Database of Waste Management Technologies Life

Biodrying 3: Combination of mechanical sorting to recover recyclables and Biological drying to produce SRF


Process Description

This configuration is more complicated than "biodrying 1" and "biodrying 2", in the sense that a higher number of mechanical sorting equipment is used, prior to the biodrying reactor, to enhance the recovery of recyclables. So, this process aims:

  • To recover recyclables such as ferrous and non ferrous metals, plastics and paper. For the recovery of plastics and paper usually optical sensors are used.
  • To dry the rest fraction (mainly containing putrescible organic waste but also non-recovered paper and other combustibles) in order to enhance its calorific value.
  • To remove inorganic (non-combustible) material, heavy particles (i.e. stones) and unsuitable material (i.e. batteries) from the dried waste in order to produce a fuel to be used in high energy demand industries: cement kilns, power stations, incinerators.

Process Mass Flow Diagram

Figure 1

Process Photo


Process Operational Data


A Biodrying facility must be accommodated in a sufficient space for the bioconversion reactor, pre-processing and post-processing equipment. According to data from various existing facilities land requirements range from 0.15 to 0.30 m2 per tonne input per year depending on the number of mechanical sorting equipment used.


Energy is used in Biodrying facilities for the removal of materials for refinement of fuel, recycling and for the shredding of the waste. Economopoulos (2007) reports 140 kWh per tonne of input MSW electricity consumption (data received from environmental impact assessment studies of two facilities in Greece), while McDougal et al. (2002) reports 55.5 kWh/t electricity consumption and 111 kWh per tonne of annual plant input heating demand for drying process. According to data of Biodrying plant provider electricity consumption is around 48 kWh/t (ECODECO, 2011).


According to data of Biodrying plant provider water consumption is 30 lt. per tonne of annual plant input.

Process Environmental Indices

Air Emissions

The most significant pollutants emitted from biodrying processes are CH4, N2O, NMVOC and NH3. CO2 emitted from composting is not fossil-derived, and therefore, it is not considered as a greenhouse gas emission. Arcadis et al. (2010) report typically 0.01 kg/t CH4 emissions, 0.02 kg/t N2O emissions, 0.039 kg/t NMVOC emissions and 0.053 kg/t NH3 emissions.


According to data of Biodrying plant provider water consumption is 0,010 m3 per tonne of annual plant input.


Solid residues from Biodrying facilities arise from rejects of pre and post-treatment processes which are disposed to landfills. Economopoulos (2007) reports residual of 165 kg per tonne of input MSW, while McDougal et al. (2002) reports 280 kg/t.