New design oil extraction equipment for soybean oil extraction plantThe material of drum doby, drum cover and valve is high strength stainless steel, the Moc of other parts are all high quality, anti-corrosion SS304, the separator shell employ SS304.
Drive structure support use SKF bearing, by employing optimal design to reduce the heigLD of the drumâs center of gravity. It can effectively lower the vibrational level of the whole separator, improve the reliability of the equipment and increase the stability of the separator.
In the dismounting and maintenance, the parts of drum can be hoisted integrally, thus make the dismounting of main lock ring more convenient, saving both time and labor, easy to install the drum.
The separator runs supercurrent, it will send warning signals and be stoped if the machine overload, to make the separator runs safely.
The separator has a less vibration and more stability through price dynamic balance of the drum.
The separator adopts separation factor technoloLD. It can separate product that is hard to separate, meanwhile, the machine has ligLD volume and use the small volume to get big capacity and high separation efficiency.
The separator adopts advance belt drive, improving the reliability and maintainability of the separator, and decreasing cost of spare parts.
The vegetable oil sunflower oil refined soybean oil filling machine is suitable for filling edible oil,olive oil,motor oil,lubricant,gear oil,engine oil,all kinds of flowing liquid and so on.the vegetable oil sunflower oil refined soybean oil filling machine can fill different shapes of bottle such as round,flat,square,etc.
New design oil extraction equipment for soybean oil extraction planttn plant
Rotocel Etraction
Process features for soybean oil extraction plant
1. Adopt stainless steel fied grid plate and increase the horizontal grid plates, which can prevent the strong miscella from flowing back to the blanking case, so as to ensure good etraction effect;
2. The rotocel etractor is driven by rack, with unique rotor of balanced design, low rotating speed, low power, smooth operation, no noise and quite low maintenance cost;
3. The feeding system can adjust the rotating speed of airlock and main engine according to the feeding quantity and maintain a certain material level, which is beneficial to the micro negative pressure inside the etractor and reduce the solvent leakage.
4. The advanced miscella circulation process is designed to reduce the fresh solvent inputs, reduce the residual oil in meal, improve the miscella concentration and save enerLD by reducing the evaporation capacity.
5. The high material layer of the etractor helps to form immersion etraction, reduce the meal quality in miscella, improve the quality of crude oil and reduce the evaporation system scaling.
6. Specially suitable for the etraction of various pre-pressed meals.
Main economic and technical parameters for soybean oil extraction plant
Capacity |
300T/D |
Residual oil in meal |
1% (soybean) |
Solvent consumption |
2Kg/T (No.6 solvent oil) |
Crude oil moisture and volatile matter |
0.30% |
Power consumption |
15KWh/T |
Steam consumption |
280KG/T (0.8MPa) |
Finished meal moisture |
13% (adjustable) |
Residual solvent in finished meal |
300PPM(qualifieddetonated eperiment) |
Towline extractor
Towline extractor Advantages:
1) The material is divided into several independent units on the material bed, which can effectively prevent miscella at all levels from fleeing hither and thither on the material layer and ensure the concentration gradient between
several sprays.
2) Immersion area appears in each lattice, which can help achieve better immersion effect.
3) The chain bo is supported by track and can prolong the service life of screen deck by not touching it.
4) The towline extractor is driven by world leading double-shaft hydraulic motor, with balance force, reliable operation and less maintenance cost.
5) Specialty suitable for the extraction of high oil and high power materials, and better immersion effect can be expected for ordinary oil plants.
Main Economic and Technical Parameters of Towline extractor (take 500T/D as an example)
Steam consumption |
280kg/t (soybean) |
Power consumption |
installed capacity 320KW |
Solvent consumption |
4kg/t (No.6 solvent) |
Residual oil in meal |
1.0% |
Moisture in meal |
12~13% (adjustable) |
Solvent in meal |
500ppm |
Urase activity |
0.05-0.25 (soybean meal) |
Total volatile matter |
0.3% |
Residual solvent |
300ppm |
Mechanical impurities |
0.2% |
Wet Meal Desolventizing Process for soybean oil extraction plant
Desolventizer toaster advantages:
a) Passivate and damage the anti-nutritional components such as the urea enzyme and trypsin in the meal, and improve meal value in use.
b) Control the protein denaturation degree in the meal , and improve the NSI inde effectively.
c) It can better regulate the color, flavor and taste of the meal.
d) It can better reduce residual solvent in the meal and regulate the meal moisture, so as to guarantee the minimum solvent consumption and safe use of the meal.
Negative pressure evaporation process for soybean oil extraction plant
The liquid from the extractor is the miscella containing grease and oil, which can be separated out according their different vaporization temperatures. Our company mainly uses vacuum evaporation technoloLD, and it can reduce solvent leakage and consumption. The separated solvent vapour is cooled and recycled back to the extractor for reuse, which can improve the solvent efficiency.
Vacuum Evaporation Advantages for soybean oil extraction plant
a) Vacuum evaporation features high efficiency, thorough desolvation and low solvent consumption in crude oil.
b) Use the second steam of desolventizer toaster and remaining steam from steam jet pump as the heat source of the first steam, which can save enerLD, reduce the condenser configuration area and save investment.
c) Due to the low temperature of the steam, the crude oil features ligLD color, good quality and low residual solvent.
Solvent condensation & recovery process for soybean oil extraction plant
Solvent condensation system combines with evaporation system closely, and evaporative condenser and steam stripping condenser all work under negative pressure. Non-condensable gas enters the enerLD saver from the shell of the first evaporator. In enerLD saver, noncondensable gas echanges heat with condensate from the evaporative condenser. Finally, the condensate temperature discharged from enerLD saver is increased, and the solvent separated from water goes to solvent holdin
g tank. The high temperature makes it unnecessary to be reheated for the recycling, so as to save enerLD. Noncondensable gas from enerLD saver enters desolventizing condenser, in which a great deal of gas is condensed, and the tail gas is discharged into the final condenser. The solvent gas from the extractor enters extraction condenser, and the noncondensable tail gas enters the final condenser. For the free gas in final condenser, diversion bo, holding tank, underground solvent library and miscella tank, cool them with low temperatured cold water to recycle most of solvent gas. The tail gas with little solvent goes to paraffin recovery process.
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