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66131_Ludwig_CH10A  5/30/2001 4:06 PM  Page 8










                       8                         Applied Process Design for Chemical and Petrochemical Plants

                                   Details of Exchange Equipment             and many states and insurance companies require compli-
                                    Assembly and Arrangement                 ance with this.
                                                                               These classes are explained in the TEMA Standards and
                         The process design of heat exchange equipment       in Rubin. 99, 100, 133
                       depends to a certain extent upon the basic type of unit con-
                       sidered for the process and how it will be arranged together
                                                                             2. Thermal Rating Standards
                       with certain details of assembly as they pertain to that par-
                       ticular unit. It is important to recognize that certain basic
                                                                               The TEMA Code    107  does not recommend thermal
                       types of exchangers, as given in Table 10-2, are less expen-
                                                                             design or rating of heat exchangers. This is left to the rat-
                       sive than others and also that inherently these problems are
                                                                             ing or design engineer, because many unique details are
                       related to the fabrication of construction materials to resist
                                                                             associated with individual applications. TEMA does offer
                       the fluids, cleaning, future reassignment to other services,
                                                                             some common practice rating charts and tables, along
                       etc. The following presentation alerts the designer to the
                                                                             with some tabulations of selected petroleum and chemical
                       various features that should be considered. Also see  physical property data in the third (1952) and sixth (1978)
                       Rubin. 281
                                                                             editions.
                       1. Construction Codes
                                                                             3. Exchanger Shell Types
                         The American Society of Mechanical Engineers (ASME)
                       Unfired Pressure Vessel Code  119  is accepted by almost all states as  The type of shell of an exchanger should often be estab-
                       a requirement by law and by most industrial insurance  lished before thermal rating of the unit takes place. The
                       underwriters as a basic guide or requirement for fabrication  shell is always a function of its relationship to the tubesheet
                       of pressure vessel equipment, which includes some compo-  and the internal baffles. Figures 10-1, 10-2, and 10-3 sum-
                       nents of heat exchangers.                             marize the usual types of shells; however, remember that
                         This code does not cover the rolling-in of tubes into  other arrangements may satisfy a particular situation.
                       tubesheets.                                             The heads attached to the shells may be welded or bolted
                         For steam generation or any equipment having a direct  as shown in Figure 10-3. Many other arrangements may be
                                                                  6
                       fire as the means of heating, the ASME Boiler Code applies,  found in references 37, 38, and 61.





































                                                                Figure 10-2. Typical shell types.
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