TW201731609A - System for metal injection and counter pressure and method using the same - Google Patents

Abstract

A system for metal injection and counter pressure has: a particle providing assembly; and a forming unit having a melting unit, a counter module and a mold unit; wherein, the particle providing assembly provides particles with metal powder and bonding agent to the melting unit, the particles is formed into melted flow by the melting unit, the melted flow is provided to the mold unit, the counter module provides counter gas with predetermined pressure to the mold unit, the melted flow forms into green tape inside of the mold module.

Description

Metal injection and back pressure system and method thereof

The invention relates to a metal injection and back pressure system and a method thereof, which are systems and methods for utilizing a back pressure gas to affect a metal shot, thereby uniformly distributing the metal powder, thereby increasing tensile strength and improving uneven shrinkage after sintering.

Metal injection molding is a technology that combines plastic injection molding, polymer and metal powder. The technology combines metal powder and binder with injection molding, mixing, heating and granulation to make injection molding raw materials, and then forms into raw embryos through high-precision special molds (injectors), and is degreased or sintered. , or automated to quickly produce high-density, high-precision and complex metal parts. This technology has the advantage of reducing the process and cost of traditional metal processing. Finally, according to the product function and specification requirements, if necessary, the second processing procedure, such as heat treatment, surface treatment, etc.

Although metal injection molding is one of the precision machining techniques, problems such as the current injection molding of finished products can also be seen in metal injection molding, such as shrinkage and warpage. Therefore, there is room for discussion on how to overcome the problems that metal injection molding may encounter.

In view of the above problems, an object of the present invention is to provide a metal injection and back pressure system and a method thereof, which are added to a counterpressure gas during metal injection molding to The metal shot is more compact when propelled, thereby increasing the tensile strength and increasing the uniformity of the metal powder in the shot during metal injection molding. When the metal powder is evenly distributed, it can improve the shrinkage after sintering.

In order to achieve the above object, the technical means of the present invention is to provide a metal injection and back pressure system, comprising: a particle providing assembly; and a molding unit having a melting module, a back pressure module and a a mold module; wherein the particles provide an assembly for providing particles to the melting module, the particles having a metal powder and a binder, the melting module forming the particles into a molten fluid, the molten flow system being supplied to the mold The module, the back pressure module provides a back pressure gas having a predetermined pressure to the mold module, and the melt flow system solidifies into a green embryo in the mold module.

The present invention provides a metal injection and back pressure method, the method comprising the steps of: providing particles; and forming a green body, the particles are supplied to a melting module to form the particles into a molten fluid, and the melt system is injected into a mold. The module, a back pressure module, provides a back pressure gas having a predetermined pressure to the mold module, and the molten flow system solidifies into a green embryo.

In summary, the metal injection and back pressure system of the present invention and the method thereof are applied to a metal injection molding process to increase a back pressure gas having a predetermined pressure to increase the density of the green embryo. Due to the pressure of the back pressure gas, the metal shot is tighter when propelled, thereby increasing the tensile strength. Therefore, by back pressure gas, it can increase the uniformity of the metal powder in the shot during metal injection molding. When the metal powder is uniformly distributed, it can improve uneven shrinkage after sintering.

10‧‧‧Mixed unit

11‧‧‧mixing unit

12‧‧‧Smashing unit

13‧‧‧granulation unit

14‧‧‧Molding unit

140‧‧‧melting module

1400‧‧‧Feed nozzle

141‧‧‧Back pressure module

1410‧‧‧Backpressure gas source

1411‧‧‧Compressor

1412‧‧‧High pressure gas control valve

1413‧‧‧First diverter valve

1414‧‧‧ gas temperature sensor

1415‧‧‧ Controller

142‧‧‧Mold module

1420‧‧‧first half model

1421‧‧‧second half mode

1422‧‧‧ cavity

1423‧‧‧jecting channel

1424‧‧‧ cavity sensor

1425‧‧‧ cavity temperature sensor

1426‧‧‧ Airway

1427‧‧・Mold temperature machine

143‧‧‧High temperature gas unit

1430‧‧‧Air compressor

1431‧‧‧Air dryer

1432‧‧‧ Flowmeter

1433‧‧‧Second diverter valve

1434‧‧‧heater

144‧‧‧Control valve

15‧‧‧Degreasing unit

16‧‧‧Sintering unit

17‧‧‧Particle supply assembly

S1~S3‧‧‧ steps

A~I‧‧‧ curve

Figure 1 is a schematic view of the metal injection and back pressure system of the present invention.

Figure 2 is a schematic diagram of a high temperature gas module and a mold module.

Figure 3 is a flow chart of the metal injection and back pressure method of the present invention.

Figure 4 is a comparison of the density of primary embryos.

Figure 5 is a comparison of the density of raw embryos after degreasing.

