# Effect of processing conditions on shrinkage in injection molding.

INTRODUCTION

The objective of this paper is first to present the results of a systematic study on the effect of processing conditions on the dimensions of as-molded products. The second objective is to show that all shrinkage data is well described by a simple equation that relates shrinkage to the local pressure history. The study was done using seven common resins, being PS, ABS, HIPS, PC, PBT, PBT-GF30 and HDPE, and systematically varying holding pressure, injection velocity, mold temperature and melt temperature.

In general we may discern three types of shrinkage in injection molding: in-mold shrinkage (shrinkage during processing which may show up in extreme cases), as-molded shrinkage (the shrinkage just after mold opening, sometimes referred to as "mold shrinkage") and post-shrinkage (time effects during storage as physical aging, recrystallization, etc.). Here we will focus on as-molded shrinkage and, briefly, on postshrinkage effects. In-mold shrinkage is discussed in detail elsewhere (1).

In the past tables or nomograms (2) were used to correct for product shrinkage during mold design. However, with the increasing demands on product tolerances more exact information is required. Recent experimental studies show that as-molded shrinkage of injection molded products is affected by processing parameters as well as by mold geometry (3-24). All studies conclude that the holding pressure is by far the most important parameter affecting shrinkage. A higher holding pressure setting decreases part shrinkage in all directions. The second most important parameter is the injection temperature (3-7). Increasing the injection temperature was usually seen to reduce shrinkage (because of a better pressure transmission). Some authors reported an increase in shrinkage with increasing mold temperature (3, 4, 6, 8) while others concluded differently (5, 9). Increasing the holding time always decreases shrinkage until leveling off occurs at the gate freeze-off time (3, 4, 10, 11).

In most studies rectangular plates or tensile bars were considered. Exceptions are center gated disk molds (12, 13), box molds (14) and a flat plate with holes (15, 16). In only a few cases the geometry was considered as a variable (17-19). Geometry may affect shrinkage in two ways. First, geometry may affect flow and hence cause orientation effects (of either amorpous phase, crystalline phase or filler particles) resulting in shrinkage anisotropy. Second, geometrical constraints (ribs, bosses, etc.) affect the shrinkage boundary conditions. These effects are discussed elsewhere (1, 10, 13, 17, 18, 20-22).

Shrinkage variations along the flowpath are usually directly related to the local cavity pressure (3, 11, 17, 18, 20). For semicrystalline PP (3, 20) and PA (17, 20) its was shown that length and width shrinkage varied differently. In most cases, width shrinkage was slightly larger than length shrinkage, the only exception being Thomas's measurements on PP (20) where close to the gate length shrinkage is larger than width shrinkage and far from the gate the reverse holds true. Shay et al. (17) reported that for amorphous polycarbonate no differences between length and width shrinkage could be detected. For fiber filled resins, large differences between shrinkage in the flow direction and in the transverse direction (width) are always reported (e.g., 6, 18, 19, 23). Typical length shrinkage values are always close to 0.2%, while shrinkage in transverse direction approaches that of unfilled resins. In contrast to in-plane shrinkage, surprisingly little agreement in the literature is found between thickness shrinkage measurements. For similar molding conditions some authors report thickness shrinkage of the same order of magnitude as in-plane shrinkage (20) while others mention thickness shrinkages many times larger (and in some cases of opposite sign) than length and width shrinkage (4, 6, 10-12, 19, 24). Possible explanations for these observations are elastic expansion of the compressed polymer due to a nonvanishing cavity pressure (9, 10, 22), elastic deformation of the mold during packing (10, 11, 22, 24), flashing at high holding pressures (12), void formation in thicker bars (19) or the much larger thermal gradient in thickness direction (6). In practice, thickness shrinkage is most probably governed by a combination the first three effects.

In most studies, shrinkage is measured between 24 and 48 hours after production (25). It is, however, well known that shrinkage continues (slowly) during storage because of physical aging or recrystallization effects (5, 8, 26, 27). Since these are self-delaying processes, shrinkage must proceed proportional to the logarithm of time (26).

As a first attempt to deal with the parameters affecting shrinkage, statistical analysis methods were used to construct empirical fit functions based on shrinkage data of a limited number of experiments (3, 5, 8, 20). It is obvious that with this approach predictions are limited to the specific testing geometry and testing window. Such "models," moreover, do not have any physical meaning and are difficult to use for interpretation purposes.

A better way to try to understand shrinkage in injection molding is to consider the mold as a closed space, setup a material balance, and calculate the amount of mass accumulated in the mold. The volumetric shrinkage then follows from the pvT-diagram (7, 12, 24). In general these models use a Tait-like equation in combination with calculated temperature and pressure histories to obtain the final volumetric product shrinkage. The disadvantage of this method is that no distinction can be made between shrinkage in flow, transverse and thickness direction. In practice, however, it is well known that thickness shrinkage can well be 5 to 10 times larger than in-plane shrinkage and that shrinkage in flow and transverse directions may differ due to filler or crystallization effects. Commercial codes like MoldFlow and C-Mold calculate shrinkage in a post processing step from the thermal stress distribution. They probably neglect pressure-induced stresses and, therefore, also the solidification pressure term outlined in the next section. This can be a possible cause of the often surprisingly large discrepancies between predicted and measured shrinkages (e.g., 12, 14, 15, 17).

Recently, three other shrinkage models were proposed. Jansen and Titomanlio (22, 28) proposed a simple thermoelastic model taking into account pressure effects and Poisson expansion on thickness shrinkage, but neglecting viscoelastic effects. Their final equations for in-plane shrinkage are similar to the semi-empirical model proposed by Kumazawa (4). A complete viscoelastic theory for shrinkage predictions is given by Bushko and Stokes (21, 29), In this paper, however, the thermoelastic model is discussed.

