陶瓷烧成中NOx生成及控制对策

通过对2种不同结构、不同烧成气氛的梭式窑的整个烧成过程中NOx生成进行测试分析，得出快速升温将增加整个陶瓷烧成过程中NOx的生成；其次，烧嘴的合理布置，改善窑体结构，加强高温阶段窑内温度场的均匀性。可以减少NOx的生成；第三，还原气氛可抑制NOx的生成；最后，提出降低陶瓷烧成中NOx生成的几点建议。     

陶瓷烧成中气氛及温度对NOX生成的影响

通过对不同烧成气氛NOX的生成进行测试分析,得出还原气氛可抑制NOX的生成.但在没有催化剂存在的情况下,CO对NO的还原效果不显著;其次,在烧成温度较低(1 200 ℃以下)、高温阶段温度场均匀性较好且使用洁净燃料(即含氮量较小的燃料)的情况下,快速升温将导致NOX生成的增加,此时快速型NOX起主要作用;第三,烧嘴的合理布置、改善窑体结构和加强高温阶段窑内温度场的均匀性可以减少NOX的生成.     

Pt／MgO催化剂上NOx存储-还原反应性能

采用稀燃一富燃交替运行方式，研究存储一还原型催化剂PL／MgO的NOx存储性能以及C3H6还原NOx反应性能。氧化存储段，NOx可被有效存储；当氧化性气氛转换为还原性气氛后，出现一个NOx峰，降低了总的转化效果。NOx峰的大小与存储段和还原段时间之比、温度等因素有关；400℃时NOx峰最小，总转化率最高。5h循环实验表明，400℃时PL／MgO催化剂再生良好，NOx转化率稳定在96％。于反应气氛中添加100mg,／m^3SO2进行了5h抗硫性实验，Pt／MgO催化剂的抗硫中毒能力明显强于Pt／BaO／Al2O3。     

气氛对垃圾焚烧中重金属迁移特性的影响

对城市生活垃圾焚烧过程中Ni、Cd、Cu、Pb、Cr和Zn 6种重金属在不同气氛中的挥发率进行了研究，同时比较了氧化性气氛和还原性气氛、中性气氛和酸性气氛以及在混合气氛中各重金属的挥发率。结果表明，氧化性和还原性气氛对Ni、Cu和Cr挥发影响较大，Cr、Cd、Pb和Zn在还原气氛下挥发率比在氧化气氛下高，而Ni和Cu则...     

Pt/MgO催化剂上NOx存储-还原反应性能

采用稀燃-富燃交替运行方式,研究存储-还原型催化剂Pt/MgO的NOx存储性能以及C3H6还原NOx反应性能.氧化存储段,NOx可被有效存储;当氧化性气氛转换为还原性气氛后,出现一个NOx峰,降低了总的转化效果.NOx峰的大小与存储段和还原段时间之比、温度等因素有关;400℃时NOx峰最小,总转化率最高.5 h循环实验表明,400℃时Pt/MgO催化剂再生良好,NOx转化率稳定在96%.于反应气氛中添加100 mg/m3SO2进行了5 h抗硫性实验,Pt/MgO催化剂的抗硫中毒能力明显强于Pt/BaO/Al2O3.     

垃圾分类背景下厨余垃圾剔除比例对生活垃圾焚烧厂NOx排放的影响

收集了生活垃圾焚烧厂关停SNCR时燃料的N排放数据以及与之对应的工况和燃料特性数据,并分析各影响因素对燃料N转化过程中不同环节的影响机理.结果表明,在工业化生产中,燃料N转化率与炉温、垃圾含水率之间不存在显著联系,而随N元素含量和固定碳含量的增加而降低,随过剩空气系数、H/N、O/N的增加而升高.据此提出了符合实际生产条件的燃料N转化路径图.该路径图表明,燃料特性对燃料N转化率和NOx生成浓度起到了决定性作用,并进一步量化了H/N和固定碳含量这2个参数与燃料N转化率之间的关系.提出通过将厨余垃圾从生活垃圾分出的方法来减少NOx生成,并以国内典型城市为例,研究了分出不同比例厨余垃圾的情况下,燃料N转化率和NOx生成浓度的变化趋势.本研究表明通过分出厨余垃圾的方法,能够降低垃圾焚烧厂的脱硝成本及氨逃逸风险,可为进一步控制生活垃圾焚烧过程中的NOx排放提供参考.     

