A.W. Chesterton
INDUSTRIES
My Chesterton
 »  Home
Hide Left Menu Hide Process Description Hide Process Image Hide Process Products

 

Evaporation


Evaporation Process: During the washing of the pulped wood chips, the weak black liquor is removed from the digester.  Due to the high water content, it is of little value as a fuel as it will not burn.  In order to process black liquor, the solids must be concentrated from 14% to 80% before a burnable waste is produced.  The concentration of black liquor is accomplished by evaporation. A series of heat exchangers or evaporators operating under vacuum is used to evaporate water from the liquor. Steam is used as the heating medium and introduced into the last stage evaporator and moves towards the first stage unit. Liquor flows in the opposite direction. A typical multiple-effect evaporator system consists of 6 evaporator vessels or effects. Concentrated liquor at 60% solids or higher is typically recovered at the end of the last effect.  Further concentration to a burnable solids concentration of 80% takes place in a separate evaporating vessel called a “concentrator”. When concentrated to 80%, the “heavy black liquor” has a fuel value that is similar to a medium grade coal. After the second evaporator, when the black liquor has reached at least 20% solids it is settled in tanks to allow wood oil soaps, resins and alcohols extracted from the wood chips to separate out.  The tall oil soaps are subjected to a process to recover sodium and are then sold as an additive for industrial lubricants.

During the washing of the pulped wood chips, the weak black liquor is removed from the digester. Due to the high water content, it is of little value as a fuel as it will not burn. In order to process black liquor, the solids must be concentrated from 14% to 80% before a burnable waste is produced. The concentration of black liquor is accomplished by evaporation. A series of heat exchangers or evaporators operating under vacuum is used to evaporate water from the liquor. Steam is used as the heating medium and introduced into the last stage evaporator and moves towards the first stage unit. Liquor flows in the opposite direction. A typical multiple-effect evaporator system consists of 6 evaporator vessels or effects. Concentrated liquor at 60% solids or higher is typically recovered at the end of the last effect. Further concentration to a burnable solids concentration of 80% takes place in a separate evaporating vessel called a “concentrator”. When concentrated to 80%, the “heavy black liquor” has a fuel value that is similar to a medium grade coal. After the second evaporator, when the black liquor has reached at least 20% solids it is settled in tanks to allow wood oil soaps, resins and alcohols extracted from the wood chips to separate out. The tall oil soaps are subjected to a process to recover sodium and are then sold as an additive for industrial lubricants.  
Locate a dist
Tech support / Request Price
Process Related Products
ARC Composites
Use Product Description
Black Liquor Evaporators ARC S3  
chemical containment ARC CS2  
chemical containment ARC CS4  
Chemical Process Pumps ARC 858  
Chemical Process Pumps ARC 982  
Chemical Process Pumps ARC S3  
Mechanical Packing
Use Product Description
Black Liquor Pumps 1760 Packing  
Black Liquor Pumps 1830 Packing  
Chemical Process Pumps 1730 Mill Pack™  
Chemical Process Pumps 1830 Packing  
Condensate Pump 477-1T Pump Packing  
Mechanical Seals
Use Product Description
Black Liquor Pumps 280 Use TC/TC-TC/CB - EP with Plan 53/54 
Black Liquor Pumps S20 Dual Cassette Seal Use TC/TC-TC/CB - EP with Plan 33/53 
Water Pump S10 Cassette Seal Use SC/CB EP with Plan 11 
Technical Products
Use Product Description
Concrete 415 Concrete Sealer  
Equipment (all types) 740 Heavy Duty Rust Guard  
Structural Steel 752 Cold Galvanizing Compound  
Threaded assemblies 725 Nickel Anti-Seize Compound  
Process Related Product Case Histories
 
MSDS Locator |  Distributor Locator |  Employment Opportunities |  Contact Us |  Privacy Policy/Terms of Use |  Legal |  Events |  Training
Copyright © 1997 - 2008 A.W. Chesterton. All rights reserved.
link