Product Specifications
| Prod Model: |
1-100T/D |
| Markets: |
North America,South America,Eastern Europe,Southeast Asia,Africa,Oceania,Mid East,Eastern Asia,Western Europe |
| Cooking Oil Refinery Line: |
1-100t/D |
| Degumming Process: |
Remove Oil Dregs/Soaps in Oil |
| Decolorizing Process: |
Remove The Dark Color in Oil |
| Deodroizing Process: |
Remove Bad Smell in Oil |
| Fractionation Process: |
Separate Stearin and Olein |
| 60 Years Experience Manufacturer: |
Have Our Own Factory, Welcome to Visit |
| Professional Engineers: |
Many Successful Cases |
| Certification: |
CE ISO9001 SGS, etc |
Product Description
Degumming and pre-bleaching Section:
Special Degumming section
Remove solubility impurity in the crude oil is degumming process. Because phospholipid is main part of solubility impurity in the crude oil. In industry, degumming also is named to get rid of phospholipid. Before distilling process for physical refinery, remove solubility impurity is a very important step, it can reduce loss in the oil, increase oil quality.
The Crude oil filtered is pumped out from the Buffer Tank. Passing through dosing system, the oil enters into the Heat Exchanger to be Heated up to designed temperature 60º C. Then go into the mixer vessel for mixing with the the phosphoric aced added via the metering Pump. The mixture flow into the acid reacting vessel for reacting for 15-20 mins.
Then separate the gums and oil via one centrifuge. Oil is exchanging heat to 70 degrees and flow into the pre-bleaching process.
Data:
Phosphoric acid (80-85%) 0.05 - 0.2% of crude oil
Working time < 20 mins
Steam < 100kg/t crude oil
Pre-Decolorizer process
The oil degummed is pumped into the decolorizer, samely open the vacuum system to rise its temperature to remove off the moisture firstly.
The clay dosed flow into the mixing tank/clay and oil firstly, then inhaled into the decolorizer vessel with the vacuum condition, which mixing for 30 mins or so under the 110 degrees and vacuum condition, after cooling(the decolorizer vessel has the water coil for cooling oil), the temperature to 70 degrees or so, which flow into the leaf filter for remove off the clay and oil go to the next process.
Note: This process could remove out 40% red color/carotenoids, the more is removed out from the distilling process.
Data
P < 5ppm; Fe ion < 0.1ppm, Cu < 0.01 ppm
Distilling process
Pump the oil decolorized into the distilling vessel in the high vacuum, and 240 degrees-260degrees oil temperature, to distillate for 4hrs.
The FFA would be remove out with the direct steams.
The final oil is out after exchanging between hot oil distilled and oil decolorized.
Note: This process is not only remove out the FFA, but also odor and most of red color / Hot sensitive decolorization.
Fractionation of oils and fats process
Dry fractionation of oils and fats is the separation of high-melting triglycerides from low-melting triglycerides by crystallization from the melt. Apart from blending, it is the cheapest process in oils and fats processing. It is a pure physical process compared to other chemical modification processes such as hydrogenation and interesterification which modify triglycerides. Dry fractionation is now applied to many kinds of fats: Palm oil, anhydrous milk fat, tallow, fish oil, lard, cottonseed oil, sunflower seed oil, palm kernel oil, tallow butter fats, and special fats.
The most important applications are: Palm olein used extensively as frying oil, palm super olein as salad oil and frying oil, the palm-MID fraction as component of cocoa butter equivalent, palm kernel stearin as cocoa butter substitute, anhydrous milk fat fractions for bakery and confectionery products, spreadable butter, tallow olein for frying oil and spreads. In this process, the fat is melted and heated to eliminate any crystal memory. The molten fat is cooled down under controlled agitation and cooling conditions to produce crystals nuclei formed by the higher melting triglycerides. Then, nuclei will grow to form crystals of the desired size. When the crystallisation has progressed far enough, the slurry is separated.
