Experimental researches regarding the influence of the injection moulding temperatures on quality plastical with complex shape.
Mihaila, Stefan ; Fazecas, Marius ; Chira, Danut 等
1. INTRODUCTION
Injection process knowledge involves work procedures, chemical
structure, thermo plasticity material properties and individual factor
reciprocal influence knowledge. That is why mould temperature adjustment
issue has to be solved function of these individual factors, which have
an important role in injection process. This is the reason why the
injection process will be shortly explained, for a better figure out
about moulds temperature adjustment.
Because of the heat, grain material is melting, then get in system.
In this stage it has to overcome sewer resistance and resistance of the
moulds drain. By the time of this above all stage, the injection, the
thermo plasticity material relieves the heat out, with other words
cooling process is starting, the metal near the system is heating.
The heat give out can be that big, that in case of an long sliding
way of the piece, the much cooled material will not be able to
completely fill the mould cavity. The reasons of this thing are more
than clear if we think about injecting the material in the mould,
talking about an Newtonian fluid, it will immediately get to the mould
wall and it is strengthtly in the edges. (fig.1)
When the drain channels expands, the solidified layer of the
interior wall of the mould expands too, and the channel which serves to
fuel the material in the direction of the running diminish, in order to
fill up the mould and even in the case of long draining channels,
several measures must be considered:
--increasing pressure and injecting speed
--increasing the temperature of the plastic material (change in
viscosity)
--The greatest efficiency is obtained by increasing pressure and
injecting speed
[FIGURE 1 OMITTED]
2. DETERMINING THE MOULD GENERAL THERMAL BALANCE EQUATION
The mould temperature is the decisive factor for cooling speed and
the injected reference point its properties. It is established according
to the amount of heat that is exchanged in the mould:
--between the thermoplastic material injected into the mould and
the mould material Q;
--between the mould and the between the mould and the environment
QE;
If we consider the thermal fluxes that enter the mould as positive,
and the fluxes that exit the mould as negative, then it can be write the
thermal balance equation:
Q= -[Q.sub.t] - [Q.sub.e], (1)
Q+ [Q.sub.e] + [Q.sub.t] = 0, (2)
[FIGURE 2 OMITTED]
3. HEAT TRANSFER BETWEEN THE PLASTICS MATERIAL AND THE MOLD
Plasticity material inserted into the mould center, field, during
an injecting cycle, to the mould body, an amount of heat Q, which can be
calculated using:
Q+ [Q.sub.E] + [Q.sub.T] = 0, (3)
where:
m--is weight of the injected piece, including the network [Kg]
[i.sub.1]--the enthalpy of the plasticity material upon removing
[Kj/Kg]
[i.sub.2]--enthalpy of the plasticity material upon insertion into
the mould
The enthalpy of the plasticity material is calculated using this:
Di = [i.sub.2] - [i.sub.1] = [c.sub.p]([T.sub.Mp] - [T.sub.D]), (4)
where:
[C.sub.p]--specific heat of the plastic material
[T.sub.mp]--the temperature of the material in the center
[T.sub.d]--removing temperature
Conductor in the mould. The quantity of heat evacuated by the piece
is taken through conductor by the mould and transported into the
temperate environment. We can consider the phenomena of conductor
stationary transfer in a plane homogenous wall (Stefanescu et al.,
1982).
The quantity of heat Q is determined using this function:
Q = [lambda]M/[delta] S([T.sub.pc] - [T.sub.pT]) (5)
where:
--[[lambda].sub.M]--thermical conductibility to the mould [W/mK];
--[delta]--the channel distance of temperature beside the mould
surfaces [m];
--S--the transversal surfaces of the mould
--[T.sub.pc]--the medium temperature of the wall cavity
- TpT - the medium temperature to the temperature wall channel
[degrees]K.
4. CONSTRUCTIVE MOULD TEMPERING SOLUTIONS FOR INJECTING HIGH
PRECISION THERMOPLASTICITY MATERIAL PARTS
4.1 Methods of cooling down complex high precision single centered
moulds
Only two methods will be presented. One used in real life (fig. 3)
and the other proposed by the author which substantiate to be superior
(fig. 4).
[FIGURE 3 OMITTED]
[FIGURE 4 OMITTED]
Follow that the analysis of a finished part, we can see that when
cooling down a product of high precision, with thick walls, that have
high contractions, it is recommended to use more cooling circuits, but
respecting the constant distance between the outline of the part and the
cooling circuit, (fig. 4) so that a higher amount of heat can be
removed.
4.2 Methods of cooling complex high precision moulds utilizable the
thermosiphon principle
This temperature adjustment method applies in general to high
complexivity moulds where there can be critical areas which cannot be
cooled down with other methods. These solutions are based on the thermo
siphon principle. (fig.5)
This concept of isobaric superconductivity is based on using a
metallic tube, 1 made of copper into which another metallic tube, 2 of
special composition with capillary structure is clamped. In tube
1's interior and between tube 1 and 2, a fluid is circulating,
fluid which can be both liquid and vapor. The liquid take part of the
heat from the exterior, passes through tube 2 in the interior and
vaporizes. A pump effect is achieved at A end towards B end where the
fluid vapors go through tube 2 and transform into liquid, giving heat to
the environment. The liquid enters the circuit towards B end of the tube
in order to take heat from the outside environment.
In this system case, thermical transfer is very fast and
constructive solutions that use this system become very efficient.
[FIGURE 5 OMITTED]
A,B-tube ends; QA absorbed heat; QB abstracted heat ; 1-exterior
tube; 2-interior tube
5. CONCLUSIONS
Optimizing the mould temperature has a very important role both in
the future quality of the product, as in productivity. Cooling
conditions from the mould have a great influence upon injected piece
warping, no matter the size and complexity .
Moulds temperature influences directly cooling time, injecting
cycle time, the efficiency of the product formed inside the mould,
crystallinity and internal tensions.
As a conclusion, we must say that the solutions presented
contribute significant to optimizing temperature in the active part of
the moulds, particularly for products of medium size with thick walls.
6. REFERENCES
De Laney, D.E., Reilly J.F. (1998). A new approach to polymer
rheology for process and quality control. Plastics Engineering, June,
Fetecau C. (2007). Plasticity injection material. Second edition.
ISBN 429-2637-28.Ed Pedagogical and didactic style. Bucharest,
Losch, K. (1997). Thinwall molding: demanding bul rewarding. Modern
Plasticity International,.
Seres, I. (1999). Moulds for injection. ISBN 973-8195-42. West
Publishing printing Oradea
Stefanescu, D., Marinescu, M., Danescu, A. (1982).--The transfer of
heat in the technical, 1st volume, conductor, convection, radiation,
global exchange. ISBN 392-5219-14.Technical Publishing House, Bucharest,
Zemanski, M.W.Bazic (1995). Enginering Termodynamics Mc. Grow Hill
Book, Co New York
***PLASTPRACTICE"--Temperature Control by Means of Fluid
Media.