HAZARDOUS WASTE MANAGEMENT
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 Mytol Process for Refining of Used    Lubricating Oil
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Mytol Process for Refining of Used Lubricating Oil
  BASE OIL,WASTE OIL RECYCLING,BASE OIL
             

Typical Recovery of Mytol Process

PRODUCT
TYPICAL FEED COMPOSITION
%WT.
RECOVERY RATE % WT.
YIELD
%
PRODUCTION KGS/HR.
PRODUCTION TPA
DRIED USED OIL
100.0
- -
- -
2000.0
15000
HEAVY LUBE BASE OIL
79.0
72.0
91.0
1440.0
10800
LIGHT LUBE BASE OIL
12.8
12.6
98.5
252.0
1890
GAS OIL /
LIGHT ENDS
5.4
5.2
96.3
104.0
780
ASPHALT
2.8
10.0
- -
200.0
1500
LOSSES
- -
0.2
- -
4.0
30



Utilities of Mytol Process

CONSUMPTION
UNIT
DEHYDRATION
VAPORIZATION & FRACTIONAL
CONDENSATION
BLEACHING
TOTAL
Power
KWH
9.9
24.8
19.5
54.2
L.P. steam Kgs/hr
(3.0 Kg/Cm2-g)
--
--
- 153.0
Export
81.0
-72.0 Export
Boiler Feed Water
M3
--
0.200
--
0.200
C.W Circulation
DT= 8oC
M3
14.0
22.50
--
36.5
C.W. (2% of circulation)
M3
0.28
0.45
--

0.73
Fuel (CV =10,000 K-cal/Kg)
- -
17.25
46.0
--
63.25

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