|  | 
                                                 |  | 
                                                 | Sprue bushings Sprue bushing connects the machine nozzle to the runner system. To  ensure clean ejection from the bushing the bushing should have a smooth,  tapered internal finish and have been polished in the direction of  draw. The use of a positive sprue puller is recommended.  A cold slug  well should also be included in the design. This prevents a slug of cold  material from entering the feed system and finally the part, which  could affect the final properties of the finished part.
 
 The dimensions of the sprue depend primarily on the dimensions of the  molded part in particular the wall thickness. As a guideline:
 
 Sprue design.The sprue must not freeze before any other cross section in order to permit sufficient transmission of holding pressure. The sprue must de- easily and reliably.
 
 | 
                                                 |  | 
|  | 
|  | 
                                                 |  | 
|  | 
|  | 
|  | 
|  | 
|  | 
                                                 | Runner geometry The ideal runner cross section is circular as this ensures favorable  melt flow and cooling. However, it takes more effort to build circular  runners because one half must be machined in the fixed mold part and the  other half in the moving mold part. The higher the surface to volume  ratio, the more efficient the runner.
 
 Full trapezoidal channels in one of the two mold halves provide a  cheaper alternative (see figure below). The rounded off trapezoidal  cross section combines ease of machining in one mold half with a cross  section that approaches the desired circular shape. The height of a  trapezoidal runner must be at least 80% of the largest width.
 
 Half round runners are not recommended because of their low volume to surface ratio.
 
 Cross sectional properties for various runner profiles.
 
 | 
                                                 |  |  | 
|  | 
|  | 
|  | 
|  | 
|  | 
                                                 | Runner dimensions The diameter of a runner highly depends on its length in addition to the  part volume, part flow length, machine capacity, and gate size.  Generally they must never be smaller than the largest wall thickness of  the product and usually lie within the range 3 mm to 15 mm. Recommended  runner dimensions are provided in the table below. The selection of a  cold runner diameter should be based on standard machine tool cutter  sizes.
 
 Maximum runner length for specific diameters.
 
 | 
                                                 |  | 
|  | 
|  | 
|  | 
|  | 
|  | 
                                                 | While large  runners facilitate the flow of material at relatively low pressure  requirements, they require a longer cooling time, more material  consumption and scrap, and more clamping force. Designing the smallest  adequate runner system will maximize efficiency in both raw material use  and energy consumption in molding. The runner size reduction is  constrained by the molding machine's injection pressure capability. 
 Initially runner diameters can be calculated with the following formula  below. Further fine-tuning can then be performed with the use of flow  analysis software where effects such as shear heating and skin layer  formation can be taken into consideration.
 
 
 | 
                                                 |  | 
|  | 
|  | 
|  | 
|  | 
|  | 
                                                 | Runner layout There are 3 basic layout systems used for multi-cavity systems. These can be catorigized as follows:
 
 Unbalanced runner systems lead to unequal filling, post-filling and cooling of individual cavities that may cause failures like:Standard (herringbone) runner system "H" bridge (branching) runner system Radial (star) runner system 
 
 Example of unbalanced feed systems.Incomplete fillingDifferences in product properties Shrinkage differences/warpageSink marksFlashPoor mold releaseInconsistency
 
 
 | 
                                                 |  | 
|  | 
|  | 
|  | 
|  | 
|  | 
                                                 | Although the  herringbone is naturally unbalanced, it can accommodate more cavities  than its naturally balanced counterparts, with minimum runner volume and  less tooling cost. With computer aided flow simulation it is possible  to adjust primary and secondary runner dimensions to obtain equal  filling patterns. Keep in mind that non-standard runner diameters will  increase manufacturing and maintenance costs. Adjusting  runner dimensions to achieve equal filling may not be sufficient in  critical parts to prevent potential failures. Special attention is  required for:
 
 It is preferred to design naturally balanced runners as shown in the figure below.Very small components Parts with thin sectionsParts that permit no sink marksParts with a primary runner length much larger than secondary runner length. 
 
 Naturally balanced feed systems.
 
 | 
                                                 |  | 
|  | 
|  | 
|  | 
|  | 
|  | 
                                                 | The "H"  (branching) and radial (star) systems are considered to be naturally  balanced. The naturally balanced runner provides equal distance and  runner size from the sprue to all the cavities, so that each cavity  fills under the same conditions. 
 When high quality and tight tolerances are required the cavities must be  uniform. Family moulds are not considered suitable. Nevertheless, it  might be necessary for economical reasons to mold different parts in one  mold. The cavity with the largest component should be placed nearest to  the sprue.
 
 The maximum number of cavities in a mold depends on the total cavity  volume including runners in relation to the maximum barrel capacity and  clamping force of the injection molding machine.
 
 Branched runners
 Each time a runner is branched, the diameter of the branch runners  should be smaller than the main runner, because less material flows  through the branches and it is economically desirable to use minimum  material in the runners.
 
 Where N is the number of branches, the relationship between the  main runner diameter (dmain) and the branch runner diameter (dbranch) is
 
 dmain= dbranch x N1/3
 At all runner  intersections there should be a cold slug well. The cold slug well  helps the flow of material through the runner system by stopping colder,  higher viscosity material moving at the forefront of the molten mass  entering into the cavity. The length of the well is usually equal to or  greater than the runner diameter and this is achieved by extending the  length of the primary runner at the intersection with the secondary  runner (see figure below).
 
 
 Recommended design of cold slug well or overflow.
 
 | 
                                                 |  | 
No comments:
Post a Comment