Department of Civil and Environmental Engineering , University of Illinois at Urbana-Champaign . Newmark Civil Engineering Laboratory, 205 N. Mathews Ave. , Urbana , Illinois 61801 , United States.
Department of Civil and Environmental Engineering , Colorado School of Mines . 1500 Illinois St. , Golden , Colorado 80401 , United States.
Environ Sci Technol. 2018 Nov 20;52(22):13591-13599. doi: 10.1021/acs.est.8b03663. Epub 2018 Nov 5.
Modeling efforts to understand the financial implications of microalgal biofuels often assume a static basis for microalgae biomass composition and cost, which has constrained cultivation and downstream conversion process design and limited in-depth understanding of their interdependencies. For this work, a dynamic biological cultivation model was integrated with thermo-chemical/biological unit process models for downstream biorefineries to increase modeling fidelity, to provide mechanistic links among unit operations, and to quantify minimum product selling prices of biofuels via techno-economic analysis. Variability in design, cultivation, and conversion parameters were characterized through Monte Carlo simulation, and sensitivity analyses were conducted to identify key cost and fuel yield drivers. Cultivating biomass to achieve the minimum biomass selling price or to achieve maximum lipid content were shown to lead to suboptimal fuel production costs. Depending on biomass composition, both hydrothermal liquefaction and a biochemical fractionation process (combined algal processing) were shown to have advantageous minimum product selling prices, which supports continued investment in multiple conversion pathways. Ultimately, this work demonstrates a clear need to leverage integrated modeling platforms to advance microalgae biofuel systems as a whole, and specific recommendations are made for the prioritization of research and development pathways to achieve economical biofuel production from microalgae.
为了理解微藻生物燃料的经济影响,建模工作通常假设微藻生物质组成和成本的静态基础,这限制了培养和下游转化过程的设计,并限制了对它们相互依赖性的深入了解。在这项工作中,动态生物培养模型与下游生物精炼厂的热化学/生物单元过程模型集成,以提高建模精度,提供单元操作之间的机理联系,并通过技术经济分析量化生物燃料的最低产品销售价格。通过蒙特卡罗模拟对设计、培养和转化参数的变异性进行了表征,并进行了敏感性分析以确定关键成本和燃料产率驱动因素。为了实现最低生物质销售价格或实现最大脂质含量而培养生物质,被证明会导致次优的燃料生产成本。根据生物质的组成,水热液化和生化分级过程(联合藻类处理)都显示出具有有利的最低产品销售价格,这支持对多种转化途径的持续投资。最终,这项工作表明,迫切需要利用集成建模平台来推进微藻生物燃料系统的整体发展,并为实现从微藻生产经济生物燃料的研发途径的优先级提出了具体建议。