注塑模具英文文献
塑料注塑模具中英文对照外文翻译文献

外文翻译及原文(文档含英文原文和中文翻译)【原文一】CONCURRENT DESIGN OF PLASTICS INJECTION MOULDS AbstractThe plastic product manufacturing industry has been growing rapidly in recent years. One of the most popular processes for making plastic parts is injection moulding. The design of injection mould is critically important to product quality and efficient product processing.Mould-making companies, who wish to maintain the competitive edge, desire to shorten both design and manufacturing leading times of the by applying a systematic mould design process. The mould industry is an important support industry during the product development process, serving as an important link between the product designer and manufacturer. Product development has changed from the traditional serial process of design, followed by manufacture, to a more organized concurrent process where design and manufacture are considered at a very early stage of design. The concept of concurrent engineering (CE) is no longer new and yet it is still applicable and relevant in today’s manuf acturing environment. Team working spirit, management involvement, total design process and integration of IT tools are still the essence of CE. The application of The CE process to the design of an injection process involves the simultaneous consideration of plastic part design, mould design and injection moulding machine selection, production scheduling and cost as early as possible in the design stage.This paper presents the basic structure of an injection mould design. The basis of this system arises from an analysis of the injection mould design process for mould design companies. This injection mould design system covers both the mould design process and mould knowledge management. Finally the principle of concurrent engineering process is outlined and then its principle is applied to the design of a plastic injection mould.Keywords :Plastic injection mould design, Concurrent engineering, Computer aided engineering, Moulding conditions, Plastic injection moulding, Flow simulation1.IntroductionInjection moulds are always expensive to make, unfortunately without a mould it can not be possible ho have a moulded product. Every mould maker has his/her own approach to design a mould and there are many different ways of designing and building a mould. Surely one of the most critical parameters to be considered in the design stage of the mould is the number of cavities, methods of injection, types of runners, methods of gating, methods of ejection, capacity and features of the injection moulding machines. Mould cost, mould quality and cost of mould product are inseparableIn today’s completive environment, computer aided mould filling simulation packages can accurately predict the fill patterns of any part. This allows for quick simulations of gate placements and helps finding the optimal location. Engineers can perform moulding trials on the computer before the part design is completed. Process engineers can systematically predict a design and process window, and can obtain information about the cumulative effect of the process variables that influence part performance, cost, and appearance.2.Injection MouldingInjection moulding is one of the most effective ways to bring out the best in plastics. It is universally used to make complex, finished parts, often in a single step, economically, precisely and with little waste. Mass production of plastic parts mostly utilizes moulds. The manufacturing process and involving moulds must be designed after passing through the appearance evaluation and the structure optimization of the product design. Designers face a hugenumber of options when they create injection-moulded components. Concurrent engineering requires an engineer to consider the manufacturing process of the designed product in the development phase. A good design of the product is unable to go to the market if its manufacturing process is impossible or too expensive. Integration of process simulation, rapid prototyping and manufacturing can reduce the risk associated with moving from CAD to CAM and further enhance the validity of the product development.3. Importance of Computer Aided Injection Mould DesignThe injection moulding design task can be highly complex. Computer Aided Engineering (CAE) analysis tools provide enormous advantages of enabling design engineers to consider virtually and part, mould and injection parameters without the real use of any manufacturing and time. The possibility of trying alternative designs or concepts on the computer screen gives the engineers the opportunity to eliminate potential problems before beginning the real production. Moreover, in virtual environment, designers can quickly and easily asses the sensitivity of specific moulding parameters on the quality and manufacturability of the final product. All theseCAE tools enable all these analysis to be completed in a meter of days or even hours, rather than weeks or months needed for the real experimental trial and error cycles. As CAE is used in the early design of part, mould and moulding parameters, the cost savings are substantial not only because of best functioning part and time savings but also the shortens the time needed to launch the product to the market.The need to meet set tolerances of plastic part ties in to all aspects of the moulding process, including part size and shape, resin chemical structure, the fillers used, mould cavity layout, gating, mould cooling and the release mechanisms used. Given this complexity, designers often use computer design tools, such as finite element analysis (FEA) and mould filling analysis (MFA), to reduce development time and cost. FEA determines strain, stress and deflection in a part by dividing the structure into small elements where these parameters can be well defined. MFA evaluates gate position and size to optimize resin flow. It also defines placement of weld lines, areas of excessive stress, and how wall and rib thickness affect flow. Other finite element design tools include mould cooling analysis for temperature distribution, and cycle time and shrinkage analysis for dimensional control and prediction of frozen stress and warpage.The CAE analysis of compression moulded parts is shown in Figure 1. The analysis cycle starts with the creation of a CAD model and a finite element mesh of the mould cavity. After the injection conditions are specified, mould filling, fiber orientation, curing and thermal history, shrinkage and warpage can be simulated. The material properties calculated by the simulation can be used to model the structural behaviour of the part. If required, part design, gate location and processing conditions can be modified in the computer until an acceptable part is obtained. After the analysis is finished an optimized part can be produced with reduced weldline (known also knitline), optimized strength, controlled temperatures and curing, minimized shrinkage and warpage.Machining of the moulds was formerly done manually, with a toolmaker checking each cut. This process became more automated with the growth and widespread use of computer numerically controlled or CNC machining centres. Setup time has also been significantly reduced through the use of special software capable of generating cutter paths directly from a CAD data file. Spindle speeds as high as 100,000 rpm provide further advances in high speed machining. Cutting materials have demonstrated phenomenal performance without the use of any cutting/coolant fluid whatsoever. As a result, the process of machining complex cores and cavities has been accelerated. It is good news that the time it takes to generate a mould is constantly being reduced. The bad news, on the other hand, is that even with all these advances, designing and manufacturing of the mould can still take a long time and can be extremely expensive.Figure 1 CAE analysis of injection moulded partsMany company executives now realize how vital it is to deploy new products to market rapidly. New products are the key to corporate prosperity. They drive corporate revenues, market shares, bottom lines and share prices. A company able to launch good quality products with reasonable prices ahead of their competition not only realizes 100% of the market before rival products arrive but also tends to maintain a dominant position for a few years even after competitive products have finally been announced (Smith, 1991). For most products, these two advantages are dramatic. Rapid product development is now a key aspect of competitive success. Figure 2 shows that only 3–7% of the product mix from the average industrial or electronics company is less than 5 years old. For companies in the top quartile, the number increases to 15–25%. For world-class firms, it is 60–80% (Thompson, 1996). The best companies continuously develop new products. AtHewlett-Packard, over 80% of the profits result from products less than 2 years old! (Neel, 1997)Figure 2. Importance of new product (Jacobs, 2000)With the advances in computer technology and artificial intelligence, efforts have been directed to reduce the cost and lead time in the design and manufacture of an injection mould. Injection mould design has been the main area of interest since it is a complex process involving several sub-designs related to various components of the mould, each requiring expert knowledge and experience. Lee et. al. (1997) proposed a systematic methodology and knowledge base for injection mould design in a concurrent engineering environment.4.Concurrent Engineering in Mould DesignConcurrent Engineering (CE) is a systematic approach to integrated product development process. It represents team values of co-operation, trust and sharing in such a manner that decision making is by consensus, involving all per spectives in parallel, from the very beginning of the productlife-cycle (Evans, 1998). Essentially, CE provides a collaborative, co-operative, collective and simultaneous engineering working environment. A concurrent engineering approach is based on five key elements:1. process2. multidisciplinary team3. integrated design model4. facility5. software infrastructureFigure 3 Methodologies in plastic injection mould design, a) Serial engineering b) Concurrent engineeringIn the plastics and mould industry, CE is very important due to the high cost tooling and long lead times. Typically, CE is utilized by manufacturing prototype tooling early in the design phase to analyze and adjust the design. Production tooling is manufactured as the final step. The manufacturing process and involving moulds must be designed after passing through the appearance evaluation and the structure optimization of the product design. CE requires an engineer to consider the manufacturing process of the designed product in the development phase.A good design of the product is unable to go to the market if its manufacturing process is impossible. Integration of process simulation and rapid prototyping and manufacturing can reduce the risk associated with moving from CAD to CAM and further enhance the validity of the product development.For years, designers have been restricted in what they can produce as they generally have todesign for manufacture (DFM) – that is, adjust their design intent to enable the component (or assembly) to be manufactured using a particular process or processes. In addition, if a mould is used to produce an item, there are therefore automatically inherent restrictions to the design imposed at the very beginning. Taking injection moulding as an example, in order to process a component successfully, at a minimum, the following design elements need