Skip to main content

Table 5 Energy balance of the self-sustaining biorefinery

From: A sustainable biorefinery to convert agricultural residues into value-added chemicals

Energy balancea

AD

EC process

Fungal fermentation b

Energy input (MJ/kg dry feedstock)

−0.16c

−1.47d

−3.63e

Energy output (MJ/kg dry feedstock)

6.95f

0

0

Net energy (MJ/kg dry feedstock)

6.79

−1.47

−3.63

Overall net energy (MJ/kg dry feedstock)

1.69

  1. All inputs are negative, and all outputs are positive
  2. a Data were calculated and adjusted based on 1 kg dry animal wastes
  3. b The fungal fermentation includes unit operations of pretreatment, enzymatic hydrolysis and fungal fermentation
  4. c The energy input for the AD unit includes both heat and electricity
  5. d The energy input for the EC unit is 446.65 kJ/L liquid digestate
  6. e The energy input for pretreatment, enzymatic hydrolysis, fungal fermentation and post-processing is 1.25 MJ/L fermentation broth (unpublished data)
  7. f The energy output of the AD is the methane energy. Low heating value of methane of 50 kJ/g methane was used for the calculation