Cerveja da indústria de etanol de milho / Semibatelada1
|
5,5 / 30 |
120,0 |
- |
0,95 / - |
1,88 / - |
1,13 / - |
2,34 / - |
2,10 / - |
(AGLER et al., 2012AGLER, M.T.; SPIRITO, C.M.; USACK, J.G.; WENER, J.J.; ANGENENT, L.T. (2012) Chain elongation with reactor microbiomes: Upgrading dilute ethanol to medium-chain carboxylates. Energy and Environmental Science, v. 5, n. 8, p. 8189-8192. https://doi.org/10.1039/C2EE22101B https://doi.org/https://doi.org/10.1039/...
) |
Cerveja de levedura fermentada / Semibatelada1
|
5,5 / 30 |
0,6 |
10,7 |
- |
- |
0,8 / 0,07 |
0,2 / 0,02 |
3,40 / 0,32 |
(GE et al., 2015GE, S.; USACK, J.G.; SPIRITO, C.M.; ANGENENT, L.T. (2015) Long-term n-caproic acid production from yeast-fermentation beer in an anaerobic bioreactor with continuous product extraction. Environmental Science & Technology, v. 49, n. 13, p. 8012-8021. https://doi.org/10.1021/acs.est.5b00238 https://doi.org/https://doi.org/10.1021/...
) |
Resíduo alimentar / Batelada |
6,0 / 30 |
20,0 |
6,0 |
0,50 / 0,08 |
0,20 / 0,03 |
1,5 / 0,25 |
0,1 / 0,02 |
- |
(WANG et al., 2014WANG, K.; YIN, J.; SHEN, D.; LI, N. (2014) Anaerobic digestion of food waste for volatile fatty acids (VFAs) production with different types of inoculum: Effect of pH. Bioresource Technology, v. 161, p. 395-401. https://doi.org/10.1016/j.biortech.2014.03.088 https://doi.org/https://doi.org/10.1016/...
) |
Resíduo alimentar / Batelada |
6,0 / 35 |
5,0 |
6,72
|
1,46 / 0,054
|
0,76 / 0,024
|
1,33 / 0,044
|
0,74 / 0,024
|
- |
(JIANG et al., 2013JIANG, J.; ZHANG, Y.; LI, K.; WANG, Q.; GONG, C.; LI, M. (2013) Volatile fatty acids production from food waste : Effects of pH, temperature, and organic loading rate. Bioresource Technology, v. 143, p. 525-530. https://doi.org/10.1016/j.biortech.2013.06.025 https://doi.org/https://doi.org/10.1016/...
) |
Resíduo alimentar / Semibatelada |
5,5 / 45 |
8,0 |
8,73
|
1,21 / 0,275
|
0,01 / 0,025
|
0,43 / 0,105
|
0,13 / 0,035
|
0,59 / 0,135
|
(LIM et al., 2008LIM, S.J.; KIM, B.J.; JEONG, C.-M.; CHOI, J.-D.-R.; AHN, Y.H.; CHANG, H.N. (2008) Anaerobic organic acid production of food waste in once-a-day feeding and drawing-off bioreactor. Bioresource Technology, v. 99, n. 16, p. 7866-7874. https://doi.org/10.1016/j.biortech.2007.06.028 https://doi.org/https://doi.org/10.1016/...
) |
Águas residuárias sintéticas / Contínuo (UASB) |
8,5 / Amb |
0,3 |
1,2 |
0,28 / 0,23 |
0,09 / 0,08 |
0,08 / 0,07 |
0,08 / 0,07 |
- |
(WANG et al., 2013WANG, D.; WANG, G.; XU, X.; YANG, F. (2013) Multiple factors influencing anaerobic acidogenic pretreatment in an up-flow non-woven biofilm reactor. Chemical Engineering Journal, v. 221, p. 37-43. https://doi.org/10.1016/j.cej.2013.01.104 https://doi.org/https://doi.org/10.1016/...
) |
Lactato / Contínuo (UASB)1
|
5,0 / 34 |
1,9 |
17,7 |
1,28 / 0,07 |
- |
0,29 / 0,02 |
- |
3,10 / 0,18 |
( KUCEK; NGUYEN; ANGENENT, 2016KUCEK, L.A.; NGUYEN, M.; ANGENENT, L.T. (2016) Conversion of L-lactate into n-caproate by a continuously fed reactor microbiome. Water Research, v. 93, p. 163-171. https://doi.org/10.1016/j.watres.2016.02.018 https://doi.org/https://doi.org/10.1016/...
) |
Água amarela (lactato) / Batelada |
5,5-6,5 / 30 |
16,0 |
4,2 |
0,02 / - |
- |
0,12 / 0,03 |
0,04 / 0,01 |
1,08 / 0,26 |
(ZHU et al., 2015ZHU, X.; TAO, Y.; LIANG, C.; LI, X.; WEI, N.; ZHANG, W.; ZHOU, Y.; YANG, Y.; BO, T. (2015) The synthesis of n-caproate from lactate: A new efficient process for medium-chain carboxylates production. Scientific Reports, v. 5, 14360. https://doi.org/10.1038/srep14360 https://doi.org/https://doi.org/10.1038/...
) |
Lodo de ETE municipal / Semibatelada |
6,6-7,1 / 55 |
2,5 |
11,4 |
0,81 / 0,07 |
0,11 / 0,01 |
0,17 / 0,01 |
0,20 / 0,02 |
- |
(HAO; WANG, 2015HAO, J.; WANG, H. (2015) Volatile fatty acids productions by mesophilic and thermophilic sludge fermentation: Biological responses to fermentation temperature. Bioresource Technology, v. 175, p. 367-373. https://doi.org/10.1016/j.biortech.2014.10.106 https://doi.org/https://doi.org/10.1016/...