to be taken into account:1. . geometry;. draft angles,. Non re-entrants shapes,. near constant wall thickness,. complexity,. split line location, and. surface finish,2. material choice;3. rationalisation of components (reducing assemblies);4. cost.In injection moulding, the manufacture of the mould to produce the injection-moulded components is usually the longest part of the product development process. When utilising rapid modelling, the CAD takes the longer time and therefore becomes the bottleneck.The process design and injection moulding of plastics involves rather complicated and time consuming activities including part design, mould design, injection moulding machine selection, production scheduling, tooling and cost estimation. Traditionally all these activities are done by part designers and mould making personnel in a sequential manner after completing injection moulded plastic part design. Obviously these sequential stages could lead to long product development time. However with the implementation of concurrent engineering process in the all parameters effecting product design, mould design, machine selection, production scheduling,tooling and processing cost are considered as early as possible in the design of the plastic part. When used effectively, CAE methods provide enormous cost and time savings for the part design and manufacturing. These tools allow engineers to virtually test how the part will be processed and how it performs during its normal operating life. The material supplier, designer, moulder and manufacturer should apply these tools concurrently early in the design stage of the plastic parts in order to exploit the cost benefit of CAE. CAE makes it possible to replace traditional, sequential decision-making procedures with a concurrent design process, in which all parties can interact and share information, Figure 3. For plastic injection moulding, CAE and related design data provide an integrated environment that facilitates concurrent engineering for the design and manufacture of the part and mould, as well as material selection and simulation of optimal process control parameters.Qualitative expense comparison associated with the part design changes is shown in Figure 4 , showing the fact that when design changes are done at an early stages on the computer screen, the cost associated with is an order of 10.000 times lower than that if the part is in production. These modifications in plastic parts could arise fr om mould modifications, such as gate location, thickness changes, production delays, quality costs, machine setup times, or design change in plastic parts.Figure 4 Cost of design changes during part product development cycle (Rios et.al, 2001)At the early design stage, part designers and moulders have to finalise part design based on their experiences with similar parts. However as the parts become more complex, it gets rather difficult to predict processing and part performance without the use of CAE tools. Thus for even relatively complex parts, the use of CAE tools to prevent the late and expensive design changesand problems that can arise during and after injection. For the successful implementation of concurrent engineering, there must be buy-in from everyone involved.5.Case StudyFigure 5 shows the initial CAD design of plastics part used for the sprinkler irrigation hydrant leg. One of the essential features of the part is that the part has to remain flat after injection; any warping during the injection causes operating problems.Another important feature the plastic part has to have is a high bending stiffness. A number of feeders in different orientation were added to the part as shown in Figure 5b. These feeders should be designed in a way that it has to contribute the weight of the part as minimum aspossible.Before the design of the mould, the flow analysis of the plastic part was carried out with Moldflow software to enable the selection of the best gate location Figure 6a. The figure indicates that the best point for the gate location is the middle feeder at the centre of the part. As the distortion and warpage of the part after injection was vital from the functionality point of view and it has to be kept at a minimum level, the same software was also utilised to yiled the warpage analysis. Figure 5 b shows the results implying the fact that the warpage well after injection remains within the predefined dimensional tolerances.6. ConclusionsIn the plastic injection moulding, the CAD model of the plastic part obtained from commercial 3D programs could be used for the part performance and injection process analyses. With the aid ofCEA technology and the use of concurrent engineering methodology, not only the injection mould can be designed and manufactured in a very short of period of time with a minimised cost but also all potential problems which may arise from part design, mould design and processing parameters could be eliminated at the very beginning of the mould design. These two tools help part designers and mould makers to develop a good product with a better delivery and faster tooling with less time and money.References1. Smith P, Reinertsen D, The time-to-market race, In: Developing Products in Half the Time. New York, Van Nostrand Reinhold, pp. 3–13, 19912.Thompson J, The total product development organization. Proceedings of the SecondAsia–Pacific Rapid Product Development Conference, Brisbane, 19963.Neel R, Don’t stop after the prototype, Seventh International Conference on Rapid Prototyping, San Francisco, 19974.Jacobs PF, “Chapter 3: Rapid Product Development” in Rapid Tooling: Technologies and Industrial Applications , Ed. Peter D. Hilton; Paul F. Jacobs, Marcel Decker, 20005.Lee R-S, Chen, Y-M, and Lee, C-Z, “Development of a concurrent mould design system: a knowledge based approach”, Computer Integrated Manufacturing Systems, 10(4), 287-307, 19976.Evans B., “Simultaneous Engineering”, Mechanical Engi neering , V ol.110, No.2, pp.38-39, 19987.Rios A, Gramann, PJ and Davis B, “Computer Aided Engineering in Compression Molding”, Composites Fabricators Association Annual Conference , Tampa Bay, 2001【译文一】塑料注塑模具并行设计塑料制品制造业近年迅速成长。
文献翻译-注塑模具

附页1:英文及中文翻译英文1.Example 24,Injection Mold for an Angle FitingIf ejectors are located behind movable side sores or slides ,the ejector plate return safety checks whether the ejectors have been returned to the molding position.If this is not the case,the molding cycle is interrupted.This safety requires a switch on the mold that is actuated when the ejector plate is in the retracted position. The ejector plate return safety thus functions only if the molding cycle utilizes platen preposition, i.e..,after the molded parts have been ejected, the clamping unit closes to the point at which the ejector plate is returned to the molding position by spring force. Only then does the control system issue the “close mold”command. In molds requiring a long ejector stroke, spring return of the ejector plate is often not sure enough. For such cases, there is an ejector return mechanism that fulfills this function.Attachment of the ejector plate return safety is shown in Figs.1 to 7.This single-cavity mold is used to produce an angle fitting.Two long side cores meet at an angle of 90°.The somewhat shorter side core is pulled by a cam pin,while the longer core is pulled by a slide.The difficulty is that blade ejectors are located under the two cores and must be returned to the molding position after having Ejected the finished part before the two cores are set as the mold closes and possibly damage the blade ejectors .Possible consequences include not only broken blade ejectors but also a damaged cavity. Either of these could result in a lengthy interruption of production. For this reason, a helical spring that permits operation with platen prepostion is placed on the ejector rod. This spring then returns the ejector plate .To ensure proper operation, a microswitch is mounted to the clamping plate,while a pin that actuates the switch is mounted in the ejector plate.After connecting the cable with the switch housing of the movable clamping plate,the ejector plate return safety is complete.Example 25,Mold for Bushings with Concealed Gating2.Example 25, Mold for Bushings with Concealed GatingAflanged bushing is to be injection molded in such a way that any remnants ofthe gate are concealed or as inconspicuous as possible.The bushing would normally require a two-plate mold with a single parting line,The molded part would then be released and ejected along its axis, which coincides with the opening direction of the mold. The gate would be located on the outer surface of the flange since it is in contact with the mold parting line.In order to satisfy the requirement for an “invisible”gate,the cavities (two rows of four) are placed between slides carrying the cores even though there are no undercuts.From a central sprue the melt flows through conical runners in the cores to pinpoint gates located on the inner surface of the bushings. As the slides move during opening of the mold the gates are cleanly sheared off flush with the adjacent part surface. The flexibility of the plastic selected is sufficient to permit release of the end of the runner from the angled runner channel.The parts are now free and can drop out of the mold.3. Example 26,Injection Mold for the Valave Housing of a Water-Mixing Tap Made from PolyacetalA valve housing had to be designed and produced for a water-mixing tap.The problem when designing the tool resulted from the undercuts in four directions.Originally occurring considerable differences in wall thicknesses have been eliminated during optimization. Demands for high precision of the cylindrical vave seat in parti-cular wer negatively influenced by various recesses in the wall and adjoining partitions,which favored sink marks and ovalness.Polyaceta (POM) had been chosen as molding materia.The complete molded part had to have homogeneous walls,and be free from flow lines if at all possible, as it would be subjected to ever-changing contact with hot and cold water during an estimated long life span.Inadequately fused weld lines would be capable of developoing into weak spots and wer therefore to be avoided at all cost.Provision has been made for an electrically heated sprue bushing in order to avoid a long sprue,provide better movement energies for the melt and maintain its temperature until it enters the cavity.The resultant very short runner leads to the gate on the edge of the pipelike housing, to be hidden by a part that is subsequently fitted to cover it.The gating,the predetermined mold temperature,the wall thickness at the critical positions and the resultant shrinkage have been employed as the basis for dimensioning the part-forming components.Two cores each cross in the pipe-shaped housing,i.e.one core each penetrates another core.This obviously presents a danger spot should the minutest deviation occur from the specified time and movement-based coordination as well as from the accuracy in the mold.The hollow cores are kept in position by mechanical delay during the first phase of mold opening,while the crossing cores are each withdrawn by an angle pin . Mechanical actuation has been preferred over a hydraulic or pneumatic one in this case in order to exclude the danger of a sequencing error (the so-called human factor) during set-up and operation.The cores consist of a beryllium-copper alloy. They are cooled by heat conducting pins.4.Example 29,Injection Mold for the Housing of a Polypropylene Vegetable DicerMolded PartThe housing accommodates a cutting disc that is driven by a hand crank . The shaft of the crank