曝气率对湿式垃圾燃料生物干燥过程中提高热值和降低含水量的影响

Abhisit Bhatsada, K. Wangyao, S. Patumsawad
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引用次数: 1

摘要

on - nuh废物转运站的机械生物处理(MBT)用于处理曼谷和大都市区产生的废物。它可以分离有机废物、回收材料和固体废物。这种固体废物可以考虑转化为固体回收燃料,因为它包含50%以上的塑料和20%的生物质。然而,由于其较高的含水量和较低的热值,这种材料被称为湿垃圾衍生燃料(wet- rdf)。此外,生物干燥工艺已被用于通过激活微生物的活性来去除水。这个过程促进了热量的产生和蒸汽的释放。然而,曝气供应是确定最佳生物干燥操作的必要条件。因此,本研究考察了曝气率对湿式rdf生物干燥过程的影响。本研究是在宽0.5 m,高1.5 m的0.375 m3方形钢溶渗仪上进行的。连续负通气的通气速率分别为0.3、0.5和0.6 m3/kg/天。实验操作时间设为5天。原料初始含水率为44.91%,低热值为3207 kcal/kg。测得的日温度为该过程中的自热值,范围为20-63℃,其峰值出现在第2-4天。作为生物活性产生的平均内部和废气在第3天达到峰值,二氧化碳浓度为4%,氧气浓度为14-16%。最终组成可降解材料和不可降解材料都减少了2%。最佳曝气速率为0.6 m3/kg/d,减水率高,有机物损失小。因此,其最佳生物干燥指数为0.171,在提高减水量的同时,保持了有机还原的碳源。为最终产品提供4901 kcal/kg的低热值和36.6%的含水率。根据RDF-3标准对当地水泥生产的要求,只有在低热值条件下才接受最佳曝气率。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Effect of Aeration rate on Wet- refuse-derived fuel Biodrying process for increasing Heating value and Water content reduction
Mechanical Biological Treatment (MBT) at On-Nuch waste transfer station is used for waste treatment generated from Bangkok and Metropolitan Area. It can separate organic waste, recycle material, and solid waste. This solid waste can be considered for converting into solid recovered fuel because it comprises more than 50% plastic and 20% biomass. However, due to its higher water content and lower heating value, this material was called wet- refuse-derived fuel (Wet-RDF). Besides, the biodrying process has been used for water removal by activating microorganism's activity. This process encourages heat production and vapor release. However, aerated supply is necessary to determine the optimal biodrying operation. Therefore, this study investigated the aeration rate effect on the Wet-RDF biodrying process. This study was performed on the 0.375 m3 square-steel lysimeters with 0.5 m wide and 1.5 m high. The continuous negative ventilation has varied the rates to 0.3, 0.5, and 0.6 m3/kg/day. The operation time was set to 5 days for the experiment. Feedstock's initial moisture content and low heating value were 44.91% and 3,207 kcal/kg, respectively. The measured daily temperature represents the self-heating value in the process for the range of 20–63 °C, and its peak was found during days 2–4. The average inner and exhaust gases as bioactivity produced peaked on day 3 at 4% carbon dioxide and 14-16% oxygen concentrations. The final composition decreased both degradable material and non-degradable material by 2%. The optimum aeration rate was o.6 m3/kg/day because of higher water content reduction and lower organic loss. In this regard, it provides the optimum biodrying index of 0.171, which raises water reduction while remaining the carbon source in terms of organic reduction. Also, 4,901 kcal/kg of low heating value and 36.6% moisture content were provided for the final product. According to the RDF-3 criteria requirement for local cement production, the optimum aeration rate was accepted only in terms of low heating value.
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