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CONTACT INFORMATION
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A. ENTERING CONDITIONS
  1. Liquid to be dried
  [List constituents of liquid and % of each. Indicate whether by volume, weight or mole %.]
*
  2. Molecular Weight of process liquid  
  3. Specific Gravity of process liquid  
  4. Specific Heat of process liquid [°F]  
  5. Vapor pressure of process liquid at inlet conditions  
  6. Viscosity of process liquid [cp]  
  7. Inlet Pressure of process liquid [psig] *
  8. Inlet Temperature of process liquid [°F] *
  9. Inlet Moisture Content of process liquid [ppm(wt) or #/hr] *

B. DESIRED OUTLET CONDITIONS
  10. Outlet Moisture Content [ppm(wt)] *
  11. If contaminants are to be removed, explain in the remarks section below.

C. OPERATING CYCLES
  12. Application is a batch process:
       A. Total amount of liquid to be dried [gal] *
       B. Total hours available for drying [hrs]  
       C. Total hours available for reactivation [hrs]  
  13. Application is a continuous process:
       A. Flow rate of liquid to be dried [gph]  
  Note: Minimum drying time on each tower is normally 8-hours, longer times may be necessary to perform all reactivation steps.

D. METHOD OF OPERATION DESIRED
  14. Manual Control  
  15. Semi-automatic Control (heater turnoff automatic)  
  16. Fully Automatic Control  
  17. Reactivation Heat Source  
  18. Once Through Open Loop Reactivation  
  19. Closed Loop Reactivation  

E. AVAILABLE PLANT UTILITIES
  20. Electric Current:
       A. Power Circuit [volts-ph-hz]  
       B. Control Circuit [volts-ph-hz]  
  21. Steam:
       A. Pressure [psig]  
       B. Temperature [°F]  
  22. Cooling Water:
       A. Pressure [psig]  
       B. Temperature [°F]  
  23. Instrument Air Pressure [psig]  
  24. Reactivation Gas:
       A. Type  
       B. Flow Rate [scfm]  
       C. Pressure [psig]  
       D. Temperature [°F]  
       E. Dew Point of Gas [°F]  

F. EQUIPMENT DESIGN DATA
  25. ASME Code Design [psig]  
  26. Electrical Construction [NEMA]  
  27. Motor Designation  
  28. Budgeted Equipment Price  
G. REMARKS
  Provide all additional information as needed
 
 
 
 
IMPORTANT

In the drying of liquids other than those that are completely miscible with water, the higher the temperature,the more moisture the liquid will hold. This may result in a dryer much larger and more expensive than need be if the temperatures were held to the lowest practical level. Likewise, if the desired effluent moisture content is specified lower than is actually required, excess quantities of desiccants or special desiccant may be required to obtain requested results. The resulting equipment may be larger and/or more expensive than necessary.

If the liquid contains entrained water, the use of a separator, settling tank or coalescer should be employed to reduce the size of the drying equipment and also to prevent the possibility of desiccant breakdown.

 
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SPX Dehydration & Filtration