Dhaundiyal Alok, Atsu Divine, Toth Laszlo
Institute of Process Engineering, Szent Istvan University, Godollo, 2100, Hungary.
Department of Energy Systems Engineering, Koforidua Technical University, Koforidua, Ghana.
Biotechnol Biofuels. 2020 Dec 7;13(1):199. doi: 10.1186/s13068-020-01840-7.
Biomass pre-treatment is gaining attention as a standalone process to improve the qualitative aspect of the lignocellulosic material. It has been gaining ground in the power station by replacing the coal with the pre-treated biomass. In this context, this paper enlightens the operating condition of carrying out the torrefaction so that the process can be made relatively more effective. The influence of physico-chemical characteristics on the heat of reaction of pyrolysis reactions, mass loss and temperature regimes are evaluated by thermogravimetry of the pre-treated samples of the pinecone; whereas, the structural transformation in the basic constituents is determined via knowing the fractional change in cellulose, hemicellulose and acid-insoluble lignin contents of the pine cone. The thermogravimetric (TGA) and differential thermal analysis (DTA) were performed to determine the physical as well as the thermal behaviour of the thermally processed biomass. The samples had undergone thermal decomposition at heating rates of 5 °C min, 10 °C min and 15 °C min. Nitrogen gas was used as a purge gas for the pyrolysis of the pre-treated samples. The volumetric rate of 200 ml min was pre-set for the thermal decomposition of the samples at 600 °C; whereas, the selected torrefaction temperature range varied from 210 to 250 °C.
The heat of reaction for the pre-treated samples was found to vary from 1.04 to 1.52 MJ kg; whereas, it was 0.91-1.54 MJ kg for the raw samples. The total annual production cost of processing 3.6 Mg of fuel in a year at a pilot scale was $ 36.72; whereas, the fiscal burden per kilogram of fuel during thermal degradation of the processed fuel was reduced by 0.08-1.5ȼ. The entropy of the system decreased with an increasing ramp rate. The exergetic gain in the system increased by 1-2%. The loss of energy during the energy-intensive processing of the pre-treated fuel was relatively low at a heating rate of 5 °C min.
By the physico-chemical assessment, it was determined that pinecones required the highest torrefaction temperature and time to provide the upgraded pinecones. It was concluded that the duration of the torrefaction should be at least 15 min for a temperature of 250 °C so that the chemical exergy of the system, energy yield and the energy density of the processed material are qualitatively improved. The volatile and ash contents were noticed to decrease during the torrefaction process. The least fractional change in the volatile content was estimated at 210 °C for a torrefaction time of 15 min; whereas, the ash content was minimum at 210 °C for a torrefaction time of 5 min.
生物质预处理作为一种改善木质纤维素材料质量的独立工艺正受到关注。它在发电站中逐渐占据一席之地,通过用预处理后的生物质替代煤炭。在此背景下,本文阐明了进行烘焙的操作条件,以使该过程能相对更有效。通过对松果预处理样品进行热重分析,评估了物理化学特性对热解反应热、质量损失和温度范围的影响;而通过了解松果中纤维素、半纤维素和酸不溶性木质素含量的分数变化,确定了基本成分的结构转变。进行热重分析(TGA)和差示热分析(DTA)以确定热加工生物质的物理和热行为。样品在5℃/分钟、10℃/分钟和15℃/分钟的加热速率下进行热分解。氮气用作预处理样品热解的吹扫气体。在600℃下对样品进行热分解时,预设的体积速率为200毫升/分钟;而选定的烘焙温度范围为210至250℃。
发现预处理样品的反应热在1.04至1.52兆焦/千克之间变化;而原始样品的反应热为0.91 - 1.54兆焦/千克。在中试规模下,每年处理3.6吨燃料的总生产成本为36.72美元;而在加工燃料热降解过程中,每千克燃料的财政负担降低了0.08 - 1.5美分。系统的熵随升温速率增加而降低。系统的有效能增益增加了1 - 2%。在5℃/分钟的加热速率下,预处理燃料在能量密集型加工过程中的能量损失相对较低。
通过物理化学评估确定,松果需要最高的烘焙温度和时间才能提供升级后的松果。得出的结论是,在250℃的温度下,烘焙持续时间应至少为15分钟,以便定性地提高系统的化学有效能、能量产率和加工材料的能量密度。在烘焙过程中,挥发性成分和灰分含量会降低。在210℃下烘焙15分钟时,挥发性成分的分数变化最小;而在210℃下烘焙5分钟时,灰分含量最低。