THEORY

The idea explored in the thermoelastic model is that during solidification no relaxation and creep occurs and that stresses start to build up as soon as the temperature drops below the solidification temperature. A product that is restrained from shrinking during solidification will then build up tensile stresses as a result of thermal and crystallization shrinkage. In addition, pressure effects should be considered. A layer that solidified under pressure is compressed with respect to atmospheric conditions. If it were to expand freely after ejection, it would expand proportionally to the pressure during solidification (denoted as [P.sub.s]). Since all layers solidify under different pressures, the product expands proportionally to the gapwise averaged solidification pressure, [Mathematical Expression Omitted]. This effect may balance or even exceed the thermal and crystallization effects. The local in-plane and thickness shrinkages, denoted as [S.sub.x], [S.sub.y] and [S.sub.z] respectively can then be expresses as (22, 28)

[Mathematical Expression Omitted] (1)

[Mathematical Expression Omitted] (2)

with

[Mathematical Expression Omitted]. (3)

Here [Alpha] and [Beta] stand for the linear expansion and compressibility, [T.sub.s] for the solidification temperature (either [T.sub.g] or [T.sub.m]), [Mathematical Expression Omitted] for the gapwise averaged crystallinity and [C.sub.cr] = ([[Rho].sub.c] - [[Rho].sub.a])/3[[Rho].sub.a] for the maximum crystallization shrinkage. The equations clearly show how expansion effects are caused by the average local pressure balance against thermal and crystallization shrinkage. Note that the second term in Eq 2 is evaluated between the instant of solidification of each layer, denoted as [t.sub.sz], and the instant of ejection, [t.sub.e]. Therefore, the thickness shrinkage equation contains a term proportional to the pressure just before ejection and takes Into account the material expansion due to a nonvanishing pressure. The last term in Eq 2 is the mold deformation term consisting of a stiffness constant and the gate freeze-off pressure, [P.sub.gf] (22). If the modulus shows a strong variation over the thickness, the equations become slightly more complicated (23).

EXPERIMENTAL

The experiments were performed on a 175-ton Engel injection molding machine with a film-gated rectangular cavity with nominal dimensions 120 x 300 x 2.4 mm. The mold is equipped with three pressure transducers at 14 mm (P1), 150 mm (P2) and 286 mm (P3) from the gate and nine thermocouples. All pressure, temperature, and screw velocity data is recorded using a data acquisition system. On one of the two mold halves a 10-mm-wide grid was engraved covering the entire product. The line thickness was approximately 5 [[micro]meter]. The distances between all grid-points were carefully measured with a Stras-mann traveling microscope and were used as a reference. Experimental shrinkages were then obtained as

S = [d.sub.mold] - [d.sub.product]/[d.sub.mold] (4)

The scatter between individual length measurements turned out to be of the order of 15 [[micro]meter]. Reference distances of 30 to 50 mm will therefore result in shrinkage errors of less than 0.05%, which was considered to be acceptable for our purposes. The standard measurement procedure consisted of measuring the coordinates of four grid points centered around transducer P2 (halfway the product) and 50 mm apart. With these data two length and two width shrinkage values were calculated. This procedure was repeated for 3 to 5 products of each molding condition. Finally all shrinkages were averaged yielding a single length and width shrinkage value for each molding condition. All products were stored in a conditioned room at 23 [degrees] C, 50%RH and were measured two days after production. For some products, measurements were repeated at increasing time intervals to assess the shrinkage change in time.

The materials used were four amorphous resins (PC, PS, ABS and HIPS) and two semicrystalline materials (PBT and HDPE), of which the PBT was also available in a 30% glass filled grade. The materials are listed in Table 1. Attention was paid in obtaining reliable [TABULAR DATA FOR TABLE 1 OMITTED] [TABULAR DATA FOR TABLE 2 OMITTED] data for the coefficients of thermal expansion and the compressibility since these are clearly the key parameters of the model above. Agreement between various data sources is often poor. It turned out that for most materials the standard deviation in reported values for [Alpha] and [Beta] was about 10% of the actual values. In Table 1 the average values are listed. In cases where the disagreement in literature data was particularly large, additional measurements were performed in our own laboratory. The measurements of the compressibility were done in a pressure cell containing silicon oil and a sample containing two strain gauges. Corrections for the effect of pressure on strain gauges were taken into account (36).

The processing conditions that were varied are the holding pressure ([P.sub.h]), screw velocity (V), melt temperature ([T.sub.i]) and mold wall temperature ([T.sub.w]). Holding time ([t.sub.h]) and cooling time ([t.sub.c]) were kept constant. All conditions are listed in Table 2. The standard conditions for every parameter are underlined.

RESULTS

Effect of Flowpath

In order to check the shrinkage uniformity along the flowpath, length and width shrinkages were measured as a function of the distance from gate for PC, PS, PBT, and HDPE. As can be seen in Fig. 1, the shrinkage for the amorphous materials PC and PS is low and constant along the flowpath. No significant anisotropy effects can be detected. For the semicrystalline PBT, the as-molded shrinkage is considerably larger and varies from 2.5% near the gate to 3% at the end of the flowpath. Near the gate, length shrinkage is slightly larger than width shrinkage. For HDPE [ILLUSTRATION FOR FIGURE 2 OMITTED] the anisotropy effects are much larger and vary along the flowpath. Near the gate, length shrinkage is about 1% larger than width shrinkage while at the end of flow the reverse is true. Note that this is similar to Thomas's observations for PP (20).

Effect of Molding Conditions

In Fig. 3 the shrinkages for all amorphous materials are plotted as a function of the processing conditions. The symbols refer to measured length (crosses) and width (triangles) shrinkages, while the full lines denote the calculated shrinkages (to be discussed in the next section). The following observations can be made. First, the shrinkages all vary between 0.4% and 0.9%. The second observation is that increasing holding pressure and melt temperature both decrease the product shrinkage. Injection velocity and mold temperature do not have large effect on shrinkage. For semicrystalline materials [ILLUSTRATION FOR FIGURE 4 OMITTED] the situation is slightly different. Now the packing pressure seems to be the parameter with the largest effect on shrinkage. All other parameters did not show clear effects, just as reported in other studies (see previous section).

