中试蓄热式甲苯分解热氧化剂高效蓄热放热条件研究

S. Iijima, K. Nakayama, M. Kubota, H. Matsuda
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引用次数: 1

摘要

本文以典型挥发性有机化合物(VOC)为例,在原料气质量流量1090 ~ 2550 kg·h−1、甲苯分解温度973 ~ 1173 K、蜂窝高度为0 . 3的条件下,研究了中试蓄热式热氧化剂(RTO)在挥发性有机化合物(VOC)热分解过程中的换热效率。1胜9负。5米,阀门开关间隔60-180秒。结果发现,以LPG燃料消耗和分解的甲苯计算的热效率最大值为0。95,原料气体质量流量1810 kg·h−1,蜂窝高度1。5米。此外,蜂窝高度从1。5到0。9 m导致原料气预热不足,导致原料气中甲苯的浓度从340 ppm增加到530 ppm,以实现甲苯的自燃,而无需LPG燃料的额外加热。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Study on High-efficiency Heat Storage and Heat Release Conditions in a Pilot-scale Regenerative Thermal Oxidizer for Toluene Decomposition
In the present work, the heat exchanging efficiency of a pilot-scale regenerative thermal oxidizer (RTO) during the thermal decomposition of volatile organic compounds (VOC) was studied using toluene as an example of a typical VOC under the following experimental conditions : raw gas mass flow rates of 1090-2550 kg・h − 1 , toluene decomposition temperatures of 973-1173 K, honeycomb heights of 0 . 9-1 . 5 m and valve switching intervals of 60-180 s . As a result, it was found that the thermal efficiency calculated from LPG fuel consumption and the decomposed toluene, gave a maximum value of 0 . 95 at a raw gas mass flow rate of 1810 kg・h − 1 in a honeycomb height of 1 . 5 m. Furthermore, it was found that a decrease in honeycomb height from 1 . 5 to 0 . 9 m caused insufficient preheating of the raw gas, which resulted in an increase in the concentration of toluene necessary in the raw gas from 340 to 530 ppm to achieve self-combustion of the toluene without additional heating by LPG fuel.
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