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优化煤气发生炉操作途径探讨 被引量:3
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作者 赵慧芬 《上海煤气》 2004年第1期27-29,共3页
文章对发生炉煤气的生产工艺进行了分析,探讨了提高发生炉煤气产质量的途径。通过对工艺参数的调整,控制气化反应温度,可以确保发生炉煤气的产量和质量。
关键词 煤气发生炉 操作途径 气化反应温度 焦炭粒度 饱和温度 入炉空气流量 灰层控制
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Self-reaction of initial active groups in coal 被引量:7
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作者 Qi Xuyao Wang Deming +1 位作者 James A Milke Zhong Xiaoxing 《International Journal of Mining Science and Technology》 2012年第2期169-175,共7页
For further understanding of self-heating of coal, we tested the reactions of seven different ranks of coal under inert atmosphere. In the test, 50-gram of coal sample ranged from 0.18 mm to 0.38 mm was put into a spe... For further understanding of self-heating of coal, we tested the reactions of seven different ranks of coal under inert atmosphere. In the test, 50-gram of coal sample ranged from 0.18 mm to 0.38 mm was put into a special designed copper reaction vessel and let pure nitrogen to flow into the coal sample from the bottom at a rate of 100 mL/min. The programmed temperature enclosure was run at a programmed rate of 0.8 ~C/min. The concentration of the carbon oxides and the coal temperature were tested. The results show that the coal reactions under inert atmosphere can generate CO and C02. The reactions under inert atmosphere are affected by coal ranks, initial pore structure of coal and sulfur content. For low ranks of coal, the productions of carbon oxides are piecewise. The coal temperature is lower than the surrounding temperature throughout the reactions under inert atmosphere, but it rises quickly and reaches a crossing point temperature in the later stage under dry-air atmosphere. Based on the analysis, it indicates the self-reaction of initial active groups exists in the self-heating of coal besides the reactions in the two parallel reactions model. Spontaneous combustion of coal is due to both the oxidation heat accumulation and the chain reaction. A new reaction model of self-heating of coal was orooosed. 展开更多
关键词 CoalSelf-heatingInitial active groupsSelf-reactionInert atmosphereCarbon oxides
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SO_2/Hg removal from flue gas by dry FGD 被引量:5
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作者 Wang Fan Wang Hongmei +4 位作者 Zhang Fan Zhu Jinwei Tian Gang Liu Yu Mao Jixian 《International Journal of Mining Science and Technology》 2012年第1期107-110,共4页
To study the mechanism of SO2 and Hg removal from flue gas, an experimental packed bed reactor was designed to simulate the dry FGD, where a mixture of lime and fly ash in ratio 1:3 w/w was used as the S02 and Hg sor... To study the mechanism of SO2 and Hg removal from flue gas, an experimental packed bed reactor was designed to simulate the dry FGD, where a mixture of lime and fly ash in ratio 1:3 w/w was used as the S02 and Hg sorbent, and steam at temperature of 100 ℃ was applied for activation of the sorbent, while the activation time set to 20 rain. The experimental factors including the SO2/Hg sorbent characteristics, 50% breakthrough time for SO2/Hg removal, sorbent packed bed depth and reaction temperature were investigated. The experimental results show that after steam activation, the BET specific surface area and specific pore volume increased from 37.8 to 45.5 m^2/g and from 0.42 to 0.51 cm^3/g, respectively. With activation of the sorbent by steam, the 50% breakthrough times of SO2 and Hg removal increased from 34 to 42 rain and from 23 to 45 rain, respectively. When the packed bed depth was increased from 5 to 25 ram. the 50% breakthrough times for Hg and S02 removal increased from 12 to 52 rain and from 6 to 47 rain, respectively. With the increase of the reaction temperature, the 50% breakthrough of SO2/Hg removal decreased accordingly. Steam activation can efficiently improve SO2/Hg removal simultaneously. 展开更多
关键词 SO2 removal Hg removal Dry FGD Sorbent activation
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