Effect of Glass Fibers on Shrinkage

This effect is shown in more detail in Fig. 5. Clearly, the addition of short glass fibers has a dramatic effect on the length shrinkage (drop from about 3% to 0.2% shrinkage). Also the effect on width shrinkage is considerable (decrease of about 0.7%). Next we see that the holding pressure affects only width shrinkage, whereas length shrinkage remains unaffected by the holding pressure. The injection velocity has only a small effect on width shrinkage and a negligible effect on length shrinkage of fiber reinforced PBT.

Post-Molding Shrinkage

Shrinkage changes were recorded over a least four decades of time, starting 20 minutes after production. The shrinkage changes in time (typically about 0.01%/decade) are shown in Table 3 below. In case of PBT and PBT-GF30 also, the weight was recorded in order to make sure that no water absorption took place during storage.

VERIFICATION OF THE THERMOELASTIC MODEL

Shrinkage predictions were obtained by using Eq. 1 and the data listed in Table 1. In order to avoid that errors in the pressure calculation would obscure the verification of Eq 1, we decided use measured pressure profiles to calculate the solidification pressure [P.sub.s](Z) (from P(t) and [z.sub.s](t)). In doing so one implicitly takes into account the effect of mass flow during packing. What counts in shrinkage calculations is the actual cavity pressure.

The solidified layer growth, [z.sub.s](t), was obtained by numerically solving a two-dimensional heat problem, including convection and dissipation effects but neglecting crystallization effects. The wall temperature and thermal parameters were considered as constant. The thermal parameters are listed in Table 4. Only one value for the crystallinity was used for all experiments since the gapwise averaged crystallinity did not vary much with processing conditions (37).

Alternatively, the solidified layer growth can be obtained from the following analytical approximations (38)

[Mathematical Expression Omitted] (5)

[Mathematical Expression Omitted], [b.sub.1] = ([Pi]/2)Bi/Bi + 1, [C.sub.1] = 4/[Pi][1 - [[Pi].sup.2]/8 / [(1 + Bi).sup.2]]

Here [Tau] = kt/([Rho][c.sub.p][D.sup.2]) denotes the dimensionless time and [B.sub.i] = hD/k the Biot number, which was taken as infinite here. In fact, it turned out that using Eq 5 instead of the numerically obtained layer growth resulted in only minor changes in the calculated shrinkages.

The results of the calculated shrinkages are included in Figs. 3 and 4 as the solid lines. It turns out that for amorphous materials the calculated shrinkages correspond almost exactly with the measured shrinkage data for all experimental conditions. For semicrystalline materials [ILLUSTRATION FOR FIGURE 4 OMITTED], the correspondence is poor and shrinkages are overpredicted. Moreover, the shrinkage predictions do not follow the experimentally observed trends with increasing holding pressure and injection velocity.

DISCUSSION

The main observation is that the simple thermoelastic model considered here is well able to predict shrinkages for amorphous materials. The fact that with these data mold shrinkage can be predicted so well clearly proves that eventual relaxation phenomena in the glass transition range did not have any effect at all on the final shrinkages. Therefore, we now can state that for amorphous materials the mold shrinkage phenomenon is well understood.

[TABULAR DATA FOR TABLE 4 OMITTED]

For semicrystalline materials the situation is different. Although the theory was designed to deal with shrinkage of the crystalline phase, the approach followed here obviously did not lead to satisfactory shrinkage predictions. Recall that possible effects on shrinkage of extra mass flow through crystallization are implicitly corrected for since the actual holding pressure was used to calculate shrinkage. Therefore, a different explanation has to be found. Some insight can be gained by inspecting the shrinkage versus pressure plots. By extrapolating to zero holding pressure an estimate of the shrinkage of a slab solidifying under ambient pressure can be obtained. By comparing this with Eq 1, it is obvious that this should correspond to the thermal contraction and crystallization terms. The slope of the shrinkage versus pressure graphs, on the other hand, is proportional to the linear compressibility, [Beta]. For unfilled PBT, for example, the thermal contraction and crystallization contributions seem to be estimated correctly whereas the compressibility is probably far too small. In fact, an excellent fit for all molding conditions would be obtained if the linear compressibility would have been a factor of ten larger.

We have reason to believe that for most experiments with crystalline materials, the product did not remain fixated in the mold and started to shrink before being completely solidified. In the derivation leading to Eq 1, however, the product was assumed to remain fixed. It is therefore expected that experiments with constrained products should yield shrinkage results closer to the predicted ones. Alternatively, one can use the in-mold shrinkage analysis (1, 22) to get a more reliable prediction.

Also, for the fiber filled PBT, the pressure term for width shrinkage was underestimated. For length shrinkage, on the other hand, the measured compressibility is of the right order but now the initial value is overestimated. The most probable cause of this overestimation is a too large value for the crystallization term, since thermal contraction is much smaller and relatively well understood. There is, in fact, no reason why (shear induced) crystallization should not cause anisotropic shrinkage, just as the other dilation terms. This, of course, then poses the practical problem of measuring the crystallization contraction in the three independent directions. An additional complication is that fibers most probably enhance shear induced crystallization (39).

Considering the post-molding shrinkage in Table 3, we observe that all shrinkage rates are relatively small. A sample of polycarbonate, for example, experiences an extra shrinkage of only 0.01% between the first day after production and 100 days later. The data for polycarbonate and polystyrene corresponds well with Greiner et al. (27) who reported at room temperature a three times larger volumetric shrinkage rate for PS as compared with PC. The negative number for width shrinkage of PBT-GF30 falls within the measurement uncertainty. The rather large difference between length and width shrinkage for HDPE is most probably related to recrystallization effects.

