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煤气化燃烧一体化链条炉排锅炉的研制 被引量:1
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作者 董芃 《工业锅炉》 2005年第5期19-21,共3页
文章详细介绍了最新研制的煤气化燃烧一体化链条炉排锅炉的技术原理及其热工和环保方面的测试结果。
关键词 工业锅炉 链条炉排 煤气化燃烧
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LNB型煤气化燃烧锅炉操作事故原因分析及预防方法探讨
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作者 高军林 许雅周 《工业锅炉》 2007年第2期55-57,共3页
总结分析了LNB型煤气化燃烧锅炉在使用时产生事故的原因,并提出相应的安全操作对策。
关键词 LNB型煤气化燃烧锅炉 事故 安全操作
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双炉室固定炉排煤气化燃烧锅炉研制
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作者 董芃 《工业锅炉》 2006年第3期11-13,共3页
文章详细介绍了最新研制的双炉室固定炉排煤气化燃烧锅炉的技术原理及其热工和环保方面的测试结果。
关键词 工业锅炉 双炉室 固定炉排 煤气化燃烧
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炉窑半煤气化燃烧室的一种加煤方法
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作者 魏伟 《节能》 北大核心 1992年第1期29-30,共2页
一些中小型工业炉窑为达到消烟除尘和节能的目的,采用了半煤气化结构的燃烧室。这类半煤气燃烧室多半是间歇式的,通常一次性加满煤,煤层厚度在400~600mm左右,燃烧所需空气量的一部分由炉篦下供入,与煤中固定碳进行燃烧反应,产生高温和... 一些中小型工业炉窑为达到消烟除尘和节能的目的,采用了半煤气化结构的燃烧室。这类半煤气燃烧室多半是间歇式的,通常一次性加满煤,煤层厚度在400~600mm左右,燃烧所需空气量的一部分由炉篦下供入,与煤中固定碳进行燃烧反应,产生高温和半煤气。 展开更多
关键词 工业炉窑 煤气化燃烧 加煤法 锅炉
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一种新型的半煤气化燃烧方式
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作者 朱道灿 孙广藩 《应用能源技术》 1992年第3期28-30,32,共4页
关键词 手烧锅炉 煤气化燃烧
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原位煤气化化学链燃烧发电系统的过程模拟
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作者 王小雨 赵海波 《动力工程学报》 CAS CSCD 北大核心 2024年第7期1026-1032,共7页
运用Aspen Plus软件构建了以Fe_(2)O_(3)/FeO为氧载体的600 MW原位煤气化化学链燃烧发电系统。基于系统的仿真结果,分别进行了能量、[火用]和[火用]成本分析。结果表明:原位煤气化化学链燃烧发电系统的净热效率为35.38%;系统中内部[火用... 运用Aspen Plus软件构建了以Fe_(2)O_(3)/FeO为氧载体的600 MW原位煤气化化学链燃烧发电系统。基于系统的仿真结果,分别进行了能量、[火用]和[火用]成本分析。结果表明:原位煤气化化学链燃烧发电系统的净热效率为35.38%;系统中内部[火用]损失最大的组件为空气反应器,占原位煤气化化学链燃烧子系统组件总内部[火用]损失的28.39%;水汽系统总内部[火用]损失在整个系统中占比较小,仅为化学链燃烧子系统的14%;原位煤气化化学链燃烧发电系统中单位[火用]成本最大的组件为空气预热器,其值为3.88,再热器、省煤器和过热器的产品单位[火用]成本也较大。 展开更多
关键词 原位煤气化化学链燃烧发电系统 [火用]分析 [火用]成本分析 仿真模拟
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煤气化-无烟燃烧立式锅炉内空气动力场的数值模拟研究 被引量:1
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作者 王擎 罗继亮 +2 位作者 孙东红 关键 孙键 《化工机械》 CAS 2002年第4期189-192,共4页
采用RNGk ε湍流模型、其动量方程利用具有三阶精度的QUICK格式离散的方法 ,对一台采用了无烟燃烧技术的锅炉炉内冷态流场进行了数值模拟 。
关键词 煤气化-无烟燃烧 立式锅炉 数值模拟 工业锅炉 空气动力场 炉内冷态流场 结构 配风方式
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煤气化-无烟燃烧锅炉抑制NO_x排放的试验研究
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作者 孙东红 王擎 +2 位作者 吕清刚 孙键 秦裕琨 《燃烧科学与技术》 EI CAS CSCD 2004年第3期240-243,共4页
煤气化 无烟燃烧锅炉作为一种新型锅炉,采用"多孔分层错列射流式"二次风,将空气分级燃烧及低氧燃烧技术有机地结合在一起.通过"0.1t/h煤无烟燃烧热态试验台"上的研究表明,该锅炉有效地抑制了NOx的排放,同传统燃烧... 煤气化 无烟燃烧锅炉作为一种新型锅炉,采用"多孔分层错列射流式"二次风,将空气分级燃烧及低氧燃烧技术有机地结合在一起.通过"0.1t/h煤无烟燃烧热态试验台"上的研究表明,该锅炉有效地抑制了NOx的排放,同传统燃烧方式相比可降低30%以上,满足现行国家环保标准中对燃油、燃气锅炉的排放要求,即低于400mg/m3. 展开更多
关键词 煤气化-无烟燃烧锅炉 多孔分层错列射流 NOX排放
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卧式煤气化—无烟燃烧锅炉炉内流动特性研究
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作者 孙佰仲 王擎 +2 位作者 车德勇 孙东红 孙键 《锅炉技术》 北大核心 2004年第2期7-9,13,共4页
采用标准本K -ε双方程模型和SIMPLE算法分别对具有同心轴和偏心轴二次风布置型式的卧式煤气化—无烟燃烧锅炉的炉内流场进行数值研究 ,预报了炉膛烟气速度分布、压力分布 ,并对计算结果进行定性分析。表明对于卧式煤气化—无烟燃烧锅... 采用标准本K -ε双方程模型和SIMPLE算法分别对具有同心轴和偏心轴二次风布置型式的卧式煤气化—无烟燃烧锅炉的炉内流场进行数值研究 ,预报了炉膛烟气速度分布、压力分布 ,并对计算结果进行定性分析。表明对于卧式煤气化—无烟燃烧锅炉 ,采用同心轴和偏心轴“多孔分层错列撞击流式”二次风 ,均可形成良好稳定的炉内空气动力场 。 展开更多
关键词 卧式 煤气化—无烟燃烧 锅炉 流动特性 数值计算 炉内流场
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煤气化无烟燃烧技术的实验与应用
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作者 贾俊曦 王擎 +1 位作者 孙东红 单明 《东北电力学院学报》 2001年第4期53-56,共4页
针对我国工业锅炉的现状及经济性差和污染严重的问题 ,结合我国的实际 ,提出了煤气化无烟燃烧技术。通过试验台上消烟除尘的实验以及实际的运行表明该锅炉能够达到环保要求 ,同时具有较高的效率 ,值得采用和推广。
关键词 工业锅炉 煤气化无烟燃烧 实验 大气污染 环境保护
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低火口半煤气燃烧炉及其应用
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作者 刘春城 赵渭国 《节能》 2002年第4期45-46,共2页
