{"title":"基于模型确定不同固体废物气化的最佳操作参数","authors":"Szabina Tomasek , Ágnes Bárkányi , Attila Egedy , Norbert Miskolczi","doi":"10.1016/j.ceja.2024.100586","DOIUrl":null,"url":null,"abstract":"<div><p>In this study a 2D visualization technique is presented that is suitable for determining the optimal operational parameters of solid waste gasification depending on the intended use of the product. Steam gasification of different wastes (wheat straw, wood, municipal solid waste (MSW), polyethylene (PE), green waste) was modelled in Aspen Plus simulation software, validated with literature data and a MATLAB – Aspen Plus inter software connection was also created to minimize the possibility of errors when the raw material composition and other parameters are changed. Correlation was found between the simulation and literature data; therefore, the model was also suitable for evaluating the effects of process parameters (<em>T</em> = 650–1100 °C, steam rate = 0–1.5 kg/h) on gas composition, lower heating value and H<sub>2</sub>/CO ratio. The model was also extended to a wide range of domestic waste types, making it possible to determine the optimal process parameters without performing a high number of time- and energy-intensive gasification experiments. Regarding the process parameters it was established that the temperature has a significant effect on the gasification reactions and shifts the chemical reactions towards hydrogen and carbon monoxide formation, but above 800 °C it has a limited effect on the gas composition, lower heating value and H<sub>2</sub>/CO ratio. The increasing steam rate also facilitated the hydrogen and carbon monoxide formation, but above a certain ratio its effect was opposite due to the water-gas shift reaction and the shorter residence times. The obtained gases can be used for energy purposes or as raw material for Low-Temperature Fischer-Tropsch synthesis, or production of aldehyde, higher alcohol, acetic acid or even polycarbonate for which the optimal temperatures and steam rates were also determined.</p></div>","PeriodicalId":9749,"journal":{"name":"Chemical Engineering Journal Advances","volume":null,"pages":null},"PeriodicalIF":5.5000,"publicationDate":"2024-01-18","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://www.sciencedirect.com/science/article/pii/S2666821124000048/pdfft?md5=86f3f9aacb0ade850c07eb59a8f4f6cc&pid=1-s2.0-S2666821124000048-main.pdf","citationCount":"0","resultStr":"{\"title\":\"Model-based determination of optimal operating parameters for different solid waste gasification\",\"authors\":\"Szabina Tomasek , Ágnes Bárkányi , Attila Egedy , Norbert Miskolczi\",\"doi\":\"10.1016/j.ceja.2024.100586\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><p>In this study a 2D visualization technique is presented that is suitable for determining the optimal operational parameters of solid waste gasification depending on the intended use of the product. Steam gasification of different wastes (wheat straw, wood, municipal solid waste (MSW), polyethylene (PE), green waste) was modelled in Aspen Plus simulation software, validated with literature data and a MATLAB – Aspen Plus inter software connection was also created to minimize the possibility of errors when the raw material composition and other parameters are changed. Correlation was found between the simulation and literature data; therefore, the model was also suitable for evaluating the effects of process parameters (<em>T</em> = 650–1100 °C, steam rate = 0–1.5 kg/h) on gas composition, lower heating value and H<sub>2</sub>/CO ratio. The model was also extended to a wide range of domestic waste types, making it possible to determine the optimal process parameters without performing a high number of time- and energy-intensive gasification experiments. Regarding the process parameters it was established that the temperature has a significant effect on the gasification reactions and shifts the chemical reactions towards hydrogen and carbon monoxide formation, but above 800 °C it has a limited effect on the gas composition, lower heating value and H<sub>2</sub>/CO ratio. The increasing steam rate also facilitated the hydrogen and carbon monoxide formation, but above a certain ratio its effect was opposite due to the water-gas shift reaction and the shorter residence times. 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引用次数: 0
摘要
本研究提出了一种二维可视化技术,适用于根据产品的预期用途确定固体废物气化的最佳操作参数。在 Aspen Plus 仿真软件中对不同废物(小麦秸秆、木材、城市固体废物 (MSW)、聚乙烯 (PE)、绿色废物)的蒸汽气化进行了建模,并与文献数据进行了验证,还创建了 MATLAB - Aspen Plus 软件间的连接,以最大限度地减少原料成分和其他参数发生变化时出现错误的可能性。模拟结果与文献数据之间存在相关性;因此,该模型也适用于评估工艺参数(T = 650-1100 °C,蒸汽速率 = 0-1.5 kg/h)对气体成分、低热值和 H2/CO 比率的影响。该模型还可扩展到多种生活垃圾类型,从而无需进行大量耗时耗能的气化实验就能确定最佳工艺参数。关于工艺参数,已确定温度对气化反应有显著影响,并使化学反应转向氢气和一氧化碳的形成,但在 800 °C 以上,温度对气体成分、较低的热值和 H2/CO 比率的影响有限。蒸汽速率的增加也促进了氢气和一氧化碳的形成,但超过一定比例时,由于水气转移反应和停留时间的缩短,其影响则相反。获得的气体可用于能源目的,或作为低温费托合成的原料,或生产醛、高级醇、醋酸甚至聚碳酸酯,其最佳温度和蒸汽速率也已确定。
Model-based determination of optimal operating parameters for different solid waste gasification
In this study a 2D visualization technique is presented that is suitable for determining the optimal operational parameters of solid waste gasification depending on the intended use of the product. Steam gasification of different wastes (wheat straw, wood, municipal solid waste (MSW), polyethylene (PE), green waste) was modelled in Aspen Plus simulation software, validated with literature data and a MATLAB – Aspen Plus inter software connection was also created to minimize the possibility of errors when the raw material composition and other parameters are changed. Correlation was found between the simulation and literature data; therefore, the model was also suitable for evaluating the effects of process parameters (T = 650–1100 °C, steam rate = 0–1.5 kg/h) on gas composition, lower heating value and H2/CO ratio. The model was also extended to a wide range of domestic waste types, making it possible to determine the optimal process parameters without performing a high number of time- and energy-intensive gasification experiments. Regarding the process parameters it was established that the temperature has a significant effect on the gasification reactions and shifts the chemical reactions towards hydrogen and carbon monoxide formation, but above 800 °C it has a limited effect on the gas composition, lower heating value and H2/CO ratio. The increasing steam rate also facilitated the hydrogen and carbon monoxide formation, but above a certain ratio its effect was opposite due to the water-gas shift reaction and the shorter residence times. The obtained gases can be used for energy purposes or as raw material for Low-Temperature Fischer-Tropsch synthesis, or production of aldehyde, higher alcohol, acetic acid or even polycarbonate for which the optimal temperatures and steam rates were also determined.