CONCLUSIONS AND FUTURE WORK

Shrinkage of injection molded products is most influenced by the holding pressure and the melt temperature. An increase in those parameters causes a decrease in shrinkage. The effects of injection velocity and mold temperature on shrinkage are much smaller and differ for each material. The simple thermoelastic model employed here to interpret the measurements was seen to give highly reliable predictions for all amorphous materials without any adjustable parameters. For semicrystalline materials, the shrinkages were overpredicted, which was attributed to in-mold shrinkage effects.

ACKNOWLEDGMENTS

The authors acknowledge PTN for their financial support and Dow Chemicals and Philips Drachten for kindly supplying most of the materials. Special thanks to Gerard Semmekrot, Ze Cunha, Kees Bos, Marco Freriksen and Hendrik de Vries, who all contributed to this project. Remko Akkerman and Krista Bouma are kindly acknowledged for their help with the numerical calculations and DSC measurements, respectively.

REFERENCES

1. K. M. B. Jansen, G. Titomanlio and R. Pantani, "In-Mold Shrinkage Measurements of PS Samples With Strain Gauges," Intern. Polym. Proc., XII, 4 (1997).

2. D. Rosato and D. Rosato, Injection Molding Handbook, 2nd ed., p. 484, Chapman and Hall, London (1995).

3. A. Mamat et al., Polym. Eng., Sci., 35, 1511 (1995).

4. H. Kumazawa, SPE ANTEC Tech. Papers, 40, 817 (1994).

5. M. F. Bain et al., SPE ANTEC Tech. Papers, 38, 977 (1992).

6. P. Delbarre et al., SPE ANTEC Tech. Papers, 87, 301 (1991).

7. A. I. Isayev and T. Hariharan, Polym. Eng. Sci., 25, 271 (1985).

8. M. R. Nagy, SPE ANTEC Tech. Papers, 39, 2155 (1993).

9. C. Liu and L. T. Manzione, Polym. Eng. Sci., 36, 1 (1996).

10. K. M. B. Jansen, G. Titomanlio, and R. Pantani, Polym. Eng. Sci., 38, 254 (1998).

11. V. Leo and C. H. Cuvelliez, Polym. Eng. Sci, 36, 1961 (1996).

12. C. A. Heiber et al., SPE ANTEC Tech. Papers, 37, 259 (1991).

13. L. P. Herbert et al., SPE ANTEC Tech. Papers, 37, 430 (1991).

14. S. J. Ni and K. K. Wang, SPE ANTEC Tech. Papers, 39, 612 (1993).

15. A. G. Gennari, SPE ANTEC Tech. Papers, 39, 3436 (1993).

16. G. Burke and D. Kazmer, SPE ANTECH Tech. Papers, 38, 1354 (1992).

17. R. M. Shay et al., Proc. RETEC (Nov. 1995).

18. H. Hies, Kunststoffe, 84, 1710 (1994).

19. C. S. Lee and A. Dubin, SPE ANTEC Tech. Papers, 36, 375 (1990).

20. R. Thomas and N. McCaffery SPE ANTEC Tech. Papers, 35, 371 (1989).

21. W. Busko and V. K. Stokes, SPE ANTEC Tech. Papers, 41, 484 (1995).

22. G. Titomanlio and K. M. B. Jansen, Polym. Eng. Sci., 36, 2041 (1996).

23. K. M. B. Jansen, D. J. van Dijk, and M. J. A. Freriksen, "Shrinkage Anisotropy in Fiber reinforced Injection Molded Products," Polym. Compos., in preparation.

24. T. W. Schmidt, PhD thesis, RWTH Aachen, Germany (1987).

25. Annual Book of ASTM Standards, Designation D995-89, Vol. 8.01 (1989).

26. L. C. E. Struik, Internal Stresses, Dimensional Stabilities and Molecular Orientations in Plastics, p. 177, Wiley and Sons, Brisbane (1990).

27. R. Greiner and F. R. Schwarzl, Rheol. Acta, 23, 387 (1984).

28. K. M. B. Jansen and G. Titomanlio, Polym. Eng. Sci., 36, 2029 (1996).

29. W. Busko and V. K. Stokes, Polym. Eng. Sci., 35, 351 (1995).

30. C-Mold 4.0 data.

31. VDMA, Kenndaten fuer die Verarbeitung Thermoplastischer Kunststoffe: Thermodynamik, Hanser Verlag, Munich (1986).

32. P. Zoller and Walsh, Standard Pressure-Volume-Temperature Data for Polymers, Technomic Publishing Company, Lancaster, Pa. (1995).

33. J. Brandrup and E. H. Immergut, Polymer Handbook, Wiley and Sons, New York (1989).

34. E. Moore, ed., Styrene Polymers, Wiley and Sons (1989).

35. H. Domininghaus, Die Kunststoffe und ihre Eigenschaften, VDI Verlag, Dusseldorf, Germany (1992).

36. K. M. B. Jansen, Experim. Mech., (in press).

37. H. W. J. de Vries, Master's thesis (1996).

38. K. M. B. Jansen, Int. J. Heat Mass Transfer, 38, 309 (1995).

39. B. Monasse, J. Mater. Sci., 27, 6047 (1992).

The objective of this paper is first to present the results of a systematic study on the effect of processing conditions on the dimensions of as-molded products. The second objective is to show that all shrinkage data is well described by a simple equation that relates shrinkage to the local pressure history. The study was done using seven common resins, being PS, ABS, HIPS, PC, PBT, PBT-GF30 and HDPE, and systematically varying holding pressure, injection velocity, mold temperature and melt temperature.

