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Balancing of Hot Runners
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.
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.
From the following diagram :
For balanced pressure drops at each exit port we have:
For balanced fill times we have:
Therefore, the total volumetric flow rate in this section of the runner system:
So that:
Rearranging, we get:
These equations can be represented by the general equation:
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:
Where,
Now,
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 ´ 108 = 2.08 ´ 109
DP = 14.5 MPa DP = 2111 p.s.i.
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