解决方案

Olive Pomace Oil Extraction Line

The olive pomace after extraction of the virgin oil by centrifugation still contains a large amount of water and a small amount of oil. Usually about 3%-5% of the pomace oil can be recovered with the solvent extraction and subsequent refining process.Suitable materials: olive pomace, sunflower cake, soybean cake, cotton seeds cake, rice bran etc.

Description

Rotocel

Solvent extraction and stripping is the core step of the entire process. Generally, Rotocel is widely used in the extraction plant with less than 600tpd capacity. According to different raw materials,solvent extraction generally includes the following sections: (1) feeding scraper (2)rotocel (3) D.T.D.C (4) Evaporation condensation.

1. Feed scraper : It is required to effectively seal the material when it enters the leaching device to prevent the solvent gas in the leaching device from overflowing from the inlet.

2. Rotocel : Immerse the oil embryo (or pre-squeezed cake) in a selected solvent to dissolve the oil in the solvent (composed of a mixed oil), and then separate the mixed oil from the solid residue meal).

2.1. The loading amount is 80-85% of the material grid;

2.2. Solvent temperature 50 ~ 55 ° C;

2.3. The temperature of the immersion feed is 50-55 ° C, and the temperature of the leaching device is 50 ° C;

3. Desolventizer-toaster : The oil mash also contains a certain amount of solvent, which is dried after desolvation and drying treatment. The volatile solvent vapor still needs to be condensed and cooled during desolvent drying, and can be recycled.

In the first pre-de-layering of steaming off, the temperature is controlled at 75 ° C, the second layer is 85 ° C, the third layer and the de-dissolving layer are controlled at 105 ° C, and the level of the evaporating layer is 1000 - 1100mm, too low direct steam blowing through the material layer, can not reach the purpose of steaming off, and at the same time, due to the low storage height, the desolvent layer can not achieve a good material sealing effect when the material layer is controlled by the height of the material layer, so that the solvent gas is from Press out the mouth to increase the dissolution.

4. Evaporation condensation : The oil mash also contains a certain amount of solvent, which is dried after desolvent drying treatment. The volatile solvent vapor still needs to be condensed and cooled during desolvent drying, and can be recycled.

Process Drawing

Olive Pomace Oil Extraction Line

Equipment Selection

Model

Grid diameter

Grid height

Grid qty

Capacity

Speed

Power

SLD-JP-280

Φ2800mm

160cm

16

30t/d

90-120RPM

1.5kw

SLD-JP-360

Φ3600mm

200cm

16

50t/d

90-120RPM

2.2kw

SLD-JP-420

Φ4200mm

200cm

18

80t/d

90-120RPM

2.2kw

SLD-JP-480

Φ4800mm

250cm

18

100t/d

90-120RPM

2.2kw

SLD-JP-600

Φ6000mm

250cm

18

200t/d

90-120RPM

3.0kw

SLD-JP-660

Φ6600mm

250cm

18

300t/d

90-120RPM

4.0kw

SLD-JP-740

Φ7400mm

250cm

18

400t/d

90-120RPM

4.0kw

SLD-JP-900

Φ9000mm

250cm

18

600t/d

90-120RPM

4.0kw

 

Comparison of technical parameters of negative pressure evaporation and atmospheric pressure evaporation

 

1st Evaporation outlet oil

2nd Evaporation outlet oil

Stripping outlet oil

Cude Oil  

Temp.

Density

Vacuum

Temp.

Density

Vacuum

Temp.

Density

Vacuum

Solvent

75-80

60-70%

 

95-100

95-98%

 

115-120

 

 

500ppm

55

70-75%

40kpa

95-100

90-95%

60kpa

100-105

99.5%

70kpa

30-50ppm

 

Inquiry

Please Feel free to give your inquiry in the form below. We will reply you in 24 hours.

  • *
  • *
+86-15637149728
ewans@sld-topoilsolution.com
8615637149728