In general we may discern three types of shrinkage in injection molding: in-mold shrinkage (shrinkage during processing which may show up in extreme cases), as-molded shrinkage (the shrinkage just after mold opening, sometimes referred to as "mold shrinkage") and post-shrinkage (time effects during storage as physical aging, recrystallization, etc.). Here we will focus on as-molded shrinkage and, briefly, on postshrinkage effects. In-mold shrinkage is discussed in detail elsewhere (1).

In the past tables or nomograms (2) were used to correct for product shrinkage during mold design. However, with the increasing demands on product tolerances more exact information is required. Recent experimental studies show that as-molded shrinkage of injection molded products is affected by processing parameters as well as by mold geometry (3-24). All studies conclude that the holding pressure is by far the most important parameter affecting shrinkage. A higher holding pressure setting decreases part shrinkage in all directions. The second most important parameter is the injection temperature (3-7). Increasing the injection temperature was usually seen to reduce shrinkage (because of a better pressure transmission). Some authors reported an increase in shrinkage with increasing mold temperature (3, 4, 6, 8) while others concluded differently (5, 9). Increasing the holding time always decreases shrinkage until leveling off occurs at the gate freeze-off time (3, 4, 10, 11).

In most studies rectangular plates or tensile bars were considered. Exceptions are center gated disk molds (12, 13), box molds (14) and a flat plate with holes (15, 16). In only a few cases the geometry was considered as a variable (17-19). Geometry may affect shrinkage in two ways. First, geometry may affect flow and hence cause orientation effects (of either amorpous phase, crystalline phase or filler particles) resulting in shrinkage anisotropy. Second, geometrical constraints (ribs, bosses, etc.) affect the shrinkage boundary conditions. These effects are discussed elsewhere (1, 10, 13, 17, 18, 20-22).

Shrinkage variations along the flowpath are usually directly related to the local cavity pressure (3, 11, 17, 18, 20). For semicrystalline PP (3, 20) and PA (17, 20) its was shown that length and width shrinkage varied differently. In most cases, width shrinkage was slightly larger than length shrinkage, the only exception being Thomas's measurements on PP (20) where close to the gate length shrinkage is larger than width shrinkage and far from the gate the reverse holds true. Shay et al. (17) reported that for amorphous polycarbonate no differences between length and width shrinkage could be detected. For fiber filled resins, large differences between shrinkage in the flow direction and in the transverse direction (width) are always reported (e.g., 6, 18, 19, 23). Typical length shrinkage values are always close to 0.2%, while shrinkage in transverse direction approaches that of unfilled resins. In contrast to in-plane shrinkage, surprisingly little agreement in the literature is found between thickness shrinkage measurements. For similar molding conditions some authors report thickness shrinkage of the same order of magnitude as in-plane shrinkage (20) while others mention thickness shrinkages many times larger (and in some cases of opposite sign) than length and width shrinkage (4, 6, 10-12, 19, 24). Possible explanations for these observations are elastic expansion of the compressed polymer due to a nonvanishing cavity pressure (9, 10, 22), elastic deformation of the mold during packing (10, 11, 22, 24), flashing at high holding pressures (12), void formation in thicker bars (19) or the much larger thermal gradient in thickness direction (6). In practice, thickness shrinkage is most probably governed by a combination the first three effects.

In most studies, shrinkage is measured between 24 and 48 hours after production (25). It is, however, well known that shrinkage continues (slowly) during storage because of physical aging or recrystallization effects (5, 8, 26, 27). Since these are self-delaying processes, shrinkage must proceed proportional to the logarithm of time (26).

As a first attempt to deal with the parameters affecting shrinkage, statistical analysis methods were used to construct empirical fit functions based on shrinkage data of a limited number of experiments (3, 5, 8, 20). It is obvious that with this approach predictions are limited to the specific testing geometry and testing window. Such "models," moreover, do not have any physical meaning and are difficult to use for interpretation purposes.

A better way to try to understand shrinkage in injection molding is to consider the mold as a closed space, setup a material balance, and calculate the amount of mass accumulated in the mold. The volumetric shrinkage then follows from the pvT-diagram (7, 12, 24). In general these models use a Tait-like equation in combination with calculated temperature and pressure histories to obtain the final volumetric product shrinkage. The disadvantage of this method is that no distinction can be made between shrinkage in flow, transverse and thickness direction. In practice, however, it is well known that thickness shrinkage can well be 5 to 10 times larger than in-plane shrinkage and that shrinkage in flow and transverse directions may differ due to filler or crystallization effects. Commercial codes like MoldFlow and C-Mold calculate shrinkage in a post processing step from the thermal stress distribution. They probably neglect pressure-induced stresses and, therefore, also the solidification pressure term outlined in the next section. This can be a possible cause of the often surprisingly large discrepancies between predicted and measured shrinkages (e.g., 12, 14, 15, 17).

Recently, three other shrinkage models were proposed. Jansen and Titomanlio (22, 28) proposed a simple thermoelastic model taking into account pressure effects and Poisson expansion on thickness shrinkage, but neglecting viscoelastic effects. Their final equations for in-plane shrinkage are similar to the semi-empirical model proposed by Kumazawa (4). A complete viscoelastic theory for shrinkage predictions is given by Bushko and Stokes (21, 29), In this paper, however, the thermoelastic model is discussed.

