减少工业炉炉壁热污染问题的理论研究

针对工业炉壁面的散热特点,建立了工业炉壁面的散热数学模型,并采用SIMPLE法对其无因次方程组进行求解,得出炉体热量主要散失在Y＝0～0.1处.对现有加热炉炉壁的散热状况进行了实测计算,并对安装炉壁档板情况下的热量回收能力进行了分析,结果显示,在基本相同的条件下,其向大气环境排放的热量可从1 524.8 W/m2下降到60.1W/m2,同时还可回收热量404 kW,大大减少了向周围环境的热污染.     

伞罩型湿式脱硫除尘塔入口结构优化模拟

利用商用CFD软件Fluent，采用k-ε湍流模型和SIMPLE算法，对新型伞罩型湿式脱硫除尘塔内的三维两相流场进行数值模拟，发现了塔内烟气入口处流场所存在的不均匀性。为将其流场调节均匀从而提高脱硫除尘效率，在数值模拟的基础上提出在入口处加装直导流板、阶梯导流板和弯曲导流板，并分析塔内y=0截面速度的分布，以及z＝0.21 m截面上的颗粒浓度、速度和压力等参数的分布。结果表明：通过加装阶梯导流板和弯曲导流板均可以将流场调节均匀，达到较理想状态，从而实现高效净化气体的目的。模拟结果对设备的优化设计和实际运行有一定的指导作用。     

Carrousel氧化沟的三维流场模拟与分析

利用CFD的Fluent软件，采用标准的三维K—ε紊流模型，对桂林市七里店污水处理厂1#氧化沟的流场进行了数值模拟，对导流墙和推进器附近的流速进行了计算分析。结果表明，氧化沟下层流速较低，局部区域流速低于0．2m／s。为了防止污泥沉降，应进一步降低推进器位置。能量损失分析表明，卡罗塞氧化沟能量损失主要来源于沿程摩擦损失和局部损失。可通过增加墙体光滑度、降低入口高度以及增加导流墙的曲率半径等措施减少能量损失，改善现有氧化沟的水力特征。     

基于Fluent的闭合环型缺氧反应器构造优化

为提高闭合环型缺氧反应器混合效果,选用基于Fluent软件的三维RNG k-ε紊流数学模型对闭合环型缺氧反应器进行流场模拟,以池底可能淤积面积比例作为混合效果的评价标准,分别从导流直墙长度、导流墙偏心距离及水下推进器偏置等3个方面对缺氧池的系统构造的最优设置进行研究。结果显示,在相同推进器功率下,导流直墙长度2.0 m为佳,导流墙偏心距离0.5 m为佳,推进器向内偏置0.5 m为佳。该研究方法及其结果可以作为闭合环型缺氧反应器的设计依据,具有较佳的技术参考价值。     

液态高炉渣热量回收利用方法及问题

钢铁冶金行业生产会产生大量的高炉渣。高炉渣由于自身温度比较高，含热量丰富，对能源工业来说是一种很好的二次资源。世界上已有一些国家对高炉渣热量的回收利用进行了一定的研究，而国内这方面的研究却很少。详细介绍了近几年国内外对高炉渣热量回收利用的情况，在此基础上，阐述了高炉渣热回收技术需要解决的关键问题和发展趋势。     

液态高炉渣热量回收利用方法及问题

钢铁冶金行业生产会产生大量的高炉渣.高炉渣由于自身温度比较高,含热量丰富,对能源工业来说是一种很好的二次资源.世界上已有一些国家对高炉渣热量的回收利用进行了一定的研究,而国内这方面的研究却很少.详细介绍了近几年国内外对高炉渣热量回收利用的情况,在此基础上,阐述了高炉渣热回收技术需要解决的关键问题和发展趋势.     

A2O氧化沟缺氧区三维流场模拟及结构形式优化

以FLUENT软件为工具，选用三维RNG k-ε紊流数学模型对重庆井口污水厂A²O氧化沟缺氧区内的流场进行模拟，分析了缺氧区内流场分布不均匀及沉泥的原因，提出了水下推进器的合理设置位置与导流墙的合理设置方式，并对优化后的缺氧区进行了模拟计算。通过优化后模拟的结果可见，在相同的功率密度下，缺氧区内的流场得到了较均匀的分布，流速从原来的0.131 m/s提升到0.204 m/s，减少了能量的损失。底部的流速也从原来的0.140 m/s提升到0.226 m/s，有效的防止或减少了沟中的污泥沉积。优化的结果对实际工程的设计也有一定的指导意义。     

