GB2039246A - Coating moulded articles - Google Patents
Coating moulded articles Download PDFInfo
- Publication number
- GB2039246A GB2039246A GB7932184A GB7932184A GB2039246A GB 2039246 A GB2039246 A GB 2039246A GB 7932184 A GB7932184 A GB 7932184A GB 7932184 A GB7932184 A GB 7932184A GB 2039246 A GB2039246 A GB 2039246A
- Authority
- GB
- United Kingdom
- Prior art keywords
- mold
- coating
- article
- molding
- pin
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000000576 coating method Methods 0.000 title claims abstract description 69
- 239000011248 coating agent Substances 0.000 title claims abstract description 66
- 239000000463 material Substances 0.000 claims abstract description 45
- 238000000465 moulding Methods 0.000 claims abstract description 18
- 238000002347 injection Methods 0.000 claims abstract description 13
- 239000007924 injection Substances 0.000 claims abstract description 13
- 229920005989 resin Polymers 0.000 claims description 23
- 239000011347 resin Substances 0.000 claims description 23
- 229920001187 thermosetting polymer Polymers 0.000 claims description 12
- 239000012530 fluid Substances 0.000 claims description 11
- 239000007788 liquid Substances 0.000 claims description 11
- 238000000034 method Methods 0.000 claims description 8
- 238000007906 compression Methods 0.000 claims description 2
- 230000006835 compression Effects 0.000 claims description 2
- 239000000498 cooling water Substances 0.000 claims description 2
- 239000000758 substrate Substances 0.000 description 13
- 239000003677 Sheet moulding compound Substances 0.000 description 8
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 8
- 239000004033 plastic Substances 0.000 description 5
- 229920003023 plastic Polymers 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000004809 Teflon Substances 0.000 description 4
- 229920006362 Teflon® Polymers 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- 239000008199 coating composition Substances 0.000 description 3
- 239000004744 fabric Substances 0.000 description 3
- AZQWKYJCGOJGHM-UHFFFAOYSA-N 1,4-benzoquinone Chemical compound O=C1C=CC(=O)C=C1 AZQWKYJCGOJGHM-UHFFFAOYSA-N 0.000 description 2
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 2
- IISBACLAFKSPIT-UHFFFAOYSA-N bisphenol A Chemical compound C=1C=C(O)C=CC=1C(C)(C)C1=CC=C(O)C=C1 IISBACLAFKSPIT-UHFFFAOYSA-N 0.000 description 2
- XSIFPSYPOVKYCO-UHFFFAOYSA-N butyl benzoate Chemical group CCCCOC(=O)C1=CC=CC=C1 XSIFPSYPOVKYCO-UHFFFAOYSA-N 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 238000009472 formulation Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000003825 pressing Methods 0.000 description 2
- 239000002990 reinforced plastic Substances 0.000 description 2
- 230000003068 static effect Effects 0.000 description 2
- OLUNIGWWQYXBJA-UHFFFAOYSA-N 2,3,4-trimethoxyphenol Chemical compound COC1=CC=C(O)C(OC)=C1OC OLUNIGWWQYXBJA-UHFFFAOYSA-N 0.000 description 1
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000000748 compression moulding Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000012809 cooling fluid Substances 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- GYZLOYUZLJXAJU-UHFFFAOYSA-N diglycidyl ether Chemical compound C1OC1COCC1CO1 GYZLOYUZLJXAJU-UHFFFAOYSA-N 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001879 gelation Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 238000007373 indentation Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000013011 mating Effects 0.000 description 1
- 239000010445 mica Substances 0.000 description 1
- 229910052618 mica group Inorganic materials 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052628 phlogopite Inorganic materials 0.000 description 1
- 238000007747 plating Methods 0.000 description 1
- 229920002689 polyvinyl acetate Polymers 0.000 description 1
- 239000011118 polyvinyl acetate Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000012047 saturated solution Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- 229920006305 unsaturated polyester Polymers 0.000 description 1
- 229920001567 vinyl ester resin Polymers 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C37/00—Component parts, details, accessories or auxiliary operations, not covered by group B29C33/00 or B29C35/00
- B29C37/0025—Applying surface layers, e.g. coatings, decorative layers, printed layers, to articles during shaping, e.g. in-mould printing
- B29C37/0028—In-mould coating, e.g. by introducing the coating material into the mould after forming the article
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C43/00—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor
- B29C43/02—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor of articles of definite length, i.e. discrete articles
- B29C43/14—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor of articles of definite length, i.e. discrete articles in several steps