drive is located in a bore in the housing. The underneath of the housing has a recess for accommodating a suction cap to attach the device to a table. The top of the housing has a filling shaft which supplies the cutting disc with the vegetables to be diced. A feed hopper will be attached to this filling shaft.The molded part weighs 386 g.MoldThe mold was designed so that the dicing chamber lies in the mold-opening direction.The housing base,the filling shaft and two other apertures are ejected with the aid of splits ,a core puller and slides.The slide,moved by the angle pin,forms the inside contour of the housing base .In the closed position,the split shoulder lies against punch and so forms the bore for attaching the suction cap to the housing base .The cylindrical slide lies in the mold parting line and each half is enclosed by the mold plates and.Guide strips lead the slide on the mold plate. The slide supports itself against the effect of the cavity pressure via the adjusting plate and the wedge. Bending of the wedge is prevented by the adjusting plate and the mold plate. The vegetable filling shaft and the passage to the dicing chamber are formed by the mobile core. Its movement is provided by the angle pin.Figure 7 shows the core guide in the guide strip.The inserted core is locked via the wedge and adjusting plate .The guide strip forms a rectangular opening in theside wall of the housing which lies half over and half under the mold parting line. It is moved by two angle pins and is locked in the closed state by two bolts. A guide strip which is bolted and doweled to the mold plate is guided in a T-solt.Finally, a slit has to be formed in the housing wall that penetrates a reinforcement there. Rectangular aperture and reinforcement are formed by the slide which is actuated by the angle pin and locked by the wedge.Two bars serve to guide the slide on the mold plate. Since the angle pins traverse out from the slide ,the core and the guide bars on mold opening, each is provided with ball catches that keep these guide elements in the “open” position. Bars and rolls support the plate on the clamp plate.Runner System/GatingThe sprue bushing lies on the axis of the housing bore, which accommodates the blade drive shaft.The end of the sprue bushing forms the face of an eye inside the dicing chamber that is a part of the crankshaft mount. A core pin protrudes into the bore of the sprue bushing and divides the sprue into three pinpoint gates.Mold Temperature ControlThe coolant is guided in bores and cooling channels in the mold plates, inserts and punches.The splits and offer sufficient space for accommodating cooling channels..Part Release/EjectionOn mold opening,the angle pins on the fixed mold side push the splits ,cores and slides on the moving side so far outward that they release the undercuts of the housing. The molded part remanis on the moving mold side.Ejector pins and ejector sleeve push the molded part out of the ejector-side mold cavities and off core pin. Since the ejector pins are contour-forming,they must be secured against twisting . On mold closing, the ejector system is brought into the injection molding position by ejector-plate return pins and buffer pins,and so too are the splits ,cores and slides by their respective angle pints.译文1.注塑模具角度为拟合如果喷射器是可移动的侧后面疮或幻灯片位于顶针板返回安全的喷射器是否已返回成型,这是不是这样,成型周期检查中断。
注塑模具之模具设计与制造外文文献翻译、中英文翻译

外文翻译:Injection moulding for Mold Design and ManufactureThe mold is the manufacturing industry important craft foundation, in our country, the mold manufacture belongs to the special purpose equipment manufacturing industry. China although very already starts to make the mold and the use mold, but long-term has not formed the industry. Straight stabs 0 centuries 80's later periods, the Chinese mold industry only then drives into the development speedway. Recent years, not only the state-owned mold enterprise had the very big development, the three investments enterprise, the villages and towns (individual) the mold enterprise's development also quite rapidly.Although the Chinese mold industrial development rapid, but compares with the demand, obviously falls short of demand, its main gap concentrates precisely to, large-scale, is complex, the long life mold domain. As a result of in aspect and so on mold precision, life, manufacture cycle and productivity, China and the international average horizontal and the developed country still had a bigger disparity, therefore, needed massively to import the mold every year .The Chinese mold industry except must continue to sharpen the productivity; from now on will have emphatically to the profession internal structure adjustment and the state-of-art enhancement. The structure adjustment aspect, mainly is the enterprise structure to the specialized adjustment, the product structure to center the upscale mold development, to the import and export structure improvement, center the upscale automobile cover mold forming analysis and the structure improvement, the multi-purpose compound mold and the compound processing and the laser technology in the mold design manufacture application, the high-speed cutting, the super finishing and polished the technology, the information direction develops .The recent years, the mold profession structure adjustment and the organizational reform step enlarges, mainly displayed in, large-scale, precise, was complex, the long life, center the upscale mold and the mold standard letter development speed is higher than the common mold product; The plastic mold and the compression casting moldproportion increases; Specialized mold factory quantity and its productivity increase; "The three investments" and the private enterprise develops rapidly; The joint stock system transformation step speeds up and so on. Distributes from the area looked, take Zhujiang Delta and Yangtze River delta as central southeast coastal area development quickly to mid-west area, south development quickly to north. At present develops quickest, the mold produces the most centralized province is Guangdong and Zhejiang, places such as Jiangsu, Shanghai, Anhui and Shandong also has a bigger development in recent years.Although our country mold total quantity had at present achieved the suitable scale, the mold level also has the very big enhancement, after but design manufacture horizontal overall rise and fall industry developed country and so on Yu De, America, date, France, Italy many. The current existence question and the disparity mainly display in following several aspects:(1) The total quantity falls short of demandDomestic mold assembling one rate only, about 70%. Low-grade mold, center upscale mold assembling oneself rate only has 50% about.(2) The enterprise organizational structure, the product structure, the technical structure and the import and export structure does not gatherIn our country mold production factory to be most is from the labor mold workshop which produces assembles oneself (branch factory), from produces assembles oneself the proportion to reach as high as about 60%, but the overseas mold ultra 70% is the commodity mold. The specialized mold factory mostly is "large and complete", "small and entire" organization form, but overseas mostly is "small but", "is specially small and fine". Domestic large-scale, precise, complex, the long life mold accounts for the total quantity proportion to be insufficient 30%, but overseas in 50% above 2004 years, ratio of the mold import and export is 3.7:1, the import and export balances the after net import volume to amount to 1.32 billion US dollars, is world mold net import quantity biggest country .(3) The mold product level greatly is lower than the international standardThe production cycle actually is higher than the international water broadproduct level low mainly to display in the mold precision, cavity aspect and so on surface roughness, life and structure.(4) Develops the ability badly, economic efficiency unsatisfactory our country mold enterprise technical personnel proportion lowThe level is lower, also does not take the product development, and frequently is in the passive position in the market. Our country each mold staff average year creation output value approximately, ten thousand US dollars, overseas mold industry developed country mostly 15 to10, 000 US dollars, some reach as high as 25 to10, 000 US dollars, relative is our country quite part of molds enterprises also continues to use the workshop type management with it, truly realizes the enterprise which the modernized enterprise manages fewTo create the above disparity the reason to be very many, the mold long-term has not obtained the value besides the history in as the product which should have, as well as the most state-owned enterprises mechanism cannot adapt the market economy, but also has the following several reasons: .The mold material performance, the quality and the variety question often can affect the mold quality, the life and the cost, the domestically produced molding tool steel and overseas imports the steel products to compare has a bigger disparity. Plastic,plate, equipment energy balance, also direct influence mold level enhancement.RSP ToolingRapid Solidification Process (RSP) Tooling, is a spray forming technology tailored for producing molds and dies [2-4]. The approach combines rapid solidification processing and netshape materials processing in a single step. The general concept involves converting a mold design described by a CAD file to a tooling master using a suitable rapid prototyping (RP) technology such as stereolithography. A pattern transfer is made to a castable ceramic, typically alumina or fused silica. This is followed by spray forming a thick deposit of tool steel (or other alloy) on the pattern to capture the desired shape, surface texture and detail. The resultant metal block is cooled to room temperature and separated from the pattern. Typically, the deposit’s exterior walls are machined square, allowing it to be used as an insert in a holding block such as a MUD frame [5]. The overall turnaround time for tooling is about three days, stating with a master. Molds and dies produced in this way have been used for prototype and production runs in plastic injection molding and die casting.An important benefit of RSP Tooling is that it allows molds and dies to be made early in the design cycle for a component. True prototype parts can be manufactured to assess form, fit, and function using the same process planned for production. If the part is qualified, the tooling can be run in production as conventional tooling would. Use of a digital database and RP technology allows design modifications to be easily made.Experimental ProcedureAn alumina-base ceramic (Cotronics 780 [6]) was slurry cast using a silicone rubber master die, or freeze cast using a stereolithography master. After setting up, ceramic patterns were demolded, fired in a kiln, and cooled to room temperature. H13 tool steel was induction melted under a nitrogen atmosphere, superheated about100︒C, and pressure-fed into a bench-scale converging/diverging spray nozzle, designed and constructed in-house. An inert gas atmosphere within the spray apparatus minimized in-flight oxidation of the atomized droplets as they deposited onto the tool pattern at a rate of about 200 kg/h. Gas-to-metal mass flow ratio was approximately 0.5.For tensile property and hardness evaluation, the spray-formed material was sectioned using a wire EDM and surface ground to remove a 0.05 mm thickheat-affected zone. Samples were heat treated in a furnace that was purged with nitrogen. Each sample was coated with BN and placed in a sealed metal