Low Consumption Palm Oil Mill Making Machine
- Usage: Palm Oil
- Type: Cold & Hot Pressing Machine
- Automatic Grade: Semi-Automatic
- Production Capacity: 98%-100%
- Model Number: Qie-20
Low Consumption Palm Oil Mill Making Machine Description
Palm Oil Mill Processs
Pretreatment flow chart for Palm oil
Palm fruit bunch → Sterilization → Threshing → Digesting → Oil press → Clarification → Shell and Kernel recovery
Palm kernel pressing machine
The processing technology parameter:
| Capacity : | 5TPH | Oil extraction rates : | 21~23% |
| Oil content in FFB : | ≥24% | Kernel content in FFB: | 6% |
| Shell content in FFB : | ≥6~7% | Fiber content in FFB : | 12~15% |
| Empty bunch content in FFB: | 23% | Press cake proportion in FFB: | 24 % |
| Oil content in empty bunch: | 5 % | Moisture in empty bunch : | 63 % |
| Solid phase in empty bunch: | 32% | Oil content in press cake: | 6 % |
| Water content in press cake : | 40 % | Solid phase in press cake : | 54 % |
| Oil content in nut: | 0.08% | Oil content in wet meter heavy phase | 1% |
| Oil content on meter solid: | 3.5% | Oil content in final effluent: | 0.6% |
| Fruit in empty bunch: | 0.05% | Water in palm kernel | ≤7% |
| Kernel in empty bunches: | 0.05% | Kernel content in cyclone fiber: | 0.15% |
| Kernel content in LTDS: | 0.15% | Kernel content in dry shell: | 2% |
| Kernel content in wet shell: | 2.5% |
Crude palm oil standard:
| FFA : | ≤ 4 % |
| Moisture : | ≤0.1 % |
| Dirt: | ≤0.02 % |
Refining flow chart for palm oil
Main Paramaters
| Soft water consumption | ≤ 160Kg/H |
| Steam consumption | ≤ 300Kg/T oil |
| Bleaching earth | 1-3Kg/T oil |
| Power consumption | ≤ 22KWH/T oil |
| Fuel consumption | 10-20Kg/T oil |
| Oil content in waste white clay | ≤ 23% |
| Phosphoric consumption | 0.5-1Kg/T oil |
Palm oil fractionation technology
Palm oil fractionation technology developed by QIE Company is with advanced technology,full computer control system and low cost of investment. It is also with high liquid oil yield,high purity solid fat, high economic benefit, and other advantages etc. Palm oil fractionation technology is a new oil processing technology. Using palm oil fractionation technology can get 8°c,14°c,18°c,24°c,33°c,44°c,55°c etc,different melting point‘s palm oil product.At the same time,It can also be used to do cottonseed oil, fish oil,pork oil and other animal oils.This prominently improves the added value of the oil products, increases the economic benefit of enterprise.
Process characteristics of Palm oil refining equipment
Process description:
The whole process of intermittent refining:
Oil inlet→heating up→deacidification→dealkalizing→washing 2-3 times→dry dehydration. The total time is about 24 hours.
According to the difference of alkali thickness and oil temperature, the process of dealkalizing is divided into two types, one is low temperature with thick alkali (its initial temperature is 20 ~ 30 ℃, alkali thickness is 20 ~ 30 Be) and another one is high temperature with light alkali (its initial temperature is 75 ℃, alkali thickness is 10 to 16 Be). The former is generally applied and the latter is mainly used for crude oil which has low acid value, light clour and lustre, and less impurity.
I. Low temperature with thick alkali:
Adjust the oil temperature to 20~30℃, then put in 20~30Be alkali liquor in 5~10 minutes, and stir it about 20~60 minutes on condition of 60r/m. Increasing the temperature slowly when notice the separate of neatsoap after reacted, 1℃ per minute, when it reach 60℃, stop stiring, keep still and make soap feet settlement, it will takes nearly 6~8 hours, then let out the soapstock.
Ⅱ. High temperature light alkali operation:
Firstly,determine the alkali thickness in accordance with the alkali value of crude oil(according to the table below), account the alkali and water added in, when the alkali value is under 5, for each unit acid value, the total water added into per ton oil is 23 kg. When the alkali value is over 5, no more than 12% of the oil heavy, the exceeded alkali is only 0.005~0.002%.
| Crude oil alkali value | <3 | 3~5 | 5~7 | 7~10 | >10 |
| Alkali thickness Be | 10 | 11 | 12 | 14 | 16 |
When operating, first mix the crude oil, heat the temperature to be 70 ~ 75 ℃ diluted saline or phosphoric acid (concentration 90%) < amount to 0.1% >, when particles appear, add alkali, then continue to stir for 40 ~ 50 minutes and heat up to be 90 ~ 95 ℃ until soap grain obviously separated, and put into nigre after 2 ~ 3 hours’ static.
Ⅲ. Washing:
After releasing the nigre, grease heated up to boom 90℃, then add in the hot water for washing, stirring. Water temperature should be about 5 ~ 10 ℃ higher than the oil temperature, for low water temperature tends to emulsification. After adding the water, continue to stir for 5 minutes, then rest 4 hours for precipitation, and release the soap water, wash 2 ~ 3 times depending on the oil quality and decide. Washed oil slowly heated up to 105℃, stirred dehydration for 1 hour, washed oil can also direct inhaled decoloring pot and vacuum drying 30 minutes.
