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Processing of  Plastics                                        293

                     Cavity      Large runnel         Cavity         Large runner
                                                        I                ,















                                                          (b) Distributed runner system
                                 Fig. 4.40  Insulated and distributed runner systems

                  Mould Clamping Force
                  In  order  to  prevent  ‘flashing’, i.e.  a  thin  film  of  plastic  escaping  out  of  the
                  mould  cavity  at  the  parting  line,  it  is  necessary  to  keep  the  mould  tightly
                  closed  during  injection  of  the  molten  plastic.  Before  setting up  a  mould  on
                  a machine it  is  always worthwhile  to  check that there is  sufficient clamping
                  force available on the machine. To do this it is necessary to be able to estimate
                  what  clamping  force  will  be  needed.  The  relationship  between  mould  area
                  and clamp requirements has occupied the minds of  moulders for many years.
                  Practical experience suggests that the clamping pressure over the projected area
                  of  the moulding  should be between  10 and 50 MN/m2 depending on factors
                  such as shape, thickness, and type of material. The mould clamping force may
                  also be estimated in the following way. Consider the moiilding of a disc which
                  is centre gated as shown in  Fig. 4.41(a). The force on the shaded element is
                  given by
                                                    i
                                        Force,  F =  Pr2nrdr                   (4.23)
                                                    o
                  The cavity pressure will vary  across the disc and it is necessary to make some
                  assumption  about this variation. Experimental studies have suggested that an
                  empirical relation of  the form
                                         P, =Po  (1  - (i)“)                   (4.24)




                  is most  satisfactory. Po  is the pressure at the gate and rn is a constant which
                  is usually between 0.3 and 0.75. It will be shown later (Chapter 5) that  ‘tn’ is
                  in fact equal to (1 -n) where ‘n’ is the index in the Power Law expression for
                  polymer melt flow.
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