氮掺杂二氧化钛负载钒磷氧催化氧化NO的实验研究

以VPO为活性组分,N掺杂TiO 2为载体,采用浸渍法制备了VPO/TiN催化剂,基于单因素实验研究了其对NO的选择性催化氧化(SCO)性能以及抗硫抗水性能。研究表明:当P/V为1/5、N/Ti为1、活性组分负载量为10%、焙烧温度为350℃时,催化剂的SCO活性最好,NO氧化率达到61%;光致发光光谱(PL)表征显示N掺杂TiO 2在催化剂表面形成的氧空位可增强催化剂对O 2的吸附;VPO/TiN催化剂抗硫抗水性能较强,反应后的催化剂表面未发现硫酸根的特征峰,水蒸气主要通过与NO竞争吸附占据活性位点来抑制催化剂的SCO活性。     

MgO低温催化臭氧降解氨氮的机制研究

研究了低温条件下单独臭氧及MgO催化臭氧化降解水中氨氮的效率和特征,并对其反应机制分别进行了探讨.结果表明,pH是影响臭氧和催化臭氧化除氨的重要因素,不仅影响溶液中NH_3与NH~+_4的比例和臭氧氧化氨氮的速率,还影响氧化产物种类,从而影响脱氮效果.10℃时,单独臭氧对水中氨氮的氧化降解效率随pH的升高而增大,pH≤9时整体降解效率不高,pH=9时仅为16.39%,而pH=10时达到41.77%.臭氧和·OH共同参与降解氨氮的过程.单独臭氧氧化氨氮生成氮气的选择性具有pH依赖性,并与Cl~-密切相关.pH低(≤9)时,氨氮多以NH~+_4形态存在,O_3与Cl~-反应生成ClO~-_x(x=1、3),再氧化NH~+_4,从而生成气态产物N_2或N_2O.MgO在低温条件下具有很强的催化臭氧化降解氨氮的能力且温度升高有利于反应的进行,0、10、20℃时,MgO催化臭氧化氨氮的效率分别为77.53%、80.17%、91.26%.此过程中,·OH参与反应的程度低,一部分氨氮降解依靠ClO~-_x氧化NH~+_4,而氨氮降解的主要途径为O_3对NH_3的直接氧化.     

密封组合形式对结构密封性能影响研究

目的研究密封组合形式对结构密封性能的影响。方法开展密封性能试验,从密封形式、装配形式和涂覆形式的3种组合形式开展试验研究,找出结构密封性能影响因素,筛选密封最优组合形式。结果结构密封3种组成形式分别为有无贴合面的密封形式,干涉装配、湿装配形式,部分涂覆、全涂覆形式。开展2种应力水平下8种密封组合形式的密封性能试验,在保证密封工艺质量条件下,按照飞机结构和受载特点选取合理密封组合形式能有效提高结构密封性能。结论在飞机应力较高、不常拆的密封部位应选择贴合面密封、干涉装配、部分涂覆的密封组合形式,在飞机结构设计要求间隙装配、常拆卸的密封部位选择贴合面密封、湿装配、部分涂覆的密封组合形式。     

钴（Ⅱ）－过氧化氢－苯基荧光酮体系催化光度法测定痕量钴的研究

本文研究了钴（Ⅱ）催化过氧化氢氧化苯基荧光酮的褪色反应，测定了反应级数和表观活化能，建立了测定痕量地的新方法。２５℃时本法检出限为２９×１０－１３ｇ／ｍｌ，线性范围为０．０４～２ｎｇ／１０ｍｌ，催化反应表观活化能为５６．１５ＫＪ／ｍｏｌ。该方法己用于维生素Ｂ１２、人发和茶叶中痕量钴的测定．结果满意，相对标准偏差为２．４～３．４％。     

亚铵法制浆造纸厂中段废水处理技术分析研究

通过对采用两级气浮做预处理 ,生物硫化床串联接触氧化做深度处理的治理技术的分析研究 ,结合废水处理工程实例 ,说明了用两级串联气浮 +硫化床 +接触氧化工艺处理造纸中段水技术切实可靠 ,该治理工艺对处理亚铵法麦草制浆造纸中段废水有较强的针对性和可行性。     

