Page 307 - Sustainability in the Process Industry Integration and Optimization
P. 307

284   Cha p te r  T w e l v e


                     may over-estimate the potential benefits. Appropriate data extraction
                     accepts only the critical sections of the plant which cannot be
                     changed. Data extraction skill develops with increased experience in
                     the application of Pinch Technology (Linnhoff March, 1998).
                        Since the release of these packages, the methodology has
                     developed further and more attempts have been made to extract
                     data automatically. However, experience and following the proper
                     rules remain valuable assets. Basic questions to ask include the
                     following:

                         1.  When is a stream a stream?
                         2.  How precise must the data be at each step?
                         3.  How can considerable changes in specific heat capacities be
                           handled?
                         4.  What rules and guidelines must be followed to extract data
                           properly?
                         5.  How can the heat loads, heat capacities, and temperatures of
                           an extracted stream be calculated?
                         6.  How “soft” are the data in a plant or process flowsheet?
                         7.  How can capital costs and operating costs be estimated?
                     12.1.1  When Is a Stream a Stream?
                     To those unfamiliar with PI, identifying a stream seems fairly
                     straightforward. In fact, many considerations are involved, and
                     accounting for them properly is key to setting up the problem. First,
                     we need not consider any stream that neither gains nor provides heat;
                     no data needs to be extracted from a stream with identical supply
                     and target temperatures and enthalpies. (Of course, in the absence of
                     perfect insulation, every stream loses or gains some heat; in many
                     cases, however, these small amounts of losses and gains can be
                     neglected.) If we do not extract data from such streams, the problem
                     is considerably simplified.
                        There are also streams that, for one reason or another, should not
                     be included in the PI problem—for example, streams that are remote
                     and streams that should not be altered for safety, product purity, and
                     operational reasons and for other (mostly practical) considerations.
                     Finally, Heat Integration deals with heat flows, which can be carried
                     not only by a pipe line but also by radiation or conduction.
                        Consider the example depicted in Figure 12.1. This example was
                     introduced, along with some data extraction rules, by Linnhoff and
                     colleagues (1982) and was later modified for use in many follow-up
                     books (e.g., Smith, 1995; Smith, 2005; Kemp, 2007) and in many courses
                     based on UMIST (later the University of Manchester) teaching
                     materials. The figure shows part of a flowsheet in which the feed
                     stream is heated to 45°C by recuperated heat in a heat exchanger and
                     then enters a processing unit. After leaving this unit, the stream is
   302   303   304   305   306   307   308   309   310   311   312