Design and Development of a Novel Hybrid Gasifier for High Ash Content Coal as feed stock

Priyank Dave, Dr. J. K. Parikh, S. A. Channiwala
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Abstract

India has large proven reserve of coal but most of the coal has large quantity of ash. Utilization of this high ash content coal is again a verychallenging task. Presently, gasification of high ash coals has not yet been in application due to the difficulties arising from the ash handlingprocesses. In this work an attempt was made to design a partially fluidized bed reactor that can handle 30 kg/hr coal as a feedstock. By usingan appropriate design procedure a complete design of a hybrid gasifier was studied deeply. The major aim of present research is todetermine the air flow rate for proper gasification, reactor diameter and reactor height, feed particle diameter, nozzle orientation and numbernozzles, reduction zone diameter and height. Experiments were carried out with feeding rate of 9.8 kg/hr with high ash content coal having39.83% ash. Satisfactory results have been found during experiments. The average producer gas generation during trial run was found to be29.8 Nm3/hr while average calorific value of producer gas was about 4500 kJ/Nm3. The work described here favours us understand the realgasification process for high ash content coal and thus facilitates the industrial application of gasification technology.
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新型高灰分煤混合气化炉的设计与研制
印度拥有大量已探明的煤炭储量,但大多数煤炭含有大量灰分。利用这种高灰分煤也是一项非常具有挑战性的任务。目前,高灰分煤的气化由于灰分处理过程的困难尚未得到应用。在这项工作中,试图设计一个部分流化床反应器,可以处理30公斤/小时的煤作为原料。采用适当的设计方法,对混合式气化炉的整体设计进行了深入的研究。本研究的主要目的是确定适宜气化的空气流量、反应器直径和反应器高度、进料颗粒直径、喷嘴方向和喷嘴数量、还原区直径和高度。试验采用高灰分煤(灰分39.83%),加料速度为9.8 kg/hr。实验结果令人满意。试运行产气平均产气量为29.8 Nm3/hr,产气平均热值约为4500 kJ/Nm3。本文所述的工作有助于我们了解高灰分煤的再气化过程,从而促进气化技术的工业应用。
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