阐述了低火口半煤气燃烧炉的基本结构和工作原理 ,给出了主要工作参数的经验公式和数据 ,并介绍了它的应用。
关键词 低火口 煤气化燃烧 应用 结构 工作原理 工作参数
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煤/钙基载氧体化学链燃烧操作参数分析 被引量:4
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作者 张建社 付国家 +1 位作者 田红景 郭庆杰 《高校化学工程学报》 EI CAS CSCD 北大核心 2012年第2期247-253,共7页
化学链燃烧作为一种新颖的燃烧技术,在化石燃料燃烧释放能量的同时能够有效分离CO2。今以CO2为气化剂气化煤炭,基于Aspen Plus流程模拟软件,研究了煤/钙基载氧体化学链燃烧过程。结果表明,以CO2为煤气化剂,各反应器含水分少,可减少热损... 化学链燃烧作为一种新颖的燃烧技术,在化石燃料燃烧释放能量的同时能够有效分离CO2。今以CO2为气化剂气化煤炭,基于Aspen Plus流程模拟软件,研究了煤/钙基载氧体化学链燃烧过程。结果表明,以CO2为煤气化剂,各反应器含水分少,可减少热损失。CaSO4载氧体具有载氧能力大以及反应活性良好等优点。气化炉中CO+H2含量随二氧化碳煤比增大逐渐增加后下降;随温度升高其含量先增加,后趋于平稳。燃料反应器中CO2+H2O含量随载氧体煤比增大,呈现先增大后减小的趋势;随温度升高其含量逐渐下降。空气反应器中CaSO4含量随空载比增大先增加后趋于平稳,随温度升高其含量趋于平稳后下降。气化炉中硫化物和氮化物含量随温度升高而下降,而燃料反应器和空气反应器中硫化物含量随温度升高增加趋势明显,氮化物含量变化不明显。最后确定了关键反应器操作参数:气化炉的二氧化碳煤比为1.8;燃料反应器的载氧体煤比为4.5;空气反应器的空载比为10.5和三反应器的操作温度分别为950、1000和1100℃。 展开更多
关键词 煤气化:化学链燃烧 CaSO4载氧体 热力学
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Effect of operating parameters on coal gasification 被引量:6
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作者 Akanksha Mishra Shalini Gautam Tripurari Sharma 《International Journal of Coal Science & Technology》 EI 2018年第2期113-125,共13页
Coal combustion and gasification are the processes to utilize coal for production of electricity and many other applications. Global energy demand is increasing day by day. Coal is an abundant source of energy but not... Coal combustion and gasification are the processes to utilize coal for production of electricity and many other applications. Global energy demand is increasing day by day. Coal is an abundant source of energy but not a reliable source as it results into high CO2 emissions. Energy industries are expected to decrease the CO2 emission to prevent global warming. Coal gasification is a process that reduces the CO2 emission and emerges as a clean coal technology. Coal gasification process is regulated by several operating parameters. A Number of investigations have been carried out in this direction. A critical review of the work done by several researchers in the field of coal gasification has been compiled in this paper. The effect of several operating parameters such as coal rank, temperature, pressure, porosity, reaction time and catalyst on gasification has been presented here. 展开更多
关键词 Coal gasification Temperature and pressure POROSITY RANK
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Reaction Kinetic Equation for Char Combustion of Underground Coal Gasification 被引量:2
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作者 YU Hong-guan YANG Lan-he +2 位作者 FENG Wei-min LIU Shu-qin SONG Zhen-qi 《Journal of China University of Mining and Technology》 EI 2006年第2期141-146,共6页
Based on the quasi-steady-state approximation, the dynamic equation of char combustion in the oxidation zone of underground coal gasification (UCG) was derived. The parameters of the dynamic equation were determined a... Based on the quasi-steady-state approximation, the dynamic equation of char combustion in the oxidation zone of underground coal gasification (UCG) was derived. The parameters of the dynamic equation were determined at 900℃ using a thermo-gravimetric (TG) analyzer connected to a flue gas analyzer and this equation. The equation was simplified for specific coals, including high ash content, low ash content, and low ash fusibility ones. The results show that 1) the apparent reaction rate constant increases with an increase in volatile matter value as dry ash-free basis,2) the effective coefficient of diffusion decreases with an increase in ash as dry basis, and 3) the mass transfer coefficient is independent of coal quality on the whole. The apparent reaction rate constant, mass-transfer coefficient and effective coefficient of diffusion of six char samples range from 7.51×104 m/s to 8.98×104 m/s, 3.05×106 m/s to 3.23×106 m/s and 5.36×106 m2/s to 8.23×106 m2/s at 900℃, respectively. 展开更多
