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CO_2 gasification rate analysis of coal char in entrained low coal gasifier

机译:夹带低煤气化炉中煤焦的CO_2气化率分析

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Coal chars of four coal types were gasified with carbon dioxide using a PDTF or TGA at high temperature and pressure. Test conditions of temperature and partial pressure of the gasifying agent were determined to simulate the conditions in air-blown or oxygen-blown entrained flow coal gasifiers. Coal chars were produced by rapid pyrolysis of pulverized bituminous coals using a DTF with a nitrogen gas flow at 1670 K. In gasification tests with the PDTF, gasification temperatures were 1670 K or below and partial pressures of carbon dioxide were 0.7 MPa or below. Carbon monoxide of 0.6 MPa or below was supplied for the gasification tests with the TGA. As a result, coal types showed a large difference in the char gasification rate with carbon dioxide, and this difference remained large without decreasing even in the high-temperature area when the gasification rate was controlled by pore diffusion the same as in entrained flow gasifiers. Inhibition of the gasification reaction by carbon monoxide was also observed. Reaction rate equations of both the nth order and Langmuir-Hinshelwood type were applied to the char gasification reaction with the random pore model and the effectiveness factor, and the applicability of these rate equations to air-blown and oxygen-blown entrained flow gasifiers evaluated. Gasification rate equations and kinetic parameters applicable to a pore diffusion zone at high temperature were obtained for each coal.
机译:使用PDTF或TGA在高温和高压下用二氧化碳将四种煤的煤焦气化。确定了气化剂的温度和分压的测试条件,以模拟气吹或吹氧气流床气化炉中的条件。通过使用DTF在1670 K的氮气流下快速热解粉煤煤来生产煤焦。在使用PDTF进行的气化测试中,气化温度为1670 K或更低,二氧化碳的分压为0.7 MPa或更低。用TGA供给0.6 MPa或以下的一氧化碳进行气化测试。结果,与夹带流化气化炉一样,通过细孔扩散控制气化率时,煤的种类与二氧化碳的焦化气化率差异较大,即使在高温区域,该差异也保持较大而没有减小。还观察到一氧化碳对气化反应的抑制。将n阶反应式和Langmuir-Hinshelwood型反应速率方程应用于具有随机孔模型和有效因子的焦炭气化反应中,并评价了这些速率方程在吹气和吹氧气流床气化炉中的适用性。对于每种煤,获得了适用于高温下的孔扩散区的气化速率方程和动力学参数。

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