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Balancing of Hot Runners


Analysis of a balanced hot runner system for six impressions in a line

In the following analysis the standard Hagen-Poiseuille equation has been assumed for the flow of a Newtonian fluid through a pipe of circular cross-section.

i.e.                                                                                                                       (1)

Where:

Q = the volumetric flow rate of the fluid,

DP = the pressure drop along the length of pipe, L.

r = the radius of the pipe and,

h = the Newtonian viscosity of the fluid.


Rearranging the equation gives :

                                                                                                                       (2)

From the following diagram :

 

 

                                                                                         (3)

                                                                     (4)

                                                   (5)

 

For balanced pressure drops at each exit port we have:

                                                                                                                                   (6)

For balanced fill times we have:

                                                                                                                                               (7)

 

Therefore, the total volumetric flow rate in this section of the runner system:

                                                                                                                                                                                     (8)

So that:

                                                                                                      (9)

   

                                                                                  (10)   

 

                                                               (11)

Rearranging, we get:

                                                                                                                      (12)

 

                                                                                                           (13)

 

                                                                                                  (14)

These equations can be represented by the general equation:

                                                                                               (15)

where n = number of exit ports for i =1 to n (n ³ j).

For the requirements of constant fill time and constant pressure drop, we have 3 equations that can be reduced to:

                                                                                                                             (16)

                                                                                                                   (17)

                                                                                                         (18)

Where,                                                                                                                      (19)

 

Now,                                                                                                                    (20)

                                                                                                                          (21)

                                                                                                                           (22)


Now, if we put in some numbers, e.g.,

The volume flow rate for a six impression mould – three impressions either side of the injection point – and an injection time of 1.5 seconds.

Q = 2.75 x 10-5 m3 s-1

Assume a constant Newtonian viscosity of,

h = 300 Nsm-2

( Not really true for polymer melts, but it gives a reasonable first order approximation)

If we make the length of each step-down, l, 15 mm and if we make the radius of both the main runner, R, and the furthest step-down, r3, be 3.75 mm, we find from equation (22) above that,

                                                        

                                                          

                                                            = 7.58 ´ 107 + 4.45 ´ 108 = 5.21 ´ 108

Therefore,                                     

So that,                                           r2 = 2.32 mm

The diameter of the central drop-down is 4.64 mm.

From equation (21) above we have,

                                                    

                                                          

                                                           = 5.21 ´ 108 + 8.9 ´ 108  = 1.41 ´ 109

                                                     

\                                                   r1 = 1.80 mm

The diameter of the first drop-down is 3.6 mm

From equations (19) & (20) we get:

                                              

                                                         

                                                           = 1.41 ´ 109 + 6.67 ´ 10=  2.08 ´ 109

                                                    

                                           DP = 14.5 MPa

                                           DP = 2111 p.s.i.

 

 

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