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Table 2 Acidogenic fermentation from various types of lignocellulosic biomass wastes and the operating parameters

From: Review and perspectives of enhanced volatile fatty acids production from acidogenic fermentation of lignocellulosic biomass wastes

Substrates

Pretreatments

Chemical compositions

Reactor

Operation mode

VFA yields

Product compositions

Main bacterial characteristics

References

Grass clipping

Ultrasound-Ca(OH)2

4 and 32 g/g volatile solids (VS) glucose and xylan released

250 mL, 35 °C, 120 rpm

Batch 12d

578 mg/g volatile solids (VS), increase 116%

82% acetic, 4% propionic and 4% butyric acids

Bacteria class: Clostridia and Bacteroidia

Wang et al. (2019a)

Grass

Carbide slag

Reduced 6% lignin and 8% hemicellulose

250 mL, 35 °C

Batch

220 mg/g volatile solids (VS), increase 38%

78% acetate, 4% propionate and 8% butyrate

Clostridium, Bacteroides

Tao et al. (2019)

Napier grass

Milling

–

250 mL flasks, 37 °C, 100 rpm, micro O2,

Batch

107.25 mg/g volatile solids (VS)

50–70% acetic and 20–50% propionic acids

–

Sawatdeenarunat et al. (2017)

Japanese cedar

Vibration milling

–

2 L, 39 °C, 30–40 rpm, pH 6.5

Semi-continuous

76 mg/g volatile solids (VS)

37% acetic and 60% propionic acids

F. succinogenes (cellulolytic bacterium), P. ruminicola (synergistically with cellulolytic bacteria), S. ruminis (propionate-producing)

Agematu et al. (2017)

Fallen leaves

Lime pretreatments

–

250-mL flasks with 10% inoculum, 37 °C, pH 8

Batch 5d

1.06 g/g volatile solids (VS), increase 160%

70% acetic and 20% butyric acids

–

Kim et al. (2013)

Sorghum stalks

Milling and acid

Hemicellulose degraded by 60%

135 mL, 55 °C,

Two steps

424 mg/g volatile solids (VS), increase 84% acetate and 116% butyrate

2.17 g/L acetic and 2.07 g/L butyric acids

–

Islam et al. (2018)

Corn stalk

Acid pretreatment

Hemicellulose reduced by 12%, cellulose increased by 15%

500 mL flask, 50 °C, 15 days, pH 7

Batch

150 mg/g volatile solids (VS)

0.86 g/L formic, 0.59 g/L acetic, 0.62 g/L butyric and 0.64 g/L lactic acid

–

Guo et al. (2011)

Corn stover

Hydrothermal

Lignin removal of 8%

500 mL, 35 °C

Batch

1.4 g/g volatile solids (VS), 3.5 times higher

20% ethanol, 66% acetic, 8% iso-butyric acid

–

Song et al. (2019b)

Corn stover

Wet-exploded

–

3 L, 37 °C, 150 rpm, pH 6.5

Batch

1.14 g/g volatile solids (VS)

50–70% acetate, 20–45% propionate

–

Murali et al. (2017)

Rice straw

1% NaOH

–

6.5 L, pH 6, HRT 8, 9 days

Semi-continuous

1 g/g volatile solids (VS)

40–60% acetate, 20–33% propionate, 12% butyrate

Predominant class: Clostridia, Bacteroidia, Bacteroidetes_vadin HA17 and Deltaproteobacteria

Lu et al. (2018)

Wheat straw

7.4% Ca(OH)2

Release 0.16 g Hemicellulose/g volatile solids (VS)

600 mL, 35 °C

Batch

223 mg/g volatile solids (VS)

60 mg/g volatile solids (VS) acetic, 150 mg/g volatile solids (VS) butyric acid

–

Reilly et al. (2014)

Wheat straw

–

–

6 L, lead bed reactor, 37 °C, solid-state

Batch

560 mg/g volatile solids (VS)

–

–

Rouches et al. (2019)

Palm fruit bunch

Cutting

–

40 L leach bed reactor, solid-state

Semi-continuous

196.5 mg/gTS

–

–

Saritpongteeraka et al. (2015)

Xylose

Acidic and thermal pretreatments

–

500 mL, pH 6.5, 30 °C

Batch

124 g/g volatile solids (VS), increase 187%

Acetate higher than 85%

Dominant: Clostridia, related with acidogenic and solventogenic processes

Mockaitis et al. (2020)