TY - JOUR
T1 - Techno-economic assessment of heterotrophic microalgae biodiesel production integrated with a sugarcane bio-refinery
AU - Sano Coelho, Renato
AU - Cuellar, Maria C.
AU - Franco, Telma T.
AU - van der Wielen, Luuk A.M.
PY - 2020
Y1 - 2020
N2 - The use of diesel fuel in crop and transportation operations is responsible for one third of the carbon emissions in sugarcane biorefineries. A possible solution is to replace it with biodiesel from lipids, directly produced from sugarcane by highly productive heterotrophic microalgae. In this study a heterotrophic microalgae biodiesel plant, integrated with a typical Brazilian sugarcane bio-refinery, was designed and evaluated. Molasses, steam, and electricity from sugarcane processing were used as inputs for microalgae production. For a non-integrated plant, the production cost of the microalgae biodiesel was estimated at 2.51 and 2.27 $/liter for fed-batch and continuous processes, respectively. Equipment for cultivation and carbon sources was the highest cost affecting the financial feasibility of the proposed design. For the integrated plant, at present ethanol and biodiesel selling prices, the profitability would be lower than a first-generation sugarcane bio-refinery using fossil diesel fuel for its operations. However, the CO2 emissions would be reduced by up to 50 000 × 103 kg per year at a cost of $83 10−3 kg−1 CO2-eq. If carbon credits are considered, the process becomes economically profitable even at present fuel prices.
AB - The use of diesel fuel in crop and transportation operations is responsible for one third of the carbon emissions in sugarcane biorefineries. A possible solution is to replace it with biodiesel from lipids, directly produced from sugarcane by highly productive heterotrophic microalgae. In this study a heterotrophic microalgae biodiesel plant, integrated with a typical Brazilian sugarcane bio-refinery, was designed and evaluated. Molasses, steam, and electricity from sugarcane processing were used as inputs for microalgae production. For a non-integrated plant, the production cost of the microalgae biodiesel was estimated at 2.51 and 2.27 $/liter for fed-batch and continuous processes, respectively. Equipment for cultivation and carbon sources was the highest cost affecting the financial feasibility of the proposed design. For the integrated plant, at present ethanol and biodiesel selling prices, the profitability would be lower than a first-generation sugarcane bio-refinery using fossil diesel fuel for its operations. However, the CO2 emissions would be reduced by up to 50 000 × 103 kg per year at a cost of $83 10−3 kg−1 CO2-eq. If carbon credits are considered, the process becomes economically profitable even at present fuel prices.
KW - bio-refinery
KW - biodiesel
KW - heterotrophic microalgae
KW - sugarcane
KW - techno-economic assessment
UR - http://www.scopus.com/inward/record.url?scp=85098485770&partnerID=8YFLogxK
U2 - 10.1002/bbb.2174
DO - 10.1002/bbb.2174
M3 - Article
AN - SCOPUS:85098485770
SN - 1932-104X
VL - 15
SP - 416
EP - 429
JO - Biofuels, Bioproducts and Biorefining
JF - Biofuels, Bioproducts and Biorefining
IS - 2
ER -