Figure 6 is a comparison of density after sintering of the raw embryos after degreasing.

The embodiments of the present invention are described below by way of specific embodiments, and those skilled in the art can readily understand the other advantages and advantages of the present invention.

Referring to FIG. 1 , the present invention is a metal injection and back pressure system comprising a mixing unit 10 , a mixing unit 11 , a pulverizing unit 12 , a granulating unit 13 , a forming unit 14 , and a Degreasing unit 15 and a sintering unit 16.

The mixing unit 10 mixes the metal powder and the binder to form a mixed powder. The binder is a combination of paraffin and polymer materials or a polymer material. The polymer material can be polypropylene. The proportion of the metal powder is 50% to 70%, preferably 55%, 60%, 65% or 70%. If the binder is a combination of paraffin and polymer materials, the ratio of the polymer material is 19% to 29%, preferably 20%, 22%, 24%, 26% or 28%, and the ratio of paraffin is 11% to 21%. %, preferably 12%, 14%, 16% or 18%. In the present embodiment, the ratio of the metal powder to the binder is for illustrative purposes only. In actual operation, the ratio is adjusted according to the type or condition of the product, so the ratio of the binder to the metal powder is not limited to the case. Bright.

The kneading unit 11 receives the mixed powder and agitates the mixed powder at a high temperature so that the bonding agent can be uniformly distributed on the surface of the metal powder to form a kneaded powder.

The pulverizing unit 12 receives the kneaded powder and pulverizes the kneaded powder to form a powder.

The granulation unit 13 receives the powder to form the powder into granules. The granulation unit 13, the pulverizing unit 12, the kneading unit 11 and the mixing unit 10 can be regarded as a granule providing assembly 17.

The molding unit 14 has a melting module 140, a back pressure module 141, a mold module 142 and a high temperature gas module 143. The melting module 140 receives the particles to form the particles into a molten fluid. The melt flow system is provided to a mold module 142. The back pressure module 141 provides a back pressure gas to the mold module 142, and the melt flow system is in the mold module. 142 solidifies into a Green Part.

Referring to FIG. 2, as further discussed, the melting module 140 has a feed nozzle 1400.

The mold module 142 has a first mold half 1420, a second mold half 1421 and a mold temperature machine 1427.

The first mold half 1420 has a cavity 1422, at least one cavity temperature sensor 1425, at least one cavity pressure sensor 1424 and an air passage 1426. The cavity temperature sensor 1425 and the cavity pressure sensor 1424 are disposed inside the first mold half 1420 and adjacent to the cavity 1422. Air passage 1426 is in communication with cavity 1422.

The second mold half 1421 has a shot channel 1423, at least one cavity pressure sensor 1424 and at least one cavity temperature sensor 1425. When the first mold half 1421 and the second mold half 1421 are closed, the feed channel 1423 is communicated with the cavity 1422. Feed nozzle 1400 extends to shot channel 1423 to inject molten fluid into cavity 1422.

The cavity pressure sensor 1424 senses changes in the pressure of the cavity 1422 to further control the timing of injection of the back pressure gas.

The cavity temperature sensor 1425 is connected to the mold temperature machine 1427, and the cavity temperature sensor 1425 senses the temperature change of the cavity 1422 to further control the injection time of the high temperature gas.

The back pressure module 141 has a back pressure gas source 1410, a compressor 1411, a high pressure gas control valve 1412, a gas temperature sensor 1414, a controller 1415 and a first diverter valve 1413. The backpressure gas source 1410 is coupled to the compressor 1411 by a line to enable the compressor 1411 to pressurize the gas from the backpressure gas source 1410. The compressor 1411 is coupled to the high pressure gas control valve 1412 by a line. The high pressure gas control valve 1412 is coupled to the gas temperature sensor 1414 and the first diverter valve 1413 by a line. The high pressure gas control valve 1412 and the gas temperature sensor 1414 are connected to the controller 1415. The controller 1415 receives the gas temperature sensed by the gas temperature sensor 1414 and controls the opening of the control valve 1412.

The high temperature gas module 143 has an air compressor 1430, an air dryer 1431, a flow meter 1432, a second diverter valve 1433, and a heater 1434.

The air compressor 1430 is coupled to the air dryer 1431 by a line to allow the air to dry. The dryer 1431 is capable of drying the air compressed from the air compressor 1430. The flow meter 1432 is coupled to the air dryer 1431 by a line to enable the flow meter 1432 to meter the amount of air from the air dryer 1431. The flow meter 1432 and the first diverter valve 1413 are coupled to the second diverter valve 1433 by a pipeline. The second diverter valve 1433 is coupled to the heater 1434 by a line.

The first diverter valve 1413 and the heater 1434 are coupled to the control valve 144 by a line. Control valve 144 is coupled to air passage 1426 by a line.

