d im = cane / bagasse density density (no-void) (no-void) at the input input portion portion dej
then and
4)
= the volume (no-void);
= density of extracted juice, and
:
d b = density of bagasse (no-void) at the output portion Wim = d im x Vim
:
Wej = dej x Vej W b = d b x V b
Toät Soemohandojo, Soemohandojo, Extraction of of a Mill, Gula Indonesia Indonesia Magazine, Volume Volume VI No.4 - 1980
Basic Approach of Miling
IV-1
Mill Material Balance
Because cane / bagasse at the input portion is considered to consist of juice and fiber as mentioned in Chapter II, and if: Wij = the weight of juice contain in cane / bagasse Vij = the volume of juice contain in cane cane / bagasse and
: Wf = the weight of fiber Vf = the volume of fiber (no-void);
Furthermore, if: dij = density of juice containing the input portion, and df then
= density of fiber (no-void) (no-void)
: Wij = dij x Vij : Wf = df x Vf
and
The identical condition applies to the output portion, that bagasse is considered to consist of juice and fiber (see Chapter II), then if:
W bj = weight of juice in bagasse V bj = volume of juice in bagasse Wf = weight of fiber, and Vf = volume of fiber (no-void), as mentioned mentioned above, And so
:
Wb = Wbj + W f .................….…..................………………………….. .................….…..................………………………….. (3)
It is understood that the weight of fiber (W f ) at the input portion as well as at the output portion {see equation (2) and equation (3)}, both have the same value (without loss). The same parameter also applied to its no-void volume of fiber (V f ). ). Then it is also understood throughout the tandem in every mill, that the weight and the no-void volume of fiber each have the same respective value.