Patent Abstract:
A thermoforming methodology for laminated thermoplastic sheets which preserves the class “A” finish and high gloss thereof. A thermoformer has a vacuum box component which includes a mold, and a pressure box component which is selectively sealable in relation to the vacuum box component. A heated laminated thermoplastic sheet is placed in the thermoformer, the class “A” side thereof facing away from the mold, and the thermoformer sealed. Vacuum is applied to the vacuum box component and simultaneously air pressure is applied to the pressure box component, including application of chilled compressed air, resulting in forming of the sheet on the mold and controlled cooling of the sheet which preserves its class “A” finish and high gloss.

Full Description:
TECHNICAL FIELD 
     The present invention generally relates to methods of thermoforming a laminated thermoplastic sheet, wherein the sheet is capable of achieving a class “A” automotive finish. More particularly, the present invention relates to a thermoforming method which consistently achieves a class “A” finish of a laminated thermoplastic sheet. 
     BACKGROUND OF THE INVENTION 
     Automobile fascias, body side moldings (BSM), rockers, etc., are typically produced by an injection molding process followed by painting. The last steps of the painting process require that the painted part be baked for about 30 minutes at, for example, 250 degrees F. This production procedure is proven and functions well. However, there are a number of negatives associated with this process, including: a high scrap rate due to paint defects, expensive tooling costs, burdensome provisions for protection against possible mutilation in handling, and poor stone impact performance in sensitive areas of a motor vehicle (ie., under highway driving conditions, stones kicked up by other motor vehicles striking certain prone areas of the painted part). 
     Presently, however, new technologies are developing with the intention of eliminating the high cost of fabricating injection molding tools, and producing parts through the aforementioned injection molding and painting process. These technologies involve, as can be understood by reference to  FIG. 1 , a laminated thermoplastic sheet  10  which is formed in a thermoforming process. The laminated thermoplastic sheet  10  is composed, for example, of a paint film  12 , which may optionally include a paint layer  12   a  and a clear coat  12   b , wherein the color, finish and gloss of the class “A” side of the laminated thermoplastic sheet is matched to that of the paint of the motor vehicle to which the laminated thermoplastic sheet is to be used. A removable mask  12   c  is provided to protect the paint film  12  is removed when the part  20  is completed. The paint film  12  is bonded onto one side of a thermoformable thermoplastic substrate  18 , via an adhesive layer  16 , wherein the substrate may be, for nonlimiting example, thermoplastic polyurethanes, polyesters, vinyl copolymers, polyvinylchlorides, thermoplastic olefin (TPO), ABS, polyethylene, and blends, copolymers and/or alloys thereof. 
     Examples of laminated thermoplastic sheets  10  and methods of forming laminated thermoplastic sheets into formed parts  20  are described in U.S. Pat. No. 4,976,896 issued on Dec. 11, 1990 to the assignee hereof, U.S. Pat. No. 4,769,100 issued on Sep. 6, 1988 to the assignee hereof, and U.S. Pat. No. 4,868,030, issued on Sep. 19, 1989 to the assignee hereof; the disclosures of each of said U.S. Pat. Nos. 4,976,896, 4,769,100 and 4,868,030 being hereby herein incorporated by reference. Other U.S. patent references describe additional aspects of laminated thermoplastic sheets and the thermoforming processes therefor, as for example U.S. Pat. Nos. 6,450,793 and 6,709,734 and U.S. Patent Application Publication 2004/0076846. 
     While the technology for thermoforming laminated thermoplastic sheets has become well established, there yet remains the problem that the thermoforming process adversely affects the gloss of the class “A” finish. For example, the gloss of the class “A” finish may start at a gloss value above 70 but, as a result of thermoforming, the gloss value becomes unacceptably less than 70. Accordingly, in the prior art of thermoforming of laminated thermoplastic sheets, parts have inconsistent finish and gloss, resulting in scrap and/or parts having a finish and/or gloss which does not well match the finish and/or gloss of the paint of conventionally painted surfaces of the motor vehicle. 
     Accordingly, what is needed in the art of thermoforming laminated thermoplastic sheets, is some methodology associated with the thermoforming process which preserves, reliably under high volume production conditions, the class “A” finish of the laminated thermoplastic sheet which well matches the finish of conventionally painted surfaces of a motor vehicle, and retains a gloss value, after thermoforming, of above 70. 
