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Decomposition of tar in gas from updraft gasifier by thermal cracking

机译:热裂解分解上吸式气化炉中的焦油

摘要

Continuing earlier work with tar reduction by partial oxidation of pyrolysis gas [1] thermal cracking has been evaluated as a gas cleaning process. The work has been focusing on cleaning gas from updraft gasifiers, and the long term purpose is to develop a tar cleaning unit based on thermal cracking. An experimental set-up has been built, in which a flow of contaminated gas can be heated up to 1290°C in a reactor made of pure Al2O3. Four measurements were made. Three with gas from a pyrolysis unit simulating updraft gasifier, and one with gas from an updraft gasifier. Cracking temperatures was 1200, 1250 and 1290°C, and the residence time at this temperature was 0.5 second. The measurements show that at the selected residence time of 0.5 second, the gas flow in a thermal tar cracking unit has to be heated to at least 1250°C to achieve sufficient tar cleaning. At 1290°C, a tar content as low as 15 mg/Nm3 was obtained on gas from an updraft gasifier. The lower heating value of the cleaned gas was 6.0 MJ/Nm3, and the energy content of the non condensable gasses was 19% higher than before cracking.
机译:通过热解气的部分氧化[1]进行的热裂化来继续进行焦油还原的早期工作已被评估为一种气体净化工艺。这项工作一直专注于上升气流式气化炉的清洁气体,长期目标是开发基于热裂化的焦油清洁装置。已经建立了一个实验装置,其中可以在由纯Al2O3制成的反应器中将被污染的气流加热到1290°C。进行了四次测量。三种气体来自模拟上流式气化炉的热解装置,另一种气体来自上流式气化炉的气体。裂化温度为1200、1250和1290℃,在该温度下的停留时间为0.5秒。测量结果表明,在选定的0.5秒停留时间下,热焦油裂化装置中的气流必须加热到至少1250°C,才能充分清洁焦油。在1290℃下,从上升气流式气化炉中获得的焦油含量低至15 mg / Nm3。净化气体的较低热值是6.0 MJ / Nm3,不可冷凝气体的能量含量比裂解前高19%。

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