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城市垃圾焚烧飞灰熔融DSC-DTA实验研究 总被引:16,自引:1,他引:15
利用高温DSC-DTA热分析仪对国内外2种城市垃圾焚烧飞灰在惰性气氛(N2)和氧化气氛(O2)下的熔融特性进行了研究.在20℃~1450℃的温度范围内采用3种温升速率进行实验.飞灰熔融过程包含多晶转变和熔融相变2种反应,多晶转变发生在480℃~670℃范围内,吸热量20kJ/kg;熔融约发生在1136℃~1231℃,在1174℃达到峰值,熔融相变潜热约700 KJ/kg,整个过程总吸热量约1800 kJ/kg.研究了CaO添加剂对飞灰熔融的影响.最后提出飞灰熔融吸热量的预测模型,模型 相似文献
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中国城市垃圾处理的主要方式正在由卫生填埋向垃圾焚烧转变. 基于中国城市垃圾焚烧处置需求特征分析,建立了技术评价指标体系,采用层次分析法,从技术的可靠性、经济性和适用性三方面,对国内外现有4种主要城市垃圾焚烧技术进行了综合评价. 结果表明:流化床技术和层燃技术在技术成熟度、技术能力和二NFDA1英污染控制等方面相对可靠,适用于我国多数大城市的垃圾焚烧处置. 国产流化床焚烧技术更加适应当前国内垃圾分类水平较差的大部分城市;层状焚烧技术则比较适用于城市垃圾管理水平高、垃圾分类较好、热值较高、垃圾处置集中度高和规模较大的城市;旋转焚烧和热解焚烧技术则较适用于垃圾成分复杂、尺寸不均匀的小城镇、工业园区垃圾处置或医疗废物处置,但二者均需加强二NFDA1英排放控制. 相似文献
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生活垃圾焚烧飞灰的污染特性 总被引:4,自引:0,他引:4
对我国两种占主导地位的焚烧炉炉型-炉排炉和流化床产生的焚烧飞灰进行分析,包括16个采用炉排炉的主要生活垃圾焚烧厂和部分使用流化床的生活垃圾焚烧厂,对焚烧飞灰从重金属含量,氯、硫、碱含量,二英含量方面对我国生活垃圾焚烧飞灰的性质做比较全面的归纳和总结。统计结果表明炉排炉焚烧飞灰重金属含量要高于流化床焚烧飞灰,Zn的最高含量在10倍以上,均值也在7倍左右,Cu的最高值为7倍,均值为3倍,Cd,Pb,Cr,Ni的均值为7倍,4倍,4倍和1.5倍。Hg的差别最小,高出30%;炉排炉焚烧飞灰的氯、硫、碱含量全面高于流化床焚烧飞灰,炉排炉焚烧飞灰和流化床焚烧飞灰的平均氯含量分别为15.41%,1.71%,SO3的平均含量分别为10.67%,2.875%,焚烧飞灰的K2O和Na2O含量接近,炉排炉焚烧飞灰的平均含量为6.06%,5.325%,流化床焚烧飞灰的平均含量为2.43%,2.63%,两种类型的焚烧飞灰在碱含量上差别没有氯、硫大;焚烧飞灰的二英含量差别巨大,炉排炉和流化床焚烧飞灰二英含量低值比较接近,而高值炉排炉焚烧飞灰要高出流化床焚烧飞灰很多。 相似文献
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垃圾焚烧飞灰熔融固化处理过程特性分析 总被引:15,自引:2,他引:13
为研究熔融固化过程中飞灰主要成分的迁移转化规律,在有温控的高温实验熔融炉中对垃圾焚烧飞灰进行了动态熔融固化实验研究,对处理后的飞灰进行了XRF、XRD分析检测,分析了飞灰熔融过程中熔融渣的主要成分、物相组成、碱度、挥发率和减容率的变化规律.试验结果表明:①飞灰中主要成分CaO、Al2O3和SiO2的质量分数随着温度的升高而增加,而主要成分Cl元素和SO3则从原来的20.59%和10.74%分别降低到0.15%和0.22%,可见高含量Cl元素和S元素是引起飞灰熔融固化挥发率高的主要原因,并且可能主要以氯化物和硬石膏的形式分解挥发,XRD的测定结果也进一步证明了这一点.②飞灰熔融前,碱度随温度的升高而显著降低,但当温度达到流动温度后,碱度值随温度的变化很小,基本保持在0.95左右.③飞灰中盐类分解挥发主要发生在1150℃~1260℃之间,在飞灰熔融温度前约100℃的范围内. 相似文献
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城市生活垃圾焚烧飞灰中钾盐浸出研究 总被引:1,自引:0,他引:1