foil packet as a precautionary measure to prevent decarburization.Artificially aged samples were soaked for 1 hour at temperatures ranging from 400 to 700︒C, and air cooled. Conventionally heat treated H13 was austenitized at 1010︒C for 30 min., air quenched, and double tempered (2 hr plus 2 hr) at 538︒C.Microhardness was measured at room temperature using a Shimadzu Type M Vickers Hardness Tester by averaging ten microindentation readings. Microstructure of the etched (3% nital) tool steel was evaluated optically using an Olympus Model PME-3 metallograph and an Amray Model 1830 scanning electron microscope. Phase composition was analyzed via energy-dispersive spectroscopy (EDS). The size distribution of overspray powder was analyzed using a Microtrac Full Range Particle Analyzer after powder samples were sieved at 200 μm to remove coarse flakes. Sample density was evaluated by water displacement using Archimedes’ principle and a Mettler balance (Model AE100).A quasi 1-D computer code developed at INEEL was used to evaluate multiphase flow behavior inside the nozzle and free jet regions. The code's basic numerical technique solves the steadystate gas flow field through an adaptive grid, conservative variables approach and treats the droplet phase in a Lagrangian manner with full aerodynamic and energetic coupling between the droplets and transport gas. The liquid metal injection system is coupled to the throat gas dynamics, and effects of heat transfer and wall friction are included. The code also includes a nonequilibriumsolidification model that permits droplet undercooling and recalescence. The code was used to map out the temperature and velocity profile of the gas and atomized droplets within the nozzle and free jet regions.Results and DiscussionSpray forming is a robust rapid tooling technology that allows tool steel molds and dies to be produced in a straightforward manner. Each was spray formed using a ceramic pattern generated from a RP master.Particle and Gas BehaviorParticle mass frequency and cumulative mass distribution plots for H13 tool steel sprays are given in Figure 1. The mass median diameter was determined to be 56 μm by interpolation of size corresponding to 50% cumulative mass. The area mean diameter and volume mean diameter were calculated to be 53 μm and 139 μm, respectively. Geometric standard deviation, d=(d84/d16)½ , is 1.8, where d84 and d16 are particle diameters corresponding to 84% and 16% cumulative mass in Figure 1.Figure1. Cumulative mass and mass frequency plots of particles in H13 tool stepsprays.Figure2 gives computational results for the multiphase velocity flow field (Figure 2a), and H13 tool steel solid fraction (Figure2b), inside the nozzle and free jetregions. Gas velocity increases until reaching the location of the shock front, at which point it precipitously decreases, eventually decaying exponentially outside the nozzle. Small droplets are easily perturbed by the velocity field, accelerating inside the nozzle and decelerating outside. After reaching their terminal velocity, larger droplets (〜150 μm) are less perturbed by the flow field due to their greater momentum.It is well known that high particle cooling rates in the spray jet (103-106 K/s) and bulk deposit (1-100 K/min) are present during spray forming [7]. Most of the particles in the spray have undergone recalescence, resulting in a solid fraction of about 0.75. Calculated solid fraction profiles of small (〜30 μm) and large (〜150 μm) droplets with distance from the nozzle inlet, are shown in Figure 2b.Spray-Formed DepositsThis high heat extraction rate reduces erosion effects at the surface of the tool pattern. This allows relatively soft, castable ceramic pattern materials to be used that would not be satisfactory candidates for conventional metal casting processes. With suitable processing conditions, fine surface detail can be successfully transferred from the pattern to spray-formed mold. Surface roughness at the molding surface is pattern dependent. Slurry-cast commercial ceramics yield a surface roughness of about 1 μm Ra, suitable for many molding applications. Deposition of tool steel onto glass plates has yielded a specular surface finish of about 0.076 μm Ra. At the current state of development, dimensional repeatability of spray-formed molds, starting with a common master, is about ±0.2%.Figure 2. Calculated particle and gas behavior in nozzle and free jet regions.(a) Velocity profile.(b) Solid fraction.ChemistryThe chemistry of H13 tool steel is designed to allow the material to withstand the temperature, pressure, abrasion, and thermal cycling associated with demanding applications such as die casting. It is the most popular die casting alloy worldwide and second most popular tool steel for plastic injection molding. The steel has low carbon content (0.4 wt.%) to promote toughness, medium chromium content (5 wt.%) to provide good resistance to high temperature softening, 1 wt% Si to improve high temperature oxidation resistance, and small molybdenum and vanadium additions (about 1%) that form stable carbides to increase resistance to erosive wear[8]. Composition analysis was performed on H13 tool steel before and after spray forming.Results, summarized in Table 1, indicate no significant variation in alloy additions.MicrostructureThe size, shape, type, and distribution of carbides found in H13 tool steel is dictated by the processing method and heat treatment. Normally the commercial steel is machined in the mill annealed condition and heat treated(austenitized/quenched/tempered) prior to use. It is typically austenitized at about 1010︒C, quenched in air or oil, and carefully tempered two or three times at 540 to 650︒C to obtain the required combination of hardness, thermal fatigue resistance, and toughness.Commercial, forged, ferritic tool steels cannot be precipitation hardened becauseafter electroslag remelting at the steel mill, ingots are cast that cool slowly and formcoarse carbides. In contrast, rapid solidification of H13 tool steel causes alloying additions to remain largely in solution and to be more uniformly distributed in the matrix [9-11]. Properties can be tailored by artificial aging or conventional heat treatment.A benefit of artificial aging is that it bypasses the specific volume changes that occur during conventional heat treatment that can lead to tool distortion. These specific volume changes occur as the matrix phase transforms from ferrite to austenite to tempered martensite and must be accounted for in the original mold design. However, they cannot always be reliably predicted. Thin sections in the insert, which may be desirable from a design and production standpoint, are oftentimes not included as the material has a tendency to slump during austenitization or distort during quenching. Tool distortion is not observed during artificial aging ofspray-formed tool steels because there is no phase transformation.注塑模具之模具设计与制造模具是制造业的重要工艺基础,在我国,模具制造属于专用设备制造业。
注塑模具外文 文献资料2

Journal of Materials Processing Technology187–188 (2007) 690–693Adaptive system for electrically driven thermoregulationof moulds for injection mouldingB.Nardin a,∗,B.ˇZagar a,∗,A.Glojek a,D.Kriˇz aj ba TECOS,Tool and Die Development Centre of Slovenia,Kidriˇc eva Cesta25,3000Celje,Sloveniab Faculty of Electrical Engineering,Ljubljana,SloveniaAbstractOne of the basic problems in the development and production process of moulds for injection moulding is the control of temperature con-ditions in the mould.Precise study of thermodynamic processes in moulds showed,that heat exchange can be manipulated by thermoelectrical means.Such system upgrades conventional cooling systems within the mould or can be a stand alone application for heat manipulation within it.In the paper,the authors will present results of the research project,which was carried out in three phases and its results are patented in A686\2006 patent.The testing stage,the prototype stage and the industrialization phase will be presented.The main results of the project were total and rapid on-line thermoregulation of the mould over the cycle time and overall influence on quality of plastic product with emphasis on deformation control.Presented application can present a milestone in thefield of mould temperature and product quality control during the injection moulding process.© 2006 Elsevier B.V. All rights reserved.Keywords:Injection moulding;Mould cooling;Thermoelectric modules;FEM simulations1.Introduction,definition of problemDevelopment of technology of cooling moulds via thermo-electrical(TEM)means derives out of the industrial praxis and problems,i.e.at design,tool making and exploitation of tools. Current cooling technologies have technological limitations. Their limitations can be located and predicted in advance with finite element analyses(FEA)simulation packages but not com-pletely avoided.Results of a diverse state of the art analyses revealed that all existing cooling systems do not provide con-trollable heat transfer capabilities adequate tofit into demand-ing technological windows of current polymer processing technologies.Polymer processing is nowadays limited(in term of short-ening the production cycle time and within that reducing costs) only with heat capacity manipulation capabilities.Other produc-tion optimization capabilities are already driven to mechanical and polymer processing limitations[3].∗Corresponding authors.Tel.:+3863490920;fax:+38634264612.E-mail address:Blaz.Nardin@tecos.si(B.Nardin).1.1.Thermal processes in injection moulding plastic processingPlastic processing is based on heat transfer between plastic material and mould cavity.Within calculation of heat transfer one should consider two major facts:first is all used energy which is based onfirst law of thermodynamics—law of energy conservation[1],second is velocity of heat transfer.Basic task at heat transfer analyses is temperature calculation over time and its distribution inside studied system.That last depends on velocity of heat transfer between the system and surroundings and velocity of heat transfer inside the system.Heat transfer can be based as heat conduction,convection and radiation[1].1.2.Cooling timeComplete injection moulding process cycle comprises of mould closing phase,injection of melt into cavity,packing pres-sure phase for compensating shrinkage effect,cooling phase, mould opening phase and part ejection phase.In most cases,the longest time of all phases described above is cooling time.Cooling time in injection moulding process is defined as time needed to cool down the plastic part down to ejection temperature[1].0924-0136/$–see front matter© 2006 Elsevier B.V. All rights reserved. doi:10.1016/j.jmatprotec.2006.11.052B.Nardin et al./Journal of Materials Processing Technology 187–188 (2007) 690–693691Fig.1.Mould temperature variation across one cycle[2].The main aim of a cooling process is to lower additional cooling time which is theoretically needless;in praxis,it extends from45up to67%of the whole cycle time[1,4].From literature and experiments[1,4],it can be seen,that the mould temperature has enormous influence on the ejection time and therefore the cooling time(costs).Injection moulding process is a cyclic process where mould temperature varies as shown in Fig.1where temperature varies from average value through whole cycle time.2.Cooling technology for plastic injection mouldsAs it was already described,there are already several differ-ent technologies,enabling the users to cool the moulds[5].The most conventional is the method with the drilling technology, i.e.producing holes in the mould.Through these holes(cooling lines),the cooling media