- B29C43/146—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor of articles of definite length, i.e. discrete articles in several steps for making multilayered articles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2791/00—Shaping characteristics in general
- B29C2791/001—Shaping in several steps
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C43/00—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2063/00—Use of EP, i.e. epoxy resins or derivatives thereof, as moulding material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
- B29K2105/06—Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Casting Or Compression Moulding Of Plastics Or The Like (AREA)
- Moulds For Moulding Plastics Or The Like (AREA)
Abstract
Apparatus for coating one surface of a molded article (28) comprises a pair of hot relatively movable die members (2, 4) which when closed, form a cavity for molding the article (28). A pin (10) is selectively movable into and out of engagement with the surface of one of the die members (2). On retraction, the pin (10) is retracted through an opening (20) in an injector nozzle (6) allowing the injector to force material into the cavity to coat the outer surface of the article (28) while the die members are partially closed. The barrel of the injector nozzle (6) is cooled. The material when injected flows substantially parallel to the outer surface of the molded article (28) from the injection orifice. The interior surface of the mold member (2) over which this material flows is roughened. <IMAGE>
Description
SPECIFICATION
In the mould coating method and apparatus
This invention relates to a nozzle for in-the-mold coating apparatus.
In-the-mold coating processes involve first molding a base portion of the article in the cavity of a pair of relatively movable die members of a die molding set. The base portion of the article is allowed to cure after which a skin forming coating material is injected onto the surface to be improved. Pressure is applied onto the die members so as to distribute the skin forming coating material substantially uniformly across the surface of the base portion and thereby substantially fill the porosity and any shrink portions on the surface. The prior art is best set forth in U.S.Patents 4,076,780; 4,076,788 and 4,082,426, all assigned to General Motors and an article entitled, "The Mechanics of Molded Coating for Compression Molded Reinforced Plastic Parts" by Robert Ongena, 33rd Annual Technical Conference, 1978,
Reinforced Plastics/Composites Institute, The Society of the Plastics Industry, Inc., Section 14B, pages 1-7; and Modern Plastics, June 1976, pages 54-56 by
William Todd.
The apparatus disclosed in the prior art consists of a pair of relatively movable die members, one of which is movabletowardsthe other through a hydraulic ram. When the die members are closed, a cavity is formed therebetween for molding an article in a desired configuration. One of the die members is characterized in that a chamber is formed therein which communicates with the cavity and is adapted to receive a metered amount of liquid coating material in the form of a thermosetting resin which is subsequently used for coating one surface of the molded article. The chamber is provided with a slidable piston or plunger which is movable through an appropriate actuator so as to displace the liquid coating material from the chamber into the cavity and onto one surface of the molded article without requiring the die members to be opened.The coating material is applied to the chamber by an injector device which has a body portion, one end of which is formed with a nozzle that is located adjacent to the chamber. The nozzle is selectively movable into and out of sealing engagement with an inlet port formed
in the associated die members and communicating with the chamber. When the base portion of the article is first being molded in the cavity, the piston in the chamber is flush with the mold cavity and so positioned that both the chamber and the inlet port are closed from communication with the cavity.
After the base portion of the article is hardened suffi cientlyto retain its shape, the piston is moved by the actuator to a second position exposing a predeter
mined volume of the chamber to the cavity. Simultaneously, the injector device is moved into the inlet port and the liquid coating material is supplied to the chamber with the hydraulic pressure on the ram being relieved. With the nozzle of the injector positioned in the inlet port, the piston is moved by the actuator towards the cavity so as to force the coating material under pressure onto the surface to be coated.The press ram is again actuated to cause the die members to move toward each other and applying pressure to the coating material and the pressure and temperature is maintained for a time sufficient for the coating material to set up suffi cientlyto allow opening of the die members and ejection of the coated molded article.