THEORY

The idea explored in the thermoelastic model is that during solidification no relaxation and creep occurs and that stresses start to build up as soon as the temperature drops below the solidification temperature. A product that is restrained from shrinking during solidification will then build up tensile stresses as a result of thermal and crystallization shrinkage. In addition, pressure effects should be considered. A layer that solidified under pressure is compressed with respect to atmospheric conditions. If it were to expand freely after ejection, it would expand proportionally to the pressure during solidification (denoted as [P.sub.s]). Since all layers solidify under different pressures, the product expands proportionally to the gapwise averaged solidification pressure, [Mathematical Expression Omitted]. This effect may balance or even exceed the thermal and crystallization effects. The local in-plane and thickness shrinkages, denoted as [S.sub.x], [S.sub.y] and [S.sub.z] respectively can then be expresses as (22, 28)

[Mathematical Expression Omitted] (1)

[Mathematical Expression Omitted] (2)

with

[Mathematical Expression Omitted]. (3)

Here [Alpha] and [Beta] stand for the linear expansion and compressibility, [T.sub.s] for the solidification temperature (either [T.sub.g] or [T.sub.m]), [Mathematical Expression Omitted] for the gapwise averaged crystallinity and [C.sub.cr] = ([[Rho].sub.c] - [[Rho].sub.a])/3[[Rho].sub.a] for the maximum crystallization shrinkage. The equations clearly show how expansion effects are caused by the average local pressure balance against thermal and crystallization shrinkage. Note that the second term in Eq 2 is evaluated between the instant of solidification of each layer, denoted as [t.sub.sz], and the instant of ejection, [t.sub.e]. Therefore, the thickness shrinkage equation contains a term proportional to the pressure just before ejection and takes Into account the material expansion due to a nonvanishing pressure. The last term in Eq 2 is the mold deformation term consisting of a stiffness constant and the gate freeze-off pressure, [P.sub.gf] (22). If the modulus shows a strong variation over the thickness, the equations become slightly more complicated (23).

EXPERIMENTAL

The experiments were performed on a 175-ton Engel injection molding machine with a film-gated rectangular cavity with nominal dimensions 120 x 300 x 2.4 mm. The mold is equipped with three pressure transducers at 14 mm (P1), 150 mm (P2) and 286 mm (P3) from the gate and nine thermocouples. All pressure, temperature, and screw velocity data is recorded using a data acquisition system. On one of the two mold halves a 10-mm-wide grid was engraved covering the entire product. The line thickness was approximately 5 [[micro]meter]. The distances between all grid-points were carefully measured with a Stras-mann traveling microscope and were used as a reference. Experimental shrinkages were then obtained as

S = [d.sub.mold] - [d.sub.product]/[d.sub.mold] (4)

The scatter between individual length measurements turned out to be of the order of 15 [[micro]meter]. Reference distances of 30 to 50 mm will therefore result in shrinkage errors of less than 0.05%, which was considered to be acceptable for our purposes. The standard measurement procedure consisted of measuring the coordinates of four grid points centered around transducer P2 (halfway the product) and 50 mm apart. With these data two length and two width shrinkage values were calculated. This procedure was repeated for 3 to 5 products of each molding condition. Finally all shrinkages were averaged yielding a single length and width shrinkage value for each molding condition. All products were stored in a conditioned room at 23 [degrees] C, 50%RH and were measured two days after production. For some products, measurements were repeated at increasing time intervals to assess the shrinkage change in time.

The materials used were four amorphous resins (PC, PS, ABS and HIPS) and two semicrystalline materials (PBT and HDPE), of which the PBT was also available in a 30% glass filled grade. The materials are listed in Table 1. Attention was paid in obtaining reliable [TABULAR DATA FOR TABLE 1 OMITTED] [TABULAR DATA FOR TABLE 2 OMITTED] data for the coefficients of thermal expansion and the compressibility since these are clearly the key parameters of the model above. Agreement between various data sources is often poor. It turned out that for most materials the standard deviation in reported values for [Alpha] and [Beta] was about 10% of the actual values. In Table 1 the average values are listed. In cases where the disagreement in literature data was particularly large, additional measurements were performed in our own laboratory. The measurements of the compressibility were done in a pressure cell containing silicon oil and a sample containing two strain gauges. Corrections for the effect of pressure on strain gauges were taken into account (36).

The processing conditions that were varied are the holding pressure ([P.sub.h]), screw velocity (V), melt temperature ([T.sub.i]) and mold wall temperature ([T.sub.w]). Holding time ([t.sub.h]) and cooling time ([t.sub.c]) were kept constant. All conditions are listed in Table 2. The standard conditions for every parameter are underlined.

RESULTS

Effect of Flowpath

In order to check the shrinkage uniformity along the flowpath, length and width shrinkages were measured as a function of the distance from gate for PC, PS, PBT, and HDPE. As can be seen in Fig. 1, the shrinkage for the amorphous materials PC and PS is low and constant along the flowpath. No significant anisotropy effects can be detected. For the semicrystalline PBT, the as-molded shrinkage is considerably larger and varies from 2.5% near the gate to 3% at the end of the flowpath. Near the gate, length shrinkage is slightly larger than width shrinkage. For HDPE [ILLUSTRATION FOR FIGURE 2 OMITTED] the anisotropy effects are much larger and vary along the flowpath. Near the gate, length shrinkage is about 1% larger than width shrinkage while at the end of flow the reverse is true. Note that this is similar to Thomas's observations for PP (20).

Effect of Molding Conditions

In Fig. 3 the shrinkages for all amorphous materials are plotted as a function of the processing conditions. The symbols refer to measured length (crosses) and width (triangles) shrinkages, while the full lines denote the calculated shrinkages (to be discussed in the next section). The following observations can be made. First, the shrinkages all vary between 0.4% and 0.9%. The second observation is that increasing holding pressure and melt temperature both decrease the product shrinkage. Injection velocity and mold temperature do not have large effect on shrinkage. For semicrystalline materials [ILLUSTRATION FOR FIGURE 4 OMITTED] the situation is slightly different. Now the packing pressure seems to be the parameter with the largest effect on shrinkage. All other parameters did not show clear effects, just as reported in other studies (see previous section).