isflowing,removing the generated and accumulated heat from the mould[1,2].It is also very convenient to build in different materials,with different thermal conductiv-ity with the aim to enhance control over temperature conditions in the mould.Such approaches are so called passive approaches towards the mould temperature control.The challenging task is to make an active system,which can alter the thermal conditions,regarding to the desired aspects, like product quality or cycles time.One of such approaches is integrating thermal electrical modules(TEM),which can alter the thermal conditions in the mould,regarding the desired prop-erties.With such approach,the one can control the heat transfer with the time and space variable,what means,that the temper-ature can be regulated throughout the injection moulding cycle, independent of the position in the mould.The heat control is done by the control unit,where the input variables are received from the manual input or the input from the injection moulding simulation.With the output values,the control unit monitors the TEM module behaviour.2.1.Thermoelectric modules(TEM)For the needs of the thermal manipulation,the TEM module was integrated into mould.Interaction between the heat and elec-trical variables for heat exchange is based on the Peltier effect. The phenomenon of Peltier effect is well known,but it wasuntilFig.2.TEM block diagram.now never used in the injection moulding applications.TEM module(see Fig.2)is a device composed of properly arranged pairs of P and N type semiconductors that are positioned between two ceramic plates forming the hot and the cold thermoelectric cooler sites.Power of a heat transfer can be easily controlled through the magnitude and the polarity of the supplied electric current.2.2.Application for mould coolingThe main idea of the application is inserting TEM module into walls of the mould cavity serving as a primary heat transfer unit.Such basic assembly can be seen in Fig.3.Secondary heat transfer is realized via conventionalfluid cooling system that allows heatflows in and out from mould cavity thermodynamic system.Device presented in Fig.3comprises of thermoelectric modules(A)that enable primarily heat transfer from or to tem-perature controllable surface of mould cavity(B).Secondary heat transfer is enabled via cooling channels(C)that deliver constant temperature conditions inside the mould.Thermoelec-tric modules(A)operate as heat pump and as such manipulate with heat derived to or from the mould byfluid cooling sys-tem(C).System for secondary heat manipulation with cooling channels work as heat exchanger.To reduce heat capacity of controllable area thermal insulation(D)is installed between the mould cavity(F)and the mould structure plates(E).Fig.3.Structure of TEM cooling assembly.692 B.Nardin et al./Journal of Materials ProcessingTechnology 187–188 (2007) 690–693Fig.4.Structure for temperature detection and regulation.The whole application consists of TEM modules,a temper-ature sensor and an electronic unit that controls the complete system.The system is described in Fig.4and comprises of an input unit(input interface)and a supply unit(unit for electronic and power electronic supply—H bridge unit).The input and supply units with the temperature sensor loop information are attached to a control unit that acts as an exe-cution unit trying to impose predefined temperate/time/position ing the Peltier effect,the unit can be used for heating or cooling purposes.The secondary heat removal is realized viafluid cooling media seen as heat exchanger in Fig.4.That unit is based on current cooling technologies and serves as a sink or a source of a heat.This enables complete control of processes in terms of temperature,time and position through the whole cycle. Furthermore,it allows various temperature/time/position pro-files within the cycle also for starting and ending procedures. Described technology can be used for various industrial and research purposes where precise temperature/time/position con-trol is required.The presented systems in Figs.3and4were analysed from the theoretical,as well as the practical point of view.The theoretical aspect was analysed by the FEM simulations,while the practical one by the development and the implementation of the prototype into real application testing.3.FEM analysis of mould coolingCurrent development of designing moulds for injection moulding comprises of several phases[3].Among them is also design and optimization of a cooling system.This is nowa-days performed by simulations using customized FEM packages (Moldflow[4])that can predict cooling system capabilities and especially its influence on plastic.With such simulations,mould designers gather information on product rheology and deforma-tion due to shrinkage as ell as production time cycle information.This thermal information is usually accurate but can still be unreliable in cases of insufficient rheological material informa-tion.For the high quality input for the thermal regulation of TEM,it is needed to get a picture about the temperature distri-bution during the cycle time and throughout the mould surface and throughout the mould thickness.Therefore,different process simulations areneeded.Fig.5.Cross-section of a prototype in FEM environment.3.1.Physical model,FEM analysisImplementation of FEM analyses into development project was done due to authors’long experiences with such packages [4]and possibility to perform different test in the virtual envi-ronment.Whole prototype cooling system was designed in FEM environment(see Fig.5)through which temperature distribution in each part of prototype cooling system and contacts between them were explored.For simulating physical properties inside a developed prototype,a simulation model was constructed using COMSOL Multiphysics software.Result was a FEM model identical to real prototype(see Fig.7)through which it was possible to compare and evaluate results.FEM model was explored in term of heat transfer physics taking into account two heat sources:a water exchanger with fluid physics and a thermoelectric module with heat transfer physics(only conduction and convection was analysed,radiation was ignored due to low relative temperature and therefore low impact on temperature).Boundary conditions for FEM analyses were set with the goal to achieve identical working conditions as in real test-ing.Surrounding air and the water exchanger were set at stable temperature of20◦C.Fig.6.Temperature distribution according to FEM analysis.B.Nardin et al./Journal of Materials Processing Technology 187–188 (2007) 690–693693Fig.7.Prototype in real environment.Results of the FEM analysis can be seen in Fig.6,i.e.temper-ature distribution through the simulation area shown in Fig.5. Fig.6represents steady state analysis which was very accurate in comparison to prototype tests.In order to simulate the time response also the transient simulation was performed,showing very positive results for future work.It was possible to achieve a temperature difference of200◦C in a short period of time(5s), what could cause several problems in the TEM structure.Those problems were solved by several solutions,such as adequate mounting,choosing appropriate TEM material and applying intelligent electronic regulation.boratory testingAs it was already described,the prototype was produced and tested(see Fig.7).The results are showing,that the set assump-tions were confirmed.With the TEM module it is possible to control the temperature distribution on different parts of the mould throughout the cycle time.With the laboratory tests,it was proven,that the heat manipulation can be practically regu-lated with TEM modules.The test were made in the laboratory, simulating the real industrial environment,with the injection moulding machine Krauss Maffei KM60C,temperature sen-sors,infrared cameras and the prototype TEM modules.The temperature response in1.8s varied form+5up to80◦C,what represents a wide area for the heat control within the injection moulding cycle.4.ConclusionsUse of thermoelectric module with its straightforward con-nection between the input and output relations represents a milestone in cooling applications.Its introduction into moulds for injection moulding with its problematic cooling construction and problematic processing of precise and high quality plastic parts represents high expectations.The authors were assuming that the use of the Peltier effect can be used for the temperature control in moulds for injection moulding.With the approach based on the simulation work and the real production of laboratory equipment proved,the assump-tions were confirmed.Simulation results showed a wide area of possible application of TEM module in the injection moulding process.With mentioned functionality of a temperature profile across cycle time,injection moulding process can be fully controlled. Industrial problems,such as uniform cooling of problematic A class surfaces and its consequence of plastic part appear-ance can be solved.Problems offilling thin long walls can be solved with overheating some surfaces at injection time.Further-more,with such application control over rheological properties of plastic materials can be gained.With the proper thermal regulation of TEM it was possible even to control the melt flow in the mould,during thefilling stage of the mould cav-ity.This is done with the appropriate temperature distribution of the mould(higher temperature on the thin walled parts of the product).With the application of TEM module,it is possible to signif-icantly reduce the cycle time in the injection moulding process. The limits of possible time reduction lies in the frame of10–25% of additional cooling time,describe in Section1.2.With the application of TEM module it is possible to actively control the warping of the product and to regulate the amount of product warpage in the way to achieve required product tol-erances.The presented TEM module cooling application for injection moulding process is a matter of priority note for the patent,held and owned by TECOS.References[1]I.ˇCati´c,Izmjena topline u kalupima za injekcijsko preˇs anje plastomera,Druˇs tvo plastiˇc ara i gumaraca,Zagreb,1985.[2]I.ˇCati´c,F.Johannaber,Injekcijsko preˇs anje polimera i ostalih materiala,Druˇs tvo za plastiku i gumu,Biblioteka polimerstvo,Zagreb,2004.[3]B.Nardin,K.Kuzman,Z.Kampuˇs,Injection moulding simulation resultsas an input to the injection moulding process,in:AFDM2002:The Sec-ond International Conference on Advanced Forming and Die Manufacturing Technology,Pusan,Korea,2002.[4]TECOS,Slovenian Tool and Die Development Centre,Moldflow SimulationProjects1996–2006.[5]S.C.Chen,et al.,Rapid mold surface heating/cooling using electromag-netic induction technology:ANTEC2004,Conference CD-ROM,Chicago, Illinois,16–20May,2004.。
模具 塑料注射成型 外文翻译 外文文献 英文文献

模具塑料注射成型外文翻译外文文献英文文献XXXThere are many different processing methods used to convert plastic pellets。
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household items。
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模具外文翻译外文文献英文文献注塑模

