Techno-economic evaluation and life-cycle assessment of poly (3-hydroxybutyrate) production within a biorefinery concept using sunflower-based biodiesel industry by-products

被引:34
作者
Kachrimanidou, Vasiliki [1 ,2 ]
Ioannidou, Sofia Maria [1 ]
Ladakis, Dimitrios [1 ]
Papapostolou, Harris [1 ]
Kopsahelis, Nikolaos [2 ]
Koutinas, Apostolis A. [1 ]
Kookos, Ioannis K. [3 ]
机构
[1] Agr Univ Athens, Dept Food Sci & Human Nutr, Iera Odos 75, Athens 11855, Greece
[2] Ionian Univ, Dept Food Sci & Technol, Argostoli 28100, Kefalonia, Greece
[3] Univ Patras, Dept Chem Engn, Patras 26504, Greece
关键词
Poly(3-hydroxybutyrate); Biorefinery; Design; Techno-economic evaluation; Life-cycle assessment; CRUDE GLYCEROL; POLY(3-HYDROXYBUTYRATE); OIL; ACID; SEPARATION; FEEDSTOCK; DESIGN;
D O I
10.1016/j.biortech.2021.124711
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
This study presents techno-economic evaluation of a biorefinery concept using biodiesel industry by-products (sunflower meal and crude glycerol) to produce poly(3-hydroxybutyrate) (PHB), crude phenolic extracts (CPE) and protein isolate (PI). The PHB production cost at two annual production capacities ($12.5/kg for 2,500 t PHB/ year and $7.8/kg for 25,000 t PHB/year) was not cost-competitive to current PHB production processes when the revenues derived from co-products were not considered. Sensitivity analysis projected the economic viability of a biorefinery concept that could achieve a minimum selling price of $1.1/kg PHB similar to polypropylene. The annual PHB production capacity and the identification of marketable end-uses with respective market prices for the co-products CPE and PI were crucial in attaining process profitability. Greenhouse gas emissions (ca. 0.64 kg CO2-eq/kg PHB) and abiotic depletion potential (61.7 MJ/kg PHB) were lower than polypropylene. Biorefining of sunflower meal and crude glycerol could lead to sustainable PHB production.
引用
收藏
页数:14
相关论文
共 46 条
[1]   Environmental life cycle comparison of polyhydroxyalkanoates produced from renewable carbon resources by bacterial fermentation [J].
Akiyama, M ;
Tsuge, T ;
Doi, Y .
POLYMER DEGRADATION AND STABILITY, 2003, 80 (01) :183-194
[2]  
[Anonymous], 2015, ENERC24232012SI26737
[3]  
[Anonymous], 2020, Feedipedia-Animal Feed Resources Information System-INRAE CIRAD AFZ and FAO: Almond Hulls and Almond By-Products
[4]   Techno-economic analysis of a biodiesel production process from vegetable oils [J].
Apostolakou, A. A. ;
Kookos, I. K. ;
Marazioti, C. ;
Angelopoulos, K. C. .
FUEL PROCESSING TECHNOLOGY, 2009, 90 (7-8) :1023-1031
[5]   Oilseeds beyond oil: Press cakes and meals supplying global protein requirements [J].
Arrutia, Fatima ;
Binner, Eleanor ;
Williams, Peter ;
Waldron, Keith W. .
TRENDS IN FOOD SCIENCE & TECHNOLOGY, 2020, 100 :88-102
[6]   Techno-economic analysis and life cycle assessment of heterotrophic yeast-derived single cell oil production process [J].
Bonatsos, Nikolaos ;
Marazioti, Constantina ;
Moutousidi, Eleni ;
Anagnostou, Angeliki ;
Koutinas, Apostolis ;
Kookos, Ioannis K. .
FUEL, 2020, 264
[7]  
Boustead I., 2000, ECOPROFILES PLASTICS
[8]  
Chinthapalli R., 2019, Com/Ind, V15, P237, DOI [DOI 10.1089/IND.2019.29179.RCH, DOI 10.1089/IND.2024.29333.PSK]
[9]   Techno-economic and profitability analysis of food waste biorefineries at European level [J].
Cristobal, Jorge ;
Caldeira, Carla ;
Corrado, Sara ;
Sala, Serenella .
BIORESOURCE TECHNOLOGY, 2018, 259 :244-252
[10]   Optimal design of upstream processes in biotransformation technologies [J].
Dheskali, Endrit ;
Michailidi, Katerina ;
de Castro, Aline Machado ;
Koutinas, Apostolis A. ;
Kookos, Ioannis K. .
BIORESOURCE TECHNOLOGY, 2017, 224 :509-514