REVISTA ROMÃNÄ DE AUTOMATICÄ - IPA SA
REVISTA ROMÃNÄ DE AUTOMATICÄ - IPA SA
REVISTA ROMÃNÄ DE AUTOMATICÄ - IPA SA
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<strong>REVISTA</strong> ROMÂNĂ <strong>DE</strong> AUTOMATICĂ<br />
3<br />
The pre-batcher meets both requirements of<br />
capability (productivity, precision dosage,<br />
possible adjustment of recipes for different<br />
asphalt mixtures, run in automatically) and<br />
the requirements of security and<br />
environmental protection.<br />
After experimental research it was developed<br />
productivity chart (fig.2) of the pre-batcher<br />
having Φ 219mm drums at the extracting<br />
bands and with the transmission of i= 40.<br />
The batching gravimetric system for natural<br />
dry aggregates and of the cold filler has a<br />
weighing error less than 1%, within SR<br />
7970:2001[4].<br />
The gravimetric batcher system for hot<br />
bitumen (fig.3) has an weighing error less<br />
than 1%, falling into the limits SR<br />
7970:2001[4].<br />
Regarding automation equipment, its prebatching<br />
and batching functions of the pilot<br />
of the central for the preparation of mixtures<br />
CEMA 15, achieved both by running and<br />
optimizing its implemented software system,<br />
are according the technical requirements<br />
provided for operating the pilot phase.<br />
Fig. 2 The productivity chart of the pre-batcher system<br />
2. Experimental researches regarding the<br />
preparation process for asphalt<br />
mixtures<br />
After the pre-batching a drying phase comes<br />
in the technological process (max. 0,5%<br />
humidity ) and the heating of natural<br />
aggregates (175 -185 o C), a process<br />
experimentally analysed in the dry drum<br />
equipped with the automated burner GAS-G<br />
4000 MN (table 1).<br />
Fig. 3 System for weighing with precision of the hot<br />
bitumen binder<br />
(Thermo-insulated recipient , on three load cells+<br />
recirculation/watering pumps + numerical mass<br />
indicator)<br />
Table 1<br />
Process parameters of burner GAS-G 4000MN<br />
Progressive<br />
Gas<br />
flow of<br />
pressure<br />
gaseous fuel<br />
(mbar)<br />
(m 3 /h)<br />
De-pressure at the Differential Burnt gas composition<br />
frontal plate of the de-pressure<br />
dryer I/O filter sacs<br />
CO 2 CO<br />
(mmH 2 O) (cmH 2 O)<br />
(%) ppm<br />
60 ... 200 200...125 5...3 10...14 11...12 2...3 1,24...1,25<br />
O 2<br />
(%)