模具外文翻译外文文献英文文献注塑模The Injection Molding1、The injection moldingInjection molding is principally used for the production of the thermoplastic parts,although some progress has been made in developing a method for injection molding some thermosetting materials.The problem of injection a method plastic into a mold cavity from a reservoir of melted material has been extremely difficult to solve for thermosetting plastic which cure and harden under such conditions within a few minutes.The principle of injection molding is quite similar to that of die-casting.The process consists of feeding a plastic compound in powered or granular form from a hopper through metering and melting stages and then injecting it into a mold.After a brief cooling period,the mold is opened and the solidified part ejected.Injection-molding machine operation.The advantage of injection molding are:(ⅰ)a high molding speed adapter for mass production is possible;(ⅱ)there is a wide choice of thermoplastic materials providing a variety of useful properties;(ⅲ)it is possible to mold threads,undercuts,side holes,and large thin section.2、The injection-molding machineSeveral methods are used to force or inject the melted plastic into the mold.The most commonly used system in the larger machines is the in-line reciprocating screw,as shown in Figure 2-1.The screw acts as a combination injection and plasticizing unit.As the plastic is fed to the rotating screw,it passes through three zones as shown:feed,compression,and metering.After the feed zone,the screw-flight depth is gradually reduced,force theplastic to compress.The work is converted to heat by conduction from the barrel surface.As the chamber in front of the screw becomes filled,it forces the screw back,tripping a limit switch that activates a hydraulic cylinder that forces the screw forward and injects the fluid plastic into the closed mold.An antiflowback valve presents plastic under pressure from escaping back into the screw flight.The clamping force that a machine is capable of exerting is part of the size designation and is measured in tons.A rule-of-thumb can be used to determine the tonnage required for a particular job.It is based on two tons of clamp force per square inch of projected area.If the flow pattern is difficult and the parts are thin,this may have to go to three or four tons.Many reciprocating-screw machines are capable of handing thermosetting plastic materials.Previously these materials were handled by compression or transfer molding.Thermosetting materials cure or polymerize in the mold and are ejected hot in the range of 375°C~410°C.T hermosetting parts must be allowed to cool in the mold in order or remove them without distortion. Thus thermosetting cycles can be faster.Of course the mold must be heated rather than chilled,as with thermoplastics.3、Basic Underfeed MouldA simple mould of this type is shown in Figure3-1,and the description of the design and the opening sequence follows.The mould consists of three basic parts,namely:the moving half,the floating cavity plate and the feed plate respectively.The moving half consists of The moving mould plate assembly,support block,backing plate,ejector assembly and the pin ejection system.Thus the moving half in this design is identical with the moving half of basic moulds.The floating cavity plate,which may be of the integer or insert-bolster design,is located on substantial guide pillars(not shown)fitted in the feed plate.These guide pillars must be of sufficient length to support the floating cavity plate over its full movement and still project to perform the function of alignment between the cavity and core when the mould is being closed.Guide bushes are fitted into the moving mould plate and the floating cavity plate respectively.The maximum movement of the floating cavity plate is controlled by stop or similar device.The moving mould plate is suitably bored to provide a clearance for the stop bolt assembly.The stop bolts must be long enough to provide sufficient space between the feed plate and the floating cavity plate for easy removal of the feed system.The minimum space provide for should be 65mm just sufficient for an operator to remove the feed system by hand if necessary.The desire operating sequence is for the first daylight to occur between the floating cavity plate.This ensures the sprue is pulled from the sprue bush immediately the mouldis opened.T o achieve this sequence,springs may be incorporated between the feed plate and the floating cavity plate.The springs should be strong enough to give an initial impetus to the floating cavity plate to ensure it moves away with the moving half.It is normal practice to mount the springs on the guide pillars(Figure3-2)and accommodate them in suitable pocket in the cavity plate.The major part of the feed system(runner and sprue)is accommodated in the feed plate to facilitate automatic operation,the runner should be of a trapezoidal form so that once it is pulled from the feed plate is can easily beextracted.Note that if a round runner is used,half the runner is formed in the floating cavity plate,where it would remain,and be prevented from falling or being wiped clear when the mould is opened.Now that we have considered the mould assembly in the some detail,we look at the cycle of operation for this type of mould.The impressions are filled via the feed system(Figure3-1(a))and after a suitable dwell period,the machine platens commence to open.A force is immediately exerted by the compression springs,which cause the floating cavity plate to move away with the moving half as previously discussed.The sprue is pulled from the sprue bush by the sprue puller.After the floating cavity plate has moved a predetermined distance,it is arrested by the stop bolts.The moving half continues to move back and the moldings,having shrunk on to the cores,are withdrawn from the cavities.The pin gate breaks at its junction with the runner(Figure3-1(b)).The sprue puller,being attached to the moving half,is pulled through the floating cavity plate and thereby release the feed system which is then free to fall between the floating cavity plate and the feed plate.The moving half continues to move back until the ejector system is operated and the moldings are ejected (Figure3-1(c)).When the mould is closed,the respective plates are returned to their molding position and the cycle is repeated.4、Feed SystemIt is necessary to provide a flow-way in the injection mould to connect the nozzle(of the injection machine)to each impression.This flow-way is termed the feed system.Normally thefeed system comprises a sprue,runner and gate.These terms applyequally to the flow-way itself,and to the molded material which is remove from the flow-way itself in the process of extracted the molding.A typical feed system for a four-impression,two plate-type mould is shown in Figure4-1.It is seen that the material passes through the sprue,main runner,branch runner and gate before entering the impression.As the temperature of molten plastic is lowered which going through the sprue and runner,the viscosity will rise;however,the viscosity is lowered by shear heat generated when going through the gate to fill the cavity.It is desirable to keep the distance that the material has to travel down to a minimum to reduce pressure and heat losses.It is for this reason that careful consideration must be given to the impression layout gate’s design.4.1.SprueA sprue is a channel through which to transfer molten plastic injected from the nozzle of the injector into the mold.It is a part of sprue bush,which is a separate part from the mold.4.2.RunnerA runner is a channel that guides molten plastic into the cavity of a mold.4.3.GateA gate is an entrance through which molten plastic enters the cavity.The gate has the following function:restricts the flow and the direction of molten plastic;simplifies cutting of a runner and moldings to simplify finishing of parts;quickly cools and solidifies to avoid backflow after molten plastic has filled up in the cavity.4.4.Cold slug wellThe purpose of the cold slug well,shown opposite the sprue,is theoretically to receive the material that has chilled at the front of nozzle during the cooling and ejection phase.Perhaps of greater importance is the fact that it provides position means whereby the sprue bush for ejection purposes.The sprue,the runner and the gate will be discarded after a part is complete.However,the runner and the gate are important items that affect the quality or the cost of parts.5、EjectionA molding is formed in mould by injecting a plastic melt,under pressure,into animpression via a feed system.It must therefore be removed manually.Furthermore,all thermoplastic materials contract as they solidify,which means that the molding will shrink on to the core which forms it.This shrinkage makes the molding difficult to remove. Facilities are provided on the injection machine for automatic actuation of an ejector system,and this is situated behind the moving platen.Because of this,the mould’s ejector system will be most effectively operated if placed in the moving half of the mould,i.e. the half attached to the moving platen.We have stated previously that we need to eject the molding from the core and it therefore follows that the core,too,will most satisfactorily be located in the moving half.The ejector system in a mould will be discussed under three headings,namely:(ⅰ)the ejector grid;(ⅱ)the ejector plate assembly; and(ⅲ)the method of ejection.5.1、Ejector gridThe ejector grid(Figure5-1)is that part of the mould which supports the mould plate and provides a space into which theejector plate assembly can be fitted and operated.The grid normally consists of a back plate on to which is mounted a number of conveniently shaped “support blocks”.The ejector plate assembly is that part of the mould to which the ejector element is attached.The assembly is contained in a pocket,formed by the ejector grid,directly behind the mould plate.The assembly(Figure5-2)consists of an ejector plate,a retaining plate and an ejector rod.One end of this latter member is threaded and it is screwed into the ejector plate.In this particular design the ejector rod function not only as an actuating member but also as a method of guiding the assembly.Note that the parallel portion of the ejector rod passes through an ejector rod bush fitted in the back plate of the mould.5.2、Ejection techniquesWhen a molding cools,it contracts by an amount depending on the material being processed.For a molding which has no internal form,for example,a solid rectangular block,the molding will shrink away from the cavity walls,thereby permitting a simple ejection technique to be adopted.However,when the molding has internal form,the molding,as it cools,will shrink onto the core and some positive type of ejection is necessary.The designer has several ejection techniques from which to choose,but in general,the choice will be restricted depending upon the shape of the molding.The basic ejection techniques are as follows:(ⅰ)pin ejection(ⅱ)sleeve ejection(ⅲ)stripper plate ejection and(Ⅳ)air ejection.Figure 2-1aFigure 2-1bFigure 3-1Figure 3-2Figure 4-1aFigure 4-1bFigure 5-1Figure 5-2注塑模1、注塑模尽管成型某些热固性材料的方法取得了一定的进步,但注塑模主要(还是)用来生产热塑性塑件。
注塑模具设计英文参考文献

