信息循环与网络化水质自动监控系统的建立

针对如何提高水质自动监控系统中数据信息的有效性这一问题 ,提出了建立监控系统反馈循环的方法。通过监控网络的反馈循环 ,使监控方案不断优化 ,获得更加符合环境监测部门要求的信息。并进一步阐述了如何通过网络实现信息在各级环境监测部门中的传输利用 ,由此构建了一个网络化的水质信息循环系统。实现对现场水质信息的实时观测与系统远程控制。     

含高浓度无机盐的肝素钠废水的处理

采用培养和驯化耐高浓度无机盐的厌氧和好氧微生物对NaCl和Na2 SO4 含量总和在 3 %左右的肝素钠废水直接进行生化处理 ,废水中的COD、BOD5、SS等污染因子去除率达 90 %以上。成功地解决了在高浓度无机盐存在下无法直接采用生化法处理高浓度有机废水的重大难题 ,并在实际工程中应用。     

反硝化新工艺生物膜-电极反应器

介绍了新型反硝化工艺 -生物膜 电极反应器 (BER)的作用机理 ,综述了影响BER处理能力的因素 ,提出了需要研究的方向。     

脱硫反应器及其应用

脱硫反应器是脱硫工艺的核心装置 ,其技术和脱硫指标将制约和决定脱硫工艺的效率。在分析中 ,比较全面地介绍和比较了近年来主要的烟气脱硫反应器设备和研究成果及应用情况 ,指出了脱硫反应器的发展方向     

Optimization of carbon dioxide absorption in a continuous bubble column reactor using response surface methodology

Carbon dioxide absorption using amine based solvents is a well-known approach for carbon dioxide removal. Especially with the increasing concerns about greenhouse gas emissions, there is a need for an optimization approach capable of multifactor calibration and prediction of interactions. Since conventional methods based on empirical relations are not efficiently applicable, this study investigates use of Response Surface Methodology as a strong optimization tool. A bubble column reactor was used and the effect of solvent concentration (10.0, 20.0 and 30.0 vol%), flow rate (4.0, 5.0 and 6.0 L min⁻¹), diffuser pore size (0.5, 1.0 and 1.5 mm) and temperature (20.0, 25.0 and 30.0°C) on the absorption capacity and also overall mass transfer coefficient was evaluated. The optimization results for maintaining maximum capacity and overall mass transfer coefficient revealed that different optimization targets led to different tuned operational factors. Overall mass transfer coefficient decreased to 34.7 min⁻¹ when the maximum capacity was the desired target. High reaction rate along with the highest absorption capacity was set as desirable two factor target in this application. As a result, a third scenario was designed to maximize both mass transfer coefficient and absorption capacity simultaneously. The optimized condition was achieved when a gas flow rate of 5.9 L min⁻¹, MEA solution of 29.6 vol%, diffuser pore size of 0.5 mm and temperature of 20.6°C was adjusted. At this condition, mass transfer coefficient reached a maximum of 38.4 min⁻¹, with a forecasted achievable absorption capacity of 120.5 g CO₂ per kg MEA.     

A novel method to synthesize polyaluminum chloride with a membrane reactor

Al13 or Alb is usually regarded as the most efficient species of polyaluminum chloride(PAC), the performance flocculant for water treatment. This paper was intended to report a new method to synthesize PAC with high content Alb, by using the membrane reactor. NaOH solutions were managed to permeate slowly through the micropores of ultrafiltration membrane into AlCl3 solutions under the suitable transmembrane pressure(TMP). Meanwhile NaOH drops size was limited to nano-scale, resulting in dramatical reduction of the characteristic diffusion time and great increment of contact interface between the strong base and AI ions in solution to favor the formation of Al(OH)4^-, the precursor of AI,3, so few precipitates and much Alb are produced. When the initial concentration of AlCl3/NaOH is 0.40/2.0 (mol/L), MWCO = 10000, TMP = 0.0085 MPa, T= 305 K and B(molar ratio of OH^-/Al^3 ) = 2.25, the quantity of Alb attains about 80%. The results of ^27Al-NMR determination showed that the Al13 content is equal to Alb content. And our PAC product has shown better flocculation effects than the commercial product.     

电催化氧化处理难降解废水技术研究进展

电催化氧化处理难降解废水技术已得到了广泛关注.本文从电极材料与应用,电极结构及反应器形状,以及与其它处理方法联用等综述了最新研究进展,并在此基础上总结出了电催化氧化技术今后的发展方向.     

跨区域灭火救援力量调集模型研究

根据当前我国消防力量配置及灭火救援的现状,在对区域内重大危险源进行灭火救援力量需求分析的基础上,以动态灭火救援圈理论为指导,遵循时间距离最短、同一行政区优先、战斗编成等级优先、类型适应以及力量调集比例限定等原则,构建基于区域重大危险源灭火救援力量需求分析,并以灭火救援战斗编成为基本单位的跨区域灭火救援力量调集模型,该模型可为消防指挥员跨区域调集灭火救援力量提供重要的决策依据。     

UASB反应器处理淀粉废水的效果及影响因素

介绍了UASB反应器处理玉米淀粉废水的效果,分析了主要因素对处理效果的影响。淀粉废水处理实际工程的运行数据表明,UASB反应器处理玉米淀粉废水具有稳定的处理效果,COD去除率在83%以上,BOD5去除率在90%以上,出水满足后续好氧处理工艺的要求;有机负荷、pH值、碱度、出水循环、SO42-和悬浮物等是影响处理效果和颗粒污泥形成及其性质的几个关键因素。     

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。