) |
Milho fibroso pré-tratado / Batelada (ASBRs) |
5,5 / 30 |
15,0 |
1,9 |
0,34 / 0,18 |
- |
0,43 / 0,22 |
- |
0,33 / 0,17 |
(AGLER et al., 2014AGLER, M.T.; SPIRITO, C.M.; USACK, J.G.; WERNER, J.J.; ANGENENT, L.T. (2014) Development of a highly specific and productive process for n-caproic acid production: Applying lessons from methanogenic microbiomes. Water Science and Technology, v. 69, n. 1, p. 62-68. https://doi.org/10.2166/wst.2013.549 https://doi.org/https://doi.org/10.2166/...
) |
Efluente de fermentador de gás de síntese + Etanol (11,4 g L-1) + Acetato (2,3 g L-1) / Contínuo (UASB) |
5,5 / 30 |
0,6 |
45,0 |
- |
- |
20 / 0,44 |
- |
1,7 / 0,04 |
(VASUDEVAN; RICHTER; ANGENENT, 2014VASUDEVAN, D.; RICHTER, H.; ANGENENT, L.T. (2014) Upgrading dilute ethanol from syngas fermentation to n-caproate with reactor microbiomes. Bioresource Technology, v. 151, p. 378-382. https://doi.org/10.1016/j.biortech.2013.09.105 https://doi.org/https://doi.org/10.1016/...
) |
Lodo primário e resíduos de lodo ativado de uma ETE / Batelada |
11,0 / 35 |
15,0 |
0,2 |
0,07 / 0,35 |
0,02 / 0,10 |
0,02 / 0,10 |
- |
0,01 / 0,05 |
(JANKOWSKA et al., 2015JANKOWSKA, E.; CHWIALKOWSKA, J.; STODOLNY, M.; OLESKOWICZ-POPIEL, P. (2015) Effect of pH and retention time on volatile fatty acids production during mixed culture fermentation. Bioresource Technology, v. 190, p. 274-280. https://doi.org/10.1016/j.biortech.2015.04.096 https://doi.org/https://doi.org/10.1016/...
) |
Glicerol (5 g L-1) + Etanol (4,6 g L-1) + I.M. Clorofórmio / Batelada |
6,5 / - |
14,0 |
1,1 |
- |
0,03 / 0,03 |
0,04 / 0,03 |
- |
0,27 / 0,25 |
(DAMS et al., 2018DAMS, R.I.; VIANA, M.B.; GUILHERME, A.A.; SILVA, C.M.; SANTOS, A.B.; ANGENENT, L.T.; SANTAELLA, S.T.; LEITÃO, R.C. (2018) Production of medium-chain carboxylic acids by anaerobic fermentation of glycerol using a bioaugmented open culture. Biomass and Bioenergy, v. 118, p. 1-7. https://doi.org/10.1016/j.biombioe.2018.07.023 https://doi.org/https://doi.org/10.1016/...
) |
Metanol (6,4 g L-1) + Acetato (3 g L-1) / Batelada / Contínuo (UASB) |
5,9-6,1 / 35 |
17,0 |
12,4 |
- |
- |
0,25 / 0,34 |
- |
- |
(CHEN et al., 2016CHEN, W.S.; YE, Y.; STEINBUSCH, K.J.J; STRIK, D.P.B.T.B.; BUISMAN, C.J.N. (2016) Methanol as an alternative electron donor in chain elongation for butyrate and caproate formation. Biomass and Bioenergy, v. 93, p. 201-208. https://doi.org/10.1016/j.biombioe.2016.07.008 https://doi.org/https://doi.org/10.1016/...
) |
5,9 / 30 |
1,5 |
15,3 |
- |
- |
1,50 / 0,10 |
- |
- |
Acetato (6,0 g L-1) + Etanol (18,4 g L-1) / Contínuo (UASB) |
5,6-8,6 / 30 |
0,7 |
62,3 |
- |
- |
1,5 / 0,02 |
- |
15,7 / 0,25 |
(GROOTSCHOLTEN et al., 2013aGROOTSCHOLTEN, T.I.M.; STEINBUSCH, K.J.J.; HAMELERS, H.V.M.; BUISMAN, C.J.N. (2013a) Chain elongation of acetate and ethanol in an upflow anaerobic filter for high rate MCFA production. Bioresource Technology, v. 135, p. 440-445. https://doi.org/10.1016/j.biortech.2012.10.165 https://doi.org/https://doi.org/10.1016/...
) |
Acetato (6,0 g L-1) + Etanol (13,7 g L-1) / Contínuo (UASB) |
6,5-7,2 / 30 |
0,2 |
206,0 |
13,8 / 0,07 |
- |
9,6 / 0,05 |
- |
55,8 / 0,27 |
(GROOTSCHOLTEN et al., 2013cGROOTSCHOLTEN, T.I.M.; STEINBUSCH, K.J.J.; HAMELERS, H.V.M.; BUISMAN, C.J.N. (2013c) Improving medium chain fatty acid productivity using chain elongation by reducing the hydraulic retention time in an upflow anaerobic filter. Bioresource Technology, v. 136, p. 735-738. https://doi.org/10.1016/j.biortech.2013.02.114 https://doi.org/https://doi.org/10.1016/...
) |