Injection molding die design is a crucial aspect of the manufacturing process to produce high-quality plastic products. Various technical references have been published over the years, providing valuable insights into the design principles, strategies, and best practices related to injection molding die design. Here are some key references that can be used as a starting point for further exploration:1.Injection Mold Design Engineering (David O. Kazmer, 2011) This bookprovides a comprehensive overview of injection mold design, covering topics such as mold geometry, gating systems, cooling and heating, ejector systems, and mold materials. It also discusses the analysis and optimization of molddesigns using computer-aided engineering tools.2.Injection Molds and Molding: A Practical Manual (Jiri Karasek, 2006)This practical manual offers a step-by-step guide to injection mold design and production. It covers various aspects of mold design, including cavity and core geometry, runner systems, venting, cooling, ejection, and mold materials. The book also addresses common design challenges and troubleshootingtechniques.3.Plastic Injection Molding: Manufacturing Process Fundamentals(Douglas M. Bryce and Charles A. Daniels, 2014) This reference provides an in-depth understanding of the injection molding process and its fundamentals. It discusses the principles of mold design, material selection, process parameters, molding defects, and mold maintenance. The book emphasizes the importance of considering the design-for-manufacturability aspect in mold design.4.Mold Design Using SolidWorks (Edward J. Bordin, 2010) Focused onmold design using SolidWorks software, this book provides practical insights into mold design methodology, including parting line creation, runner system design, cooling strategies, and mold analysis. It also covers advanced topicssuch as hot runner systems and side actions.5.Designing Injection Molds for Thermoplastics (H.T. Rowe, 2010) Thiscomprehensive reference addresses the design considerations specific tothermoplastic injection molds. It covers mold configuration, gating design,cooling strategies, shrinkage and warpage control, and mold materials. Thebook also includes case studies and practical tips for mold design optimization.6.Mold-Making Handbook (Kurtz Ersa Corporation, 2009) Thishandbook offers practical advice on mold design, construction, andmaintenance. It covers topics like mold steel selection, surface finishing, cavity design, cooling channels, ejection systems, and high-precision molding. Thereference provides insights into the latest developments in mold-makingtechnology.These references provide a solid foundation for understanding injection mold design principles, methodologies, and considerations. Additionally, industrypublications, research papers, and case studies can offer further insights into specific design aspects, material selection, and advanced techniques. It is important to consult multiple sources and stay updated with the latest trends and advancements in injection mold design to ensure efficient and robust manufacturing processes.。
注塑模具原理与基本方法外文文献翻译、中英文翻译

外文资料翻译资料来源:文章名:Tribological assessment of the interface injection mold/plastic part 书刊名:tribology international作者:crossmark出版社:journal homepage文章译名:注塑模具原理及基本方法姓名:学号:指导教师(职称):专业:班级:所在学院:外文原文:The sector of plastics processing is relatively young compared to cast iron, steel or glass industry. So it still has a very strong development potential. One of the current challenges of the plastic injection process is linked to the importance given to product design that enables a strong differentiation[1]. Plastic parts with an increased technical level of surface accuracy are required in the areas of luxury, packaging, automotive, including the medical and optics. Their development involves the improvement of the fabrication process, and one of the keys lies in the mastery of the surface conditions of the molds.Injection molding is a cyclic process, characterized by 5 phases: dosing, injection, packing, cooling and ejection . The raw material that is dosed in the machine must be pure and conserved before use at an adequate temperature in order to be as dried as possible. This is necessary to avoid condensation inside the mold. The injection phase is characterized by high fl ow rates and hence high shear rate (tangential effect). As the molten material enters the mold, two heat transfer mechanisms occur: convection (between the melted material and mold surface) and viscous dissipation (due to the effect of injection speed on the injected material viscosity). As the fi lling is complete, the mold is uphold at a predetermined pressure and so the packing phase is initiated. During this phase, the molten polymer continues to be introduced into the mold to compensate for the shrinkage of the already injected material as it cools down. After a speci fi c time, the cooling phase (contrary to the cooling state which begins during injection and packing phase) of the entire assembly starts and so also the solidi fi cation process of the plastic part. As the material solidi fi es and shrinks in the mold, the dominant heat transfer mechanism is conduction. When the part is suf fi cient solidi fi ed, it is ejected from the mold. During this last phase, a normal effect can be attributed to the ejection force and adhesion phenomena can occur between the mold surface and the plastic part[2].Despite the undeniable diversity of con fi gurations available (in terms of combination: mold material, surface fi nish and processed materials), the producers are faced with similar dif fi culties. Thus, the key shortcomings that stand out, more or less combined, can be summarize as follows:●t he fouling phenomena which require frequent stops for cleaning;●c orrosion phenomena that can greatly limit the lifetime of the mold cavity as a function of the type of injected polymer;●p roblems of sticking and releasing in function of the injected materials and surface quality;●p roblems in keeping the polishing quality;●s cratches or shocks during use or storage.The available literature approaches experimental and/or numerical, various aspects regarding the plastic injection molding process. One of them is the fi lling and fl ow behavior of molten polymers.[3]Bociaga and Jaruga studied the formation of fl ow, weld and meld lines by developing a new method of fl ow visualization, which can prove helpful in the identi fi cation of weakareas on injected parts. Also the effect of pressure and cavity thickness were assessed. Same topic was treated by Ozdemir etal.[4],comparing the behavior of molten HDPE (high density poly-ethylene) and PE experimentally and numerically.During molding, friction forces act fi rst between the mold surface and the molten polymer and second when the plastic part is ejected from the mold. Bull etal.[5] adapted the ASTM rubber wheel abrasion test to simulate the conditions of wear produced by the glass fi lled polymers on the barrel surface of an injection molding machine. Various coatings were tested, but unfortunately they tended to have a weak performance on account of the test conditions.[6] developed a prototype apparatus to study the friction properties of molding thermoplastics during ejection phase. The measured friction coef fi cient had a tendency to increase with the roughness. But when the roughness was reduced the friction coef fi cient increase due to the rising adhesion forces effect. The scanning electron microscopy images of the mold surface and the ones for the polycarbonate (PC) and polypropylene (PP) plastic parts, revealed a clear replication of the mold surface on the parts.Transient in nature, injection molding process involves not only several heat transfer mechanisms, phase change and time varying boundary conditions, but goes further in adding the effect of material properties and geometry of the injected part.[7] Bendada etal performed a study to evaluate the nature of thermal contact between polymer and mold through the different phases of a typical injectioncycle. Their fi ndings concluded that the thermal contact resistance was not negligible, not constant with time and was strongly linked with the process conditions.The existing number of studies concerning the phenomena present at the interface mold surface/polymer is relatively low to other related topics. Besides, they don’t focus on studying the current limitations of the plastic injection process at a microscopic scale, taking into account various macroscopic in fl uences. To overcome plastic injection molding shortcomings, the contact conditions at the interface between mold surface and plastic part have to be identi fi ed. This work focus on the effect of the polishing quality, the mold geometry and the injected material on that interface, by studying the corrosion-mechanical attack and the mechanical -physical- chemical one.2. Method and materials2.1. MaterialsFour polymers were chosen to be injected: ionomer resin (E-MMA Surlyn s PC 2 000), styrene-acrylonitrile resin (SAN Tyril 790), polyamide with 25% glass fi bers (PA66GF25) and poly-carbonate (PC Makrolon LQ 2647). Surlyn is a copolymer of ethylene and methacrylic acid where some of the acid groups are neutralized to form the sodium salt. The acid in the polymer gives polarity and reduces crystallinity. The ionic bonding between the polymer chains gives outstanding melt strength, toughness and clarity. The reason of choosing Surlyn was based on the experience of our industrial partners, which fi nd it particularly corrosive despite its good properties. Surlyn is also a copolymer, optically transparent and brittle in mechanical behavior. It's considered in this study a reference material, usually used in cosmetics, luxury and automobile domains. PA66GF25 is an aliphatic-polyamide, reinforced with 25% glass fi bers. PA66 has an excellent balance of strength, ductility and heat resistance. The glass fi bers exert an abrasive effect and thus affect the mechanical protection of the polishing. PC is composed by carbonate groups. It has a high impact-resistance, low scratch-resistance and is highly transparent to visible light. It is usually used for the production of eyewear lenses and exterior automotive components.2.2. MoldsTwo molds, made of hardened steel (52 HRC) containing 13% to 15% ofChromium, with different geometries were used, one with a mirror polished surface (complex geometry) and another with an optical polished surface (simple geometry) . The mold has two parts: the stamp and the matrix. For the mold with complex geometry the stamp is of 149 119 80 mm in size and the matrix of 149 119 50 mm. In case of the one with a simple geometry, the stamp is of 50 70 mm in size and the matrix has a cylinder form with a diameter of 70 mm. The surface fi nish of the mirror and optical polished molds involved a polishing cloth and diamond paste. Further details on the polishing process are con fi dential.The mirror polished mold was specially designed for this study by Technimold (a mold maker) to highlight the role of angles and obstacles in the formation of defaults. Also the mold design did not include a special feature that can evacuate the air. This was done intentionally in order to submit the polished surfaces to aggressive conditions. The molding process was performed at “Center Technique dela Plasturgie et des Composites”(IPC, France) on a 50 T Engel machine. The injection parameters, listed in Table 2, were chosen in accordance with standard speci fi cations for the injected polymers. Based on a numerical simulation they were adapted to respond in conformity with the mold design. Two injection campaigns were conducted on this type of mold. After the fi rst campaign, on the plane part of the mold stamp, an insert with a diameter of 12 mm and a height of 8 mm, was mounted to facilitate the morphology assessment.For the Surlyn injection, 3000 parts were injected in the fi rst campaign. After surface analysis, the mold was submitted to the industrial cleaning operation. The second campaign consisted in the injection of 3700 more parts. SAN and PA66GF25 were injected on the same mold. During the fi rst campaign, only 8000 SAN parts were injected. Before starting a second campaign, the mold was polished entirely. The second campaign consisted in the injection of 300 parts of SAN. The insert was changed before starting the injection of 12 200 PA66GF25 parts.2.3. MethodThe surface expertize consisted in two main steps: the microscopy analysis and the inter ferometry measurements before and after injection process. Due to their large dimensions and elevated mass, the surface analysis of the mirror polished