PRODUCT LIST
- 
            
Edible Oil Production Plant Project
 - 
            
Biodiesel Production Plant Project
- Pretreatment System in Biodiesel Project
 - Esterification System Biodiesel Project
 - Transesterification System in Biodiesel Project
 - Methyl Ester Distillation system in Biodiesel Project
 - Used Cooking Oil Biodiesel Making Machine
 - Vegetable Oil Biodiesel Making Machine
 - Acid Oil Biodiesel Making Machine
 - Palm Oil Biodiesel Making Machine
 - Animal Oil Biodiesel Making Machine
 
 - 
            
Skid-Mounted Biodiesel Unit
 - 
            
MCT Oil Production Plant
 
Technical Requirements of the Continuous Degumming and Deacidification Section
	Technical requirements of the continuous degumming and deacidification section:
	1. After the filtering, the impurity content of the crude oil should be no more than 0.2%
	2. After the pre-heating, add the phosphoric acid into the crude oil and the temperature is 60 ℃
	3. The concentration of addition phosphoric acid is 85%. The addition amount of phosphoric acid is equal to 0.03%-0.15% of the oil weight.
	4. The acid reaction time is 15-40min.
	5. When doing alkali refining, the concentration of addition alkali liquor is 10%-20%( baume degree) or according to small sample test to ensure.
	6. Theoretically, the addition amount of alkali: 7.14×10-4 × oil weight × acid price. For the acidification section, alkali amount of phosphoric acid is calculated according to increase amount of acid value. That is, 1.6× the addition amount of phosphoric acid, super alkali amount is equal to 10%-15%of theoretic alkali amount.
	7. The reaction temperature of alkali is 80-45℃, the reaction time is 10-50min, and the stir speed is about 15-40rpm.
	8. The temperature of oil-soap mixture in soap centrifuge is 85-90℃,the pressure of light export oil is 0.10-0.30MPa.
	9. When doing washing, the temperature of addition soft water is 90-95℃, the addition amount is equal to 10%-15% of oil weight.
	10. The temperature of oil-water mixture into dewatering centrifuge is 85~90℃,the pressure of light export oil is 0.10-0.30MPa.
	11. The oil temperature is 105~130℃ which will into the desolvation or dryer tower,and its vacuum degree is -0.09MPa.
	12. After the desiccation process, the water content in oil is 0.05-0.1%, must not exceed 0.2%, or it will have adverse effect on the back-end processing of refining process.