补充碳源对交替式厌氧/好氧生物滤池生物蓄磷/回收磷的影响

碳源不足是废水高效脱氮除磷、磷回收的限制因素,研究高效利用碳源同时能提高磷回收效果的的新工艺及其运行方式尤为重要。本研究采用连续式厌氧/好氧交替生物滤池(AABF)处理低碳磷比废水(COD/P=11),并研究碳源的补充方式(间歇型、连续型、连续循环型)、补充周期对生物滤池除磷、回收磷的影响;采用生物膜吸收并蓄积废水中的磷,并采用定期补充碳源方式诱导生物滤池内聚磷菌群(PAOs)充分释磷,以便形成高浓度的磷回收液,同时在PAOs胞内积累内源性碳,用于后续的生物除磷。结果表明,连续循环型碳源补充方式优于其他两种碳源补充方式,合理缩短碳源补充周期利于提高AABF的生物除磷以及磷回收效率;定期补充AABF进水碳源可增加AABF生物膜内聚羟基丁酸酯(PHB)含量、大幅提高AABF厌氧释磷浓度、提高厌氧释磷(磷回收)过程中PAOs的对碳源的利用效率。     

低能耗印染废水处理工艺与运行条件

采用UASB反应器+三段好氧+混凝沉淀组合工艺处理印染工业园废水。结果表明,工程运行中,通过导流墙的设置,UASB水解酸化反应器的运行以及运行工况的控制,在出水稳定在《城镇污水处理厂污染物排放标准》(GB18918—2002)一级A标准时,该系统处理每吨污水电费为0.36元。     

活动导流墙同心圆工艺处理生活污水的试验研究

活动导流墙同心圆工艺为在OCO技术的基础上革新改进的一种新型污水处理技术.通过导流墙开角可以进行混合液回流量的调节,实现系统良好生物脱氮除磷效能的优化平衡.正交试验分析得出了该工艺处理中等浓度生活污水运行工况的最佳参数值,即主反应器总水力停留时间(HRT)为9.5 h,好氧曝气区中部溶解氧浓度为1.5 mg/L,污泥龄(SRT)为18 d,系统出水水质能够满足《城镇污水厂污染物排放标准》(GB18918-2002)的一级B标准的相关要求.试验结果表明,HRT和好氧曝气区DO水平是影响工艺污染物整体去除效能的关键因素,系统中存在着明显的同时硝化反硝化脱氮现象.     

Field Dynamic Calibration of SO2 Recording Instruments

Recent air pollution legislation, introduced as a Clean Air Act into New South Wales, the most populous and most heavily industrialized Australian State relies mainly upon the establishment of maximum limits of emission of air impurities. Regulations made under the Act set out the first of a series of such limits which cover the more commonly encountered pollutants. Other limits will be included later as knowledge is accumulated but, in the meantime, where standards have not been fixed the "best practicable means" of controlling air pollution must be used. To facilitate administration and to provide financial support for scientific and engineering services in the form of the Air Pollution Control Board, industries of significant air pollution potential have been designated as scheduled premises and pay annual license fees. Further technical support for the legislation is provided by an Air Pollution Advisory Committee.     

How to select the best tree planting locations to enhance air pollution removal in the MillionTreesNYC initiative

Highest priority zones for tree planting within New York City were selected by using a planting priority index developed combining three main indicators: pollution concentration, population density and low canopy cover. This new tree population was projected through time to estimate potential air quality and carbon benefits. Those trees will likely remove more than 10 000 tons of air pollutants and a maximum of 1500 tons of carbon over the next 100 years given a 4% annual mortality rate. Cumulative carbon storage will be reduced through time as carbon loss through tree mortality outweighs carbon accumulation through tree growth. Model projections are strongly affected by mortality rate whose uncertainties limit estimations accuracy. Increasing mortality rate from 4 to 8% per year produce a significant decrease in the total pollution removal over a 100 year period from 11 000 tons to 3000 tons.     

Combined simulation of combustion and gas flow in a grate-type incinerator

Computational fluid dynamic (CFD) analysis of the thermal flow in the combustion chamber of a solid waste incinerator provides crucial insight into the incinerator's performance. However, the interrelation of the gas flow with the burning waste has not been adequately treated in many CFD models. A strategy for a combined simulation of the waste combustion and the gas flow in the furnace is introduced here. When coupled with CFD, a model of the waste combustion in the bed provides the inlet conditions for the gas flow field and receives the radiative heat flux onto the bed from the furnace wall and gaseous species. An unsteady one-dimensional bed model was used for the test simulation, in which the moving bed was treated as a packed bed of homogeneous fuel particles. The simulation results show the physical processes of the waste combustion and its interaction with the gas flow for various operational parameters.     