Effect of Glass Fibers on Shrinkage

This effect is shown in more detail in Fig. 5. Clearly, the addition of short glass fibers has a dramatic effect on the length shrinkage (drop from about 3% to 0.2% shrinkage). Also the effect on width shrinkage is considerable (decrease of about 0.7%). Next we see that the holding pressure affects only width shrinkage, whereas length shrinkage remains unaffected by the holding pressure. The injection velocity has only a small effect on width shrinkage and a negligible effect on length shrinkage of fiber reinforced PBT.

Post-Molding Shrinkage

Shrinkage changes were recorded over a least four decades of time, starting 20 minutes after production. The shrinkage changes in time (typically about 0.01%/decade) are shown in Table 3 below. In case of PBT and PBT-GF30 also, the weight was recorded in order to make sure that no water absorption took place during storage.

VERIFICATION OF THE THERMOELASTIC MODEL

Shrinkage predictions were obtained by using Eq. 1 and the data listed in Table 1. In order to avoid that errors in the pressure calculation would obscure the verification of Eq 1, we decided use measured pressure profiles to calculate the solidification pressure [P.sub.s](Z) (from P(t) and [z.sub.s](t)). In doing so one implicitly takes into account the effect of mass flow during packing. What counts in shrinkage calculations is the actual cavity pressure.

The solidified layer growth, [z.sub.s](t), was obtained by numerically solving a two-dimensional heat problem, including convection and dissipation effects but neglecting crystallization effects. The wall temperature and thermal parameters were considered as constant. The thermal parameters are listed in Table 4. Only one value for the crystallinity was used for all experiments since the gapwise averaged crystallinity did not vary much with processing conditions (37).

Alternatively, the solidified layer growth can be obtained from the following analytical approximations (38)

[Mathematical Expression Omitted] (5)

[Mathematical Expression Omitted], [b.sub.1] = ([Pi]/2)Bi/Bi + 1, [C.sub.1] = 4/[Pi][1 - [[Pi].sup.2]/8 / [(1 + Bi).sup.2]]

Here [Tau] = kt/([Rho][c.sub.p][D.sup.2]) denotes the dimensionless time and [B.sub.i] = hD/k the Biot number, which was taken as infinite here. In fact, it turned out that using Eq 5 instead of the numerically obtained layer growth resulted in only minor changes in the calculated shrinkages.

The results of the calculated shrinkages are included in Figs. 3 and 4 as the solid lines. It turns out that for amorphous materials the calculated shrinkages correspond almost exactly with the measured shrinkage data for all experimental conditions. For semicrystalline materials [ILLUSTRATION FOR FIGURE 4 OMITTED], the correspondence is poor and shrinkages are overpredicted. Moreover, the shrinkage predictions do not follow the experimentally observed trends with increasing holding pressure and injection velocity.

DISCUSSION

The main observation is that the simple thermoelastic model considered here is well able to predict shrinkages for amorphous materials. The fact that with these data mold shrinkage can be predicted so well clearly proves that eventual relaxation phenomena in the glass transition range did not have any effect at all on the final shrinkages. Therefore, we now can state that for amorphous materials the mold shrinkage phenomenon is well understood.

Table 3. Shrinkage Change in Time [%/Decade] for Standard Conditions of All Materials Considered in This Study. Aging Conditions: 23 [degrees] C, 50% Humidity. PC PS ABS HIPS PBT PBT-GF30 HDPE Length 0.005 0.023 0.015 0.025 0.006 -0.002 0.033 Width 0.005 0.016 0.008 0.021 0.004 0.008 0.01?

[TABULAR DATA FOR TABLE 4 OMITTED]

For semicrystalline materials the situation is different. Although the theory was designed to deal with shrinkage of the crystalline phase, the approach followed here obviously did not lead to satisfactory shrinkage predictions. Recall that possible effects on shrinkage of extra mass flow through crystallization are implicitly corrected for since the actual holding pressure was used to calculate shrinkage. Therefore, a different explanation has to be found. Some insight can be gained by inspecting the shrinkage versus pressure plots. By extrapolating to zero holding pressure an estimate of the shrinkage of a slab solidifying under ambient pressure can be obtained. By comparing this with Eq 1, it is obvious that this should correspond to the thermal contraction and crystallization terms. The slope of the shrinkage versus pressure graphs, on the other hand, is proportional to the linear compressibility, [Beta]. For unfilled PBT, for example, the thermal contraction and crystallization contributions seem to be estimated correctly whereas the compressibility is probably far too small. In fact, an excellent fit for all molding conditions would be obtained if the linear compressibility would have been a factor of ten larger.

We have reason to believe that for most experiments with crystalline materials, the product did not remain fixated in the mold and started to shrink before being completely solidified. In the derivation leading to Eq 1, however, the product was assumed to remain fixed. It is therefore expected that experiments with constrained products should yield shrinkage results closer to the predicted ones. Alternatively, one can use the in-mold shrinkage analysis (1, 22) to get a more reliable prediction.

Also, for the fiber filled PBT, the pressure term for width shrinkage was underestimated. For length shrinkage, on the other hand, the measured compressibility is of the right order but now the initial value is overestimated. The most probable cause of this overestimation is a too large value for the crystallization term, since thermal contraction is much smaller and relatively well understood. There is, in fact, no reason why (shear induced) crystallization should not cause anisotropic shrinkage, just as the other dilation terms. This, of course, then poses the practical problem of measuring the crystallization contraction in the three independent directions. An additional complication is that fibers most probably enhance shear induced crystallization (39).

Considering the post-molding shrinkage in Table 3, we observe that all shrinkage rates are relatively small. A sample of polycarbonate, for example, experiences an extra shrinkage of only 0.01% between the first day after production and 100 days later. The data for polycarbonate and polystyrene corresponds well with Greiner et al. (27) who reported at room temperature a three times larger volumetric shrinkage rate for PS as compared with PC. The negative number for width shrinkage of PBT-GF30 falls within the measurement uncertainty. The rather large difference between length and width shrinkage for HDPE is most probably related to recrystallization effects.

