Extruder Oil Press Oil Extracting Press Soy Bean Oil Press Flaxseed Oil Press Machine Mini Crude Oil Refinery

Extruder Oil Press Oil Extracting Press Soy Bean Oil Press Flaxseed Oil Press Machine Mini Crude Oil Refinery

extruder oil press oil extracting press  soy bean oil push flaxseed oil push device Mini Crude Oil Refinery

Solution Description

1.Compendium

Use rational refiner technologies, a tiny investment decision, straightforward operation. According to the top quality of cake, adjust technological parameter, a lot of kinds of oil grade can bu produced.
2.Scope and uncooked substance
Scope:5T/D Palm Oil Refinery Line 
Raw substance:

Acid(HOKmmg/g) :< 15.0
Impurity(%) :≤ two.
Humidity and volatile(%) :≤2.
three. Prepare: Finished oil comply the Chinese CZPT
four.CZPT focus on
CZPTtric intake:< 24 kw·h/t oil 
Cycle Water consumption: < 15m3/t oil
Gentle drinking water :< 180kg/t oil
 Accessory usage:Clay < 3%, phosphoric acid <0.2%
Refiner intake
L%=1- refining generate% has relation with top quality of impolite oil and acid price.
five.Description of the Procedure.

five.2. Description of primary Procedure
The crude palm oil has significantly less hydratable & non-hydratable phosphoric acid and substantial FFA. So the line is adopted the physical refining approach, which is not only much much more affordable and successful than chemical refining, but also leads to no air pollution by means of waste h2o and exhaust air.

Degumming and Pre-bleaching Part:
Unique Degumming Section
Eliminate solubility impurity in the crude oil is degumming procedure. Simply because phosphoric acid is major portion of solubility impurity in the crude oil. In industry, degumming also is named to get rid of phosphoric acid. Before distilling method for actual physical refinery, take away solubility impurity is a quite crucial action, it can reduce loss in the oil, increase oil quality.
The Crude oil filtered is pumped out from the Buffer Tank. Passing via dosing program, the oil enters into the Heat Exchanger to be Heated up to made temperature 60ºC. Then go into the mixer vessel for mixing with the the phosphoric aced additional via the metering Pump. The combination flow into the acid reacting vessel for reacting for fifteen-20mins. 
Then separate the gums and oil by means of a single centrifuge. Oil is exchanging warmth to 70 degrees and movement into the pre-bleaching process.
Information: 
Phosphoric acid (eighty-eighty five%) .05 – .2% of crude oil
Doing work time < 20mins
Steam < 100kg/t crude oil 

Pre-Decolorizer Method 
the oil degummed is pumped into the decolorizer, samely open up the vacuum system to increase its temperature to remove off the humidity first of all. 
The clay dosed movement into the mixing tank/clay and oil firstly,, then inhaled into the decolorizer vessel with the vacuum problem, which mixing for 30mins or so below the 110 degrees and vacuum situation, following cooling(the decolorizer vessel has the h2o coil for cooling oil), the temperature to 70 degrees or so, which movement into the leaf filter for get rid of off the clay and oil go to the next method. 
Note: This approach could get rid of out forty% purple colour/carotenoids, the a lot more is eliminated out from the distilling procedure.
Information: P < 5ppm,Fe ion < 0.1ppm, Cu < 0.01ppm
Distilling Method 
Pump the oil decolorized into the distilling vessel in the higher vacuum, and 240 levels -260degrees oil temperature, to distillate for 4hrs.
The FFA would be remove out with the direct steam. 
The ultimate oil is out after exchanging in between scorching oil distilled and oil decolorized.
Observe: This process is not only take away out the FFA, but also odor and most of purple colour / Very hot delicate decolorization.

Fractionation of oils and fats Procedure 
Dry fractionation of oils and fats is the separation of high-melting triglycerides from minimal-melting triglycerides by crystallization from the melt. Apart from mixing, it is the most inexpensive approach in oils and fat processing. It is a pure bodily method when compared to other chemical modification procedures such as hydrogenation and interesterification which modify triglycerides. Dry fractionation is now applied to a lot of types of fat: 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 critical apps are: palm olein employed thoroughly as frying oil, palm super olein as salad oil and frying oil, the palm-mid portion as ingredient of cocoa butter equivalent, palm kernel stearin as cocoa butter substitute, anhydrous milk excess fat fractions for bakery and confectionery products, spreadable butter, tallow olein for frying oil and spreads. In this method, the fat is melted and heated to eradicate any crystal memory. The molten unwanted fat is cooled down beneath controlled agitation and cooling problems to produce crystals nuclei fashioned by the increased melting triglycerides. Then, nuclei will increase to kind crystals of the desired dimensions. When the crystallisation has progressed far enough, the slurry is separated. 
The last oil could be separated into 18degrees, 24degrees, 33degrees in accordance to melting degrees.
Transmit very hot oil CZPT
The furnace is an natural and organic CZPT heating furnace with normal liquid oil for the medium the gasoline could be coal and diesel oil, waste oil. The hot temperature oil pump forcedly convey the sizzling oil recycle into the making use of method, recognize to transmit the heats indirectly from the furnace to making use of program. 
The critical is that the furnace is not high strain boiler, to reduce the inspecting price each and every calendar year.

Main Data: 

The electrical power of Supporting Heat

Working 

Temperature

Working Pressure

Valve of Pipe

Coal/wood 

Usage

Heat Efficiency

3*105kcal/h

≤340ºC

≤1MPa

80mm

69.5/100kg/h

≥70%

Vacuum Pump System

Steam and drinking water jet vacuum pump program for distilling technique.

Design

Max Force

Capability

Drinking water Pump

Steam Force

Steam Use

Recycling CZPT Drinking water Required

QSWJ-40

3mmHg

40m3/h

4kw

.3MPa

35kg/h

2.8t/h


Main Tasks Scope:

—–thirty-5000T/D cooking oil seeds pretreatment task
—–30-5000T/D cooking oil seeds extraction undertaking
—–ten-500T/D crude cooking oil refining machine 
—- 5-200T/D crude oil mill refinery machine 

—-ten-2000T/D edible oil refining machine 

—-1-200T/D mini cooking oil mill plant

Our Services

CZPT & CZPT

Firm Info

ZheJiang Double CZPTs CZPTry I/E CO.,LTD

A professional collection of research ,style, production and sales of Oil producing machine,animal food device ,extruder machine for pet and treats,and several other type of meals device.

Our company has a big manufacturing factory with 40 years rich experiences based on one CZPT machinery started by our government machinery department, we adopts advanced production technology, sophisticated equipment and have won abundant strength after many years of development accumulation. 

Our puffed machinery has won the 1999 best national evaluation,and passed the ISO 9001 CZPT CZPT Authentication in 2000.More proudly, we have achieved the CE certificate to convenient more CZPTean customers.

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CE&ISO Certification

Extruder Oil Press Oil Extracting Press Soy Bean Oil Press Flaxseed Oil Press Machine Mini Crude Oil Refinery