Product Details

Low residual oil rate in the cake sunflower oil expeller line

Place of Origin Shandong, China (Mainland)
Brand Name MJ
Certification ISO 9001 ,CE,BV, ISO
Model Number Cotton Seed Oil Extraction Machine
Min.Order Quantity 1 set
Price Cotton Seed Oil Extraction Machine
Packaging Details standard package
Delivery Time contact with us
Payment Terms T/T,Western Union
Supply Ability Expeller Pressed Machine

Product Features

Shandong Leader Machinery Co.,ltd. supply different capacities for different Low residual oil rate in the cake sunflower oil expeller line needs. Below is the main technical data of our main mini crude oil refinery. It's designed to process a very wide range of vegetable oils, including cottonseed oil, rice bran oil, sunflower seed oil, soya oil, palm oil, palm kernel oil. In addition to vegetable oil, it is also efficient for animal oils and fats, such as fish oil, seal oil and more.

Low residual oil rate in the cake sunflower oil expeller line

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 30 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 the 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 project.

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

9. Screw oil press machine, Hydraulic oil press machine for different capacity.

Available oil crops

Product Description

Pretreatment flow chart for Sunflower oil

Cleaning→Shelling→Softening→Flaking→Cooking→Prepressing

Flaking machine

Solvent Extraction Flow chart for Sunflower oil

Rotocel Extractor

Main Parameters

Residual oil in meal

≤1% (Peanut)

Solvent consumption

≤3Kg/T(6#solvent oil)

Crude oil moisture and volatile matter

≤ 0.30%

Power consumption

≤ 15KWh/T

Steam consumption

≤280Kg/T (0.8MPa)

Finished meal moisture

≤ 10-13% (adjustable)

Residual solvent in finished meal

≤ 300PPM (qualified detonated experiment

The advantage of LD desolventizer1, Passivate and destruct the anti-nutrition in the meal, such as the urease and the trypsin,improve the use value of the meal.2, Control the protein denaturation degree of the meal, effectively improve the meal’s NSI index3, To adjust the color, flavor and granularity of the meal.4, To reduce the residual solvent in the meal, adjust the moisture of the meal, to ensure the lowest solvent consumption and safe use of meal in production.


Refining flow chart for Sunflower 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

Process characteristics of 3T/D edible 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

3~5

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%) , when particles appear, add alkali, then continue to stir for 40 ~ 50 minutes and heat up to be 90 ~ 95 ℃ until soap 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

3T/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

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 %

Workshop

Packaging & Shipping

Laboratory

Approvals

Contact Information

*Description of Low residual oil rate in the cake sunflower oil expeller line
Low residual oil rate in the cake sunflower oil expeller line is screw-driven oil making machine that used to extract oil from seeds and kernels for edible purposes.Shandong Leader Machinery Co.,ltd. series cooking oil making machine price is an advanced oil seed processing machine, characterized by their high oil output rate, good quality,simple design,easy and continuous operation. It can be used to process various oil seeds, such as rape seeds, peanut soybean,sesame, sunflower seed, copra, vegetable seeds.

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2.low residual oil rate in the cake sunflower oil expeller line features
1. Low residual oil rate in the cake sunflower oil expeller line use advanced production technology, adopt panasonic magnetron, long life, effect;
2. adopt stainless steel, compact structure,no energy dissipation, save energy;
3. tunnle type design, fast drying, cover small area;
4.drying and sterilizing simultaneously,one equipment has many usages.
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low residual oil rate in the cake sunflower oil expeller line advantages
*Cast iron machine base.
*High Manganese steel.
* Special gear box structure make the rotating speed averagely.
*Compact structure,stable function,simple maintenance.
* Vegetable oil seeds, soybeans, peanuts, cotton seeds, sesame seeds, palm kernel, coconut etc

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

LD Miss Candy
Skype: leaderfoodmachine9
Mobile: +86 18363700691 (Also WhatsApp & Wechat)
Email: sales9@ldfoodmachine.com

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