Page 389 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition
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             .01  L....J..��-'-..;,_;c.....J.....l-.1..-1--'-..J.......1-J....-'-'--L.�'-'--'--'--'-'-""---'--'-�'-'--'-.1..-...1.-'-...L.....J--l...--"-'----'--'--'---'-...L.....J-'---"-�--'--'--'--'-..J.......1--l......._,
               0         i2       24        36        48       60        72       84        96        108      120
                                                     Capacity  -  lbs.  Air  per  hour
          Figure  6-118.  A typical  relative  comparison  of various designs  of steam jet ejectors.  Based on  same  steam  consumption,  100 psig  steam
          pressure and 85°F water.  Curves represent the capacity of ejectors designed for maximum air handling capacity at any one particular suction
          pressure.  By permission,  Graham  Manufacturing Co.
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