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The three most common types of shell-and-tube exchangers are (1) fixed tube sheet design, (2) U-tube design, and  (3) floating-head type.    In all three types, the front-end head is stationary while the rear-end head can be either stationary or floating , depending on the thermal stresses in the shell, tube, or tube sheet, due to temperature differences as a result of heat transfer.   The exchangers are built in accordance with three mechanical standards that specify design, fabrication, and materials of unfired shell-and-tube heat exchangers.    Class R is for the generally severe requirements of petroleum and related processing applications.   Class C is for generally moderate requirements for commercial and general process applications.   Class B is for chemical process service. The exchangers are built to comply with the applicable ASME Boiler and Pressure Vessel Code, Section VIII (1998), and other pertinent codes and/or standards.   The TEMA standards supplement and define the ASME code for heat exchanger applications. In addition, state and local codes applicable to the plant location must also be met.