An integrated assessment model for cross-country pipelines

The cross-country petroleum pipelines are environmentally sensitive because they traverse through varied terrain covering crop fields, forests, rivers, populated areas, desert, hills and offshore. Any malfunction of these pipelines may cause devastating effect on the environment. Hence, the pipeline operators plan and design pipelines projects with sufficient consideration of environment and social aspects along with the technological alternatives. Traditionally, in project appraisal, optimum technical alternative is selected using financial analysis. Impact assessments (IA) are then carried out to justify the selection and subsequent statutory approval. However, the IAs often suggest alternative sites and/or alternate technology and implementation methodology, resulting in revision of entire technical and financial analysis. This study addresses the above issues by developing an integrated framework for project feasibility analysis with the application of analytic hierarchy process (AHP), a multiple attribute decision-making technique. The model considers technical analysis (TA), socioeconomic IA (SEIA) and environmental IA (EIA) in an integrated framework to select the best project from a few alternative feasible projects. Subsequent financial analysis then justifies the selection. The entire methodology has been explained here through a case application on cross-country petroleum pipeline project in India.     

Preparation of rare-earth metal complex oxide catalysts for catalytic wet air oxidation

Catalytic wet air oxidation (CWAO) is one of the most promising technologies for pollution abatement. Developing catalysts with high activity and stability is crucial for the application of the CWAO process. The Mn/Ce complex oxide catalysts for CWAO of high concentration phenol-containing wastewater were prepared by coprecipitation. The catalyst preparation conditions were optimized by using an orthogonal layout method and single-factor experimental analysis. The Mn/Ce serial catalysts were characterized by Brunauer-Emmett-Teller (BET) analysis and the metal cation leaching was measured by inductively coupled plasma torch-atomic emission spectrometry (ICP-AES). The results show that the catalysts have high catalytic activities even at a low temperature (80°C) and low oxygen partial pressure (0.5 MPa) in a batch reactor. The metallic ion leaching is comparatively low (Mn<6.577 mg/L and Ce<0.6910 mg/L, respectively) in the CWAO process. The phenol, COD_Cr, and TOC removal efficiencies in the solution exceed 98.5% using the optimal catalyst (named CSP). The new catalyst would have a promising application in CWAO treatment of high concentration organic wastewater. Translated from Techniques and Equipment for Environmental Pollution Control, 2005, 6(2): 40–44 [译自: 环境污染治理技术与设备]     

中国对流层二氧化硫光化学氧化过程的数值研究

利用一个三维非静力区域大气化学输送模式与中尺度气象模式MM5相连接构成一个数值模拟系统，模拟了中国地区对流层臭氧与其前体物的分布以及二氧化硫转化为硫酸盐的过程，模式扬地面源排放、大气输送和扩散、干沉积、气相化学反应和云雨过程。结果表明：日间，O3浓度主要由NOx和NMHC的源排放和光化学反应过程支配，大气辐射是光化学反应强弱的决定因子，其强度可使SO2、O3和SO4^2-的生成浓度呈现不同的日变化和季节变化，结果表明高浓度的O3对二氧化硫转化为硫酸盐的化学过程有很大的促进作用，然而，这种作用受NMHC浓度的影响很大，较高浓度的NMHC使O3浓度上升，但同时增加了对OH等自由基的消耗，使SO2的转化率降低。     

LPWCO method for the treatment of high concentrated organic wastewater

Based on wet air oxidation (WAO) and Fenton reagent, thispaper raises a new low pressure wet catalytic oxidation(LPWCO)which requires low pressure for the treatment of highlyconcentrated and refractory organic wastewater. Compared withgeneral wet air oxidation, the pressure of the treatment(0.1-0.6MPa) is only one of tens to percentage of latter(3.5-10MPa). Inaddition, its temperature is no more than 180℃.Compared withFenton reagent, while H2O2/COD(weight ratio) less than 1.2, theremoval of COD in the treatment is over twenty percents more thanFenton's even the value of COD is more than 14000mg/L. In thispaper, we study the effect factor of COD removal and the mechanismof this treatment. The existence of synergistic effect (catalytic oxidation and carbonization) for COD removal in H2SO4-Fenton reagent system under the condition of applied pressure and heating (0.1-0.6MPa, 104-165℃) was verified. The best condition of this disposal are as follows:H2O2/COD(weight ratio)=0.2-1.0, Fe2+ 0.6×10-3 mol, H2SO4 0.5mol, COD>1×104mg/L, the operating pressure is 0.1-0.6MPa and temperature is 104-165℃. This method suit to dispose the high-concentrated refractory wastewater, especially to the wastewater containing H2SO produced in the manufacture of pesticide, dyestuff and petrochemical works.     

含柠檬酸盐电镀废水的处理

对含柠檬酸盐电镀废水的几种处理方法的比较表明,氯化钡添加法能较好地使柠檬酸盐沉淀,操作简便,处理效果理想,其柠檬酸根离子的去除率达98％以上。