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现有耐火砖干燥窑普遍存在热能浪费大、热效率低、生产效率低以及车间热污染、环境污染等问题。本文提出一种集群间歇式耐火砖干燥窑余热利用新工艺,采用余热回收技术回收窑体和耐火砖在降温段排放的物理显热,用来对刚刚进入升温段的冷窑和冷砖坯进行预热,可以节能约30%,对耐火材料行业节能减排、降本增效具有重要的参考价值。 相似文献
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对15台同型号贯流式蒸汽锅炉进行能效测试.测试用锅炉主要热损失为排烟热损失,占到总损失的85%以上.对比TSG G0002-2010中对锅炉设计参数的要求,分析了锅炉热损失产生的原因及节能方法,以指导锅炉节能运行和节能改造. 相似文献
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热网管道热损失现场测试方法探讨程宗颐扬子石油化工公司节能办公室一、引言实验室内园管稳态热流,热损失测试方法比较成熟,但热网管道现场热损失测试时,遇到的往往是非稳态情况,增加了测试的难度。笔者谨以多年从事保温节能与现场热损失测试的实践,以现场实测与室内... 相似文献
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迴转窑的燃烧控制除提高产品质量与产量外,还具有节省能源,防止公害等意义。实现迴转窑废气中的低氧控制,是工业窑炉的一个重要节能途径。 一、低氧燃烧与节能 进入炉膛的实际空气量和燃烧所需的理论空气量之比和空气比,以μ表示。 相似文献
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一、问题的提出耐火材料厂的生产工艺大致由如下几个流程:原料→粉碎→湿料烘干→配料→压制成型→砖坯烘干→半成品检验→烘成→检验成品其中湿料的烘干、砖坯的干燥和砖的烧成分别在干燥窑和隧道窑中进行。干燥窑一般使用燃料直接燃烧加热干燥,也有用蒸汽间接干燥,而砖坯的烧成,则在隧道窑中进行。隧道窑是耐材厂的关键热工设备。砖在窑中的整个过程分预热、烧成、冷却三个阶段。烧成温度较高,一般大于1350~1430℃,消耗了大量的燃料。预热的介质来自烧成带的燃烧产物.冷却介质为外界空气。送入的空气冷却着已烧成的但温度… 相似文献
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排烟热损失是锅炉各项热损失中最大的一项,它直接影响锅炉效率及发电煤耗。一般情况下,排烟温度每升高10℃,煤耗将增加2 g/(kW·h)左右。因此,降低排烟温度、回收烟气热量对于节能降耗、提高经济效益具有重要的实际意义。对火电厂节能环保供热装置的设计及应用进行了探讨。该设备采用烟气余热回收技术,将高温排烟热量传递给空气,再进行城市及工业区供热,实现了热量的回收,节省了燃煤量,同时也减少了污染物的排放,还提高了锅炉效率,有利于城市及工业区的可持续发展。 相似文献
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炼油装置加热炉节能途径与制约因素 总被引:1,自引:0,他引:1
加热炉是炼油装置的能耗大户,其节能水平对于提高炼油装置的节能水平具有重要意义。介绍了加热炉主要的节能途径:优化换热流程,降低加热炉热负荷;加热炉与其他设备联合回收余热;降低排烟温度、降低过剩空气系数、减少不完全燃烧损失、减少散热损失以提高加热炉热效率。探讨了上述节能途径的主要技术措施及应注意的问题。阐述了进一步提高加热炉节能水平的制约因素:降低排烟温度,要考虑经济性和露点腐蚀;过分降低炉外壁温度,会导致费用过高;预热空气温度过高对环保不利。提出了进一步提高加热炉节能水平的建议;认真净化燃料,降低露点温度;开发新的余热回收工艺;开发并应用“蓄热式高温空气预热贫氧燃烧技术”等新的燃烧技术;加强运行管理。 相似文献
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热风炉空气预热器是纳米碳酸钙生产过程中重要的节能设备,可以降低排烟温度,提高能源利用率。目前广泛采用的光滑圆管空气预热器体积庞大,换热效率低,造成排烟温度高,不仅污染环境,而且浪费大量的热量。为了解决这一问题,将椭圆扭曲管应用于热风炉空气预热器。结果显示,以椭圆扭曲管为换热元件的椭圆扭曲管空气预热器体积小、耗用钢材少、换热效率高,提高了烟气余热利用效率,降低燃料消耗量。以空气为工质,分别对椭圆扭曲管和圆管进行数值模拟,对比分析其传热性能。结果表明,相对于圆管,空气在椭圆扭曲管内湍动性更强,换热效果更好。通过对实际的工程案例进行分析,将椭圆扭曲管应用于热风炉空气预热器可减少换热面积27.9%,缩小体积37%,具有良好的节能节材效果。 相似文献
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A simple model is presented to assess the thermal performance of a cement industry with an integrated view to improve the productivity of the plant. The model is developed on the basis of mass, energy and exergy balance and is applied to an existing Portland cement industry in Indonesia. The data obtained from industry show that the burning efficiency and the second law efficiency of the kiln system are 52.07% and 57.07% respectively. Cooler efficiency and heat recovery efficiency are 47.75% and 51.2% respectively. The unaccounted loss at kiln system was found to be 1.85% and that of cooler system was 19%. The high loss at cooler was mainly due to the convection and radiation losses from the uninsulated cooler. Irreversibility of the system was found to be about 20%, which is due to the conversion from chemical to thermal energy. The thermal energy conservation opportunities are identified. This study show that by replacing industrial diesel oil (IDO) with waste heat recovery from kiln and cooler exhaust for drying of raw meal and fuel, and preheating of combustion air, a cement industry in Indonesia can save about 1.264 × 105 US dollars per year. 相似文献
