Strona 2_redak - Instytut Agrofizyki im. Bohdana DobrzaÅskiego ...
Strona 2_redak - Instytut Agrofizyki im. Bohdana DobrzaÅskiego ...
Strona 2_redak - Instytut Agrofizyki im. Bohdana DobrzaÅskiego ...
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84<br />
Table 10.1. Measured (k s ) and calculated (k ϕ ) values of the pressure ratio of seeds and corresponding<br />
values the angle of internal friction 3 (mean ± St.dev)<br />
Seeds k s k 3 = 1.1(1 – sinϕ) 3 (deg)<br />
Amaranthus<br />
Pea<br />
White mustard<br />
Buckwheat<br />
Soybean<br />
Lentil<br />
0.62 ± 0.02<br />
0.53 ± 0.01<br />
0.43 ± 0.01<br />
0.59 ± 0.02<br />
0.37 ± 0.02<br />
0.74 ± 0.01<br />
0.70 ± 0.02<br />
0.59 ± 0.01<br />
0.64 ± 0.01<br />
0.68 ± 0.02<br />
0.55 ± 0.01<br />
0.80 ± 0.02<br />
21.3 ± 0.8<br />
27.3 ± 0.6<br />
24.7 ± 0.4<br />
22.0 ± 0.8<br />
30.1 ± 0.9<br />
15.5 ± 0.6<br />
Table 10.2. Range of variability of the pressure ratio of grain and food powders [145] and values<br />
recommended by Eurocode 1 [50]<br />
Material<br />
Barley<br />
Corn<br />
Oat<br />
Wheat<br />
Rye<br />
Rape seeds<br />
Soybens<br />
Sugar<br />
Wheat flour<br />
Exper<strong>im</strong>ental Eurocode 1 [50]<br />
k s k 3 = 1.1(1 – sinϕ) K<br />
0.30-0.47<br />
0.30-0.67<br />
0.40-0.49<br />
0.31-0.44<br />
0.32-0.52<br />
0.24-0.46<br />
0.35-0.40<br />
0.31-0.47<br />
0.26-0.37<br />
0.50-0.59<br />
0.49-0.60<br />
0.63-0.68<br />
0.46-0.62<br />
0.58-0.67<br />
0.56-0.64<br />
0.54-0.55<br />
0.44-0.50<br />
0.50-0.52<br />
0.59<br />
0.53<br />
–<br />
0.54<br />
–<br />
–<br />
0.63<br />
0.50<br />
0.36<br />
11. AIRFLOW RESISTANCE<br />
11.1. Effects of density, moisture and packing<br />
The main task of the design of a drying or aeration system is to define the<br />
operating airflow that in match with the pressure-drop-air-velocity relationship will<br />
assure the desired course of designed process. Apart from air velocity, other factors<br />
were found to influence the resistance of the bedding to airflow and, consequently,<br />
the pressure drop.<br />
Theoretical modelling of static-bed-drying of grain employs four variables [23]:<br />
mass flow rate of air, air humidity ratio, air temperature, and kernel temperature.<br />
In developing the mathematical model several s<strong>im</strong>plifying assumptions have to be<br />
introduced, one of those being that airflow through the grain is uniform and one<br />
d<strong>im</strong>ensional, with no transfer the in transverse direction. However, moisture and<br />
temperature distribution in a silo is generally non-uniform in practical storage<br />
conditions. Thus for aeration control, location of humidity and temperature probe