Techno-economic aspects of a safflower-based biorefinery plant co-producing bioethanol and biodiesel

被引:54
作者
Khounani, Zahra [1 ]
Nazemi, Farshid [2 ]
Shafiei, Marzieh [3 ]
Aghbashlo, Mortaza [4 ]
Tabatabaei, Meisam [1 ,3 ,5 ]
机构
[1] AREEO, Microbial Biotechnol Dept, ABRII, Karaj, Iran
[2] Isfahan Univ Technol, Dept Chem Engn, Esfahan 8415683111, Iran
[3] BRTeam, Karaj, Iran
[4] Univ Tehran, Fac Agr Engn & Technol, Dept Mech Engn Agr Machinery, Coll Agr & Nat Resources, Karaj, Iran
[5] Univ Teknol MARA UiTM, Fac Plantat & Agrotechnol, Shah Alam 40450, Selangor, Malaysia
关键词
Biorefinery; Safflower plant; Techno-economic analysis; Bioethanol; Biodiesel; Biogas; MUNICIPAL SOLID-WASTE; COOKING OIL WCO; ETHANOL-PRODUCTION; SUSTAINABILITY PARAMETERS; EXERGOECONOMIC ANALYSIS; EXERGY ANALYSIS; LIFE-CYCLE; LOW-POWER; BIOGAS; OPTIMIZATION;
D O I
10.1016/j.enconman.2019.112184
中图分类号
O414.1 [热力学];
学科分类号
摘要
Safflower plant is a promising energy crop, which is compatible with arid and semi-arid climate conditions. This study is set to perform a techno-economic assessment of an integrated biorefinery located in Iran, using safflower seed and safflower straw as feedstock for production of bioethanol as the main product, biodiesel as the most valuable byproduct while biogas, glycerol, solid residue, and sodium sulfate are the other valuable byproducts. In the first Scenario (A), glucose, xylose, and arabinose are fermented into ethanol by using Zymomonas mobilis produced in a seed train unit. While in the other Scenario (B), Saccharomyces cerevisiae is supplied externally by a yeast production facility and is used to ferment glucose into ethanol. Both scenarios are simulated using Aspen Plus software and a cash flow analysis is performed using well-known economic indices for the biofuel industry presented by the National Renewable Energy Laboratory. The profitability index is 1.14 for Scenario A, showing its cost-effectiveness. However, this index is found to be 0.81 for Scenario B, revealing the fact that this approach is not economically justified for implementation. More specifically, the use of Z. mobilis instead of S. cerevisiae as fermenting microorganism enhances the profitability of the project by lowering ethanol production cost from 0.12 $/L to 0.09 $/L and minimum ethanol selling price from 0.67 $/L to 0.43 $/L. Moreover, in both scenarios, biodiesel production boosts the total annual sale values by 39% and 55% for scenario A and B, respectively. In general, 1.86 and 2.44 times improvements in this economic index are respectively obtained for scenario A and B because of byproduct credits. The outcomes of sensitivity analysis also shows that the discount factor and safflower seed price have large impacts on the profitability of the developed biorefineries. Overall, Z. mobilis appears to be a preferred biocatalyst for bioethanol fermentation through the biorefinery platform from the techno-economic viewpoint.
引用
收藏
页数:15
相关论文
共 63 条
[1]  
Aden A., 2002, National Renewable Energy Laboratory: Lignocellulosic biomass to ethanol process design and economics utilizing cocurrent dilute acid prehydrolysis and enzymatic hydrolysis for corn stover
[2]   Technoeconomic analysis of the dilute sulfuric acid and enzymatic hydrolysis process for the conversion of corn stover to ethanol [J].
Aden, Andy ;
Foust, Thomas .
CELLULOSE, 2009, 16 (04) :535-545
[3]   Biopower and biofertilizer production from organic municipal solid waste: An exergoenvironmental analysis [J].
Aghbashlo, Mortaza ;
Tabatabaei, Meisam ;
Soltanian, Salman ;
Ghanavati, Hossein .
RENEWABLE ENERGY, 2019, 143 :64-76
[4]   Comprehensive exergoeconomic analysis of a municipal solid waste digestion plant equipped with a biogas genset [J].
Aghbashlo, Mortaza ;
Tabatabaei, Meisam ;
Soltanian, Salman ;
Ghanavati, Hossein ;
Dadak, Ali .
WASTE MANAGEMENT, 2019, 87 :485-498
[5]   Multi-objective exergetic and technical optimization of a piezoelectric ultrasonic reactor applied to synthesize biodiesel from waste cooking oil (WCO) using soft computing techniques [J].
Aghbashlo, Mortaza ;
Hosseinpour, Soleiman ;
Tabatabaei, Meisam ;
Soufiyan, Mohamad Mojarab .
FUEL, 2019, 235 :100-112
[6]   Exergoeconomic and exergoenvironmental co-optimization of continuous) fuel additives (acetins) synthesis from glycerol esterification with acetic acid using Amberlyst 36 catalyst [J].
Aghbashlo, Mortaza ;
Tabatabaei, Meisam ;
Jazini, Hossein ;
Ghaziaskar, Hassan S. .
ENERGY CONVERSION AND MANAGEMENT, 2018, 165 :183-194
[7]   Exergoeconomic analysis of a DI diesel engine fueled with diesel/biodiesel (B5) emulsions containing aqueous nano cerium oxide [J].
Aghbashlo, Mortaza ;
Tabatabaei, Meisam ;
Khalife, Esmail ;
Shojaei, Taha Roodbar ;
Dadak, Ali .
ENERGY, 2018, 149 :967-978
[8]   Exergy analysis of a lignocellulosic-based biorefinery annexed to a sugarcane mill for simultaneous lactic acid and electricity production [J].
Aghbashlo, Mortaza ;
Mandegari, Mohsen ;
Tabatabaei, Meisam ;
Farzad, Somayeh ;
Soufiyan, Mohamad Mojarab ;
Gorgens, Johann F. .
ENERGY, 2018, 149 :623-638
[9]   On the exergoeconomic and exergoenvironmental evaluation and optimization of biodiesel synthesis from waste cooking oil (WCO) using a low power, high frequency ultrasonic reactor [J].
Aghbashlo, Mortaza ;
Tabatabaei, Meisam ;
Hosseinpour, Soleiman .
ENERGY CONVERSION AND MANAGEMENT, 2018, 164 :385-398
[10]   Neat diesel beats waste-oriented biodiesel from the exergoeconomic and exergoenvironmental point of views [J].
Aghbashlo, Mortaza ;
Tabatabaei, Meisam ;
Mohammadi, Pouya ;
Khoshnevisan, Benyamin ;
Rajaeifar, Mohammad Ali ;
Pakzad, Mohsen .
ENERGY CONVERSION AND MANAGEMENT, 2017, 148 :1-15