Low residual oil in the cake sunflower oil press

Introduction
Low residual oil in the cake sunflower oil press is suitable for the normal pressure/micropressure/water decoction/warm maceration/hot reflux forced circulation/permeation extraction & concentration,organic solvent recovery concentration and other processes in Chinese traditional medicine, health products, biological, pharmaceutical, cosmetic and food industries.This is the ideal equipment for Shandong Leader Machinery Co.,ltd., research institutes,research and development departments and laboratories of enterprises and institutions,and many varieties,small batch production of pharmaceutical plant.

Low residual oil in the cake sunflower oil press

Company Information

LD chemical engineering equipment co,. Ltd is mainly focused on all kinds of pressure vessel and edible oil processing machine manufacturing. Established in 1978, With rich experience in this field which make us to be the goLDn supplier on alibaba and the sales volume is always in the top within the industry. Now we have more than 300 workers, fixed assets have reached 90000 thousands. We rewarded ISO9001, which is the manufacture license of special equipment certification, and design license of special equipment certification. Our seller is oil machinery. We produce the complete oil production line, ranging from small scale screw oil press machine to the Turn-key project. Our products and project have been exported to many countries, such as Asia, America, Middle east, Africa, Europe etc.

WHY Choose us

1,Over 25 years experience in oil pressing equipment field, ranking first in LD,China.

2, Cooperate with LD Machine Design Research Institute and LD 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,LD Desolventizer with most advanced technology in solvent extraction section .

5, Automatic Contorl System with PLC.

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, LD 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 making and dewaxing turn-key project
6.10-200T/D Fatty acid esterification production cooking oil production line.

7.30-300T/D palm oil pressing line.

8.100-300T/D Coconut, peanut, sesame oil making project.

9.100-300T/D Coconut, peanut, sesame oil making project.

Available oil crops

Soybean, Palm, Palm kernel, Rice bran, Sunflower seed, Corn germ, Castor seed, Groundnut, Rapeseed, Copra, Almond, Sesame, Cotton seeds, Mustard seed, Pine nut, Shea nut, Grape seed, Tea seed, etc.

The techmology of my company for pretreatment and pre-pressing which mainly include the cleaning , decrustation extrusion,flaking,cooking and pre-pressing and so on .Considering the different characteristic of oil seeds and the customer requirements,we can provide you the special design,in order to adjust the oilseed to the optimun state ,which will improve the oil yield and the cake quality.

Pretreatment process feature:

1) Different combinations of process can process various oil plants in one workshop.

2) Use special intensified pretreatment technology for aroma peanut oil to make it more aroma.

3) Adopt advanced and reliable shelling technology to meet higher requirements for protein content in meal.

4) Extrusion treatment is used for raw materials with hard extraction, large-sized powder, and large capacity, which can reduce residual oil and solvent consumption, and increase the capacity by 50-80%.

5) The new technology of shelling and low-temperature treatment can ensure high protein and least denaturation.

1.Sunflower pretreatment flow chart:

Cleaning→Shelling→Flaking→Cooking→Pre-press

Main process description:

Vibration cleaning sieve

Flaking Mill

Cooking machine

Process feature:

Pretreatment process feature:

1) Different combinations of process can process various oil plants in one workshop.

2) Use special intensified pretreatment technology for aroma peanut oil to make it more aroma.

3) Adopt advanced and reliable shelling technology to meet higher requirements for protein content in meal.

4) Extrusion treatment is used for raw materials with hard extraction, large-sized powder, and large capacity, which can reduce residual oil and solvent consumption, and increase the capacity by 50-80%.

5) The new technology of shelling and low-temperature treatment can ensure high protein and least denaturation.

Economic and technical parameters

Steam consumption:Soybean≤90kg/t Materials(Soybean moisture12%,Temperature:20°C)

Power consumption:365.95KW(Installed power)

Soybean extrusion cake quality:

Moisture ≤10%

Temperature 55°C~60°C

Oil content 19-24%

2.Extraction flow chart

Material embryos→Extraction→Wet meal→Evaporation→Cooling→Product meal packing

↓

Mixed oil→Filter→Negative pressure evaporation → Crude oil

↓

Solvent recovery

Negative pressure evaporation advantages:

• Vacuum evaporation features high efficiency, thorough de-solvation and low solvent consumption in crude oil.

• 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 energy, reduce the condenser configuration area and save investment.

• Due to the low temperature of the steam, the crude oil features light color, good quality and low residual solvent.

Main economic and technical parameters:

3. Crude oil Refining

Continuous Oil Refining Process Introduction

Alkali hot water

Crude oil→filter→mix→reactor→mix→reactor→centrifugal separation→oil residue

↑ ↓

Phosphoric acid hot water→mix ↓

↓ ↓

degumming oil←cooler←dry←centrifuge separation←mix←alkali liquor

↓ ↓

↓ vacuum steam jet pump← steam citric acid

↓ ↓ ↓

↓ ↓ ↓

bleaching earth→mix→decoloring→filter→decoloring oil→ mix→ heat

↓

refined oil←filter←cool←deodorizing←vacuum

Oil Refining Workshop inside

3T/D oil refinig 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.

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%.

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.

Low residual oil in the cake sunflower oil press Features
v High efficiency: On the basis of original single vertebral and oblique vertebral structure,this device optimizes the product structure and integrates the concentration equipment to have the function of extraction,concentrate and organic solvent recovery.This device can do the hot reflux recycle extraction and concentrate,normal extracion and concentrate etc,simplifying the operation procedures,make the extraction,filtration,concentrate,condensation and other production processes completed in one step,greatly saved the material and extraction time.Working efficiency has improved by 20~35% compared with the general extraction machine.

AAA1

Low residual oil in the cake sunflower oil pressv High conversion rate: During the extraction process, the hot solvent (water or alcohol) is added to the material continuously,the solvent from top to bottom pass through the material dissolved the active ingredient,so that the active ingredients in the material liquid is increased by more than 1 times than the average extraction.

AAA2

If you have any demand about microwave drying equipment and edible oil refining equipment, pls feel free contact us any time.

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