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106                                                 MECHANICAL ENGINEER’S DATA  HANDBOOK





             3.3  Vapours

             A substance may exist as a solid, liquid, vapour or gas.   rise (at constant pressure) required to do this is known
             A mixture of liquid (usually in the form of  very small   as the ‘degree of superheat’. The method of determin-
             drops) and dry vapour  is known as a  ‘wet vapour’.   ing the properties of vapours is given, and is to be used
             When all the liquid has just been converted to vapour   in conjunction with vapour tables, the most compre-
             the substance is  referred to as ‘saturated vapour’ or   hensive of  which are for water vapour. Processes are
             ‘dry saturated vapour’. Further heating produces what   shown  on  the  temperature-entropy   and  en-
             is known as ‘superheated vapour’ and the temperature   thalpy-entropy diagrams.

             Symbols used:                               Specific enthalpy of  wet vapour
               p=pressure  (Nm-’  (=pascal); Nmm-2; bar   h, = h, + x(h, - h,) = h, + xh,,
                  (E 1OSNm-’);  millibar (E 100Nm-’))    specific entropy of  wet  vapour
               t = temperature  (“C)
               t, = saturation temperature (“C)          sx=sf+x(s,-sf)=sf +xs,,
               T= absolute temperature (K N “C + 273)    Superheated  vapour  Tables  (e.g.  for  water)  give
               u = specific volume (m3 kg - ’)           values of  u, u, h, and s for a particular pressure and a
               u,=specific  volume of liquid (m3 kg-’)   range of temperatures above the saturation tempera-
              u,=specific  volume of saturated vapour  (m3 kg-’)   ture t,.  For steam above 70 bar use u=h-pu.
               u = specific internal energy (kJ kg- I)
              u, = specific internal energy of liquid (kJ kg- ’)   3.3.2   TemperatureEntropy diagram
              ug= specific internal energy of  vapour  (kJ kg-’)   (T-s diagram)
              u,, = specific internal energy change from liquid to
                  vapour (kJkg-’)                        Various processes are shown for a vapour on the T-s
               h =specific enthalpy (kJ kg - I)          diagram. AB is an isothermal process in which a wet
              h, = specific enthalpy of liquid, kJ/kg    vapour becomes superheated. CD shows an isentropic
              h, = specific enthalpy of  vapour, kJ/kg   expansion from the superheat to the wet region. EF is a
              h,, = specific enthalpy change from liquid to vapour   polytropic process in the superheat region.
                  (latent heat) kJ/kg
               s = specific entropy, kJ/kg K
               sf = specific entropy of  liquid, kJ/kg K   reg  m                   i
                                                           Liquid
                                                           Liquid
               sg = specific entropy of  vapour, kJ/kg K   T  region  Fv
              sfg = specific entropy change from liquid to vapour,
                  kJ/kg K
               x = dryness fraction                                             \    P1
                                                           /       Wet vapour   \
                                                                   region
             3.3. I  Properties of vapours                                        S

                             Mass  of  dry  vapour
             Dryness fraction x =
                             Mass  of  wet  vapour       3.3.3   Enthalpy of a vapour
             Specific volume of wet vapour u, = uf( 1 - x) + XD,==XU,   The  enthalpy  is  represented  by  the  area  under  a
             (since u, is small)                         constant pressure line on the T-s  diagram. Area h, is
             Specific internal energy of wet  vapour     the enthalpy of  the liquid at saturation temperature,
             u, = Uf + x(u, - Uf) = Uf + XUfs            h,,  is the enthalpy corresponding to the latent  heat,
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