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A boiler plant is presented, in which the fuel is dried before combustion in a silo with air. The drying air is heated in a recuperative heat exchanger by the heat of flue gases. Hot air is then blown through the bed of fuel in the drying silo, while the fuel dries and the air cools down and becomes humidified. Heat of the moist exhaust air of the silo is recovered for the drying air and combustion air by a recuperative heat exchanger. Modelling of the thermal behaviour of the plant helps in understanding complex interdependencies of the two heat exchangers, the boiler and the dryer. The models of the heat exchangers and applications in analysing the boiler system are described in this paper. Calculating the combinations of extreme operational conditions gives the input data needed in comparing different types of heat exchangers, dimensioning the heat transfer area, choosing the control strategy and selecting the operating parameters and set‐values of the control system. Results of verification measurements and practical operation at a 40 kWth pilot plant and a 500 kWth demonstration plant are also discussed. Using engineering correlation formulas for heat and mass transfer, an adequate accuracy between the model and the measurements was achieved. Fouling was detected to be a major problem with the flue gas heat exchanger. However, in absence of condensation, the increase of a fouling layer with respect to time was observed to be low. Fouling was also a problem with the drying exhaust gas heat exchanger, but after the installation of a simple dust collector, a reasonable cleaning period was achieved. A mixed‐flow configuration was found to be the most appropriate for the flue gas heat exchanger. In order to avoid condensation of the flue gas the drying exhaust gas heat exchanger is indispensable in Finnish climate in the considered system. In addition to this, it decreases the need of fuel. A parallel‐flow type was found the most appropriate as the drying exhaust gas heat exchanger. Copyright © 2004 John Wiley & Sons, Ltd. 相似文献
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有机热载体炉烟气余热回收技术浅析 总被引:2,自引:0,他引:2
长期以来,有机热载体炉排烟温度偏高,造成大量的能源浪费,严重影响了锅炉运行的经济性。为减少热能损失,对烟气余热回收技术的可行性方案、工程应用实例进行了阐述;并指出通过锅炉烟气余热利用技术回收排烟中的显热和潜热,可以大大提高有机热载体炉的热效率,实现节能降耗。 相似文献
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从目前立式燃油锅炉的发展现状出发,针对某小型立式燃油锅炉热效率不高,NO_x排放偏高的缺点,提出了相应改造方案,建立传热模型分析改造前后炉内燃烧与传热过程,并通过实验进行相关测试研究。经过分析和实验,结果表明:通过在炉膛中加装内炉胆,强化了燃烧与传热过程,提高了热效率,并改善了烟气排放;改造后的燃油锅炉炉膛温度分布均匀,无明显高温区,过量空气系数由1.10降低至1.05以下,NO_x排放降低25%以上,排烟温度明显降低,热效率提高2个百分点左右,以上均证明了该改造方案的可行性。 相似文献