通过物理化学表征手段和多因素水浸试验对城市生活垃圾焚烧飞灰的性质和飞灰中钾盐浸出规律进行研究.结果表明,飞灰的主要成分为CaO、KCl和NaCl,平均粒径为12.599μm,水洗后的飞灰颗粒粒径会变大,而比表面积变小.粒径范围0.037~0.075 mm飞灰中的金属元素含量对飞灰金属总量贡献率全部在60%左右.浸出过程中,在pH=12的条件下,搅拌强度为400 r·min~(-1),浸出温度为90℃,采用液固质量比为5∶1能使氯化钾的浸出率达到90%以上.浸出液中含有大量的可溶性氯化钾表明飞灰中的钾盐可以通过水洗、过滤、纯化、分布结晶的方式收,氯化钾晶体纯度可达到90%. 相似文献
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Xiao Gang Ni Mingjiang Chi Yong Jin Yuqi Zhang Jiaquan Miao Qi Cen Kefa 《Frontiers of Environmental Science & Engineering in China》2007,1(4):498-503
In order to eliminate secondary pollution caused by municipal solid waste (MSW) incineration, a MSW gasification and melting
process is proposed. The process is expected to reduce the emission of pollutants, especially heavy-metals and dioxins. In
this paper, the combustible components of MSW and simulated MSW were gasified in a lab-scale fluidized bed at 400°C–700°C
when the excess air ratio (ER) was between 0.2 and 0.8. The experimental results indicated that the MSW could be gasified
effectively in a fluidized bed at approximately 600°C–700°C when excess air ratio was 0.2–0.4. The melting characteristics
of two typical fly ash samples from MSW incinerators were investigated. The results indicated that fly ash of pure MSW incineration
could be melted at approximately 1,300°C and that of MSW and coal co-combustion could be melted at approximately 1,400°C.
When temperature was over 1,100°C, more than 99.9% of the dioxins could be decomposed and most of the heavy-metals could be
solidified in the slag. Based on the above experiments, two feasible MSW gasification and melting processes were proposed
for low calorific value MSW: (1) sieved MSW gasification and melting system, which was based on an idea of multi-recycle;
(2) gasification and melting scheme of MSW adding coal as assistant fuel.
