Pereira Joana P C, Lopez-Gomez Gustavo, Reyes Noelia G, van der Wielen Luuk A M, Straathof Adrie J J
Department of Biotechnology, Delft University of Technology, Delft, The Netherlands.
Biotechnol J. 2017 Jul;12(7). doi: 10.1002/biot.201600657. Epub 2017 Mar 29.
The conceptual design of a bio-based process for 2-butanol production is presented for the first time. Considering a hypothetical efficient producing strain, a vacuum fermentation is proposed to alleviate product toxicity, but the main challenge is the energy-efficient product recovery from the vapor. Three downstream scenarios were examined for this purpose: 1) multi-stage vapor recompression; 2) temperature swing adsorption; and 3) vapor absorption. The processes were simulated using Aspen Plus, considering a production capacity of 101 kton/yr. Process optimization was performed targeting the minimum selling price of 2-butanol. The feasibility of the different configurations was analyzed based on the global energy requirements and capital expenditure. The use of integrated adsorption and absorption minimized the energy duty required for azeotrope purification, which represents 11% of the total operational expenditure in Scenario 1. The minimum selling price of 2-butanol as commodity chemical was estimated as 1.05 $/kg, 1.21 $/kg, and 1.03 $/kg regarding the fermentation integrated with downstream scenarios 1), 2), and 3), respectively. Significant savings in 2-butanol production could be achieved in the suggested integrated configurations if more efficient microbial strains were engineered, and more selective adsorption and absorption materials were found for product recovery.
首次提出了一种基于生物的2-丁醇生产工艺的概念设计。考虑到一种假设的高效生产菌株,提出了真空发酵以减轻产物毒性,但主要挑战是从蒸汽中高效回收产物。为此研究了三种下游方案:1)多级蒸汽再压缩;2)变温吸附;3)蒸汽吸收。使用Aspen Plus对这些工艺进行了模拟,考虑的生产能力为101千吨/年。以2-丁醇的最低销售价格为目标进行了工艺优化。基于全球能源需求和资本支出分析了不同配置的可行性。集成吸附和吸收的使用使共沸物纯化所需的能量负荷最小化,这在方案1中占总运营支出的11%。作为商品化学品,2-丁醇的最低销售价格估计分别为与下游方案1)、2)和3)集成发酵时的1.05美元/千克、1.21美元/千克和1.03美元/千克。如果设计出更高效的微生物菌株,并找到用于产物回收的更具选择性的吸附和吸收材料,那么在建议的集成配置中2-丁醇生产可实现显著的成本节约。