开发材料驱动的第三阶段木质纤维素原料生物精炼系统

Swapan K Ray, Riyadh H Bhuiyan, Tanvir Muslim and M Q Ehsan*, 
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摘要

生物精炼厂的运营现状面临着一系列技术和经济障碍,其中包括与产品多样化、环境影响和有效废物管理相关的挑战。本研究阐述了一种高度简化且技术经济可行的材料驱动型第三阶段木质纤维素原料生物精炼系统,旨在从多种木质纤维素生物质和预处理化学品(如含氮、钾、磷(NPK)的材料)中依次提取非结构和结构成分。为构建生物精炼系统,对不含萃取物的木质纤维素生物质采用了一种热压顺序磷酸氢氧化钾预处理方法,有效地将大量非木材和硬木样本分馏为其结构成分。在预处理过程中,主要的结构成分,即半纤维素(77%-98%)、纤维素/纤维素(77%-93%)和木质素(75%-85%)被分离出来。此外,还利用氢氧化铵从废液中回收了预处理化学品(约 100%),作为结晶和液体形式的宝贵 NPK 肥料。对生物精炼系统(小型工厂;使用木质纤维素生物质:通过建立一个确定性模型,对生物精炼系统(小型工厂;使用的木质纤维素生物质:7300 吨/年;生产能力:19568 吨/年;预计资本成本:3100 万美元;运营成本:2348 万美元)进行了技术经济分析,结果表明投资回收期为 6.69 年。还利用确定性模型进行了局部敏感性和不确定性分析,并对投资回报率的变化进行了评估。此外,还为生物精炼厂开发了上层建筑,显示了潜在的下游操作。包括 "从摇篮到终点 "生命周期评估在内的总体研究表明,生物精炼厂是一种绿色、可持续的木质纤维素生物质转化技术,其原子经济性超过 95%。
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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Development of a Material-Driven Phase III Lignocellulosic Feedstock Biorefinery System

The present status of operational biorefineries confronts an array of technological and economic hurdles, encompassing challenges related to product diversification, environmental impacts, and efficient waste management. In this study, a highly streamlined and techno-economically viable material-driven phase III lignocellulosic feedstock biorefinery system is delineated, aiming to sequentially extract non-structural and structural components from diverse lignocellulosic biomass and pretreatment chemicals such as nitrogen-, potassium-, and phosphorus- (NPK) containing materials. To construct the biorefinery system, a thermo-pressurized sequential phosphoric acid-potassium hydroxide pretreatment method was employed on extractives-free lignocellulosic biomass, effectively fractionating numerous non-wood and hardwood samples into their structural components. Applying the pretreatment process, the primary structural components, i.e., hemicellulose (77 to 98%), cellulose/pulp (77 to 93%), and lignin (75 to 85%), were separated. The pretreatment chemicals were also recovered (around 100%) as valuable NPK fertilizers in crystalline and liquid forms from the spent liquors by using ammonium hydroxide. A techno-economic analysis was performed on the biorefinery system (small-scale plant; lignocellulosic biomass used: 7300 t/y; production capacity: 19,568 t/y; estimated capital cost: 31.00 million USD; operating cost: 23.48 million USD) by developing a deterministic model that showed a payback period of 6.69 years. Local sensitivity and uncertainty analyses were also performed using the deterministic model, and changes in the return on investment were evaluated. Additionally, a superstructure was developed for the biorefinery, showing potential downstream operations. Overall studies, including cradle-to-gate lifecycle assessment, demonstrated that the biorefinery is a green and sustainable technology for the conversion of lignocellulosic biomass with greater than 95% atom economy.

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