Small scale palm oil refining machinery for 1-80 TPLDhe 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.
Small scale palm oil refining machinery for 1-80 TPH
The process before oil refining is extraction,oil leaching is advantageous to oil refining.
Leaching is divided into three types :
1. Towline extractor : The amount of processing is 7000T/D .
2. Ring extractor : The amount of processing is 3000T/D.
3.Rotocel extractor: The amount of processing is 1500T/D.
The towline extractor working principle of leaching :
1. After pretreatment of the oil into the leaching, solvent (n-hexane) will be sprayed on the surface of the oil in the oil, most of the oil will be solvent extraction.
The oil concentration of the first funnel is relatively high, generally 60%-65%. Oil is directly pumped.
2. Oil after the second funnel, solvent will again sprayed on oil, again leaching, oil concentration and mixed oil obtained by solvent content is lower, more and more high.
3. Oil is shipped out extractor.
After leaching will get two products :
1. Mixed oil (oil and solvent) : Mixed oil first enters the first evaporation equipment, steam enters from the equipment below, mixed oil and steam full contact. The first evaporation in 0.006-0.08Mpa negative condition. The oil temperature is 105-110 C. Then enter the second evaporation, the same process.
2. The cake containing solvents : Solvent containing cake steamed into the offline, two layers of steaming offline is preparing to break free, full and cake contact, indirect heating of cake, then is Breathable layer -- desolventizing layer -- drying layer -- cooling layer
The last step leaching :
Steamed out of the solvent into the condenser for cooling, cannot be condensed gas into paraffin recovery system, and then enters the analytical column to paraffin absorption solvents, gas separation.
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