生物转鼓工艺好氧同步处理工业废气中的SO2和NOx

为提升基于脱硫脱硝工艺的生物转鼓对工业废气中SO2、NOx的处理效果,在好氧条件下,分析了生物转鼓的启动过程、稳态下的生物相群落结构,考察了不同进气质量浓度下生物转鼓对SO2、NOx的处理效果和去除负荷,并探讨了生物转鼓同步脱硫脱硝过程中N和S的转化途径.结果表明:生物转鼓的启动挂膜需耗时约25d;门水平的脱硫脱硝优势...     

SO_2在高岭土表面气-粒转化及影响因素

利用自制气溶胶反应器通过实验研究了不同相对湿度(RH)、光照、NOx和NH3条件对SO_2在高岭土表面的气-粒转化过程和SO_2-4生成量的影响。结果表明:RH是影响高岭土表面SO_2转化及SO_2-4生成的最重要因素,随着RH的增加,高岭土表面SO_2的转化量及SO_2-4的生成量也明显增加,其中SO_2转化量最大增幅达600%;光照条件对高岭土表面SO_2的转化及SO_2-4的生成也有一定影响,光照越强SO_2的转化量及SO_2-4的生成量越高;NOx和NH3的存在会促进SO_2在高岭土表面的转化和SO_2-4的生成,协同作用明显。     

污泥在CO_2气氛下热解CO与CH_4的生成特性

利用热重-红外(TG-FTIR)联用技术研究了典型市政污水污泥在CO_2和N_2气氛下的热解特性。基于TG-FTIR分析结果,采用等温模式配合法研究了CO_2气氛下污泥固定床热解过程中CO和CH_4的生成特性,建立了CO和CH_4的生成动力学机理模型,并同传统N_2气氛下污泥热解情况进行了对比,理论模型利用实际实验数据进行了验证分析。结果表明,在实验温度范围内2种气氛下CO与CH_4的生成情况有着比较明显的差异,CO_2气氛下CH_4释放浓度在峰值和总量上都要低于N_2气氛,CH_4释放峰值来得更早,释放时间更为集中,释放过程也结束得更快。相反,CO的释放浓度峰值,总量以及持续时间在CO_2气氛下都要远远高于N_2气氛,随着温度的升高,差距越来越大,CO_2的存在大大促进了CO的生成。经实验验证,理论推导所得的模型公式对于热解产物生成有着良好的预测结果。     

垃圾焚烧飞灰对陶瓷砖烧成影响的研究

利用DTA-TGA分析及烧成实验2种方法确定不同配比物料制陶瓷砖的最佳烧成温度及烧成范围,并对结果进行了比较;测定了不同配比物料在各自最佳烧成温度下烧成所得制品的性能及浸出毒性。结果表明:DTA-TGA分析所得烧成温度略高于实际烧成温度;飞灰掺加量的增加有利于降低陶瓷砖的烧成温度,当掺加量为10%、20%和30%时,制品最佳烧成温度分别为1 132、1 031和985℃;各配比物料在各自最佳烧成温度下烧成的制品均达MU20强度等级,满足抗风化的要求,制品浸出毒性远低于危险废物浸出毒性鉴别标准。     

