Industrial single-screw and twin-screw prototype reactor pyrolysis for bio-oil and charcoal production from biomass: A case study of cogon grass (Imperata cylindrica)

IF 6 Q1 ENGINEERING, MULTIDISCIPLINARY
Kittiphop Promdee , Tharapong Vitidsant
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引用次数: 0

Abstract

Biomass conversion by pyrolysis process is important in renewable energy because the current global situation changes the use of energy in various forms according to the demand. The pyrolysis process is different in terms of temperature, pressure, reactor type and biomass control before entering the reactor. This research compares the efficiency of single-screw pyrolysis reactor and twin-screw pyrolysis reactor in producing bio-oil from cogon grass (Imperata cylindrica) for industrial development by analyzing the oil content and chemical and physical properties of bio-oil from pyrolysis process at temperature between 400 °C and 500 °C. The analysis of biomass, bio-oil and charcoal properties was performed using physicochemical methods and GC–MS. The results showed that the liquid phase from the pyrolysis process using a twin-screw at 500 °C had the highest value of 58.75 % and 37.39 % bio-oil. In comparison, the bio-oil yield from single-screw at 500 °C was 55.23 % liquid phase and 33.76 % bio-oil. GC–MS analysis revealed that the majority of hydrocarbon compounds were phenol, benzene, 1-ethyl-3‑methoxy, and pyridine 2-methyl. The bio-oil from the twin-screw reactor contained more benzene, 1-ethyl-3‑methoxy, and pyridine 2-methyl than the bio-oil from the single-screw reactor. The carbon content of the bio-oil from the twin-screw reactor (53.23 wt%) was higher than that of the bio-oil from the single-screw (38.23 wt%). The bio-oil from the twin-screw reactor had a higher heating value than the bio-oil from the single-screw reactor at all temperatures. The viscosity of bio-oil from the single-screw reactor had a low point (0.353 Pascal/min) at 25 °C, which was equal to that of bio-oil from the twin-screw reactor (0.354 Pascal/min). Single-screw reactors and twin-screw reactors are efficient in producing bio-oil, especially twin screw reactors. The results of this research are pilot projects to establish industrial pyrolysis reactors focusing on biomass conversion to energy fuels for further sustainable domestic energy development.
通过热解工艺进行生物质转化在可再生能源领域非常重要,因为当前的全球形势改变了根据需求以各种形式使用能源的方式。热解工艺在温度、压力、反应器类型和进入反应器前的生物质控制方面各不相同。本研究比较了单螺杆热解反应器和双螺杆热解反应器在利用白茅(Imperata cylindrica)生产生物油以促进工业发展方面的效率,分析了在 400 °C 至 500 °C 温度下热解过程产生的生物油的含油量、化学和物理特性。采用物理化学方法和气相色谱-质谱法对生物质、生物油和木炭的特性进行了分析。结果表明,在 500 °C 温度下使用双螺杆进行热解过程产生的液相生物质含量最高,为 58.75%,生物油含量为 37.39%。相比之下,在 500 °C 下使用单螺杆产生的生物油产量为 55.23 % 的液相和 33.76 % 的生物油。气相色谱-质谱分析表明,大部分碳氢化合物是苯酚、苯、1-乙基-3-甲氧基和 2-甲基吡啶。双螺杆反应器产生的生物油中苯、1-乙基-3-甲氧基和 2-甲基吡啶的含量高于单螺杆反应器产生的生物油。双螺杆反应器产生的生物油的碳含量(53.23 wt%)高于单螺杆反应器产生的生物油(38.23 wt%)。在所有温度下,双螺杆反应器产生的生物油的热值都高于单螺杆反应器产生的生物油。单螺杆反应器产生的生物油在 25 °C 时的粘度较低(0.353 帕斯卡/分钟),与双螺杆反应器产生的生物油的粘度(0.354 帕斯卡/分钟)相当。单螺杆反应器和双螺杆反应器都能高效生产生物油,尤其是双螺杆反应器。这项研究成果是建立工业热解反应器的试点项目,重点是将生物质转化为能源燃料,以进一步促进国内能源的可持续发展。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
Results in Engineering
Results in Engineering Engineering-Engineering (all)
CiteScore
5.80
自引率
34.00%
发文量
441
审稿时长
47 days
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