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64                   Valve Selection Handbook

            Direction of  Flow Through Globe Valves

              The  question  of  direction  of  flow  through  globe  valves  has  two
            answers.
              If  the  possibility  exists  that  flow  from  above  the  disc  can  remove
            either the disc  from  the stem or a component from  the disc,  flow  directed
            from  below  the  disc  is  mandatory.  In  this  case,  hand-operated  globe
            valves  with  rotating  stem  and  metal  seatings  can  be  closed  fluid-tight
            without  undue effort,  only  if  the  fluid  load  on  the  underside  of  the  disc
                                                           39
            does  not exceed  about  40-60 kN (9,000-13,000 lb).  With  a  non-rotat-
            ing stem and roller-bearing  supported  stem nut, as in the valves shown in
            Figure 3-10 and Figure  3-11, hand operated  globe valves with metal seat-
            ings  may  be  closed  fluid-tight  against  a  fluid  load  of  about  70-100 kN
            (16,000-22,000 lb), depending on the leakage  criterion  and the construc-
                           39
            tion of the valve.  One particular advantage of flow directed  from  below
            the  disc  is  that the  stuffing  box  of  the  closed  valve is  relieved  from  the
            upstream pressure.  On the debit  side,  if the valve has been closed  against
            a hot  fluid  such as  steam,  thermal contraction of the  stem after  the valve
            has been closed  can be just enough to induce seat  leakage.
              If flow is directed from  above the disc, the closing  force from  the fluid
            acting  on  top  of  the  disc  supplements  the  closing  force  from  the  stem.
            Thus, this direction of flow increases  greatly the  sealing reliability of the
            valve. In this case,  hand-operated  globe  valves with  a rotating  stem may
            be opened without excessive  effort,  only if the fluid  load acting on top of
                                                                  39
            the disc does not exceed  about 40-60 kN (9,000-13,000 lb).  If the stem
            is  of  the  nonrotating type  with  a  roller-bearing  supported  stem  nut, the
            globe valve may be opened  by hand  against a fluid load  of about 70-100
                                 39
            kN  (16,000-22,000 lb).  If the  fluid  load  on  top  of the  disc  is higher, a
            bypass  valve may have  to be provided  that permits  the downstream sys-
            tem to be pressurized before the globe valve is  opened.

            Standards Pertaining to Globe Valves

              Appendix C provides  a list of U.S.  and British  standards pertaining to
            globe valves.
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