The prior art mold dies are maintained in a parallel configuration by hydraulic cylinders mounted on the bottom press plates pushing upward against the upper plate. The cylinders also part the dies for injection. A fifteen hundred ton ram forces the upper plates downward resulting in two hydraulics operating against each other. The apparatus of the prior art, though a significant advance in the art, is extremely complex involving a toggled nozzle which comes into contact with the mold, fills a reservoir then retracts, then the contents of the reservoir are injected into the mold.
The present invention eliminates the need for the toggle mechanism, the reservoir, the reservoir fluid ejector system, and the prior art hydraulic leveling system.
The present invention is directed to a water cooled valved injector nozzle which is permanently mounted in a hot die member. The injector nozzle injects directly into the mold cavity. Mechanical assists on the corners of the movable upper die need not be used to supplement the lifting force created by the hydraulic fluid used to open the mold. Conventional heel blocks are used to maintain the dies in a parallel configuration. In addition, appropriate controls need not be employed to synchronize with the opening of the mold or with the rate of flow of the coating material into the cavity. In addition, means such as the ForceNelocity control system described by William Todd in his article entitled, "Control System Promises Advance Compression Molding Technology," printed in Modern Plastics, June 1976 on pages 54-56 need not be used.
The present invention in another aspect is directed to a process and apparatus including a water cooled valved injector nozzle which is permanently mounted in a hot die member. The injector nozzle injects directly into the mold cavity. A stream is injected parallel to a roughened substrate surface.
The die forming the roughened surface has, in turn, a rough surface. Mechanical assists on the corners of the movable upper die need not be used to supplementthe lifting force created by the hydraulic fluid used to open the mold. Conventional heel blocks may be used to maintain the dies in a parallel configuration. In addition, appropriate controls need not be employed to synchronize with the opening of the mold or with the rate of flow of the coating material into the cavity.
The material of the article to which the in-the-mold coating is applied may contain glass fibres. It is preferably hot when the coating is injected.
The dies of the mold preferably have a shear edge, and when they are slightly separated for the injection of the coating preferably a seal is maintained at the shear edge. The relative positioning of the dies may be controlled solely by the ram of the mold. The molding sequence including the injection of the in the-mold coating and the separation of the dies for this injection may be controlled using the mold timer, e.g. the degas cycle of the timer may be used to control the die separating and injection cycle.
One way of carrying out the invention is described in detail below by way of example with reference to the drawing which illustrates only in which
Figure 1 is a view partially in section of a mold having the valved injection nozzle mounted in the lower die thereof.
Figure 1 a is a view partially in section of the valved injector nozzle of Figure 1, showing the remainder of the valve structure.
Figure 2 is a perspective view and an end view of the Teflon (Registered Trade Mark) baffel used in the injection nozzle of Figure 1.
Figure 3 is a figure of the dies showing heel blocks.
Figure 4 is a top view of the bottom die showing a roughened surface.
Referring to the drawings, a conventional hydraulic press, not shown, supports a pair of relatively movable die members 2 and 4, the lower one of which identified by reference numeral 2, is rigidly secured to the base while the upper die member 4 is fixedly connected with a plate member which, in turn, is movable vertically through a double acting hydraulic ram mounted on the support member. The hydraulic ram serves to raise the upper die member 4 relative to the lower die member 2 and, although not shown, the upper die member 4 is guided during such movement through appropriate guide mem
bers. Thus, by actuating the hydraulic ram, the upper
die member 2 can assume an open raised position or
a lowered closed position as shown in Figure 1.
When the die members 2 and 4 are closed, they form
a cavity for molding a plastic article under heat and
pressure in a desired configuration. The die members 2 and 4 can not only serve to mold a plastic article as seen in Figure 1, but, in addition, the die member 2 incorporates parts and components to be described hereinafter that provide a coating on one surface of the molded article. The coating is in the form of a liquid skin forming thermosetting resin which is injected against the surface being coated.
