铁屑流化床预处理-催化氧化-混凝沉淀组合工艺处理有机硅废水

采用铁屑流化床预处理、负载活性炭催化剂催化氧化和混凝沉淀组合工艺处理有机硅废水。废水经铁屑流化床预处理后Cu^2＋的去除率达99．90％，COD去除率达23．9％；负载活性炭催化剂催化氧化的最佳工艺条件：催化剂质量浓度为0．5g/L，H202质量浓度为2400mg/L，不投加FeSO4，反应时间为60min，体系pH为3-4，COD去除率达82％。催化氧化后的废水经混凝沉淀处理，调节pn为8-9，可达标排放。     

城市生活垃圾的热解产气特性

以城市生活垃圾中的可燃组分为实际物料,在外热式固定床热解实验台上,通过对比不同物料在不同加热温度的情况,研究了垃圾热解的产气特性,对影响产气特性的因素进行了探讨.     

移动床生物膜工艺特点、研究现状及发展

悬浮载体生物膜工艺（MBBR）又称悬浮填料移动工艺，是在20世纪90年代中期得到开发和应用的，它吸收了传统的活性污泥法和生物膜法两者的优点而成为一种高效的污水处理方法。在国外，悬浮载体移动膜工艺已进入使用阶段。我国在悬浮载体移动膜工艺上基本还处于研究阶段。对这一工艺的特点、研究现状及方向作了介绍。     

滇西北优质富锰矿控矿条件分析

本文采用建造与构造相互作用的观点，从沉积学、构造学和锰质来源三个方面研究了位于滇西北地区的优质富锰矿的唯一矿床——鹤庆锰矿。鹤庆锰矿产出于晚三叠世卡尼一诺利期剧烈下陷的一个台沟环境。该台沟盆地的生成与西缘台褶带卡尼一诺利中期区域性南北向深大断裂带的右行走滑拉张活动有直接的关系。成矿经由以玄武岩浆活动为代表的地热系统对盆地基底矿源层中锰质的萃取、生物吸收以热水喷流形式进入盆地的矿质而成矿的多阶段过程；区域性深大断裂、玄武岩浆活动、矿源层三者的有效时空组合是形成扬子地块西缘卡尼一诺利期优质富锰矿的控制因素。结合区域地史资料分析，认为在滇西北成群产出优质富锰矿的可能性很小。     

絮凝体形态学和密度的探讨(Ⅱ)——致密型絮凝体形成操作模式

论述了致密型絮凝剂形成操作的两种模式：脱水收缩和逐一附着，前者通过长时间机械搅拌进行，后者通过上向流造粒流化床操作进行。实验结果表明，两操作均可生成接近于球形的致密化团粒，但脱水收缩条件下生成的团粒仍具有颗粒有效密度随粒径增大而降低的特点，其分形维数为２．４０－２．４７，而逐一附着条件下生成的团粒密度基本上与粒径无关，可认为其分开维数接近于３。通过讨论上向流造粒流化床操作条件，并将实验得到的致密型     

沸腾炉烟尘磨损性及对策

沸腾炉烟尘含尘浓度高达200一300g／m^3，并且温度高，成分杂，其对净化系统的磨损性不容忽视。本文通过探讨高浓度沸腾炉烟尘的磨损机制，针对湘南某化工厂运行实践，提出了切实可行的防磨损系列措施。     

160 h of chemical-looping combustion in a 10 kW reactor system with a NiO-based oxygen carrier

Chemical-looping combustion, CLC, is a technology with inherent separation of the greenhouse gas CO₂. The technique uses an oxygen carrier made up of particulate metal oxide to transfer oxygen from combustion air to fuel. In this work, an oxygen carrier consisting of 60% NiO and 40% NiAl₂O₄ was used in a 10 kW CLC reactor system for 160 h of operation with fuel. The first 3 h of fuel operation excepted, the test series was accomplished with the same batch of oxygen carrier particles. The fuel used in the experiments was natural gas, and a fuel conversion to CO₂ of approximately 99% was accomplished. Combustion conditions were very stable during the test period, except for the operation at sub-stoichiometric conditions. It was shown that the methane fraction in the fuel reactor exit gas was dependent upon the rate of solids circulation, with higher circulation leading to more unconverted methane. The carbon monoxide fraction was found to follow the thermodynamical equilibrium for all investigated fuel reactor temperatures, 660–950 °C. Thermal analysis of the fuel reactor at stable conditions enabled calculation of the particle circulation which was found to be approximately 4 kg/s, MW. The loss of fines, i.e. the amount of elutriated oxygen carrier particles with diameter <45 μm, decreased during the entire test period. After 160 h of operation the fractional loss of fines was 0.00022 h⁻¹, corresponding to a particle life time of 4500 h.     

Removal of Zn and Ni by adsorption in a fixed bed of wheat straw

Zn⁺² and Ni⁺² in a solution were removed by biosorption in a fixed bed of wheat straw Triticum aestivum. The removal rate and the mass transfer coefficient for Zn⁺² and Ni⁺² were found to be proportional to the liquid superficial velocity to the power of 0.31 for the range of the particle Reynolds number from 18 to 445 (equivalent liquid rates of 0.00070–0.0175 m³ m⁻² s⁻¹). This agrees well with reported literature for mass transfer in a packed bed of solid particles under a laminar flow regime. Effect of the solution pH, temperature and the particle size (0.5, 1.0, 1.5 and 2.0 in.) on biosorption of Zn⁺² and Ni⁺² was also investigated. Biosorption of both Zn⁺² and Ni⁺² increased significantly with the solution pH from 4.0 to 7.0. On the other hand, Zn⁺² and Ni⁺² removal appeared to be insensitive to liquid temperature from 25 to 30 °C. Nevertheless, a 25% increase in the percentage removal of metal ions was observed with further increase of liquid temperature from 30 to 35 °C. However, the biosorbent particle size did not seem to have a systematic effect on the biosorption of Zn⁺² and Ni⁺². In addition, biosorption of Zn⁺² was not affected considerably by co-adsorption of the bimetal solution while biosorption of Ni⁺² decreased about 14%.     

UASB-SBR处理涤纶短纤维废水的实验研究

分别采用水解酸化与好氧（SBR）、厌氧（UASB）与好氧（SBR）工艺对涤纶短纤维废水的生物降解性能进行研究。水解酸化与好氧工艺在进水COD为1 900 mg/L的时候,去除率在80%左右。采用UASB-SBR工艺,进水COD为2700 mg/L时,COD去除率可以达到96%,出水COD〈100 mg/L。实验研究表明,涤纶短纤维废水更适合采用UASB-SBR工艺来处理,并且能够取得较好的效果。     

沸腾炉大气污染物的生成与排放特征分析

以20台沸腾炉(功率小于等于60 MW)的燃料特性分析数据和大气污染物的排放实测数据为基础,利用统计分析方法,研究了燃烧过程中排放的颗粒物(PM)、SO_2和NO_x初始排放浓度的影响因素,分析了沸腾炉PM、SO_2和NO_x排放现状,探讨了我国中小型沸腾炉PM、SO_2和NO_x排放管理控制的潜力和可行性.实验结果表明:在锅炉运行负荷大于等于80%的条件下,中小型沸腾炉PM的初始排放浓度基本上不受锅炉出力、过量空气系数和燃煤灰分含量的影响;燃煤的硫含量越高,SO_2初始排放浓度越高;过量空气系数越大,燃煤挥发分越低,NO_x初始排放浓度越高.