Method of operate for descoloring
1 start the vacuum pump,vacuum degree ≥700mmHg
First, after washing of alkali refining inhaled decoloring pot, stirring, at the same time warming up to 90 ℃, and stir another 30 minutes, decrease moisture below 0.1%, then inhale a few decoloring agents “white earth, activated carbon >, the quantity depends on the oil color, generally, oil amount 2 ~ 4%, stirring 30 minutes, cooled to 70 ℃, use compressed air pressure to filter oil machines to separate the white earth and oil, then get decoloring oil.
Method of operate for deodorizating
l By vacuum pump oil bleaching inhaled deodorization pot, up to 755 mmHg in vacuum degree , begin distillation and deodorization timing;
l Deodorizating time : 4 Hours
l Deodorization temperature: 240℃/755mmHg~260℃/759mmHg
l Deodorization vacuum degree: above 755mmHg
l There is steam distillation during the whole timing process.
l After deodorization, shut off the direct steam in vacuum condition , close conduction oil,open the valve for cooling water.,until the oil temperature nearly 40~80 ℃,shut off the vacuum pump valve,make test of the oil sample,if it is passed inspection,packing and finish all the manufacturing of edible oil.
Characteristics
l Both short mixed and long mixed process are adapted in washing sector, which ensures washing effectiveness.
l Equipped with vertical leaf filter to remove used bentonite from the oil, operating conveniently and continuously, low laboring tense, keeps environment well, keeps oil residence in deposable bleaching earth in low level.
l Due to accurate stirring method, decreased the maximum distance between the oil of cooling facet so as to ensure the same temperature of crystal with same quality. Better guaranteed that in the process of crystallization, crystal will not cluster in a intense area.
l Flexible system, cooling curve can be easily altered by changing water temperature, thus the kinds of products can be changed easily.
The main economic technical parameters:
| Capacity T/D | 1-200T/D |
| Steam consumption | 900KG/T oil |
| Electric consumption: | 28Kwh/T oil |
| Water(soften water) | 150Kg/T oil |
| Phosphoric acid | 2~3 kg/T oil |
| Alkali | Acid valuex1-3kg/T oil |
| Circulating water cooling water yield | 150M3/H |
| Bleaching earth consumption | 3-5Kg/toil |
| Waste bleaching earth oil content | <25~35% |
| Refining losses | Acid valuex1.2(chemical refining) |
| acid valuex | 0.6(physics refining) |
| Bleaching losses | The quantity of bleaching earth×0.25% |
| Deodorization loss consumption | ≤0.5% |
| Refining rate | 1-refining consumption % |
WHY Choose us
1,Over 25 years experience in oil pressing equipment field, ranking first in Henan,China.
2, Cooperate with Henan Machine Design Research Institute and Henan University of Technology in the oil equipment, protein extraction, phospholipid extraction,etc. R&D and application of new technology.
3,Approval by CE Certificate, Quality Systerm Certificate, France BV Certificate, which guarantee the quality of the equipment.
4,DTDC Desolventizer with most advanced technology in solvent extraction section and Automatic Contorl System.
Main Technology
1,Pretreatment and Pre-pressing technology.
2,Solvent Extraction Technology.
3,Edible oil Refining Technology.
4,Dewaxing and Degreasing Technology.
5,Soybean protein concentrated and protein isolates Technology.
6,Peanut oil cold pressing and superfine fragrant peanut oil Technology.
7,Palm fruit pressing Technology.
8,Palm oil fractionation Technology.
Main Business Field
1.10-500T/H oil material first cleaning,drying and storage section turn-key project.
2.100-3000 T/D oil pretreatment, shelling and pre-press workshop turnkey project (soybean hot peeling, bean skin crushing; the soybean extrusion, high oil contained pre-press cake extrusion, and high oil contained embryos puffed; of direct puffed). Rice bran production line turn-key project.
3.Leaching workshop turnkey project (Towline extractor, Rotocel extractor, loop type extractor, DTDC separated machine, the full negative pressure evaporation, paraffin wax recovery, leaching workshop degum, phospholipid concentrate).
4.30-1000T/D oil continuous grade two or one physical (chemical) refining production line.
5.20-600T/D sunflower oil, rice bran oil, corn germ oil dewaxing turn-key project
6.10-200T/D Fatty acid esterification production cooking oil production line.
Technical parameters of Low Consumption Palm Oil Mill Making Machine
| Voltage | 220V/380V/440V |
| Power(W) | 15KW |
| Dimension(L*W*H) | 6000*700*5600mm |
| Weight | 3000KG, 1-30Tons |
| Certification | ISO9001/CE/BV |
| After-sales Service Provided | Engineers available to service Machine overseas |
| Raw material | Palm Fruit |
| Name | palm oil mill Bangladesh |
| Warranty | One Year |
| Character | Oil Processing Line |
| Advantage | Energy Saving |
| Common capacity(TPD) | 1-100THD |
| Material | Stainless Steel |
| Certificate | ISO9001/CE/BV |
| Export market | Global |