In order to deliver the liquid thermosetting resin coating material to the surface to be improved, the lower die member 2 has been designed so as to include a valved injector nozzle 6. In this regard, the lower die member 2 is formed with a horizontally oriented cylindrical recess 8 in which valved injector nozzle 6 is permanently mounted. Valve pin 10 is connected to an actuator in the form of a double acting hydraulic piston 12 movable in cylinder 14. By directing pressurized fluid to one end or the other of the hydraulic cylinder 14, the piston 12 is movable between the fabric bumper 16 and fabric bumper 18.
Movement of the piston 12 to fabric bumper 18 opens injector valve 20. In the open position, thermosetting resin 22 flows through material inlet 24, stainless steel barrel 26, through open valve 20 and into the mold cavity.
The injector device 6 is carried by the lower die member 2 which as seen in Figure 1, includes a cylindrical recess 8 having its end portion 30 threaded, which serves to securely mount the injector device to the lower die member 2 by threaded nozzle end 32. The outer sleeve member 34 is secured at its left-hand end as seen in Figure 1 to an elongated inner barrel 26 through flange 35 at its right-hand end. The outer sleeve member 34 is attached to barrel 26 through the injector nozzle assembly 36. Between the inner periphery surface of a portion of the sleeve member 34, and the outer surface of barrel 26, are passages for cooling fluid to be directed from inlet 38 to the nozzle assembly 36 and then to exhaust at outlet port 40.A Teflon (Registered Trade Mark) baffel 42 is positioned in the outer sleeve member 33 to direct the flow of cooling water to the cooling chamber 43 of injector nozzle assembly 36. As seen in Figure 2, Teflon baffel 42 has flat surfaces 44 and 45 which permits water to flow between the outer sleeve member 34 and the
Teflon baffel 42 and enter the injector nozzle assembly 36. The barrel 26 fits through the hole 46 in the baffle 42. Directing cooling of the water to the injector nozzle assembly 36 keeps the injector nozzle assembly cool enough that it does not cause the resin injected by the nozzle to cure, but warm enough so that it does not cool the part of the mold to which it is attached and cause undercure of resin in that area.
The valved nozzle is opened and closed by air at 100 psi (689 kPa) or hydraulic fluid at 1,000 psi (6894 kPa). When hydraulic fluid (including air) is directed via a port 48 in centre flange 35, to the chamber at the left-hand side of the piston member 12, the pin 10 is shifted toward the right allowing resin to be injected into the mold. On the other hand, when hydraulic fluid is directed via a port 50 in end flange 52 to the chamber at the right side of piston member 12, the pin 10 of the injector device moves to the left closing the valve at 20 and completing the smooth surface on the inside of die 2.
Air is the preferred fluid as it eliminates the danger of contaminating the injector resin with hydraulic fluid. The injector resin is maintained at 1,000 psi (6894 kPa) so that any leakage will be resin into the air chamber and not vice-versa.
The in-the-mold coating resin is fed into the valved injector at resin inlet 24, which is adapted to be connected through a conduit (not shown) to a source of pressure supplied ingredients which make up one or a two component thermosetting resin system. If a two component resin is used, a static mixer such as that made by Kenics Corporation serves to mix the two liquid components of the thermosetting resin system prior to introduction through port 24. Other known mixers can also be used. It should be apparent that when the pin 10 is moved toward the right, the nozzle will be opened and permit the thermosetting resin coating material to flow into the upper die member 2 if the pressure is great enough to overcome the pressure exerted by the press on the die.
The lower die 2 has a roughened inner surface 3.
This imparts a roughened surface to the substrate part. Flow of in-the-mold coating resin across the roughened surface causes a separation of resin and filler leaving a resin-rich layer on the substrate surface. The resin-rich layer appears to aid adhesion.
The indentations in the surface of the die can range from about about 0.001 mm to 0.01 mm.
The apparatus described above operates as follows. Initially the upper die member 4 is raised relative to the lower die member 2 so as to expose the cavity portion within the lower die member. Slabs of sheet molding compound are then placed in the bottom of the lower die member 2 within the cavity at appropriate locations. Pin 10 is positioned to form a smooth inner surface with the inner surface of die 2 by pressurization of port 50. The mold is pressurized, driving the heated upper die member 4 downwardly into telescoping engagement with the fixed heated lower die member 2. As the upper die member 4 closes on the lower die member 2, the slabs of sheet molding compound are deformed under heat and pressure and flow to fill the mold cavity and any rib forming grooves therein so as to form a ribbed substrate identified by the reference numeral 28.The molding pressure generated by the ram of the mold is maintained on the upper die member 18 until the substrate 28 cures and hardens sufficiently to permit separation of the upper die member 4 without adversely affecting the substrate. Mold timer No. 1 is set at 1/2 to 5 minutes to accomplish the initial cure.