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Translated from Environmental Science, 2006, 27(1): 69–73 [译自: 环境科学] 相似文献
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Experimental study on MSW gasification and melting technology 总被引:1,自引:0,他引:1
XIAO Gang JIN Bao-sheng ZHONG Zhao-ping CHI Yong NI Ming-jiang CEN Ke-f XIAO Rui HUANG Ya-ji HUANG He 《环境科学学报(英文版)》2007,19(11):1398-1403
In order to develop municipal solid waste (MSW) gasification and melting technology, two preliminary experiments and a principle integrated experiment were fulfilled respectively. The gasification characteristics of MSW are studied at 500-750℃ when equivalence ratio (ER) was 0.2-0.5 using a fluidized-bed gasifier. When temperature was 550-700℃ and ER was 0.2-0.4, low heat value (LHV) of syngas reaches 4000-12000 kJ/Nm3. The melting characteristics of fly ash were investigated at 1100-1460℃ using a fixed-bed furnace. It was proved that over 99.9% of dioxins could be decomposed and most heavy-metals could be solidified when temperature was 1100-1300℃. The principle integrated experiment was carried out in a fluidized-bed gasification and swirl-melting system. MSW was gasified efficiently at 550-650℃, swirl-melting furnace maintains at 1200-1300℃ stably and over 95% of fly ash could be caught by the swirl-melting furnace. The results provided much practical experience and basic data to develop MSW gasification and melting technology. 相似文献
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Gang Xiao Baosheng Jin Mingjiang Ni Kefa Cen Yong Chi Zhongxin Tan 《Frontiers of Environmental Science & Engineering in China》2011,5(2):193-204
Considering high-moisture municipal solid waste (MSW) of China, a steam dried MSW gasification and melting process was proposed,
the feasibility was tested, and the mass and energy balance was analyzed. Preliminary experiments were conducted using a fixed-bed
drying apparatus, a 200 kg per day fluidized-bed gasifier, and a swirl melting furnace. Moisture percentage was reduced from
50% to 20% roughly when MSW was dried by slightly superheated steam of 150°C–350°C within 40 min. When the temperature was
less than 250°C, no incondensable gas was produced during the drying process. The gasifier ran at 550°C–700°Cwith an air equivalence
ratio (ER) of 0.2–0.4. The temperature of the swirl melting furnace reached about 1240°C when the gasification ER was 0.3
and the total ER was 1.1. At these conditions, the fly ash concentration in the flue gas was 1.7 g·(Nm3)−1, which meant over 95% fly ash was trapped in the furnace and discharged as slag. 85% of Ni and Cr were bound in the slag,
as well as 60% of Cu. The mass and energy balance analysis indicates that the boiler heat efficiency of an industrial MSW
incineration plant reaches 86.97% when MSW is dried by steam of 200°C. The boiler heat efficiency is sensitive to three important
parameters, including the temperature of preheated MSW, the moisture percentage of dried MS Wand the fly ash percentage in
the total ash. 相似文献
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CHI Yong WEN Jun-ming ZHANG Dong-ping YAN Jian-hu NI Ming-jiang CEN Ke-fa 《环境科学学报(英文版)》2005,17(4):699-704
IntroductionWiththedepletionofspaceforlandfillingofmunicipalsolidwasteandtherisingpricesforrawmaterials ,moreandmorefluidizedbedincineratorshavebeenusedtotreatMSWduetotheprimaryadvantagesofhygieniccontrol,volumereductionandenergyrecovery .BecausetheMSWhas… 相似文献
