Page 40 - Chemical Process Equipment - Selection and Design
P. 40

REFERENCES  15
             TABLE 1.9. Typical Utility Characteristics
                      _-
                                   Steam                                             Electricity
                  Pressure (psig)   Saturation (“F)   Superheat (“F)         Driver HP       Voltage
                         -
                     15-30        250-275                                      1-100      220,440,  550
                      150           366                                       75-250      440
                     400            448                                      200-2500     2300,4000
                     600            488         100-1 50                    Above 2500    4000,  13,200
                      ___
                  --          Heat Transfer Fluids
                     “F                   Fluid
                  Below 600   petroleum oils                    processes often  demands more or less extensive pilot plant  effort.
                  Below 750    Dowttherm and others             This point is stressed by specialists and manufacturers of  equipment
                  Below 11 00   fused salts
                  Above 450   direct firing  and electrical heating   who  are  asked  to  provide  performance  guaranties.  For  instance,
             -                                                  answers  to  equipment  suppliers’  questionnaires  like  those  of
                                 Refrigerants                   Appendix C may require the potential purchaser to have performed
                                                                certain tests.  Some of  the  more obvious areas  definitely requiring
                      “F                  Fluid
                                                                test  work  are filtration,  sedimentation,  spray,  or  fluidized bed  or
                                                                any other  kind of  solids drying, extrusion pelleting, pneumatic and
                     40-80     chilled water
                     0-50      chilled brine arid glycol solutions   slurry conveying, adsorption, and others. Even in such thoroughly
                   -50-40      ammonia, freons, butane          researched  areas  as  vapor-liquid  and  liquid-liquid  separations,
                   -1 50-50    ethane or propane                rates, equilibria, and efficiencies may need to be tested, particularly
                   -350--150   methane, air, nitrogen           of  complex mixtures. A  great deal can be found out, for instance,
                   -400--300   hydrogen                         by  a batch distillation of  a complex mixture.
                   Below -400   helium                             In some areas, suppliers make available small scale equipment
                                                                that can be used to explore suitable ranges of  operating conditions,
                                Cooling Water                   or they may do the work themselves with benefit of their extensive
                                                                experience. One engineer in the extrusion pelleting field claims that
                 S~pply at 80-90°F
                 Return at 115°F. with 125°F maximum            merely feeling the stuff between his fingers enables him to properly
                 Return at 170°F (salt water)                   specify  equipment  because  of  his  experience  of  25  years  with
                 Return above  126°F (tempered water or steam condensate)   extrusion.
                                                                   Suitable test procedures often are supplied with “canned” pilot
                                 Cooling Air                    plants.  In  general,  pilot  plant  experimentation  is  a  profession in
                                                                itself, and the  more sophistication brought to bear on it the more
                      Supply at 85-95°F                         efficiently can the work be done. In some areas the basic relations
                     Temperature approach to process, 40°F      are  known so  well  that  experimentation suffices to evaluate a few
                      Power input, 20 HP/1000 sqft of bare surface
                                                                parameters in a mathematical model. This is not the book to treat
                                                                the  subject  of  experimentation,  but  the  literature  is  extensive.
                                   Fuel
                                                                These books may be helpful to start:
             Gas: 5-10  psig, up to 25 psig for some types of burners, pipeline gas at
              1000 Btu/SCF
             Liquid: at 6 million Btu/barael                    1. R.E.  Johnstone  and  M.W.  Thring,  Pilot  Plants,  Models  and
                                                                  Scale-up Methods  in  Chemical  Engineering,  McGraw-Hill, New
                               Compressed Air                     York, 1957.
            -                                                   2.  D.G. Jordan,  Chemical Pilot Plant Practice,  Wiley-Interscience,
                       Pressure levels of 45, 150, 300, 450 psig
                                                                  New York, 1955.
                                                                3. V. Kafarov,  Cybernetic  Methods  in  Chemistry  and  Chemical
                                instrument Air
                                                                  Engineering,  Mir Publishers, Moscow, 1976.
                              45 psig, 0°F dewpoint             4.  E.B.  Wilson, An Introduction to  Scient@c Research,  McGraw-
                                                                  Hill, New York, 1952.




             REFERENCES                                           McGraw-Hill, New York, 1984; earlier editions have not been obsolesced
                                                                  entirely.
             7.1.  Process Design                               4.  Sinnott,  Coulson,  and  Richardsons,  Chemical  Engineering,  Vol.  6,
                                                                  Design, Pergamon,  New York, 1983.
             . Books Essential to a Private Library
                                                                B.  Other Books
             I. Ludwig,  Applied  Process  Design  for  Chemical  and  Petroleum  Plants,
               Gulf, Houston 1977-1983,  3 vols.                 1.  Aerstin  and  Street,  Applied  Chemical  Process  Design,  Plenum,  New
             2. Marks  Standard  Handbook  for  Mechanical  Engineers,  9th  ed.,   York, 1978.
               McGraw-hlill, New York,  1987.                    2. Baasel,  Preliminary  Chemical  Engineering  Plant  Design,  Elsevier,  New
             3. Perry,  Green,  and  Maloney,  Perry’s  Chemical  Engineers  Handbook,   York, 1976.
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