共查询到19条相似文献,搜索用时 140 毫秒
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在一维热态煤粉炉上进行了粉煤灰干法、尾部增湿以及灰浆湿法烟气脱硫试验.结果表明,利用高钙粉煤灰组织炉内或尾部烟气的脱硫都能取得一定的效果.研究发现:干法脱硫效果是粉煤灰对SO2的物理吸附和化学反应吸收两个过程共同作用的结果;在增湿和湿法脱硫中,自由水分的存在是提高脱硫率的关键因素,而湿法中钙硫比对脱硫的影响占据主导地位.试验结果表明:干法脱硫效果最差;增湿脱硫效果明显提升,灰浆脱硫效果最优,当钙硫比为0.864~1.86时,脱硫率为53%~78%,达到了中等脱硫效果,具有工程应用前景. 相似文献
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高钙煤灰颗粒与液滴碰撞增湿脱硫过程的模型研究 总被引:2,自引:0,他引:2
为模拟增湿活化反应器内高钙煤灰颗粒的增湿脱硫过程,采用随机轨道模型分别跟踪颗粒群与液滴群,以相邻单元间26条颗粒流通道模型统计未增湿条件下的初始颗粒流量,以液滴群的空间单元捕捉效率为单元体内颗粒流量守恒方程的源项(汇)系数,来迭代各单元通道上的未增湿颗粒流量,耦合煤灰颗粒与液滴群的碰撞过程。并进一步考虑反应器内气、液、固多相湍流物理化学反应过程,建立了三维场内高钙煤灰低温增湿脱硫总体模型,初步预测了高钙煤灰增湿脱硫过程,模型预测与试验结果具有很好的吻合特性。图10参9。 相似文献
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干式烟气脱硫技术进展及其应用前景分析 总被引:2,自引:0,他引:2
对国内外有广泛应用前景的几种干式烟气脱硫技术进行了介绍,分析了这些脱硫技术的特点,并针对上海地区电厂燃用高钙低硫煤的实际情况,提出了采用高钙粉煤灰增湿活化脱硫的简易脱硫方法。 相似文献
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Longfei Tang Huidong Fan Jifeng Guo Weichen Zeng 《Energy Sources, Part A: Recovery, Utilization, and Environmental Effects》2018,40(8):999-1009
This investigation reports the exploration of the mechanism for coal desulfurization utilizing ultrasonic (US) with peroxyacetic acid. Changes in surface and pore diameter for coal samples were determined before and after US treatment. To study its chemical effect, production regularities of hydroxyl radical under US field was analyzed by the iodine release method. Experimental results showed that the specific surface area, total pore volume and average pore size of treated samples were improved compared to untreated coal. In addition, the production rule of hydroxyl radical was consistent with that of desulfurization rate. XPS analysis results indicated that the removals of pyrite, mercaptan, and sulfur ether from coal were more than 60%, while thiophene, sulfoxide and sulfone were difficult to remove from coal. The further oxidation of sulfur-containing groups in coal was obtained due to the physical and chemical effects of the ultrasonic. These findings confirmed that the synergistic action of physical and chemical effects of the US played an important role in this desulfurization process, which could serve as a reference for further optimizing the coal desulfurization process. 相似文献
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J. Mi J. Ren J.-C. Wang W.-R. Bao K.-C. Xie 《Energy Sources, Part A: Recovery, Utilization, and Environmental Effects》2013,35(14):1261-1268
Abstract The extractive desulfurization of four high sulfur coals from China were promoted with ultrasonic and microwave in tetrachloroethylene organic solvents. It was shown that the joint promotion with ultrasonic and microwave had an active effect on extractive desulfurization. The rate of desulfurization increased with the increase of time in ultrasonic field as well as with the power of ultrasonic, but declined with the increase of the particle size of coal. The rate of desulfurization was not identical for different coal, which was perhaps related to the existed forms of organic sulfur in coal. 相似文献
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A. Demirbas 《Energy Sources, Part A: Recovery, Utilization, and Environmental Effects》2013,35(2):161-167
Abstract This study is an attempt to desulfurize organic sulfur from coal samples with ferric hexacyanoferrate (II), Fe4 [Fe(CN)6], as the desulfurization agent. Effect of temperature, particle size and concentration of ferrocyanide ion on desulfurization from the coal samples has been investigated. The temperature and stirring time are the most important parameters for the level of desulfurization of organic sulfur. Removal of organic sulfur content increased continuously with increasing temperature from 298 to 368 K. The organic sulfur removal rate sharply increases from 10 min to 30 min stirring time. After 30 min, it reaches a value of plateau. Particle size between ?100 mesh and ?200 mesh slightly affects the amount of organic sulfur removal. Gradual increase in the concentration of ferric hexacyanoferrate (II) raised the magnitude of desulfurization, but at higher concentration, the variation is not significant. 相似文献
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《Energy》2001,26(8):759-774
In order to promote the desulfurization efficiency of calcium-based sorbents during coal combustion in traveling grate boilers, the influences on sulfur removal of the thermal conditions and the sorbents were discussed in this paper. It was found that the SO2 concentration first rises, then declines along the traveling grate and reaches the peak near the midpoint of the grate. The fluctuation of the SO2 concentration over time in the flue gas is mainly affected by the flame temperature. When the particle size of the sorbents decreases from 75 to 0.1 μm, the sulfur removal efficiency will increase slightly. A reasonable Ca/S molar ratio is about 2 when sorbents are blended with the coal on the grate and its further increase has little benefit to desulfurization. A new, so-called two-stage desulfurization process — sulfur capture firstly in the coal bed and secondly in the combustion gas — is suggested as it can greatly promote the sulfur removal efficiency up to 70∼80%. By X-ray powder diffraction analysis, some thermal stable phases were identified in the sulfur retention cinder obtained from the on-grate process. 相似文献
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M. Gürü B. V. Sariöz Ç. Çakanyildirim 《Energy Sources, Part A: Recovery, Utilization, and Environmental Effects》2013,35(11):981-987
Abstract It is becoming popular to use fossil fuels efficiently since the necessary energy is mostly supplied from fossil fuels. Altough there are high lignite reservoirs, high sulfur content limits the efficient use of them. In this article, we aimed to convert combustible sulfur in coal to non-combustible sulfate form in the ash by oxidizing it with a hydrogen peroxide solution. The parameters affecting the sulfur conversion were determined to be: hydrogen peroxide concentration, reaction time, mean particle size at constant room temperature and shaking rate. The maximum desulfurization efficiency reached was 74% of the original combustible sulfur with 15% (w/w) hydrogen peroxide solution, 12 hours of reaction time, and 0.25 mm mean particle size. 相似文献