Design and techno-economic evaluation of microbial oil production as a renewable resource for biodiesel and oleochemical production

被引:272
|
作者
Koutinas, Apostolis A. [1 ]
Chatzifragkou, Afroditi [1 ]
Kopsahelis, Nikolaos [1 ]
Papanikolaou, Seraphim [1 ]
Kookos, Ioannis K. [2 ]
机构
[1] Agr Univ Athens, Dept Food Sci & Human Nutr, GR-11855 Athens, Greece
[2] Univ Patras, Dept Chem Engn, Patras 26504, Greece
关键词
Microbial oil; Fermentation; Biodiesel; Design; Techno-economic evaluation; LIPID PRODUCTION; DENSITY CULTIVATION; YARROWIA-LIPOLYTICA; GLYCEROL; OPTIMIZATION; RACEWAYS; MODEL; FUELS; ACID;
D O I
10.1016/j.fuel.2013.08.045
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Experimental results from the open literature have been employed for the design and techno-economic evaluation of four process flowsheets for the production of microbial oil or biodiesel. The fermentation of glucose-based media using the yeast strain Rhodosporidium toruloides has been considered. Biodiesel production was based on the exploitation of either direct transesterification (without extraction of lipids from microbial biomass) or indirect transesterifaction of extracted microbial oil. When glucose-based renewable resources are used as carbon source for an annual production capacity of 10,000 t microbial oil and zero cost of glucose (assuming development of integrated biorefineries in existing industries utilising waste or by-product streams) the estimated unitary cost of purified microbial oil is $ 3.4/kg. Biodiesel production via indirect transesterification of extracted microbial oil proved more cost-competitive process compared to the direct conversion of dried yeast cells. For a price of glucose of $ 400/t oil production cost and biodiesel production cost are estimated to be $ 5.5/kg oil and $ 5.9/kg biodiesel, correspondingly. Industrial implementation of microbial oil production from oleaginous yeast is strongly dependent on the feedstock used and on the fermentation stage where significantly higher productivities and final microbial oil concentrations should be achieved. (C) 2013 Elsevier Ltd. All rights reserved.
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页码:566 / 577
页数:12
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