As described above, after the mold module 142 is clamped, the first diverter valve 1413 causes the high pressure gas from the control valve 141 to enter the second diverter valve 1433, and the gas system from the flow meter 1432 flows into the second diverter valve 1433. The high pressure gas system is mixed with the gas and flows into the heater 1434 to form a high temperature and high pressure gas. The high temperature and high pressure gas system flows into the control valve 144 and is controlled by the control valve 144 to flow into the cavity 1422 via the air passage 1426 to heat the cavity 1422.

Alternatively, the gas system from flow meter 1432 flows into second diverter valve 1433 and is heated by heater 1434 and controlled by control valve 144 to flow into cavity 1422 via air passage 1426 to heat cavity 1422.

When there is molten fluid in the cavity 1422, the high pressure gas system from the first diverter valve 1413 flows into the control valve 144 and is controlled by the control valve 144 to flow into the cavity 1422 via the air passage 1426, which is a back pressure gas. . The pressure of the high pressure gas is 1 to 300 bar, which is based on actual conditions and is not limited by the present case.

The degreasing unit 15 receives the raw embryos and degreases the green embryos at a predetermined temperature.

The sintering unit 16 receives the degreased green embryo and sinters the green embryo at a predetermined temperature, and the sintered green germ is formed into a finished product.

Please refer to FIG. 3 and FIG. 1 together. The present invention is a metal injection and back pressure method, and the steps thereof include:

S1, granules are provided, and a predetermined proportion of the metal powder and the binder are mixed in a mixing unit 10 to form a mixed powder. The mixed powder is supplied to a kneading unit 11 and kneaded at a predetermined kneading temperature to form the mixed powder into a kneaded powder having a predetermined kneading temperature of 180 ° C to 220 ° C, preferably 190 ° C, 195. °C or 200 °C. The kneaded powder is supplied to the pulverizing unit 12 to pulverize the kneaded powder into powder end. The powder is supplied to the granulation unit 13 to form the powder into granules. Alternatively, the pellet-providing assembly 17 performs the above-described mixing, kneading, pulverizing, and granulating operations to form the metal powder and the binder into particles.

S2, raw embryo molding. The particle system is supplied to the melting module 140 to form the particles into a molten fluid. The melt system is injected into the mold module 142, and the back pressure module 141 provides a back pressure gas having a predetermined pressure to the mold module 142. The melt flow system solidifies into a living embryo. The predetermined pressure is from 45 to 200 bar.

S3, demineralization and sintering of raw embryos. The germline is supplied to a degreasing unit 15 for degreasing at a first predetermined temperature of 40 to 60 ° C, preferably 45 ° C, 50 ° C or 55 ° C.

If the binder is a polymer material and paraffin, the degreasing procedure is divided into two parts: cold degreasing and thermal degreasing. First, cold degreasing is carried out, and the raw embryos are first introduced into a solvent to separate the paraffin from the green embryo. The hot degreasing is further carried out, and the green embryo is degreased at a first predetermined temperature, which is to separate the polymer material from the green embryo.

When the binder is a polymer material, an acid gas is degreased, and the polymer material is separated from the green material by the acid gas system.

The degreased green germ line is supplied to a sintering unit 16, and the sintering unit 16 sinters the green embryo at a second predetermined temperature to sinter the green embryo into a finished product. The second predetermined temperature is 1250 ° C to 1500 ° C, preferably It is 1300 ° C, 1350 ° C, 1380 ° C, 1400 ° C or 1450 ° C.

As described above, the present invention is described by a metal tensile test piece having a size of 110.05 mm × 23.05 mm × 4 mm dog bone type sheet. The shrinkage after sintering was 15%.

As shown in Fig. 4, it is a comparison map of primary embryo density. The curve A indicates that when the molten fluid is in the mold module 142, the back pressure module 141 does not provide the back pressure gas, and the density distribution of the green embryo in the three regions of the near pouring, the middle and the far casting. Curve B indicates that when the molten fluid is in the mold module 142, the back pressure module 141 provides a back pressure gas having a pressure of 50 bar. Curve C indicates that when the molten fluid is solidified in the mold module 142, the back pressure module 141 provides a back pressure gas having a pressure of 100 bar.

As shown in Figure 4, when the pressure of the back pressure gas is large, the density of the green embryo is higher. Large, on the other hand, if no back pressure gas is provided, the density of the green embryo is smaller.

As shown in Fig. 5, it is a comparison of the density of the raw embryos after degreasing. Curve D represents the density distribution of the green shoots of the above curve A after degreasing. Curve E represents the density distribution of the green shoots of the above curve B after degreasing. Curve F represents the density distribution of the green shoots of the above curve C after degreasing.

As shown in Fig. 5, when the pressure of the back pressure gas is large, the density of the degreased green embryo is greater, whereas if no back pressure gas is supplied, the density of the degreased green embryo is smaller.

