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Packed Methanol Distillation Column Low Operating Pressures With Theoretical Plate

Packed Methanol Distillation Column Low Operating Pressures With Theoretical Plate

Packed Methanol Distillation Column Low Operating Pressures With Theoretical Plate
Packed Methanol Distillation Column Low Operating Pressures With Theoretical Plate Packed Methanol Distillation Column Low Operating Pressures With Theoretical Plate Packed Methanol Distillation Column Low Operating Pressures With Theoretical Plate

Large Image :  Packed Methanol Distillation Column Low Operating Pressures With Theoretical Plate Get Best Price

Product Details:

Place of Origin: CHINA
Brand Name: DEA
Certification: UL
Model Number: JZ-50

Payment & Shipping Terms:

Minimum Order Quantity: 1 Set
Price: negotiation
Packaging Details: Packed in wooden case
Delivery Time: 6-8 weeks
Payment Terms: T/T
Supply Ability: 10 Sets per Month
Detailed Product Description
Material: Stainless Steel 304/S316L Column Size: DN50*800-1600mm
Reboiler: 20L~30L Receiver Size&quantity: 10L*2
Distillation Column Type: Packed Tower Theoretical Plate: 10-20
High Light:

lab distillation column

,

fractional distillation tower

1.1 KW Vacuity Distillation Column for CBD / THC / Hemp oil / Cannabissativa

 

——Particular features

Continuous distillation process.
Low operating pressures (100~10000Pa ,100Pa=1mbar).
Short residence time.
High evaporation rates.
Processing of high-boiling, high-viscosity or crystallizing products is possible.
Can be used as a reboiler for column.
Low fouling on evaporator wall.

 

Type JZ-50
Material stainless steel 304/S316L

Distillation column type

packed tower

Theoretical plate

10-20
Temperature Room temp~200/300 ℃(depend on the oil heater)
Column size DN50*800-1600mm
Reboiler 20L~30L
Receiver
size&quantity
10L*2
Condenser HTA 0.86 (m2)
Vacuity MIN:0.5mbar(depend on the nature of material and vacuum pump&vacuum pump not included)
Floor area length*width*height=1000*800*2500-3300 (mm)
Power 1.1KW(without pump) 
Voltage 220V-60HZ
Warranty 12 Month

 

The various components of crude oil have different sizes, weights and boiling temperatures; so, the first step is to separate these components. Because they have different boiling temperatures, they can be separated easily by a process called fractional distillation. The steps of fractional distillation are as follows:

 

You heat the mixture of two or more substances (liquids) with different boiling points to a high temperature. Heating is usually done with high pressure steam to temperatures of about 1112 degrees Fahrenheit / 600 degrees Celsius.

The mixture boils, forming vapor (gases); most substances go into the vapor phase.

The vapor enters the bottom of a long column (fractional distillation column) that is filled with trays or plates. The trays have many holes or bubble caps (like a loosened cap on a soda bottle) in them to allow the vapor to pass through. They increase the contact time between the vapor and the liquids in the column and help to collect liquids that form at various heights in the Distillation Column. There is a temperature difference across the Distillation Column (hot at the bottom, cool at the top).

The vapor rises in the column.

As the vapor rises through the trays in the Distillation Column, it cools.

When a substance in the vapor reaches a height where the temperature of the column is equal to that substance's boiling point, it will condense to form a liquid. (The substance with the lowest boiling point will condense at the highest point in the column; substances with higher boiling points will condense lower in the column.).

The trays collect the various liquid fractions.

The collected liquid fractions may pass to condensers, which cool them further, and then go to storage tanks, or they may go to other areas for further chemical processing

Fractional distillation is useful for separating a mixture of substances with narrow differences in boiling points, and is the most important step in the refining process.

This content is not compatible on Distillation Column.

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