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palm cake oil solvent extraction equipment
- Sunflower Seed Oil Plant Equipment
[email protected]
- Shandong
- CE,ISO9001
- 1 unit
- contact us
- Standard packing
- T/T,Western Union,L/C
- 50100 Set/Sets per Year depend on the requirements of the clients
- Heidi2020-07-10 09:46:19
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Product Details
Solvent consumption: | ≤ 2Kg/T (No.6 solvent oil) | color: | based on the requirements of clients | capacity: | depend on the need of clients |
Steam consumption: | ≤ 280KG/T (0.8MPa) | Finished meal moisture: | ≤ 13% (adjustable) | Crude oil moisture and volatile matter: | ≤ 0.30% |
Residual oil in meal: | ≤ 1% | certification: | BV,CE, ISO9001, etc... | Power consumption: | ≤ 15KWh/T |
condition: | new |
Product Description
Sunflower oil production line basic flow chart:oilseeds pretreatmentâpre-pressingâSolvent extractionâoil refining.Our engineer can design different process of sunflower oil extraction machinery, according to the different requirements and target price.
Leader Edible Oil Refining Processes Co., LTDcan configure design process sunflower seed oil extraction production line for the customer, under normal circuLDtances, process engineers will configure the latest technoloLD to customers depending on customer requirements and target price.
Specifications
Oil solvent extractor:Rotocel extractor
Wet meal toast-desolventizing,
Solvent condensing recovery,
Wax recovery.
palm cake oil Solvent extraction equipment
Rotocel Extraction
Process Features of LD Rotocel Extraction:
1. Adopt stainless steel fixed 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 extraction effect;
2. The rotocel extractor 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 extractor 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 extractor helps to form immersion extraction, reduce the meal quality in miscella, improve the quality of crude oil and reduce the evaporation system scaling.
6. Specially suitable for the extraction of various pre-pressed meals.
Main Economic and Technical Parameters of Rotocel Extractor (take 300T soybean extraction as an example)
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 |
â¤300PPM (qualified detonated experiment) |
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 box 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
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 index 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
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:
a) Vacuum evaporation features high efficiency, thorough de-solvation 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
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 exchanges 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 holding 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 box, 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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Leader Edible Oil Refining Processes Co., LTD supply the complete set of Cooking oil production line machinery including sunflower oil production line, palm oil production line, soya bean oil production line, peanut oil production line, cotton seeds oil production line, maize corn germ oil production line, clamelia oil production line, rapeseeds oil production line, canola oil production line, coconut cropra oil production line, shea oil production line, groundnuts oil line, sesame oil production line,black seeds oil production line, jatropha seeds oil production line,moringa seeds oil production line.
Welcome Contact us any time!
Contact:Heidi
Skype:heyabc
Tel:+86 15953125015(also Whatsapp)
Email:[email protected]
Leader Edible Oil Refining Processes Co., LTD is your LD choice!
Contact Us
- Leader Edible Oil Refining Processes
- Email[email protected]
- AddressNo3.Suihua Road,Gaoxin District.Jinan,CHINA
- Phone(Working Time)0531-85064681
- WhatsApp+15953125015
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