Biocatalytic Production of 2-α-D-Glucosyl-glycerol for Functional Ingredient Use: Integrated Process Design and Techno-Economic Assessment

被引:7
|
作者
Kruschitz, Andreas [1 ,2 ]
Nidetzky, Bernd [1 ,2 ]
机构
[1] Austrian Ctr Ind Biotechnol Acib, A-8010 Graz, Austria
[2] Graz Univ Technol, Inst Biotechnol & Biochem Engn, A-8010 Graz, Austria
关键词
advanced biomanufacturing; integrated process design; techno-economic assessment; 2-alpha-D-glucosyl-glycerol; sucrose phosphorylase; waste prevention; FRUCTOSE DEHYDRATION; REACTIVE EXTRACTION; SUGARS; ACID; PURIFICATION; SOLVENT; GLUCOSYLGLYCEROL; ISOMERIZATION; BIOSYNTHESIS; BIOMASS;
D O I
10.1021/acssuschemeng.1c07210
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Advanced biomanufacturing builds on production processes that are both profitable and sustainable. Integrated design of process unit operations, geared to output efficiency and waste minimization and guided by a rigorous techno-economic assessment, is essential for development aligned to these central aims. Here, we demonstrate such a development for the biocatalytic production of the biological extremolyte 2-O-alpha-D-glucosyl-glycerol (2-GG) for functional ingredient application. The process was aligned in scale over all steps (similar to 180 g product; similar to 2.5 L reaction mixture) and involved continuous enzymatic synthesis from sucrose and glycerol interlinked with reactive extraction and nanofiltration for product isolation (purity of similar to 80 wt %) and side stream recovery. Glycerol used in similar to 6-fold excess over sucrose was recycled, and hydrothermal conversion into 5-(hydroxymethyl)furfural was evaluated for the fructose by-product released from sucrose. Based on a process mass intensity (total mass input/mass product) of 146, similar to 80% of the total mass input was utilized and an E-factor (mass waste/mass product) of 28 was obtained. EcoScale analysis revealed a penalty point score of 44, suggesting an acceptable process from a sustainability point of view. Process simulation for an annual production of 10 tons 2-GG was used for the techno-economic assessment with discounted cash flow analysis. The calculated operating costs involved 35 and 47% contributions from materials and labor, respectively. About 91% of the material costs were due to chemicals for the reactive extraction-acidic stripping step, emphasizing the importance of material reuse at this step. Glycerol recycling involved a trade-off between waste reduction and energy use for the removal of water. Collectively, the study identifies options and boundaries of a profitable 2-GG process. The minimum selling price for 2-GG was calculated as similar to 240 sic kg(-1) or smaller. The framework of the methodology presented can be generally important in applied bio-catalysis: it facilitates closing of the gap between process design and implementation for accelerated development.
引用
收藏
页码:1246 / 1255
页数:10
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