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针对连续退火炉辐射管加热段热处理温度偏低,达不到退火工艺要求的问题,对辐射管加热段供热系统燃烧状态进行诊断.发现该段供热系统的空煤气配比不合理、部分烧嘴的煤气压力偏低,从而引起燃烧状态不佳,炉温偏低等现象.从燃烧状况优化的角度出发,对辐射管烧嘴燃烧过程、燃料介质配比等进行了研究,分析烧嘴前煤气压力偏低的问题,发现煤气结焦和管道积灰导致堵塞,再利用烟气成分分析等手段确定辐射管烧嘴的最佳燃烧效率点,使各支烧嘴的燃烧状况趋于一致,空煤气配比合理,提高燃烧效率和加热质量.然后进行拖偶试验对退火炉的热处理温度进行考核验证.结果 表明,通过燃烧状况诊断和调试,使辐射管加热段热处理温度提高了100℃以上,达到热处理工艺要求. 相似文献
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以土壤热传导方程和K_1—ζ湍流模型为基础,采用温度场叠加法对土壤—空气埋管换热系统进行了三维动态数值模拟,计算了埋管出口温度随时间的动态变化。研究了埋管管长、管径、风速等对换热器出口温度的影响。模拟结果表明:①换热器出口温度随外界气温和土壤表面获得的辐射能的周期性变化而呈周期性变化;②随着管长增加和管径减小,出口温度降低,而且受气温和太阳辐射的影响减小;③随着人口风速减小,出口温度降低且变化幅度减小,供冷性能提高。并进行了实验验证,实测数据与模拟结果之差不超过0.8℃。 相似文献
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为了确保燃煤锅炉掺烧污泥后炉内燃烧安全稳定并控制NOx的生成,以国内某典型1 000 MW超超临界燃煤锅炉为研究对象,利用CFD软件计算研究了不同的污泥掺烧方式对锅炉温度场和NOx生成的影响。结果表明:在燃煤锅炉不同层的燃烧器掺烧污泥,掺烧污泥的燃烧器对应高度均出现了温度的下降和NOx排放浓度的降低;随着污泥分别由下往上在B,D,F层燃烧器进行掺烧,在炉膛出口处烟温升高,NOx排放浓度降低;在保持F层燃烧器总热值不变的情况下进行掺烧时,能保证锅炉整体温度水平,掺烧污泥比例越高,炉膛出口烟温越低,NOx生成量越少;在F层燃烧器掺烧污泥燃烧效果较好,有利于NOx减排,是最适合污泥掺烧的燃烧器层。 相似文献
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Thermo‐Economic Analysis and Multiobjective Optimization of Dual Pressure Combined Cycle Power Plant with Supplementary Firing 下载免费PDF全文
The heat recovery steam generator (HRSG) and duct burner are parts of a combined cycle which have considerable effect on the steam generation. The effect of the gas turbine, duct burner and HRSG on power generation is investigated to reduce exergy destruction and power loss in the gas turbine. The results show that with an increase in duct burner flow rate, pressure loss in the recovery boiler increases, steam generation increases on the HP side while it decreases on the LP side. With a reduction in the HP pinch point, thermal recovery increases while the LP pinch point does not have a significant effect. Then, power loss due to pressure drop in the gas turbine and the electricity cost are considered as two objective functions for optimization. Finally, the sensitivity analysis on ambient temperature, compressor pressure ratio, fuel lower heating value, duct burner fuel rate, condenser pressure and main pressure are performed and results are reported. It is concluded that with an increment in compressor pressure ratio, the duct burner flow rate and consequently steam generation increases while electricity cost decrease. 相似文献
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污泥与煤混烧发电是一种较有发展前景的污泥处理方法,而混烧过程中产生的大量HCl气体会造成受热面腐蚀等危害。利用水平管式反应炉研究了升温速率、燃烧温度、污泥掺混比例以及反应气氛等因素对HCl释放的影响,考察了CaCO3添加量和添加温度对HCl脱除效果,并利用GAS-MET DX4000型红外气体分析仪实时测定HCl释放浓度。结果表明:随着污泥掺烧比例增加,HCl释放体积增加,而Cl→HCl转化率降低;温度升高会促进HCl释放,但600℃后Cl→HCl转化率变化不大;载气中氧气比例升高使得部分HCl转化为Cl2,导致样品中Cl→HCl转化率降低;高升温速率导致HCl释放峰值变大;Ca/(S+0.5Cl)摩尔比增大,则HCl脱除率增加,且Ca/(S+0.5Cl)摩尔比为2时,700℃是HCl脱除最佳温度。 相似文献
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针对目前天然气掺氢后燃烧效率及氮氧化物排放研究较少的问题,应用组分输运模型、涡耗散概念燃烧模型和Do辐射模型,结合GRI-22化学反应机理,建立柔和燃烧模拟模型,通过与实验结果对比验证了模型的可靠性,进一步应用该模型分析不同掺氢比例对燃烧特性的影响。结果表明,随着掺氢比例增加,燃料与氧化剂的混合程度逐渐提高,混合气体的径向分量不断减小;由于反应速率和放热速率提高,燃烧器内部的温度升高,热力型氮氧化物含量增高,主要集中于燃烧器后端;燃料进口速度增大会导致燃烧器内燃烧不完全、出口处温度降低,氧气浓度升高,氮氧化物含量降低。研究发现,天然气中掺入氢气更有利于达到柔和燃烧条件。 相似文献
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Chenghang Zheng Leming Cheng Kefa Cen Jacques P. Bingue Alexei Saveliev 《International Journal of Hydrogen Energy》2012
