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T y p i c a l P i t f a l l s a n d How t o Avo i d T h e m   285



                                    150°
                                 160°
                                      ΔH 3
                                    190°
                                            120°                   40°
                            Reactor       80°         45°    45°           10°
                                                ΔH 2                  ΔH 1  Feed
                                            140°         Unit      140°
                     FIGURE 12.1  Partial fl owsheet for example process.


                     heated further by two heat exchangers and then enters a reactor. The
                     reactor requires the feed stream to be at 165°C. The question is: How
                     many streams should be extracted?
                         1. Three streams: 10–45°C, 45–80°C, and 80–165°C
                         2. Two streams: 10–45°C and 45–165°C
                         3. One stream: 10–165°C
                        Choosing option 1 yields a design exactly like the original one;
                     there will again be three heat exchangers with the same heat transfer
                     duties as before. This case accounts for claims of “no process
                     improvement” by some PI critics. Option 2 presents more degrees of
                     freedom: the first heat exchanger would be the same, but the other
                     could be modified. Extracting two streams would be appropriate for
                     cases when the processing unit requires a feed temperature of close
                     to 80°C.
                        Option 3 provides the most degrees of freedom and scope for
                     improvement, but with this design the processing unit feed could be
                     at any temperature between the 10°C supply and the reactor target of
                     165°C. If the processing unit is, say, a filter (as assumed by Smith,
                     2005), then there would probably be some restriction on the filter
                     supply temperature to ensure proper operation of the filter. If the
                     processing unit is storage (as assumed by Linnhoff et al., 1982), then
                     the supply temperature might be restricted to a different range
                     (depending, e.g., on whether liquid or gas is stored). This simple
                     example demonstrates that choosing the right stream from which to
                     extract data cannot be a fully automatic process. Making this choice
                     requires assessments related to specific processing units and
                     performance requirements for the plant.
                     12.1.2  How Precise Must the Data Be at Each Step?
                     There are frequently questions about required data precision, and a
                     common excuse for not applying PI analysis is that the data on a
                     plant is not sufficiently precise. However, the process of applying PI
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