During the cure cycle, sink marks are usually formed above the ribs due to shrinkage occurring.
Similarly, the surface of the substrate may also have other imperfections, such as porosity, line cracks, etc. Such defects in the outer surface of the substrate 28 are eliminated by providing a cosmetic coating to the surface to be improved. This coating is applied according to this invention during the final stages of curing of the substrate.
In applying the coating, the ram pressure of the mold initially is relieved on the upper die member 4 by operation of a timer T-2, which is set at about 1 to 4 seconds. This opens the mold 1/2 inch. Pressurized fluid is directed through port 48 to the left side of the piston member 12 while the other side of the piston member is vented via port 50. The degas timer T-3 of the mold is used to control both the movement of pin 10 and the mold opening time. In-the-mold coating material is injected for about 1 to 15 seconds through material inlet port 24. When T-3 has timed out, the press comes back down to tonnage and is timed out by T-4 (about 1 to 15 minutes) to cure the coating. Simultaneously with the press coming down, pin 10 is moved back to form part of the inner mold wall.
During the time that the pin 10 is retracted, the coating material flows into the cavity. The coating material moves outwardly parallel to the surface of the substrate 28 hydraulically pressing the latter tightly against the upper die member 4 and thereby preventing its dislodgement or unseating therefrom.
Following the pressurized supply of the coating material onto the lower surface of the substrate 28, the press is once again activated so as to close the die members 2 and 4 and cause the coating material to be uniformly distributed on the surface to be coated.
Heel blocks 60 which mate with recesses 62 align the dies of the closing mold. Guide pins and mating recesses can also be used in conjunction with the heel blocks. The pressures and temperatures as well as the type of coating material that can be utilized with the apparatus according to this invention is fully described in U.S.A. patent applications nos. 814502 of 11th July 1977 and 897980 of 20th April 1978 see published German application OLS 2830433. Accordingly, attention is directed to these applications for a full understanding of the process that can be practiced with this invention.
Specific examples for injecting the coating by using an injection nozzle which has a pin protruding through the opening in the nozzle will now be set forth. In the closed position the end of the pin forms a small portion of the inner mold surface. In the open position, the pin is pulled back from the mold and from the opening in the nozzle allowing coating material to be injected into the mold. The pin is stabilized against rotation so that it will always form a smooth surface with the mold wall in the closed position. The nozzle is at a different temperature from the mold because it is water cooled.
Charge weights giving as much as .5mm of coating have been used, but an average of .07 to .10mum of coating has generally been enough to give both opacity and complete coverage. Since the usual substrate part averages 2.5mm in thickness, a typical coating has required about .03 to .05gm of coating per gm of SMC (sheet molding compound) used.
Simple coating charge placements, often a single pool or strip formed by high pressure injection usually have provided complete coverage.
Mold temperatures from 140 to 1 600C have given satisfactory coatings. A minimum cure time of 10 to 30 seconds at 1500C has been used but slower cure rates have sometimes been required to prevent too rapid gelation resulting in incomplete coverage.
Higher molding pressures, as expected, provide better coverage of steeper, lower draft surfaces.
However, the typical pressures needed to mold the base SMC part have also generally been adequate to give a complete coating.
The principle aim of the in-the-mold coating has been to fill voids, reduce sinks and act as a replacement for the primer-sealer now commonly used by custom molders of SMC.
In-the-mold coated parts have passed the automotive tests normally used.
In the following examples as elsewhere in the specification and claims, all parts and percentages are by weight unless otherwise specified.
Example I
A 1973 Oldsmobile grill opening panel was molded using a standard Rohm & Haas unsaturated polyester based sheet molding compound using 6895 kPa pressure (1,000 psi). The press used was manufactured by Erie Press in Erie, PA. Most of the presses made by the various manufacturers have automatic degas controls or they can be added.
