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两段发生炉冷煤气中水分来源与控制 被引量:2
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作者 苑卫军 郭健 陈玲 《煤化工》 CAS 2009年第6期40-42,45,共4页
从两段式煤气发生炉的造气原理和生产过程入手,系统分析了煤气生产、加压和输送过程中,煤气中水的入项及出项,并介绍了优化发生炉的操作、优化煤气净化工艺、提高煤气输送压力等控制煤气含水量的措施,煤气含水量的降低既利于环境控制,... 从两段式煤气发生炉的造气原理和生产过程入手,系统分析了煤气生产、加压和输送过程中,煤气中水的入项及出项,并介绍了优化发生炉的操作、优化煤气净化工艺、提高煤气输送压力等控制煤气含水量的措施,煤气含水量的降低既利于环境控制,又有助于节约能源和提高产品质量。 展开更多
关键词 两段式煤气发生炉 煤气含水量 来源 控制
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高炉煤气脱湿方法及效益分析 被引量:1
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作者 马元 《冶金动力》 2012年第6期34-36,共3页
经过除尘后的高炉净煤气含有随原燃料、高炉鼓风及除尘时(湿法)带入的水分,这些水分不但降低煤气的热值,还加速管道腐蚀,减少用气设备的使用寿命。根据煤气脱湿研究结果,提出了利用丝网脱水、初步冷凝和深度冷凝方法或丝网脱水与溶液吸... 经过除尘后的高炉净煤气含有随原燃料、高炉鼓风及除尘时(湿法)带入的水分,这些水分不但降低煤气的热值,还加速管道腐蚀,减少用气设备的使用寿命。根据煤气脱湿研究结果,提出了利用丝网脱水、初步冷凝和深度冷凝方法或丝网脱水与溶液吸附法对煤气进行脱湿的方案,钢厂中煤气脱湿不但有节能、降耗、延长管道和用气设备寿命等经济效益,其社会效益也十分显著。 展开更多
关键词 煤气含水量 脱湿 焦比 效益
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介绍一种高炉煤气丝网除雾器
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作者 杨晓东 《冶金动力》 1989年第1期21-21,共1页
重钢3~#、4~#高炉,炉顶压力19.6kPa,其煤气清洗系统中的脱水器为重力式,其结构如(图1)所示:圈1 脱水器筒体直径2200mm。
关键词 丝网除雾器 高炉煤气 脱水器 煤气含水量 实际工作 重力式 炉顶压力 清洗系统 排水孔 壳体直径
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Pulsating hydraulic fracturing technology in low permeability coal seams 被引量:10
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作者 Wang Wenchao Li Xianzhong +1 位作者 Lin Baiquan Zhai Cheng 《International Journal of Mining Science and Technology》 SCIE EI CSCD 2015年第4期681-685,共5页
Based on the difficult situation of gas drainage in a single coal bed of high gas content and low perme- ability, we investigate the technology of pulsating hydraulic pressure relief, the process of crank plunger move... Based on the difficult situation of gas drainage in a single coal bed of high gas content and low perme- ability, we investigate the technology of pulsating hydraulic pressure relief, the process of crank plunger movement and the mechanism of pulsating pressure formation using theoretical research, mathematical modeling and field testing. We analyze the effect of pulsating pressure on the formation and growth of fractures in coal by using the pulsating hydraulic theory in hydraulics. The research results show that the amplitude of fluctuating pressure tends to increase in the case where the exit is blocked, caused by pulsating pressure reflection and frictional resistance superposition, and it contributes to the growth of fractures in coal. The crack initiation pressure of pulsating hydraulic fracturing is 8 MPa, which is half than that of normal hydraulic fracturing; the pulsating hydraulic fracturing influence radius reaches 8 m. The total amount of gas extraction is increased by 3.6 times, and reaches 50 LJmin at the highest point. The extraction flow increases greatly, and is 4 times larger than that of drilling without fracturing and 1.2 times larger than that of normal hydraulic fracturing. The technology provides a technical measure for gas drainage of high gas content and low permeability in the single coal bed. 展开更多
关键词 Gas drainage Pulsating hydraulic fracturing Fatigue damage Permeability improvement
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CBM geology conditions study of Gemudi syncline,Western Guizhou Province
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作者 WU Cai-fang OU Zheng FENG Qing ZHANG Jie-fang 《Journal of Coal Science & Engineering(China)》 2010年第3期288-291,共4页
Through the analysis of the surrounding rock, coal seam burial depth, coal quality and hydrologic geological condition, the methane-bearing property characteristics of the coal reservoir in the Gemudi syncline were el... Through the analysis of the surrounding rock, coal seam burial depth, coal quality and hydrologic geological condition, the methane-bearing property characteristics of the coal reservoir in the Gemudi syncline were elucidated. Most of the wall rock of the coal reservoir is mudstone and silt, which is a favourable enclosing terrane. Burial depth of the main excavating coat seam is moderate. The groundwater activity is thin, and there are absolute groundwater systems between each coal seam, which make poor intercon- nections to accelerate CBM enrichment. In our research, the area coal reservoir meta- morphosis is high, CBM content is high, hole-cranny system development degree is high, and permeability of the great mass of the main coal seam exceeds 0.1×10^-3 μm2, The result demonstrates that the southeast of the Gemudi syncline has the best conditions for prospecting and exploiting CBM. 展开更多
关键词 Gemudi syncline CBM geological condition coal reservoir characteristics permeability
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Comparison of steam-gasification characteristics of coal char and petroleum coke char in drop tube furnace 被引量:4
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作者 丁路 周志杰 +1 位作者 霍威 于广锁 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2015年第7期1214-1224,共11页
The steam-gasification reaction characteristics of coal and petroleum coke (PC) were studied in the drop tube furnace (DTF). The effects of various factors such as types of carbonaceous material, gasification temp... The steam-gasification reaction characteristics of coal and petroleum coke (PC) were studied in the drop tube furnace (DTF). The effects of various factors such as types of carbonaceous material, gasification temperature (1100- 1400 ℃) and mass ratio of steam to char (0.4:1, 0.6:1 and 1:1 separately) on gasification gas or solid products were investigated. The results showed that for all carbonaceous materials studied, H2 content exhibited the largest part of gasification gaseous products and CH4 had the smallest part. For the two petroleum cokes, CO2 content was higher than CO, which was similar to Zun-yi char. When the steam/char ratio was constant, the carbon con- version of both Shen-fu and PC chars increased with increasing temperature. When the gasification temperature was constant, the carbon conversions of all char samples increased with increasing steam/char ratio. For all the steam/char ratios, compared to water gas shift reaction, char-H2O and char-CO2 reaction were further from the thermodynamic equilibrium due to a much lower char gasification rate than that of water gas shift reaction rate. Therefore, kinetic effects may play a more important role in a char gasification step than thermodynamic effects when the gasification reaction of char was held in DTF, The calculating method for the equilibrium shift in this study will be a worth reference for analysis of the gaseous components in industrial gasifier. The reactivity of residual cokes decreased and the crystal layer (L002/d002) numbers of residual cokes increased with increasing gasification temperature. Therefore, L002/d002, the carbon crystallite structure parameter, can be used to evaluate the reactivity of residual cokes. 展开更多
关键词 Drop tube furnaceSteam/char ratioThermodynamic equilibriumReactivity
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