回转窑式纯氧熔融焚烧垃圾技术研究

生活垃圾安全无害化处理是目前迫切需要解决的问题,直接气化熔融焚烧垃圾技术以降低二恶英排放方面巨大优势得到广泛关注,在此基础上提出纯氧熔融焚烧垃圾技术,几乎可以实现所有二次污染物近零排放。以350 t/d回转窑垃圾焚烧炉为例,对纯氧代替空气应用在回转窑上熔融焚烧垃圾系统进行了详细热力计算及分析。结果表明,纯氧熔融焚烧垃圾系统的锅炉效率可达90.56%,回转窑熔融焚烧系统还可以在垃圾焚烧后灰渣达到熔融温度的条件下,保持该系统热量平衡,稳定燃烧。并参考回转窑设计标准对该纯氧熔融焚烧城市生活垃圾的回转窑参数进行确定。     

回转窑在医废焚烧工程应用中的参数优化

以规模3 t/h的某医疗废物焚烧生产线为依托,优化分析了回转窑焚烧装置核心控制参数(窑头温度、供风量及窑转速),考察了不同负荷、回转窑转动模式及进料方式对焚烧效果的影响,结果表明:窑头温度升高,有利于提高焚烧效果,是影响焚烧效果最重要的工艺参数;75%负荷时最佳工况是窑头温度850℃、窑转速0.09 r/min、供风量7 000 Nm3/h;连续反转的回转窑转动模式和恒流量的连续进料技术,有助于保持良好焚烧工况,炉渣热灼减率分别达到2.6%和2.3%。     

不同原理分析仪观测大气中氮氧化物对比研究

氮氧化物(NOx)是大气二次光化学污染臭氧的重要前体物,但目前对其总量和分量的测量仍存在着一些难以解决的问题。选择3种不同原理的市售氮氧化物分析仪在广东和北京进行比对观测实验,从而比较其各自的优缺点及适用性。结果表明,钼转化法(MC)测得的NOx比光转化法(LC)及液相化学发光法(LPC)所测得的值都明显偏高,可近似认为是NOy。LPC检测NO2时受到PAN等含有—NO2生色基团的干扰,结果比LC略高。LC测得的NOx值与实际大气最为接近。MC测定的NOx比实际值高,但能满足空气质量指标监测的需求;LC能够准确测定大气中的NOx,但造价太高,仅适用于大气化学机理研究;而LPC原理的仪器适合于短时间的航测、高塔和系留艇进行垂直梯度观测。     

危险废物回转式流化冷渣多段焚烧系统焚烧特性研究

危险废物的处理和处置是摆在我国各级市政府面前的紧迫任务。然而我国已经运行的危险废物焚烧装置普遍存在回转窑挂壁结渣、热灼减率偏高和污染排放超标等问题,作者通过将回转窑和流化床特点相结合的方法提出了一种新型危险废物回转式流化冷渣多段焚烧处置装置。该装置采用回转窑(一燃室)、二燃室和流化床结合的热解-流化焚烧工艺,特别是采用控制窑头温度避免了回转窑挂壁结渣;采用流化冷渣装置延长未燃烬渣的焚烧时间,解决了热灼减率偏高问题;水冷式烟气急冷装置可以将烟气温度从1 100℃降到200℃,防止了二恶英的尾部低温再生成。该系统运行稳定可靠,可以处理医疗垃圾和大多数的固态和液态危险废物,实现了烟气污染物尤其是二恶英排放达到国家标准的目标。同时对该系统运行时窑头温度分布、二燃室炉膛出口氧量变化、回转窑和炉膛升温特性、燃烧室外壁温度分布等几方面运行数据都进行了详细的介绍,为危险废物焚烧炉的运行提供了宝贵的经验数据。     

On the Occurrence of Transient Puffs in a Rotary Kiln Incinerator Simulator II. Contained Liquid Wastes on Sorbent

The generation of transient puffs resulting from the batch introduction of liquid waste into a 73 kW (250,000 Btu/h) rotary kiln incinerator simulator was investigated. The liquid was added onto a sorbent, enclosed in cylindrical cardboard containers that were introduced into the combustion chamber one at a time. A statistically designed parametric investigation determined the effects of liquid mass, liquid composition, kiln temperature, and kiln rotation speed on the total magnitude and instantaneous intensity of the pollutant puff leaving the kiln. Liquid "wastes" investigated included toluene, methylene chloride, carbon tetrachloride, and No. 5 fuel oil. Transient puffs from these wastes were monitored using on-line measurements for FID-measurable hydrocarbons, CO, and integrated particulate filter loadings, although the suitability of any one of these indicators depended on the chemical nature of the waste involved.