The automatic degas cycle of the press was activated to control the sequence necessary for molding the parts, opening the mold to inject the in-the-mold coat and reclose on the proper pressure to coat the parts. The parts were molded and were excellent in appearance. They were tested and passed all the tests run. The coating in some instances was so thick that a cross-hatch adhesive could not be run. The one-component in-the-mold coating was 2.2mm thick. The molding sequence was as follows.
All four timers on press were used. Timer No. 1 (T- 1) is the precure timer and was set at 2-1/2 minutes to mold and cure the part. When the cure time has elapsed and the press comes off tonnage,
T-2 times the flow of oil to return the ram (set at 1-11/12 seconds), this opens the mold to 13mm.
In-the-mold coating material was then injected into the mold with the timer on the injector being the
T-3 time, which, in this case, was set at 13 seconds.
When T-3 has timed out, the press came back down and onto tonnage and was timed out by T-4 (60 seconds) to cure the coating.
This whole sequence worked very well for molding and coating parts and the press repeated the same sequence correctly every time except T-2 which appeared to result in a 3mm variation either way once in a while. This is understandable as break-away force needed can and will fluctuate with fluctuation in charge weight and charge placement when shears are as wide open as on this part.
With this set-up precure pressure and cure pressure were different to hide sinks over bosses and ribs. Mold cure pressure was reduced to 78740
Kg/area of front end (100 tons/area front end) less than precure tonnage to reduce the tendency for parts to crack.
An interface signal from T-2 is used to activate the injector and another signal from T-3 is used to shut it off. This eliminates a need for a separate timer for the injector. During injection a seal was maintained by the shear edge of the mold. The following inthe-mold coating composition was the one injected through a cooled injection nozzle positioned between the parting surfaces of the mold and injecting
parallel to the parting surfaces.
The coating composition used had the following formulation.
Components Parts
Vinyl ester resin' in styrene (believed to be 66% copolymer of acrylic acid and diglycidyl ether of bisphenol A in 44% styrene some trimethoxyphenol is present for cross-linking) 200 40% polyvinyl acetate, free of carboxyl groups, dissolved in 60% styrene2 80
Styrene 46 Canadian talc 0.03mm average particle length 200
Suzorite mica (phlogopite) 0.03mm average particle length 140
Tertiary butyl benzoate 6
Saturated solution of parabenzoquinone in styrene (inhibitor) 0.6
Dialkyl phosphate3 (mold release) 3.0 'DowXD 9013.02 2Union Carbide LP90 3Zelac NE duPont
The following are the processing parameters and test results of Example
Mold temperature 2950F SMC cure time 2 mins.
Coating cure time 1 min.
Coating thickness 3 to 18 mils (18
mils on horizontal
uniform)
The parts are presently being evaluated in actual handling and use. No failures have been reported.
Example Il Example I was repeated manufacturing test parts using a two component in-the-mold coating composition. The formulation is generally set forth in
U.S. Patent 4,081,578. A proportioning pump was used. The pump has two large cylinders. The piston in each cylinder was driven by a common drive so that each piston moved exactly the same distance.
One cylinder contained one reactive component and the other cylinder contained the other reactive component. The displacement of the two cylinders is more than sufficient for one in-the-mold coating. The output from the two cylinders was mixed in a static mixer (Kenics Mixer) and injected into the mold using the valved injector nozzle of the present invention. The cure time for the in-the-mold coating was one minute.
Other than the above recited differences, the same procedure was followed as that set forth in Example
1.
The preferred mold has a chrome or nickel-plated cavity. The interior faces of the mold are preferably roughened by impingement with glass beads or sand-blasted prior to chrome plating. The roughened surface causes a separation of the resin and filler of the in-the-mold coating giving a resinrich phase at the interface between the substrate and the in-the-mold coating.
Both the injector and the proportioning pump are available from the Tompkins-Johnson Co. 2425 West
Michigan Avenue, Jackson, Michigan 49202.
Various changes and modifications can be made in this construction without departing from the spirit of the invention.