关键词 underground coal gasification CHAR COMBUSTION kinetic equation thermo-gravimetric
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Control of combustion area using electrical resistivity method for underground coal gasification 被引量:12
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作者 Selivanova Tatiana Grebenyuk Igor Belov Alexey 《International Journal of Mining Science and Technology》 SCIE EI 2012年第3期351-355,共5页
Underground coal gasification (UCG) is one of the clean technologies to collect heat energy and gases (hydrogen, methane, etc.) in an underground coal seam. It is necessary to further developing environ- mentally ... Underground coal gasification (UCG) is one of the clean technologies to collect heat energy and gases (hydrogen, methane, etc.) in an underground coal seam. It is necessary to further developing environ- mentally friendly UCG system construction. One of the most important UCG's problems is underground control of combustion area for efficient gas production, estimation of subsidence and gas leakage to the surface. For this objective, laboratory experiments were conducted according to the UCG model to iden- ti[y the process of combustion cavity development by monitoring the electrical resistivity activity on the coal samples to setup fundamental data for the technology engineering to evaluate combustion area. While burning coal specimens, that had been sampled from various coal deposits, electrical resistivity was monitored. Symmetric four electrodes system (ABMN) of direct and low-frequency current electric resistance method was used for laboratory resistivity measurement of rock samples. Made research and the results suggest that front-end of electro conductivity activity during heating and combusting of coal specimen depended on heating temperature. Combusting coal electro conductivity has compli- cated multistage type of change. Electrical resistivity method is expected to be a useful geophysical tool to for evaluation of combustion volume and its migration in the coal seam. 展开更多
关键词 Underground coal gasificationMonitoringElectro conductivityLaboratory experimentCoal specimen
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Spontaneous coal combustion producing carbon dioxide and water 被引量:7
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作者 DENG Cunbao WANG Jiren +1 位作者 WANG Xuefeng DENG Hanzhong 《Mining Science and Technology》 EI CAS 2010年第1期82-87,92,共7页
Gas products from the process of coal oxidization and spontaneous combustion have been studied at different temperatures with FTI spectroscopic tests. With temperatures rising to about 30~100 ℃, water and carbon diox... Gas products from the process of coal oxidization and spontaneous combustion have been studied at different temperatures with FTI spectroscopic tests. With temperatures rising to about 30~100 ℃, water and carbon dioxide gas were formed and from about 105~150 ℃, carbon monoxide was produced. Using the DFT B3LYP method with a 6-311G basis set, the reaction system, where spontaneous combustion between coal and oxygen occurs and produces water and monoxide, has been studied, with the geometric configuration for all stagnation points on the potential reaction energy surface optimized. With a frequency analysis and an IRC method, transient formations were tested. Our results indicate that in the reaction of coal oxidization and spontaneous com-bustion producing carbon dioxide and water, oxygen molecules attack carbon atoms of the terminal of the propyl alcohol group on the lateral chain of benzene rings, which causes this propyl alcohol group to produce the acid (-CH2-CH2-COOH) group and water. This acid group continues its break up into carbon dioxide and the (-CH2-CH3) ethyl group. We have come to the conclusion that this water-and-carbon dioxide-production reaction is spontaneous, based on the observation of the energy released by the reaction. 展开更多
