Anaerobic digestion as a core process for sustainable energy production in the soybean biorefinery: A techno‐economic assessment

Ana Paula Paulinetti , Isabela Mehi Gaspari Augusto , Lia Paula Poloni Batista , Arthur Gregorio Barbosa Tavares , Roberta Albanez , Suzana Maria Ratusznei , Giovanna Lovato , José Alberto Domingues Rodrigues
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引用次数: 14

Abstract

With the ever-growing environmental concern about natural resources depletion and the search for alternative energy sources, anaerobic digestion technology emerges as a core process in biorefineries. One of the limiting factors for full-scale use of this process is the scarcity of studies that technically and economically evaluate more flexible and unconventional technologies, such as Anaerobic Sequencing Batch Biofilm Reactors (AnSBBR) with immobilized biomass. Therefore, this paper carried out a techno-economic evaluation regarding the implementation of AnSBBR reactors, on an industrial scale, in the treatment of soybean molasses and glycerin. The assessment was based on the best published results presented by this type of reactor on a laboratory scale. The scale-up estimate resulted in a configuration of 8 AnSBBR reactors with 1000 m³ each in the treatment of 59 tons-molasses⋅day−1. The energy produced by this system could reach 18.6 GWh⋅year−1 and would have an initial investment of USD 7.6 million with an annual return of USD 2.2 million. On treating 17 tons-glycerin⋅day−1, the estimate resulted in a configuration of 6 AnSBBR reactors with 900 m³ each. The energy produced could reach 6.3 GWh⋅year−1 and would have an initial investment of USD 5.8 million with an annual return of USD 1 million.

Abstract Image

厌氧消化作为大豆生物炼制中可持续能源生产的核心过程:技术经济评估
随着人们对自然资源枯竭的日益关注和对替代能源的探索,厌氧消化技术成为生物炼制的核心工艺。限制该工艺全面应用的因素之一是缺乏技术和经济上评估更灵活和非常规技术的研究,例如固定化生物质厌氧顺序间歇生物膜反应器(AnSBBR)。因此,本文对在工业规模上实施AnSBBR反应器处理大豆糖蜜和甘油进行了技术经济评价。该评估是基于该类型反应器在实验室规模上发表的最佳结果。放大后的估计结果是配置8个AnSBBR反应器,每个反应器1000 m³,处理59吨糖蜜。该系统的发电量可达18.6 GWh·年−1,初始投资760万美元,年回报220万美元。在处理17吨甘油的情况下,估计结果是6个每个900 m³的AnSBBR反应器的配置。发电量可达6.3 GWh·年−1,初始投资580万美元,年回报100万美元。
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CiteScore
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