Claims (9)
1. A method of molding an article of thermoset- ting material including the steps of molding a first thermosetting material in a mold, and after at least partially curing the first material injecting a second thermosetting material into the mold to form an inthe-mold coating, the said second material when injected flowing within the mold substantially parallel to the surface of the molded first material from an injection orifice.
2. A method according to claim 1 wherein the mold is formed of at least two dies which are parted from their fully closed position when said second material is injected.
3. A method of molding an article of thermosetting material, including the steps of molding a first thermosetting material in a mold, and after at least partially curing the first material injecting a second thermosetting material into the mold to form an inthe-mold coating, wherein the mold has a rough surface which forms a corresponding surface of the first material when molded, the said second material flowing between said rough surface and said corresponding surface when molded.
4. Apparatus for injecting a liquid thermosettable resin coating onto a hot compression molded article between two sealed mold dies, comprising
a cooled injector head having a pin valve, one end of the pin forming part of the interior surface of the
mold when the valve is closed, the body of the pin extending through the cooled injector head in the closed position of the valve.
5. Apparatus for molding an article and subsequently coating one surface of such molded article, said apparatus comprising a pair of relatively movable die members which, when closed, form a cavity wherein an article is molded in a desired configuration, means operatively associated with said die
members for moving said die members towards and away from each other into open and closed positions
respectively, an inlet port formed in said one of said
die members, an injector device for supplying a metered amount of liquid coating material under
pressure, said injector device having a head portion
provided with connected concentric outer and inner
sleeve members which form a cooling water
chamber, the inner and outer sleeve members each
having inner and outer ends, the inner end of the
inner sleeve member being attached to a nozzle so
as to permit said injector device to supply a metered
amount of liquid coating material a feeder tube
formed by the inner surface of said inner sleeve memberforsaid liquid coating material, an end flange secured to said outer end of said outer sleeve member and having an annular bore formed therein, a centre flange connected to said other end of said outer sleeve and to the feeder tube, a piston located in said annular bore, and a pair of ports in said flanges adapted to direct pressurized fluid to one side or the other of said piston member so as to open and close the nozzle so when the nozzle is open the liquid coating material will flow th rough said feeder tube, wherein there is provided a means for permanently attaching the nozzle of the injector device to a die member, a pin connected to the piston for moving said pin between a first position wherein said pin seals the nozzle and forms part of the inner wall of a die and a second position wherein the pin is retracted by said piston through the nozzle opening to allow coating material to be injected into the mold.
6. A valve for in-the-mold coating apparatus substantially as herein described with reference to and as shown in the accompanying drawings.
7. Apparatus for molding an article substantially as herein described with reference to and as shown in the accompanying drawings.
8. A method of molding an article substantially as herein described with reference to the accompanying drawings.
9. An article produced by a method according to any one of claims 1 to 3 and 7.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US05/944,093 US4245976A (en) | 1977-07-11 | 1978-09-20 | Nozzle valve for in-the-mold coating apparatus |
| US05/974,583 US4235833A (en) | 1977-07-11 | 1978-12-29 | In-the-mold coating apparatus and method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| GB2039246A true GB2039246A (en) | 1980-08-06 |
| GB2039246B GB2039246B (en) | 1982-09-22 |
Family
ID=27130193
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB7932184A Expired GB2039246B (en) | 1978-09-20 | 1979-09-17 | Coating moulded articles |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB2039246B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5383775A (en) * | 1993-03-16 | 1995-01-24 | Hanano Corporation | Powdery mold release agent spray device |
| WO2004035697A1 (en) * | 2002-10-16 | 2004-04-29 | Omnova Solutions Inc. | Coating for providing a tactile surface to molded articles |
-
1979
- 1979-09-17 GB GB7932184A patent/GB2039246B/en not_active Expired
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5383775A (en) * | 1993-03-16 | 1995-01-24 | Hanano Corporation | Powdery mold release agent spray device |
| WO2004035697A1 (en) * | 2002-10-16 | 2004-04-29 | Omnova Solutions Inc. | Coating for providing a tactile surface to molded articles |
Also Published As
| Publication number | Publication date |
|---|---|
| GB2039246B (en) | 1982-09-22 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PCNP | Patent ceased through non-payment of renewal fee |