化床;4-11月,干化床中的污泥腐殖化指数从0．079升高到0．742,芦苇床从0．042升高到0．715。经过3Y的稳定化处理,污泥的腐殖化程度和腐熟度得到有效提高。     

白云石石灰结晶流化床污水除磷工艺优化

为了获取优化的污水除磷工艺,基于前期对白云石石灰结晶流化床去除厌氧消化上清液中磷的工艺条件和参数的初步探究,考察了不同酸化程度下白云石石灰释放Mg2+、Ca2+的效果,并根据MAP反应特点,选择出酸化液体积为5、6.5和10 m L,分别对应n(Mg)/n(P)为0.6、1.4、2.2进行后续实验。利用响应面法(RSM)对白云石石灰结晶流化床强化除磷工艺的影响因素进行分析和探讨,考察了p H值、n(Mg)/n(P)与停留时间(HRT)(分别记为X1、X2、X3)及各因素之间交互作用对磷去除率的影响,并利用扫描电子显微镜、X射线衍射和傅里叶变换红外光谱对产物进行表征,得出最佳工艺参数为p H=9.5、n(Mg)/n(P)=2.2、HRT=3.0 h。RSM法所建立的回归模型显著,实验精准度、精密度和可信度均在合理范围内,回归方程中X1、X2、X3、X1X2、X1X3、X21、X22、X23对磷去除率影响显著。产物MAP晶形较好,但由于废水的碱度较大(20 mmol/L),产物中含有大量的Ca CO3沉淀。     

Improving Predictive Models of In‐Stream Phosphorus Concentration Based on Nationally‐Available Spatial Data Coverages

Spatial data are playing an increasingly important role in watershed science and management. Large investments have been made by government agencies to provide nationally‐available spatial databases; however, their relevance and suitability for local watershed applications is largely unscrutinized. We investigated how goodness of fit and predictive accuracy of total phosphorus (TP) concentration models developed from nationally‐available spatial data could be improved by including local watershed‐specific data in the East Fork of the Little Miami River, Ohio, a 1,290 km² watershed. We also determined whether a spatial stream network (SSN) modeling approach improved on multiple linear regression (nonspatial) models. Goodness of fit and predictive accuracy were highest for the SSN model that included local covariates, and lowest for the nonspatial model developed from national data. Septic systems and point source TP loads were significant covariates in the local models. These local data not only improved the models but enabled a more explicit interpretation of the processes affecting TP concentrations than more generic national covariates. The results suggest SSN modeling greatly improves prediction and should be applied when using national covariates. Including local covariates further increases the accuracy of TP predictions throughout the studied watershed; such variables should be included in future national databases, particularly the locations of septic systems.     

Fenton流化床陶瓷膜反应器处理造纸废水的膜污染与清洗

采用Fenton流化床陶瓷膜反应器处理造纸废水二级出水,研究了陶瓷膜膜污染的机理,提出了相应的清洗再生方案。实验结果表明:Fenton流化床陶瓷膜反应器处理后废水的溶解性有机碳和色度去除率分别达到84.2%和94.1%。通过Darcy定律模型计算,过滤阻力主要来自于滤饼层阻力,约占总阻力的62.1%;滤饼层中主要污染物为悬浮固体,约占滤饼层总质量的75.4%;疏水性有机物是造成滤饼层污染的主要溶解性有机物,而亲水性有机物更易造成膜孔堵塞;腐殖酸对滤饼层和膜孔堵塞影响较大,而蛋白质比多糖更易引起膜孔堵塞。采用HNO_3清洗污染膜效果最佳,在HNO_3质量分数1.00%、反应时间15 min时,膜通量恢复率达73.6%。     

A^2/O-MBR组合工艺运行优化与氮磷深度控制的分析

为了遏制水环境不断恶化的趋势,应加强对氮、磷超标的治理工作,促进水生态环境平衡发展。本文采用A^2/O-MBR作为主体工艺,后续辅以化学除磷和以深床滤池为反硝化单元的组合工艺,确保最终出水满足天津市《城镇污水处理厂污染物排放标准》(DB12/599-2015)A标准排放要求。     

撞击流技术在环保领域的应用研究进展

撞击流作为一种过程强化技术,其优势在于能够显著强化相间传递和微观混合,可应用于环保工艺、设备中,以达到提高污染物去除效率的目的。本文在简述撞击流基本原理和特性的基础上,详细阐述了国内外撞击流技术在细颗粒物(PM2.5)脱除、烟气脱硫脱硝、废水处理、废气吸收等方面的应用现状,分析了该技术的应用效果和优势,同时介绍了一种可用于废水处理的新型双组分层式撞击流反应器。最后指出,深入探究撞击流复杂体系的机理以及耦合其他新型技术是未来研究的主要方向。     

Emissions and distribution of methyl bromide in field beds applied at two rates and covered with two types of plastic mulches

A field experiment was conducted to compare two plastic mulches and two application rates on surface emissions and subsurface distribution of methyl bromide (MBr) in field beds in Florida. Within 30 minutes after injection of MBr to 30 cm depth, MBr had diffused upward to soil surface in all beds covered with polyethylene film (PE) or virtually impermeable film (VIF) and applied at a high rate (392 kg/ha) and a low rate (196 kg/ha). Due to the highly permeable nature of PE, within 30 minutes after injection, MBr volatilized from the bed surfaces of the two PE-covered beds into the atmosphere. The amount of volatilization was greater for the high rate-treatment bed. On the other hand, volatilization of MBr from the bed surfaces of the two VIF-covered beds were negligible. Volatilization losses occurred from the edges of all the beds covered with PE or VIF and were greater from the high rate-treatment beds. Initial vertical diffusion of MBr in the subsurface of the beds covered with PE or VIF was mainly upward, as large concentrations of MBr were detected from near bed surfaces to 20 cm depth in these beds 30 minutes after injection and little or no MBr was found at 40 cm depth. The two VIF-covered beds exhibited greater MBr concentrations and longer resident times in the root zone (0.5–40 cm depth) than corresponding PE-covered beds. Concentrations of MBr in the root zone of the high rate-treatment beds were 3.6–6.1 times larger than the low rate-treatment beds during the first days after application. In conclusion, VIF promoted retention of MBr in the root zone and, if volatilization loss from bed edges can be blocked, volatilization loss from VIF-covered beds should be negligible.     

养殖污水生物处理的新型流态化技术原理及其应用案例

以COD、NH4+-N、SS值高以及臭味大的水质特征的养殖污水作为研究对象,针对一般处理模式中的生物反应器存在污泥相停留时间短、耐负荷冲击能力低、除碳与脱氮不能协调以及投资运行费用大等问题,自行研制了具有强化传质与混合功能的射流循环厌氧与气升循环好氧流态化反应器,实现了A/O2的组合生物强化工艺,再辅以预处理与后处理工艺,实践了规模为216 m3/d的工程设计与运行,通过连续6个月的运行数据来评价所提出工艺的工程效果。在A、O1与O2的运行负荷(kg COD/(m3.d))分别为6、6及0.5的近似条件下,当进水COD、BOD5、NH 4+-N和SS浓度分别为11 000～13 000、5 500～6 500、560～640和7 000～9 000 mg/L时,处理后出水浓度分别可降低至56.8～59.2、4.7～4.9、8.6～9.5和37.0～39.4 mg/L,各项指标均达到《广东省水污染物排放限值》(DB4426-2001)第2时段的一级排放标准限值要求,取得了明显的工程实效,表明所开发的技术有推广应用的价值。