基于亚麻荠秸秆的颗粒与乙醇生产一体化系统的技术经济分析

Cuong N. Dao, Lope G. Tabil, Edmund Mupondwa, Tim Dumonceaux, Xue Li and Ajay K. Dalai
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引用次数: 0

摘要

本研究提出了一种创新的生物炼制概念,将微生物预处理(MBP)、湿储存(WS)和蘑菇培养结合起来,将草本生物质转化为高价值产品,包括生物燃料颗粒、火鸡尾菇和乙醇。这种环保的方法减少了预处理时间,经济地去除木质纤维素结构,并提高了致密颗粒的耐久性和酶消化率。生物炼制模式包括五个颗粒蘑菇生产设施(颗粒工厂A)和一个乙醇工厂(乙醇工厂A),战略位置位于加拿大萨斯喀彻温省萨斯katoon以南约140公里(50°53 ' 16.1 " N, 106°42 ' 15.5 " W),以最大限度地减少颗粒运输距离。颗粒厂A的年产能为25万吨,每吨的单位生产成本(UPC)为201-242美元,主要由真菌液体接种制备的成本驱动。这些成本超过了传统的蒸汽爆炸颗粒厂,如天然气(每吨181美元)和生物质燃烧系统(每吨166美元)。因此,乙醇厂A使用这些颗粒生产乙醇的成本为每升1.32美元,而集中式MBP秸秆包乙醇厂的成本为每升0.89美元,传统稀酸预处理厂的成本为每升0.57美元。这种生物炼制概念的经济可行性要求最低乙醇销售价格(MESP)为每升1.03美元,并且至少有50%的农民参与,才能在没有蘑菇信贷的情况下实现正净现值(NPV)。然而,整合来自火鸡尾菇生产的收入显著提高了财务结果,使颗粒厂A的净现值增加了100亿美元。这可以降低颗粒的销售价格,将MESP降至每升0.77美元,颗粒采购成本为每吨100美元。这些发现证明了这种创新生物炼制模式的经济可行性和可持续性,强调了将微生物预处理技术与多样化收入流相结合的潜力。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Technoeconomic analysis of an integrated camelina straw-based pellet and ethanol production system†

Technoeconomic analysis of an integrated camelina straw-based pellet and ethanol production system†

This study proposes an innovative biorefinery concept, integrating microbial pretreatment (MBP), wet storage (WS), and mushroom cultivation to transform herbaceous biomass into high-value products, including biofuel pellets, Turkey tail mushrooms, and ethanol. This environmentally friendly approach reduces pretreatment times, economically delignifies lignocellulosic structures, and improves the durability and enzymatic digestibility of densified pellets. The biorefinery model includes five pellet-mushroom production facilities (Pellet Plant A) and one ethanol plant (Ethanol Plant A), strategically located approximately 140 km south of Saskatoon (50°53′16.1′′N, 106°42′15.5′′W) in the province of Saskatchewan, Canada, to minimize pellet transport distances. Pellet Plant A, with a capacity of 250 000 t per year, incurs unit production costs (UPC) of US$201–242 per t, primarily driven by the cost of fungal liquid inoculum preparation. These costs exceed those of conventional steam-explosion pellet plants, such as natural gas-fired (US$181 per t) and biomass-fired systems (US$166 per t). Consequently, ethanol produced at Ethanol Plant A, using these pellets, costs US$1.32 per L, compared to US$0.89 per L for centralized MBP straw bales-to-ethanol plants and US$0.57 per L for conventional dilute acid pretreatment plants. The economic viability of this biorefinery concept requires a minimum ethanol selling price (MESP) of US$1.03 per L and at least 50% farmer participation to achieve a positive net present value (NPV) without mushroom credits. However, integrating revenue from Turkey tail mushroom production significantly enhances financial outcomes, increasing Pellet Plant A's NPV by up to US$10 billion. This enables a reduction in pellet selling prices, lowering the MESP to US$0.77 per L with a pellet purchasing cost of US$100 per t. These findings demonstrate the economic feasibility and sustainability of this innovative biorefinery model, emphasizing the potential of combining microbial pretreatment technologies with diversified revenue streams.

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