CONCLUSIONS AND FUTURE WORK

Shrinkage of injection molded products is most influenced by the holding pressure and the melt temperature. An increase in those parameters causes a decrease in shrinkage. The effects of injection velocity and mold temperature on shrinkage are much smaller and differ for each material. The simple thermoelastic model employed here to interpret the measurements was seen to give highly reliable predictions for all amorphous materials without any adjustable parameters. For semicrystalline materials, the shrinkages were overpredicted, which was attributed to in-mold shrinkage effects.

ACKNOWLEDGMENTS

The authors acknowledge PTN for their financial support and Dow Chemicals and Philips Drachten for kindly supplying most of the materials. Special thanks to Gerard Semmekrot, Ze Cunha, Kees Bos, Marco Freriksen and Hendrik de Vries, who all contributed to this project. Remko Akkerman and Krista Bouma are kindly acknowledged for their help with the numerical calculations and DSC measurements, respectively.

REFERENCES

1. K. M. B. Jansen, G. Titomanlio and R. Pantani, "In-Mold Shrinkage Measurements of PS Samples With Strain Gauges," Intern. Polym. Proc., XII, 4 (1997).

2. D. Rosato and D. Rosato, Injection Molding Handbook, 2nd ed., p. 484, Chapman and Hall, London (1995).

3. A. Mamat et al., Polym. Eng., Sci., 35, 1511 (1995).

4. H. Kumazawa, SPE ANTEC Tech. Papers, 40, 817 (1994).

5. M. F. Bain et al., SPE ANTEC Tech. Papers, 38, 977 (1992).

6. P. Delbarre et al., SPE ANTEC Tech. Papers, 87, 301 (1991).

7. A. I. Isayev and T. Hariharan, Polym. Eng. Sci., 25, 271 (1985).

8. M. R. Nagy, SPE ANTEC Tech. Papers, 39, 2155 (1993).

9. C. Liu and L. T. Manzione, Polym. Eng. Sci., 36, 1 (1996).

10. K. M. B. Jansen, G. Titomanlio, and R. Pantani, Polym. Eng. Sci., 38, 254 (1998).

11. V. Leo and C. H. Cuvelliez, Polym. Eng. Sci, 36, 1961 (1996).

12. C. A. Heiber et al., SPE ANTEC Tech. Papers, 37, 259 (1991).

13. L. P. Herbert et al., SPE ANTEC Tech. Papers, 37, 430 (1991).

14. S. J. Ni and K. K. Wang, SPE ANTEC Tech. Papers, 39, 612 (1993).

15. A. G. Gennari, SPE ANTEC Tech. Papers, 39, 3436 (1993).

16. G. Burke and D. Kazmer, SPE ANTECH Tech. Papers, 38, 1354 (1992).

17. R. M. Shay et al., Proc. RETEC (Nov. 1995).

18. H. Hies, Kunststoffe, 84, 1710 (1994).

19. C. S. Lee and A. Dubin, SPE ANTEC Tech. Papers, 36, 375 (1990).

20. R. Thomas and N. McCaffery SPE ANTEC Tech. Papers, 35, 371 (1989).

21. W. Busko and V. K. Stokes, SPE ANTEC Tech. Papers, 41, 484 (1995).

22. G. Titomanlio and K. M. B. Jansen, Polym. Eng. Sci., 36, 2041 (1996).

23. K. M. B. Jansen, D. J. van Dijk, and M. J. A. Freriksen, "Shrinkage Anisotropy in Fiber reinforced Injection Molded Products," Polym. Compos., in preparation.

24. T. W. Schmidt, PhD thesis, RWTH Aachen, Germany (1987).

25. Annual Book of ASTM Standards, Designation D995-89, Vol. 8.01 (1989).

26. L. C. E. Struik, Internal Stresses, Dimensional Stabilities and Molecular Orientations in Plastics, p. 177, Wiley and Sons, Brisbane (1990).

27. R. Greiner and F. R. Schwarzl, Rheol. Acta, 23, 387 (1984).

28. K. M. B. Jansen and G. Titomanlio, Polym. Eng. Sci., 36, 2029 (1996).

29. W. Busko and V. K. Stokes, Polym. Eng. Sci., 35, 351 (1995).

30. C-Mold 4.0 data.

31. VDMA, Kenndaten fuer die Verarbeitung Thermoplastischer Kunststoffe: Thermodynamik, Hanser Verlag, Munich (1986).

32. P. Zoller and Walsh, Standard Pressure-Volume-Temperature Data for Polymers, Technomic Publishing Company, Lancaster, Pa. (1995).

33. J. Brandrup and E. H. Immergut, Polymer Handbook, Wiley and Sons, New York (1989).

34. E. Moore, ed., Styrene Polymers, Wiley and Sons (1989).

35. H. Domininghaus, Die Kunststoffe und ihre Eigenschaften, VDI Verlag, Dusseldorf, Germany (1992).

36. K. M. B. Jansen, Experim. Mech., (in press).

37. H. W. J. de Vries, Master's thesis (1996).

38. K. M. B. Jansen, Int. J. Heat Mass Transfer, 38, 309 (1995).

39. B. Monasse, J. Mater. Sci., 27, 6047 (1992).

Printer friendly Cite/link Email Feedback | |

Author: | Jansen, K.M.B.; Dijk, D.J. Van; Husselman, M.H. |
---|---|

Publication: | Polymer Engineering and Science |

Date: | May 1, 1998 |

Words: | 3935 |

Previous Article: | The recovery behavior of crosslinked closed cell polyolefin foams. |

Next Article: | Effects of processing conditions and copolymer molecular weight on the mechanical properties and morphology of compatibilized polymer blends. |

Topics: |

## Reader Opinion