氨氮与亚硝酸盐比对推流式ANAMMOX反应器影响研究

进水基质中NH3-N与NO2--N比例是影响推流式ANAMMOX反应器性能的重要参数。该比例与NH3-N、NO2--N、TN的去除率以及NH3-N与NO2--N的反应比例等参数呈良好的相关性。在同一进水TN负荷条件下,存在一个最佳的进水比例,使TN去除率达到最大。NH3-N和NO2--N的反应比例随着进水基质比例的变化而变化。在反应器中发生的ANAMMOX反应可能有多种含氮的产物形式(不仅是N2一种)。进水基质比例的变化可能会导致ANAMMOX反应复杂化,多种反应途径同时并存。     

含腐蚀凹坑尿素合成塔的安全评定与分析

对尿素合成塔上封头腐蚀凹坑采用中国SAPV-95和美国API579规范分别进行安全评定，给出安全裕度，简略分析安全评定的结果。     

TCA785移相控制芯片应用方法的改进

TCA785是德国西门子公司生产的一种性能优秀的移相控制芯片 ,该器件具有温度适应范围宽 ,对过零点的识别更加可靠 ,输出脉冲的整齐度更好 ,移相范围更宽等优点 ,此外 ,由于TCA785的输出脉冲宽度可以手动自由调节 ,因此 ,该器件可广泛应用在晶闸管控制系统中。文章根据TCA785芯片的使用特点以及在逆变器实际运用中可能出现的一些问题 ,提出了一种改进的设计方法     

TOPSwitch集成电路在DC/DC电源设计中的应用

文章介绍了PWM／MOSFET二合一的TOPSwitch系列集成电路及其在DC／DC电源设计中的应用，还介绍了基本反馈方式的DC／DC拓扑结构及其改进措施，并对由TOPSwitch集成电路构成的DC／DC电源进行了抗中子实验。     

Reactor modelling for electrochemical processes

This paper presents a relatively straightforward approach to the modelling of electrochemical reactors operated in batch or continuous modes. The models are based on ideal flow assumptions of either well-mixed or plug flow and incorporate reaction rate models based on electrochemical kinetics and mass transport at one electrode. General characteristics of the reactor models are described, particularly with regard to the need for good mass transport in metal recovery applications. An example is given on the use of the model in the recovery of a heavy metal (Cd²⁺) from an acidified solution containing Cd(II) and Fe(III) ions. The reaction rate model is based on experimental data.     

Effect of H2O2 addition mode on enzymatic removal of phenol from wastewater in the presence of polyethylene glycol

The effect of batch and semi-batch additions of the stoichiometric amount of H₂O₂ on enzymatic removal of phenol has been studied over the phenol concentration range of 1-10 mmol/L. It is found that the ratio between the maximum H₂O₂ concentration during the reaction and the initial horseradish peroxidase concentration ((H₂O₂)_max/(HRP)_o) controls the rate of phenol removal by horseradish peroxidase in the presence of the additive, polyethylene glycol. An optimum range of this ratio is determined to be between 10 and 25 μmol/U. Empirical models are proposed to predict the values of (H₂O₂)_max/(HRP)_o required to treat given phenol concentrations under different modes for adding H₂O₂.     

乳液聚合螺旋半园管夹套反应釜

本文将螺旋半园管夹套反应釜与传统的夹套反应釜进行了对比 ,并介绍了螺旋半园管夹套釜在乳液聚合中的应用     

反应器网络综合优化方法的研究进展

反应器网络综合优化方法在选择反应器类型和反应工艺条件时,比传统的方法表现出了很大的优势。综述了各类反应器网络综合优化方法的基本原理和研究进展,并分析了它们的优缺点。这些方法有基于过程特征的方法,包括可得区法和导数分析法;超结构优化法;目标类方法,包括目标法、构造目标法和构造MINLP法;以及经验推断法和分布参数法等。最后分析了这方面研究的发展趋势。     

Modeling the continuous melt transesterification of bisphenol-A and diphenyl carbonate in a continuous stirred tank reactor

A model of continuous melt transesterification of bisphenol-A and diphenyl carbonate in a continuous stirred tank reactor is developed using phase equilibria assumption and the method of molecular weight moments. The model equations can be simplified into a polynomial system that has 17 equations and 17 unknowns. Solution of the polynomial system gives out almost every aspects of the continuous transesterification process. Molecular weight and polydispersity index, end group ratio of hydroxyl to phenyl carbonate, contents of molecular species, and lost diphenyl carbonate fractions are studied in different operation parameters.     

Optimization of anodic oxidation and Cu–Cr oxide catalyst preparation on structured aluminum plates processed by electro discharge machining

This paper describes the optimization of three processes applied in fabrication of a microstructured reactor for complete oxidation of volatile organic compounds. The first process involves the optimization of the electro discharge machining (EDM) method to produce a set of microchannels with a high length to diameter ratio of 100, with a standard deviation from the average diameter below 0.2%, and with a surface roughness not higher than 2.0 μm. To satisfy these criteria, fabrication of microchannels must be carried out with two machining passes in the Al51st alloy. Then, the effect of several parameters on the anodization current efficiency with respect to oxide formation was studied. The best process conditions to get a 30 μm porous alumina layer in a 0.4 M oxalic acid electrolyte, were found to be a temperature of 1 °C, an anodic current density of 5 mA/cm², and 23 h oxidation time. At last, the resulting coatings were impregnated with an aqueous solution of copper dichromate followed by drying and calcination at 450 °C to produce active catalysts. The effect of a copper dichromate concentration, number of impregnation cycles (1 or 2), and different after-treatments on catalytic activity and stability in complete oxidation of n-butane were studied. The catalytic activity of the obtained coatings is superior to that of alumina supported pelletized catalysts even at much lower loadings of active metals.