Ethanol Extraction Equipment

CannaBusiness
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1

Solvent storage tank

  1. Design pressure: Atmospheric pressure
  2. Volume: 200L
  3. Jacket working pressure：0.25MPa
  4. Manufacturing standard: steel welded atmospheric pressure vessel.
  5. Material SS304."

Low-Temperature Coolant Circulation Pump

  1. Capacity of water storage: 200L
  2. No-load minimum: -80℃
  3. Flow (L/min): 40L/min
  4. Temperature adjustment: Room temperature-80
  5. Rated power (W): 550W"

Centrifuge(Explosion proof )
Dry material: 10kg per batch, 2-3 batches per hour"
"Buffer tank
1.Design pressure: Atmospheric pressure
2.In-tank medium: Extracted liquid

Micropore filter

  1. Flow: 3T/h
  2. Outer Diameter of Import and Export
  3. Pipe: 38.1mm
  4. Working pressure: 0.05～0.6MPa"

Storage tank

  1. Design pressure: Atmospheric pressure
    2.Volume：150L
    3.Jacket design pressure：0.15MPa
  2. Manufacturing standard: steel welded atmospheric pressure vessel.
  3. Material SS304."

Single Effect Evaporator
Concentrate tank
Ethanol processing rate: 100L/H
Heater tube temperature: 117 ℃
Receiving tank volume: 200L
Cycle water consumption: 5T/h

Cooling tower
Cooling tower volume: 16.8m³/h

Product storageg tank
Volume: 200L
Design pressure: Atmospheric pressure
Jacket design pressure: 0.15MPa

Chiller (air cooling type)
Rated power (W): 9.5KW
No-load minimum: -5 ℃
Temperature adjustment: Room temperature -5 ℃
Flow (L/min) : 12 m³/h"

2

Do you know how much ethanol you lose per run?
Also do you know how much ethanol you reclaim per run?

3

Do you anticipate you would be fabricating a daisy chain where all fluid wetting parts are 316SS?

4

The whole system will lose 5% ethanol per run and 95% ethanol removal.

5

Yes, all fluid wetting parts are 316 SS.

1 Like
6

Are the solvent or storage tanks not SS304 or do you mean you have a complete SS316 option?

7

We have a complete SS316 option

8

EEE
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