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268                                                      Chapter 6


            VESSEL DESIGN

            Although  a  mechanical  or  civil  engineer  normally  designs  vessels,  the  process
            engineer  should  have  some  knowledge  of  the  mechanical  design  of vessels.  For
            example, the process engineer  may have to  make a preliminary  design of vessels
            for  a cost  estimate.  Reactors,  fractionators,  absorbers,  heat  exchangers,  and  some
            phase  separators  are  classified  as vessels.  What makes  an absorber  an  absorber,
            for  example, is  its internal design. A vessel consists of a cylindrical shell and end
            caps, called heads. For  safety,  vessel design is governed by codes.  An example is
            the ASME (American Society of Mechanical Engineers)  Boiler and Pressure Ves-
            sel Code.  Engineers who agreed on what is a safe procedure for designing vessels
            formulated this code.
                Most vessels in the process industries are thin-walled vessels, which have a
            wall thickness  of  less  than  about  5% of the  inside  diameter  of a vessel.  Internal
            pressure  acting  on  the  walls  of  a  cylindrical  vessel  produces  a  longitudinal  and
            radial stress, also called hoop stress.  For thin-wall vessels, it may be assumed that
            the radial  stress  is  approximately uniform  across  the  wall.  Rase  and Borrow  [1],
            for  example,  showed that the radial  stress, produced by  an internal pressure, P,  is
            given by Equation 6.1.

               PD
            S = ——                                                       (6.1)
               4t s
            where the diameter of the vessel is D. The radial stress is larger than the longitudi-
            nal stress, and thus it must be used to calculate the wall thickness,  1$. If a cylindri-
            cal vessel fails,  it will split longitudinally.
                Vessels larger  in diameter  than  about  30  in  (0.672 m)  and above  are fabri-
            cated  from  plates,  which  are  formed  into  cylinders,  called  shells,  and  welded
            longitudinally. Shells smaller than 30 in (0.672) may be extruded and thus will not
            contain  a  longitudinal  weld.  Shells  may then be joined  by  welding  circumferen-
            tially to  form  longer  shells. After  fabricating  the  shell, end  caps,  called heads, are
            welded to the  shell to form  the vessel. Because the  weld may have  imperfections,
            the radial  stress will be  less than its maximum value.  Thus,  S is multiplied  by a
            joint  or  weld  efficiency,  E, which depends  on the  type  of  x-ray  inspection  of  the
            weld. Thus,

                PD M
            o o  ————                                                    (0.^1
                4t s

            where the mean diameter, D, is the average of the outside and inside diameters.
                                  M





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