Page 102 - Process Equipment and Plant Design Principles and Practices by Subhabrata Ray Gargi Das
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4.6 Mechanical detailing    99




               is preferred from the point of economy and common spares inventory holding. Industrial designs
               mostly use tube length of 2.5 m and higher.
                  Choosing longer tube length (for a given surface area) requires fewer tubes and less complicated
               tube sheet with fewer holes drilled. This also decreases the shell diameter resulting in lower cost.
               However, mechanical cleaning is limited to 6 m (20 ft) tubes and shorter, although standard ex-
               changers can be built with tubes up to 12 m (40 ft). Maximum tube length limit may also be dictated by
               transportation limitation (up to 30 m typically).
                  Part of the tube length within the tube sheet (TS) and the portion within the dead space in the
                                      floating head are not considered for heat transfer and baffle spacing cal-
                                      culations. However, in case of U-tubes, a credit for the bend portion is
                                      considered. The effective tube length (L e ), i.e., the length used for
                    Effective tube length
                                      calculating heat transfer area and baffle spacing, is estimated as follows



                 Table 4.9 Materials for noncorrosive and corrosive service.
                               Service                                     Material
                Noncorrosive service
                 Any HE type, T < 100 C                       Al and austenitic Cr-Ni steel

                                                               1
                 Any HE type,  100 <T <  45 C                 3 Ni steel

                                                               2
                 Any HE type,  45 <T < 0 C                    Carbon steel (impact tested)

                 Any HE type, 0 <T < 500 C                    Carbon steel

                 Shell and tube T > 500 C                     Refractory lined steel

                Corrosive service
                 Mildly corrosive serve; tempered cooling water  Carbon steel
                 Sulphur bearing oils at T > 300 C; hydrogen at  Ferritic Co-Mo and Cr-Mo alloys

                 elevated temperature
                 Tubes for moderately corrosive service; cladding  Ferritic Cr steel
                 for shell and channel in contact with corrosive
                 sulphur bearing oil
                 Corrosion resistance duties                  Austenitic Cr-Ni steel
                 Mildly corrosive fluids                       Aluminium
                 Freshwater cooling in surface condensers;    Copper allow: admiralty brass, cupronickel
                 seawater cooling
                 Resistance to mineral acids and chloride-    High Ni-Cr-Mo alloys
                 containing acids
                 Seawater cooler and condensers               Titanium
                 Highly corrosive services                    Carbon/graphite
                 Exposure to sea and brackish water           Coatings: aluminium, epoxy resins
                 Channels for seawater coolers                Lining: lead, rubber
                 General corrosion resistance                 Lining: austenitic Cr-Ni steel
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