As shown in Fig. 6, it is a density comparison diagram of a degreased green embryo after sintering. The curve G is a graph showing the density comparison of the green embryos of the above-described curve D after sintering. The curve H is a graph showing the density comparison of the green embryos of the above-described curve E after sintering. Curve I is a graph showing the density comparison of the green embryos of the above-mentioned curve F after sintering.

As shown in Fig. 6, when the pressure of the back pressure gas is large, the density of the sintered green embryo is greater, whereas if no back pressure gas is supplied, the density of the sintered green embryo is smaller.

In summary, the metal injection and back pressure system of the present invention and the method thereof are applied to a metal injection molding process to increase a back pressure gas having a predetermined pressure to increase the density of the green embryo. Due to the influence of the metal powder and the binder on the back pressure gas, the separation of the powder from the metal powder and the binder may be greatly reduced. The main reason is that the shear stress near the gate is reduced, resulting in the viscosity of the binder. It does not suddenly drop, so it reduces the defects of depression or deformation caused by uneven shrinkage. Moreover, under the influence of the pressure of the back pressure gas, the metal shot material is tighter when propelled, thereby increasing the tensile strength, so that by back pressure gas, it can increase the uniformity of the metal powder in the shot during metal injection molding. When the metal powder is uniformly distributed, it can improve uneven shrinkage after sintering.

The specific embodiments described above are only used to exemplify the features and functions of the present invention, and are not intended to limit the scope of the present invention, and may be used without departing from the spirit and scope of the invention. Equivalent changes and modifications made to the disclosure of the invention are still covered by the scope of the following claims.

10‧‧‧Mixed unit

11‧‧‧mixing unit

12‧‧‧Smashing unit

13‧‧‧granulation unit

14‧‧‧Molding unit

140‧‧‧melting module

141‧‧‧Back pressure module

142‧‧‧Mold module

143‧‧‧High temperature gas unit

15‧‧‧Degreasing unit

16‧‧‧Sintering unit

17‧‧‧Particle supply assembly

Claims (8)

A metal injection and back pressure system comprising: a particle providing assembly; and a molding unit having a melting module, a back pressure module and a mold module; wherein the particles provide an assembly Having particles to the melting module, the particles having a metal powder and a binder, the melting module forming the particles into a molten fluid, the melt flow system being provided to the mold module, the back pressure module providing a predetermined The pressure back pressure gas is supplied to the mold module, and the melt flow system is solidified into a living embryo in the mold module. The metal injection and back pressure system of claim 1, further comprising a degreasing unit and a sintering unit, the degreasing unit receiving the raw embryo and degreasing the raw embryo; the sintering unit receiving The green embryo is degreased, and the green embryo is sintered to form the green embryo into a finished product. The metal injection and back pressure system of claim 1, wherein the particle providing assembly has a mixing unit, a mixing unit, a pulverizing unit and a granulating unit; the mixing unit is a metal powder and The binder is mixed to form a mixed powder; the kneading unit receives the mixed powder, and the mixed powder is stirred at a high temperature to form a kneaded powder; the pulverizing unit receives the kneaded powder, and kneads the kneaded powder The powder is pulverized to form a powder; the granulating unit receives the powder to form the powder into granules. A metal injection and back pressure method, the method comprising: providing particles; and forming a green body, the particles are supplied to a melting module to form the particles into a molten fluid, and the molten liquid system is injected into a mold module, The back pressure module provides a back pressure gas having a predetermined pressure to the mold module, and the melt flow system solidifies into a green embryo. The metal injection and back pressure method of claim 4, wherein the predetermined pressure is 45 to 200 bar. The metal injection and back pressure method described in claim 4, wherein In the step of providing granules, a granule provides an assembly for mixing, kneading, pulverizing and granulating the metal powder and the mixture, so that the metal powder and the binder are formed into granules; or a predetermined ratio The metal powder and the binder are mixed in a mixing unit to form a mixed powder, which is supplied to a kneading unit and kneaded at a predetermined kneading temperature to form the mixed powder into a kneaded powder. The kneaded powder is supplied to a pulverizing unit to pulverize the kneaded powder into a powder which is supplied to a granulating unit to form the powder into granules. The metal injection and back pressure method according to claim 4, further comprising the step of degreasing and sintering the raw embryo, the raw germ system being supplied to a degreasing unit for degreasing at a first predetermined temperature. The degreased germline is supplied to a sintering unit which sinters the green body at a second predetermined temperature to sinter the green embryo into a finished product. The metal injection and back pressure method according to claim 7, wherein the raw embryo degreasing system is sequentially subjected to a cold degreasing and a thermal degreasing; or the binding agent is a polymer material, and an acid gas degreasing is performed. The acid gas system removes the polymer material from the green body.