The final oil could be separated into 18 degrees, 24degrees, 33degrees according to melting degrees.
| No. | Name | Model | Q'Ty (Set) | Power
(KW) | Note |
|
| Degumming Process |
| P101 | Gear pump | KCB83.3 | 1 | 1.5 | Flux 5t/h,lift 6m |
| Flow meter | LZD40 | 1 |
| Glass steel |
| FI101 | Bag filter | DL50 | 2 |
| Materials Q235, with 1 set filter cloths and pressure gauge. |
| T101 | Refining Vessel | YLG160 | 1 | 2.2/4 | 2.5t/Batch, Dia.1.6 m. Φ38 coil with adjust-speed gear motor.Materials Q235 |
| V102 | Hot water Tank | Φ60 | 1 |
| Materials Q235,3mm thickness, with coil |
| Decolorization Process |
| T102 | Decolorizer Vessel | TSGΦ160 | 1 | 3 | Materials Q235,2.5t/Batch, Dia.1.6 m. Φ38 coil with adjust-speed gear motor |
| T106 | Soapsuds Catcher | Φ50 | 1 |
| Materials Q235,3mm thickness |
| T107 | Soapsuds Storer | Φ30 | 1 |
| Materials Q235,3mm thickness |
| V109 | Clay Tank | Φ50 | 1 |
| Materials Q235,3mm thickness |
| X101a | Clay Filter | BT-500 | 1 | 1.5 | 500*500mm, 24 pcs plates, with 1 set filter cloths and pressure gauge. |
| V104 | Bleached oil tank | 2.5*1.5*1.2m | 1 |
| 3tons, 3mm thickness |
| Distilling /Deodorizer Process |
| T103a | Distilling Vessel | TCG160 | 1 | SS304 | 2.5t/Batch, Dia.1.6 m. Height with 3 m, Φ38 double coil |
| T103b | Water pump | 80D12*4 | 1 | 4 | Flux 32m3/h,lift 40m |
| X101b | Safe filter | AF-30 | 1 |
| Bag filter, Φ0.3m,stainless steel |
| P103 | Product Oil Pump | KCB-83.3 | 1 | 2.2 | Flux-5t/h,suction-5m |
| T104 | Heat exchanger | Φ150 | 1 |
| deodorized oil and decolorized oil heat exchanger,Materials Q235, 6mm thickness |
| Matched Equipment Inside Workshop |
| P102 | Screw Pump | G35/1 | 1 | 3 | Flux-8t/h, suction-50m |
| P101a-e | Oil Pump | KCB-83.3 | 3 | 1.5 | Flux-5t/h, suction-6m |
| F102 | Control power box | DK-5 | 1 |
| Control the whole electrical motors |
| P105a,b | Water Pump | TPW32/160 | 2 | 1.5 | Flux-5m3/h,lift-30m |
| Energy System |
| C102b | Vacuum system | Vacuum steam Jet pump /IVZP(8/20) | 1 |
| With the steam for producing the vacuum for distilling system |
| P106b | Water Pump | TPW65/125 | 1 | 4 | Flux 30m3/h, lift 17m |
| P107 | Water Pump | TPW80/125 | 1 | 5.5 | Flux 60m3/h, lift 17m |
| Compressed Air System |
| K01 | Air compressor | 2V/1.2/10 | 1 | 5.5 | Supply for the air for clearing the filter cake of the filter cloth |
| K02 | Air tank | 0.27 cube | 1 | Φ300*1.2m, 3mm thickness steel plate |
| Public Parts |
| Transfer hot oil furnace | RD20C | 1 | Supply for the high temperature energy to the system. |
| Transfer hot oil pump | RY40/25 | 3 | 2.2kw; Flux 10m3/h, lift 28m |
| T205 | Cooling water tower |
| 1 | 1.5kw; Flux 50m3/h |
| F102 | Power box | KZX 5 | 1 | Control the electrical motors |
| Total |
|
| 45.3kw |
The company is a professional manufacturer specialized in production of oil pressing machines under the Ministry of Machinery Industry of the State.
Now we have and develop the main products:
Vegetable oil machine;
Biodiesel oil machine;
Biomass machine;
Flour mill machine and line, etc.
Its products have been well sold to nearly 40 states and areas both home, enjoying a high reputation, which have got the first of the similar products in 1999 and passed ISO9001 in Jan., 2000.
We have the special exporting company, also to find the others'product according to the inquires of clients!
