PRODUCTION OF BIO-DIESEL
PLANT OF 25,000 TN/YEAR, EXPANDABLE TO 50,000 TN/YEAR
STAGE 1:
PRE-TREATMENT OF CRUDE DEGUMMED SOYBEAN OIL
Necessary Services:
- Permanent supply of compressed air _7 bar.
- Stable supply of three-phase electricity 380 VAC.
- 2 bar dry saturated steam for heating.
- 7 bar dry saturated steam for vacuum equipment.
- Soft water.
Process Diagram
STAGE 2:
PRODUCTION OF BIODIESEL AND GLYCERIN IN A COMPACT BIODIESEL PRODUCTION UNIT OF 25000 TON-YEAR (C.P.U.)
Input
- Refined soy oil (from pre-treatment).
- Methanol from external storage tanks.
- Methylate (KOH 32% + Methanol - KM32) from external storage tanks. (Alkoxide). (Catalyst 32%).
Output
- Refined biodiesel to external expedition tanks.
- Glycerin (G-phase) to external expedition tanks.
COMPACT CELL OF 12500 TON-YEAR OF BIO-DIESEL PRODUCTION
