PRODUCTION OF 1,3-PROPANEDIOL FROM CRUDE GLYCEROL: BIOPROCESS DESIGN AND PROFITABILITY ANALYSIS

被引:7
|
作者
Espinel-Rios, S. [1 ,2 ]
Ruiz-Espinoza, J. E. [1 ]
机构
[1] Univ Autonoma Yucatan, Fac Ingn Quim, Periferico Norte Km 33-5,Tablaje Catastral 13615, Merida 97203, Mexico
[2] Wageningen Univ & Res, Bioproc Engn, Droevendaalsesteeg 1,Bldg 107, NL-6708 PB Wageningen, Netherlands
来源
关键词
1,3-propanediol; glycerol; modelling; simulation; economic analysis; FERMENTATION;
D O I
10.24275/uam/izt/dcbi/revmexingquim/2019v18n3/Espinel
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Crude glycerol is the major byproduct of the biodiesel industry, and its low price due to its abundant market supply impacts negatively on this industry. The microbial production of 1,3-propanediol (1,3-PD) is a very promising way for valorizing glycerol. Clostridium diolis DSM 15410 converts glycerol into 1,3-PD and it is of industrial value due to its high fermentation yields and productivities. The aim of this study was to design a biotechnological process for the continuous production of 1,3-PD (> 99.0% purity) from crude glycerol using C. diolis DSM 15410 as biological system and evaluate the process economic profitability under different scenarios. Optimal fermentation parameters were considered for the analysis. The effects of the selling price of 1,3-PD ($2.3-$6 /t), the purchase cost of crude glycerol ($100-$300/t) and the process throughput (100-1,000 kg 1,3-PD/h) on the process profitability were studied. The results showed that the process is economically profitable over a wide range of scenario combinations. This paper serves as a means for strategic decision making (e.g., go/no-go investment decisions) and further optimization of the 1,3-PD production process from crude glycerol.
引用
收藏
页码:831 / 840
页数:10
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