Techno-economic assessment of non-sterile batch and continuous production of lactic acid from food waste
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In: Bioresource Technology, Vol. 289, 121631, 01.10.2019.
Research output: Journal contributions › Journal articles › Research › peer-review
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TY - JOUR
T1 - Techno-economic assessment of non-sterile batch and continuous production of lactic acid from food waste
AU - Peinemann, Jan
AU - Demichelis, Francesca
AU - Fiore, Silvia
AU - Pleissner, Daniel
PY - 2019/10/1
Y1 - 2019/10/1
N2 - Non-sterile lactic acid (LA) fermentation of highly viscous food waste was demonstrated in batch and continuous flow fermentations. With Streptococcus sp., an indigenous consortium, and/or applied glucoamylase, food waste was fermented without addition of external carbon or nitrogen sources. Experimental results were used for economic and energy evaluations under consideration of different catchment area sizes from 50,000 to 1,000,000 inhabitants. During batch mode, addition of glucoamylase resulted in a titer (after 24 h), yield, and productivity of 50 g L −1, 63%, and 2.93 g L −1h −1, respectively. While titer and yield were enhanced, productivity was lower during continuous operation and 69 g L −1, 86%, and 1.27 g L −1h −1 were obtained at a dilution rate of 0.44 d −1 when glucoamylase was added. Both batch and continuous flow fermentations were found economically profitable with food waste from 200,000 or more inhabitants.
AB - Non-sterile lactic acid (LA) fermentation of highly viscous food waste was demonstrated in batch and continuous flow fermentations. With Streptococcus sp., an indigenous consortium, and/or applied glucoamylase, food waste was fermented without addition of external carbon or nitrogen sources. Experimental results were used for economic and energy evaluations under consideration of different catchment area sizes from 50,000 to 1,000,000 inhabitants. During batch mode, addition of glucoamylase resulted in a titer (after 24 h), yield, and productivity of 50 g L −1, 63%, and 2.93 g L −1h −1, respectively. While titer and yield were enhanced, productivity was lower during continuous operation and 69 g L −1, 86%, and 1.27 g L −1h −1 were obtained at a dilution rate of 0.44 d −1 when glucoamylase was added. Both batch and continuous flow fermentations were found economically profitable with food waste from 200,000 or more inhabitants.
KW - Chemistry
KW - Biorefinery
KW - Fermentation
KW - Lactic acid
KW - non sterile
KW - TEA
UR - http://www.scopus.com/inward/record.url?scp=85067279604&partnerID=8YFLogxK
U2 - 10.1016/j.biortech.2019.121631
DO - 10.1016/j.biortech.2019.121631
M3 - Journal articles
C2 - 31220764
VL - 289
JO - Bioresource Technology
JF - Bioresource Technology
SN - 0960-8524
M1 - 121631
ER -