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In all the municipal solid waste (MSW) disposal technology, incineration with gasification and melting has been taken as a environmentally sound and zero emission technology owing to avoiding second-pollution of heavy metals and dioxin. In this background, a new direct gasification and melting incineration process with co-current shaft furnace is put forward. In this process, MSW and combustion-supporting air are co-current from top to bottom in a shaft furnace. Fuel gas from pyrolysis and gasification burns completely in the bottom in order to offer energy for slag melting. The simulation experiment of the co-current shaft furnace has been done. The results of simulation experiment show that the temperature on the condition of co-current is much higher than on the condition of countercurrent at the bottom of reaction tube and so is the CO2 quantity discharged from reaction tube. It can be concluded that the co-current shaft furnace is more suitable for direct gasification and melting incineration process. 相似文献
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稳定均匀的燃烧温度是确保减少垃圾焚烧系统大气污染物排放量的一个重要因素.采用内旋流流化床(ICFB)进行了城市生活垃圾焚烧实验,探讨了不同的布风速度、垃圾焚烧量、流化床浓相区高度和不同种类垃圾对焚烧稳定性的影响,并给出了流化床内部温度和CO、NOX、SO2等大气污染物的浓度变化.内旋流流化床采用非均匀布风,低速风的移动区尚未流化时,浓相区温度存在一定的不均匀性,低速风区流速超过2倍初始流化速度后,浓相区温度是均匀一致的;流化床的床料具有较好的蓄热能力,较厚的床层有利于提高燃烧的稳定性,可减少垃圾给料和垃圾热值的波动对燃烧温度造成的不利影响;垃圾的焚烧效果与垃圾的热值有直接关系,焚烧低热值垃圾时,为了提高焚烧温度并达到较好的排放指标,需要增加一定量辅助燃料进行助燃;内旋流流化床在燃烧稳定性以及燃烧温度控制上具有一定优势. 相似文献
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针对我国城市生活垃圾热值低等特性。在流化装置上进行了城市生活垃圾与煤混燃实验,研究了在混燃过程中城市生活垃圾与煤掺烧比例及床层温度变化对NO和N2O排放浓度的影响。实验结果显示,随掺烧垃圾量逐渐增加时,NO排放浓度降低。而N2O排放浓度先降低然后增加,当城市生活垃圾与煤掺烧比例恒定时,随床温的增加NO排放浓度增加,N2O排放浓度呈下降趋势,采用前向式神经网络,以掺烧比和床温作为输入参数,对NO的排放进行预测。结果显示精度较高。 相似文献
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以陶粒为载体,采用常温浸渍法制备了负载型镍基催化剂,并利用X射线衍射分析(XRD)、X射线荧光分析(XRF)、BET、环境扫描电镜-能谱仪分析(ESEM-EDX)和元素分析等对其进行了表征,该催化剂BET表面积为101.3m2/g.活性组分NiO颗粒平均粒径约为2μm,均匀分散在载体表面.并在下吸式固定床气化炉中,进行水蒸气催化气化城市生活垃圾有机组分的实验来评价镍基催化剂的催化活性.结果表明,在镍基催化剂的作用下,H2和CO含量明显增加,H2含量最高达43.22%,CO2、CH4、C2H4和C2H6.平均含量降至1%以下.催化气化过程的产氢率远远高于气化过程,最高达19.9mol H2/kg,低温段催化气化的潜在产氢率高于气化过程,但高温段低于气化过程;高温有利于气化产气中H2和CO的生成,还可以促进CH4、C2H4和C2H6的分解.催化气化过程的焦油产率、灰渣产率明显低于气化过程,特别是焦油产率降至2%以下,而产气率则高于气化过程. 相似文献
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Study on pyrolysis and gasification of wood in MSW 总被引:3,自引:1,他引:3
NI Ming-jiang XIAO Gang CHI Yong YAN Jian-hu MIAO Qi ZHU Wen-li CEN Ke-fa 《环境科学学报(英文版)》2006,18(2):407-415
In order to develop municipal solid waste(MSW) pyrolysis/gasification and melting technology with low emission and high efficiency, it was planed that all the main components in MSW and some typical kinds of MSW were pyrolyzed/gasified to propose an expert system for raw MSW. In this paper, wood, which was a prevalent component in MSW, was pyrolyzed and gasified in fluidized-bed reactors at different apparent excess air ratios (EARs), temperatures and fluidizing velocities. For pyrolysis, with tem- perature increasing from 400℃ to 700℃, the yield of pyrolysis char decreased while that of pyrolysis gas increased (in this paper respectively from 28% to 20% and from 10% to 35%), and when temperature was 500℃, the yield of pyrolysis tar reached the highest, up to 38% in this paper. It was the optimum for gasification when temperature was 600℃ and apparent EAR was 0.4. Under the experimental conditions of this paper, gasification efficiency achieved 73%, lower heat value(LHV) reached 5800 kJ/(Nm^3) and yield of syngas was 2.01 Nm^3/kg. Lower fluidizing velocity was useful to upgrade gasification efficiency and LHV of syngas for wood gasification. Based on the results, the reactive courses and mechanism were analyzed respectively for wood pyrolysis and gasification. 相似文献