Air Pollution Control of an Electric Furnace Steelmaking Shop

The body of information presented in this paper is directed to design engineers, operating management and others who may be concerned with the prevention of atmospheric emissions from electric arc steelmaking furnaces. Inland Steel Co. has recently begun operating its first electric furnace shop. Air pollution control equipment for the shop was installed to meet or exceed the legal requirements of applicable air pollution ordinances and regulations. General shop production requirements were established at 100 tons of steel per hour (maximum) to meet sales forecasts and intermediate production facility requirements. Conventional swing roof furnace design was selected for the pair of furnaces in the shop.     

垃圾焚烧炉炉膛温度的影响因素

垃圾焚烧过程的不稳定会导致大量有害物质的生成,为确保垃圾的清洁燃烧需要将炉膛温度控制在850℃以上,为此测试了焚烧炉运行的主要可控参数对炉膛温度的影响。结果表明,垃圾堆放位置在垃圾池深3～8 m处,并经过6 d以上发酵脱水后适合焚烧;炉膛温度随给料量、一次风率和一次风温增加而增大,随过量空气系数增加而降低,其中给料量宜控制在95%～110%之间;当过量空气系数为1.6、一次风率为90%、一次风温为260℃、给料量为100%时炉膛温度达901℃。     

Integrated evaluation of aerogenic pollution by air-transported heavy metals (Pb, Cd, Ni, Zn, Mn and Cu) in the analysis of the main deposit media

The composition of the ambient air is constantly changing; therefore, the monitoring of ambient air quality to detect the changes caused by aerogenic pollutants makes the essential part of general environmental monitoring. To achieve more effective improvement of the ambient air quality, the Directive 2008/50/EC on ‘Ambient Air Quality and Cleaner Air for Europe’ was adopted by the European Parliament and the European Council. It informed the public and enterprises about a negative effect of pollution on humans, animals and plants, as well as about the need for monitoring aerogenic pollutants not only at the continuous monitoring stations but also by using indicator methods, i.e. by analysing natural deposit media. The problem of determining the relationship between the accumulation level of pollutants by a deposit medium and the level of air pollution and its risks is constantly growing in importance. The paper presents a comprehensive analysis of the response of the main four deposit media, i.e. snow cover, soil, pine bark and epigeic mosses, to the long-term pollution by aerogenic pollutants which can be observed in the area of oil refinery influence. Based on the quantitative expressions of the amounts of the accumulated pollutants in the deposit media, the territory of the oil refinery investigated in this paper has been referred to the areas of mild or moderate pollution.     

Expanding Blast Furnace Slag Without Air Pollution

Expansion of blast furnace slag causes emissions of hydrogen sulfide, creating an air pollution problem common throughout the steel industry. This paper describes a new process, called pelletizing which eliminates the air pollution problem while at the same time producing a superior slag product.     

Air Pollution Acronyms

Abstract

Computational fluid dynamic (CFD) analysis of the thermal flow in the combustion chamber of a solid waste incinerator provides crucial insight into the incinerator’s performance. However, the interrelation of the gas flow with the burning waste has not been adequately treated in many CFD models. A strategy for a combined simulation of the waste combustion and the gas flow in the furnace is introduced here. When coupled with CFD, a model of the waste combustion in the bed provides the inlet conditions for the gas flow field and receives the radiative heat flux onto the bed from the furnace wall and gaseous species. An unsteady one-dimensional bed model was used for the test simulation, in which the moving bed was treated as a packed bed of homogeneous fuel particles. The simulation results show the physical processes of the waste combustion and its interaction with the gas flow for various operational parameters.     

The New Clean Air Act Operating Permit Program: EPA’s Proposed Regulations

The 1990 Clean Air Act Amendments added a new Title V to the Act which establishes an operating permit program for numerous sources of air pollution. Certain sources are currently required to obtain a construction or “new source review” permit; the 1990 Amendments will require many more sources to apply for a permit which will give them permission to operate. CAA Title V was modeled on the National Pollutant Discharge Elimination System (NPDES) permit provisions of the Clean Water Act, but there are important differences between the two statutes.

Although many states already have their own operating permit programs, by late 1993 every state must establish a program that meets the requirements of Title V and EPA’s implementing regulations. EPA recently proposed these regulations, and by the statutory deadline of November 15, 1991 hopes to issue final regulations establishing the minimum elements of state operating permit programs. These regulations will significantly affect implementation of air pollution measures for years to come because a Title V operating permit will have to assure compliance with all applicable CAA requirements. In addition, permitted sources will be required to pay fees to cover the costs of the permit program.