Results demonstrate that puffs formed during transient conditions are generated easily, even with small quantities of wastes and with the kiln operating at 100 percent excess air. High kiln temperatures and increased kiln rotation speeds exacerbated the generation of puffs, due to increased liquid evaporation rates. Transient puffs may contain hazardous products of incomplete combustion (PICs) even though adequate destruction and removal efficiencies are achieved. Mixtures of chlorinated and nonchlorinated principal organic hazardous constituents (POHCs) in the waste can lead to the formation of more diverse chlorinated compounds than are formed from a single chlorinated POHC such as carbon tetrachloride alone.

This paper is the second of a series. Its companion paper, Part I, which has been published previously,¹ is concerned with solid plastic wastes.     

Rotary Kiln Incineration of Dichloromethane and Xylene: A Comparison of Incinerability Characteristics Under Various Operating Conditions

Comparisons are made, for the first time, between the combustion characteristics of dichloromethane and xylene in an industrial rotary kiln incinerator. The comparisons are made under different operating conditions, including variable kiln rotation rate and operation both with and without turbulence air. Continuous gas composition and temperature measurements and batch gas composition measurements were obtained from two vertical locations hear the exit region of the rotary kiln. The measurements show that there is significant vertical stratification at the exit of the kiln. Addition of turbulence air enhanced combustion conditions throughout the kiln during xylene processing. During dichloromethane processing, however, the addition of turbulence air had minimal effect and only promoted greater bulk mixing; chlorinated compounds transported from the lower kiln during operation with turbulence air were not efficiently processed in the upper kiln. Evolution of test liquids from the bed was not constant but rather was characterized by intermittent peaks. The field-scale data of this work suggest that the evolution rate of the test liquid was increased as kiln rotation rate increased. Many of the differences between xylene and dichloromethane processing during these experiments are explained by a simple stoichiometric analysis.     

Nitric oxide formation in an iron oxide pellet rotary kiln furnace

A one-dimensional numerical model was developed to simulate the effects of heat and mass transfer on the formation of oxides of nitrogen (NOx) in a rotary kiln furnace for iron oxide pellet induration. The modeled kiln has a length-to-diameter ratio of approximately seven. The principal mechanism of heat transfer is radiation from the flame, which was described by the net radiation method. The well known Zeldovich mechanism was used to predict thermal NOx generation. Temperature fluctuations in the vicinity of the flame were estimated with a clipped Gaussian probability density function. The thermal energy and mass balance model equations were solved numerically. The model is capable of predicting temperature profiles and NOx production rates in agreement with observed plant performance. The model was used to explore the effects of process changes on the total NOx formation in the kiln. It was concluded that the gas temperature as well as the partial pressure of oxygen in the process gases controls the rate of NOx formation. Lowering the temperature of the kiln gases by increasing the secondary air flow rates requires simultaneously decreasing the pellet production rate in order to maintain the pellet temperatures needed for blast furnace conditions.     

弧叶型旋转窑烧制污泥陶粒实验研究

实验选取污水污泥、粉煤灰和港口淤泥为原辅材料,采取正交实验设计物料质量配合比与烧制工艺参数,遴选出最佳物料配比和优化的烧制工艺;依照选定物料配比和工艺参数采用弧叶型旋转窑烧制污泥陶粒并测定产品的1 h吸水率,软化系数,堆积密度,表观密度,颗粒级配,粒型系数以及产品浸出毒性等技术指标,选取制得陶粒产品替代全部天然石料配制...