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Table 2 Activity parameters for conversion plants in the regional foreground. Model plant concepts representative of the region were developed in collaboration with the German Biomass Research Centre (DBFZ) [64]. All flows unless otherwise stated are kg/MJ biodiesel produced, values have been rounded up to the nearest decimal place

From: RELCA: a REgional Life Cycle inventory for Assessing bioenergy systems within a region

 

Small

Medium

Infrastructure

  

Oil mill

Cold press

Hot press

Biodiesel plant

Batch

Continuous

Oil mills

  

Rapeseed

7.98 × 10−1

6.72 × 10−1

Electricity input (MJ MJ−1)a

2.69 × 10−1

2.3 × 10−2

Thermal energy input (MJ MJ−1)b

5.1210−2

Sodium hydroxide

8.06 × 10−5

Phosphoric acid

5.38 × 10−5

Presscake (output) c,d

5.2 × 10−2

4.03 × 10−2

Biodiesel plants

  

Rapeseed oil c

2.71 × 10−2

2.69 × 10−2

Electricity input (MJ/MJ)a

2.34 × 10−3

1.84 × 10−3

Thermal energy input (MJ/MJ)b

2.77 × 10−2

1.66 × 10−2

Methanol

3.58 × 10−3

2.93 × 10−3

Potassium hydroxide

2.69 × 10-4

2.69× 10−4

Sodium hydroxide

8.06 × 10−5

Sulphuric acid

1.96 × 10−4

1.7 × 10−4

Hydrochloric acid

2.69 × 10−4

Biodieselc

2.69 × 10−2

2.69 × 10−2

Crude Glycerol d

3.47 × 10−3

3.23 × 10−3

FFA

5.4 × 10−4

2.69 × 10−4

Fertiliser

5.4 × 10−4

2.69 × 10−4

  1. aElectricity mix for Germany 2010 was taken from [100]
  2. bThermal energy refers to German natural gas mix, taken from [101]
  3. cEnergetic allocation was carried out using the following lower heating values (LHV): press cake was taken to be 18.7 MJ/kg, crude press oil 36 MJ/kg and biodiesel 37.2 MJ/kg biodiesel [102]
  4. dOutput in italics refers to by-products. For this simple example, by products (except for press cake) were not considered; however, they are provided here to show the balances for each plant concept. Crude glycerol (approx. 80 % glycerol)