A reciprocal flow porous burner with an external heat source in the middle section was studied numerically to access the reactor efficiency for synthesis gas generation. The temperature and species profiles were predicted using a two temperature model with a detailed chemical mechanism. The effect of the variation of the power of the external heat source on the hydrogen and carbon monoxide yields was studied. The energy conversion efficiencies of the system with various power levels of the external heat source were evaluated. It is found that H2 and CO yields increase significantly with the addition of the external heat source due to the temperature increase in the middle section of the burner. The CO2 emissions remain small. The methane conversion ratio increases with increase of the power of the external heat source reaching 97%. The H2 and CO conversion ratios yields are nearly doubled as the power of the external heat source increases from 0 to 750 W. The cold gas energy conversion efficiency decreases as the power of the external heat source increases. At the same time, the syngas energy conversion efficiency increases from 41% to 70%, while hydrogen energy conversion efficiency increases from 28% to 46%. 相似文献
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《International Journal of Hydrogen Energy》2019,44(47):26049-26062
With the increasing need to reduce greenhouse gas emission and adopt sustainability in combustion systems, injection of renewable gases into the pipeline natural gas is of great interest. Due to high specific energy density and various potential sources, hydrogen is a competitive energy carrier and a promising gaseous fuel to replace natural gas in the future. To test the end use impact of hydrogen injection into the natural gas pipeline infrastructure, the present study has been carried out to evaluate the fuel interchangeability between hydrogen and natural gas in a residential commercial oven burner. Various combustion performance characteristics were evaluated, including flashback limits, ignition performance, flame characteristics, combustion noise, burner temperature and emissions (NO, NO2, N2O, CO, UHC, NH3). Primary air entrainment process was also investigated. Several correlations for predicting air entrainment were compared and evaluated for accuracy based on the measured fuel/air concentration results in the burner. The results indicate that 25% (by volume) hydrogen can be added to natural gas without significant impacts. Above this amount, flashback in the burner tube is the limiting factor. Hydrogen addition has minimal impact on NOX emission while expectedly decreasing CO emissions. As the amount of hydrogen increases in the fuel, the ability of the fuel to entrain primary air decreases. 相似文献
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建立了CCRT系统模型,并根据试验参数对模型进行了标定。分别比较了不同工况下,燃用B20、BD50、BD100时DOC对常规排放气体的转化效率以及CPF的颗粒物再生情况。发现:DOC对NO的转换效率各工况差别较大,主要受排气温度影响;对CO及HC整体转化效率处于较高水平,去除效果较为理想。平衡时CPF内残留的颗粒物质量随转速升高而增加,随负荷增加而减少;低负荷、高转速工况是CPF再生效果最差的工况。随着生物柴油掺混比例的上升,DOC的NO_2出口浓度及NO转化效率上升,而对DOC的HC和CO去除效果影响较小; CPF残留颗粒物质量在高转速区域有所下降,而在中低负荷区域有所上升。主要原因是燃用生物柴油引发的排气温度降低和颗粒物排放降低。低负荷、高转速工况下,燃用BD50时CPF的再生效果最佳。 相似文献