molds was per-formed using a classic optical microscope. For the optical polished one, thanks to smaller dimensions, the microscope analysis could be carried out using a numerical optical microscope (Keyence) and a high resolution environmental scanning electron microscope (FEI XL30 ESEM). Although two injection campaigns have been performed, the results presented in this paper, refer only to the surface expertize performed at the end of the second campaign. For the injected plastic parts, only the interface between mold matrix plane part and plastic part is discussed in this paper.In order to identify the chemical composition of different deposits found on the mirror polished mold surfaces, a Fourier Transform Infrared (FTIR) spectrometer was used for the analysis.3. Results and discussions3.1. Mirror polished mold3.1.1. Injection Surlyn sAll along the stamp plane part, deposits different in texture and consistence can be observed (Fig. 5). Their location and morphologyseem to indicate the fl ow direction of the molten polymer. Also it can be noticed, towards the end of the fl ow, the deposits grow in terms of thickness and occupied surface.The type of deposit observed in Fig. 5e and f is also observed after the fi rstinjection campaign (3000 injected parts), and appeared that the cleaning operation has been able to remove it, but formed again during the second injection campaign (3700 injected parts). This particular deposit is located between the extremity of the oval bump and the hole where one of the ejection pins acts. Also in this location the fl ow changes direction, more precisely makes a left turn; fact also revealed by the deposit morphology. Its existence can be explained starting with the effect of the injection speed on the molten polymer viscosity, which is considered to be a heat transfer mechanism that occurs during the injection process. Due to the geometry factor, the viscous dissipation creates a temperature gradient which sensitizes this area. During the packing phase, as the mold continues to be fi lled, the location identi fi ed is one of the last to be reached by the molten polymer. As the holding phase begins and with it the solidi fi cation, the temperature gradient that appears in the injection phase continues to act and by doing so it delays the solidi fi cation in this area. When the established time for the holding phase expires, the mechanism of ejection is set in motion. The ejection pin is close to the identi fi ed location and as it was affected by the temperature gradient and has not yet been entirely solidi fi es, it will also be the fi rst area to be separated from the mold surface. All these can explain the appearance of the adhesion phenomenon.In the deposit appears like a thin fi lm and is also located in an area where the fl ow changes direction. It could also be justi fi ed by the temperature gradient, but its aspect and composition suggest that may another phenomena can occur. The infrared analysis performed on this area suggest that only some of the wave numbers match with the ones from the spectrum registered for the injected part It is possible that the gases released from the contact of the molten polymer with the mold surface reacted with the additives from the raw material composition and facilitated the separation of the thin layer that stick on the mold surface. Also the “scraped” aspect of this deposit indicates that is more likely that this type of deposit has formed during the injection phase.Holes (form 14.6nm to 404nm deep) are observed before injection probably due to polishing.Their morphology evolves during injection process:the holes expand in occupation area and depth(39.7nm to 877nm).the pointing red arrows indicate the presence of the evolved holes.They exhibit two types of morphology.The first type illustrated shows very small holes focused altogether in smaller or larger spots and the second type illustrated presents a hole surrounded by a “cloud” of small holes.Due to the inclusions in the bulk material,grains dislocation could occur causing the formation of holes during polishing process.Those holes are modified in term of depth and area during injection process.As reported,stress corrosion cracking can affect the molds,starting at a microscopic level and revealing itself at crack.The primary causal elements are the metallurgy of steel,the presence of chlorine in the water used in the cooling lines of the mold and the stresses on the tool during molding.It is known that Chromium gives the steel corrosion resistance,by providing a protective oxide layer.Thus it is possible that due to the polishing defects(holes),the thickness of the layer is compromised and thus when a high viscous corrosive polymer,like Surlyn,is injected,the areas affected by holes,are submitted to corrosion nature of Surlyn(based on the experience of industrial project partners),can create an aggressive environment at the mold/molten polymer interface due to the gases release.The high viscosity of Surlyn and its capability to stick onto the mold surface also plays a role in terms of exerting a mechanical-physico-chemical attack on the area where the defaults are located.All these statements allow to catalog this default as corrosion pit.4.ConclusionsThis study has allowed the identification and evaluation of defaults that occur during plastic injection process,at microscopic scale.The results obtained highlight the different damage mechanisms sustained by the mold surface,as a function of polishing,geometry and injected material.It can be also observed that for each material injected there is a difference of level of wear and damage mechanism between the stamp and the matrix.Surlyn injection exhibited considerable amount of deposits on the mold stamp.It seems that the physico-chemical conditions,created during the injection by this type polymer,favored the adhesion.Also in the case ,the coupling effects of polishing quality,the injected material,adhesion and the lack of the mold feature that evacuates air,tend to form corrosion pits on a mirror polished surface.SAN and PA66GF25 polymers were injected successively on the samemold.The mold surface presented polishing defaults(holes)before injection.The holes were enlarged in the direction perpendicular to the injection flow due to abrasive effect of glass fibers.A critical characterization of the mold surface topography was performed in order to identify the location and the type of defaults that occur when more or less aggressive material were injected in molds with different geometries.All the results provided can be taken into consideration for the design of a “chameleon” coating that can overcome present drawback.注塑模具原理与基本方法译文:与铸铁、钢铁或玻璃工业相比,塑料加工行业相对年轻。
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Employing current design approaches for plastic parts will fail to produce the true minimum manufacturing cost in these cases.
The demand for small and thin plastic components for miniaturization assembly has considerably increased in recent years.
Other factors besides minimal material usage may also become important when manufacturing thin plastic components.
1
sink mark [11] and the part deformation after molding [12], analyzing the effects of wall thickness and the flow length of the part [13], and analyzing the internal structure of the plastic part design and filling materials flows of the mold design [14]. Reifschneider [15] has compared three types of mold filling simulation programs, including Part Adviser, Fusion, and Insight, with actual experimental testing. All these approaches have established methods that can save a lot of time and cost. However, they just tackled the design parameters of the plastic part and mold individually during the design stage. In addition, they did not provide the design parameters with minimum manufacturing cost. Studies applying various artificial intelligence methods and techniques have been found that mainly focus on optimization analysis of injection molding parameters [16,17]. For in-stance He et al. [3] introduced a fuzzy- neuro approach for automatic resetting of molding process parameters. By contrast , Helps et al. [18,19] adopted artificial neural networks to predict the setting of molding conditions and plastic part quality control in molding. Clearly, the development of comprehensive molding process models and computer-aided manufacturing provides a basis for realizing molding parameter optimization [3 , 16,17]. Mok et al. [20] propose a hybrid neural network and genetic algorithm approach incorporating Case-Based Reasoning (CBR) to derive initial settings for molding parameters for parts with similar design features quickly and with acceptable accuracy. Mok’s approach was based on past product processing data, and was limited to designs that are similar to previous product data. However, no real R&D effort has been found that considers minimizing manufacturing costs for thin plastic components. Generally, the current practical approach for minimizing the manufacturing cost of plastic components is to minimize the thickness and the dimensions of the part at the product design stage, and then to calculate the costs of the mold design and molding process for the part accordingly, as shown in Fig. 1. The current approach may not be able to obtain the real minimum manufacturing cost when handling thin plastic components. 1.2Manufacturing requirements for a typical thin plastic component As a test example, the typical manufacturing requirements for a thin square plastic part with a center hole, as shown in Fig. 2, are given in Table 1.
Thus, current approaches for plastic part design and manufacturing focus primarily on establishing the minimum part thickness to reduce material usage.
Minimizing manufacturing costs for thin injection
molded plastic components
1. Introduction
In most industrial applications, the manufacturing cost of a plastic part is mainly governed by the amount of material used in the molding process.
The assumption is that designing the mold and molding processes to the minimum thickness requirement should lead to the minimum manufacturing cost.
Nowadays, electronic products such as mobile phones and medical devices are becoming ever more complex and their sizes are continually being reduced.
Thus, tackling thin plastic parts requires a new approachቤተ መጻሕፍቲ ባይዱ alongside existing mold design principles and molding techniques.
1.1 Current research
Today, computer-aided simulation software is essential for the design of plastic parts and molds. Such software increases the efficiency of the design process by reducing the design cost and lead time [1]. Major systems, such as Mold Flow and C-Flow, use finite element analysis to simulate the filling phenomena, including flow patterns and filling sequences. Thus, the molding conditions can be predicted and validated, so that early design modifications can be achieved. Although available software is capable of analyzing the flow conditions, and the stress and the temperature distribution conditions of the component under various molding scenarios, they do not yield design parameters with minimum manufacturing cost [2,3]. The output data of the software only give parameter value ranges for reference and leaves the decision making to the component designer. Several attempts have also been made to optimize the parameters in feeding [4–7], cooling [2,8,9], and ejection These attempts were based on maximizing the flow ability of molten material during the molding process by using empirical relation ships between the product and mold design parameters. Some researchers have made efforts to improve plastic part quality by Reducing the