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436    CHAPTER 18 LIQUEFACTION OF GASES




                          10
                                      Joule–Thomson cooling cannot occur in this region

                           8                                      Joule–Thomson coefficient
                         Reduced pressure, p R / bar  6 4  Joule–Thomson coefficient positive
                                                                   negative in this region




                                                   in this region

                           2
                                      Saturation
                                        line
                           0
                            0       1       2       3       4       5      6       7
                                               Reduced temperature, T  / K
                                                              R
             FIGURE 18.10
             Inversion region in terms of reduced pressure (p R ¼ p/p c ) and reduced temperature (T R ¼ T/T c ) Note the
             saturation line.
             operating on a vapour compression cycle (i.e. the typical refrigeration cycle), except that it includes a
             heat exchanger to transfer energy equal to Q A and Q B from the high-temperature working fluid to that
             which has already been cooled through throttling processes. The two throttling processes depicted in
             Fig. 18.11(a) both bring about cooling through the Joule–Thomson effect. The operating processes in
             the Linde plant will now be described: it will be assumed that the plant is already operating in steady
             state and that a supply of liquefied gas exists. The gas is supplied to a compressor at state 1 and make-
             up gas is supplied at state 11, which is the same as state 1. This is then compressed to a high, su-
             percritical pressure (which might be hundreds of atmospheres) by a multistage reciprocating
             compressor with interstage cooling. The gas finally reaches state 2, and it is then passed through a heat
             exchanger which cools it to state 3. At this point it is throttled for the first time, and is cooled by the
             Joule–Thomson effect to state 4 and passed into a receiver. Some of the gas entering the receiver is
             passed back to the compressor via the heat exchanger, and the remainder is passed through a second
             throttle until it achieves state 6. At this stage it is in the liquid–vapour region of the state diagram, and
             liquid gas can be removed at state 9. The yield of liquid gas is y, defined by the quality of state point 6
             on the T–s diagram.


             18.2.4 INVERSION POINT ON p-v-T SURFACE FOR WATER
             The Joule–Thomson effect for water was met early in the study of thermodynamics (see Chapter 1,
             Section 1.5.8.3.2*). It was shown that the quality (dryness fraction) of water vapour could be increased
             by passing the wet vapour through a throttle. This process is an isenthalpic one in which the pressure
             decreases. The liquid–vapour boundary for water is shown in Fig. 18.12, and it can be seen that the

             *
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