Skip to main content

Table 1 Characterization of the desolventizing/toasting processes of rapeseed mealsa

From: Effect of the desolventizing/toasting process on chemical composition and protein quality of rapeseed meal

 

Rapeseed meal

Desolventizing/toasting

Ab

Bb

Cb

Db

Ec

Residence time, min

48

64

76

93

60

Indirect heat, kPa

850

850

850

850

450

Direct steam flow rate, kg/h

15

15

15

15

30

Temperature, °C

126d

128d

125d

115d

120e

114e

129e

134e

107e

Toasting condition

WetTCf

WetTCf

WetTCf

WetTCf

DryTCg

  1. WetTC = wet toasting conditions; DryTC = dry toasting conditions
  2. aRapeseed meals A-E represent five differently processed rapeseed meals under standardized and defined conditions in a pilot plant
  3. bProduced from marc one
  4. cBlend of rapeseed meal manufactured from marc two under the same processing conditions as for rapeseed meals A-D
  5. dAverage temperature on tray five of the desolventizer/toaster. Tray five was not used for production of rapeseed meal E
  6. eAverage temperature on tray six of the desolventizer/toaster
  7. fUse of indirect heat at 850 kPa and direct unsaturated steam (15 kg/h) with mean residence time in the desolventizer/toaster of 48, 64, 76, and 93 min for rapeseed meals A, B, C, and D, respectively
  8. gBlend of rapeseed meals produced from marc two was exposed for 30 min up to a maximum temperature of 100 °C to direct saturated steam application (30 kg/h), followed by indirect heat treatment at 107 ° C for 30 min at 450 kPa. Additional residence time in the desolventizer/toaster was 60 min compared to rapeseed meals A-D