关键词 spontaneous coal combustion infrared spectrum DFT reaction mechanism
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A back analysis of the temperature field in the combustion volume space during underground coal gasification 被引量:3
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作者 Chen Liang Hou Chaohu +1 位作者 Chen Jiansheng Xu Jiting 《Mining Science and Technology》 EI CAS 2011年第4期581-585,共5页
The exact shape and size of the gasification channel during underground coal gasification(UGC) are of vital importance for the safety and stability of the upper parts of the geological formation.In practice existing g... The exact shape and size of the gasification channel during underground coal gasification(UGC) are of vital importance for the safety and stability of the upper parts of the geological formation.In practice existing geological measurements are insufficient to obtain such information because the coal seam is typically deeply buried and the geological conditions are often complex.This paper introduces a cylindrical model for the gasification channel.The rock and soil masses are assumed to be homogeneous and isotropic and the effect of seepage on the temperature field was neglected.The theory of heat conduction was used to write the equation predicting the temperature field around the gasification channel.The idea of an excess temperature was introduced to solve the equations.Applying this model to UCG in the field for an influence radius,r,of 70 m gave the model parameters,u1,2,3...,of 2.4,5.5,8.7...By adjusting the radius(2,4,or 6 m) reasonable temperatures of the gasification channel were found for 4 m.The temperature distribution in the vertical direction,and the combustion volume,were also calculated.Comparison to field measurements shows that the results obtained from the proposed model are very close to practice. 展开更多
关键词 Underground coal gasification Gasification channel Temperature field Combustion space areaBack analysis
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Analysis of NO_X Emission Characteristics of Pulverized Coal Combustion in Different Atmosphere
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作者 刘汉涛 尉庆国 苏铁熊 《Journal of Measurement Science and Instrumentation》 CAS 2011年第2期201-204,共4页
Researches on the NOx emission characteristics of HT (Huangtai coal), LC(Laicheng) coal are carried out in different atmosphere. The results show that the NOx emission time is postponed in O2/N2 atmosphere mixed w... Researches on the NOx emission characteristics of HT (Huangtai coal), LC(Laicheng) coal are carried out in different atmosphere. The results show that the NOx emission time is postponed in O2/N2 atmosphere mixed with CO. The releasing times of volatile nitrogen and char nitrogen approach, the amount of NOx reduces. In high 02 concentration atmosphere mixed with CO2, the nitrogen releasing times cane ahead of time, NOx congregate in the beginning of the combustion. On the contrary, nitrogen releases separately, and the amount of NOx reduces greatly. 展开更多
关键词 fuel nitrogen releasing characteristics pulverized coal NOx
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