     SUMMARY OF THE INVENTION 
     The present invention is a thermoforming methodology for laminated thermoplastic sheets which preserves, reliably under high volume production conditions, the class “A” finish of the laminated thermoplastic sheet which well matches the finish and gloss of conventionally painted surfaces of a motor vehicle, wherein the sheet retains a gloss value, after thermoforming, of above 70. 
     The thermoforming process according to the present invention utilizes a thermoforming apparatus including one or more heating stations and a thermoformer. The thermoformer has two mutually separable components: a vacuum box component which includes a mold, and a pressure box component in which chilled, pressurized air is introduced in order to thereby control cooling of the laminated thermoplastic sheet, which controlled cooling results in preservation of the class “A” finish and gloss value above 70. 
     A laminated thermoplastic sheet, as for example of the type described hereinabove, is loaded, in a conventional manner, onto a frame at a first station of a thermoformer apparatus. 
     Thereafter, the frame containing the laminated thermoplastic sheet is moved to a heating station, wherein preferably both the class “A” side of the sheet and the opposite class “B” side of the sheet are each heated by respective heater banks. The heater station heats the laminated thermoplastic sheet into a moldably softened state. Optionally, a pre-heat station may be provided. 
     Next, the laminated thermoplastic sheet is moved into position in the thermoformer, wherein the vacuum box and pressure box components are presently separated from each other, wherein of the laminated thermoplastic sheet is disposed between the vacuum box and pressure box components, and wherein the class “A” side of the sheet faces toward the pressure box component and the class “B” side of the sheet faces toward the mold of the vacuum box component. 
     Now, the vacuum box and pressure box components are mutually closed together, whereby the perimeter surfaces thereof mutually engage to provide an air-tight seal therebetween. 
     Once the perimeters of the vacuum box and pressure box components mutually seal, a cooling line in the mold is activated, and a vacuum (by “vacuum” is meant air pressure below atmospheric pressure) is applied to the vacuum box side of the laminated thermoplastic sheet, causing the class “B” side of the sheet to be sucked formingly onto the surface of the mold, and simultaneously compressed air (by “compressed air” is meant air under pressurization above atmospheric pressure) is forced into the pressure box component at the class “A” side of the laminated thermoplastic sheet, causing the sheet to be pressed formingly onto the surface of the mold. 
     As soon as the laminated thermoplastic sheet has formed onto the surface of the mold, the compressed air is vented as chilled compressed air (by “chilled compressed air” is meant compressed air at a temperature below substantially 70 degrees F.) is continuously flushed into the pressure box. The chilling of the chilled compressed air can be provided, for example, by a refrigeration and/or a throttling process. The chilled compressed air cools the laminated thermoplastic sheet in a rapid and controlled manner which is critical to preservation of finish and gloss of the class “A” side thereof. Alternatively, the chilled compressed air can be used throughout the forming and cooling processes. 
     Critical to the success of forming a class “A” part is the rate of cooling of the class “A” side of the laminated thermoplastic sheet. The class “A” side temperature needs to be reduced to less than 190 degrees F. within 30 seconds of initial forming of the sheet on the mold, more preferably within 20 seconds, and most preferably within 15 seconds. An infrared temperature sensor is used to indicate the class “A” side temperature of the laminated thermoplastic sheet. 
     Once the part is formed of the laminated thermoplastic sheet, the vacuum box and pressure box components are again separated, and the formed laminated thermoplastic sheet is removed, in a conventional manner from the mold. Next, the formed thermoplastic sheet is moved to a next station where it is removed, in a conventional manner, from the frame, put onto a cooling fixture, and then moved to a trimming station which trims it so as to provide a completed part. 
     Accordingly, it is an object of the present invention to eliminate the injection molding fabrication and painting process by providing a laminated thermoplastic thermoformed part having a class “A” finish and having a preserved gloss value above 70. 
     This and additional objects, features and advantages of the present invention will become clearer from the following specification of a preferred embodiment. 
    
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         FIG. 1  is a broken-away, sectional side view of a prior art thermoformed part, the part being conventionally thermoformed from a conventional laminated thermoplastic sheet. 
         FIG. 2  is a flow chart of thermoforming steps according to the method of the present invention. 
         FIGS. 3A through 3G  are schematic views depicting a series of sequential steps of the method of  FIG. 2 . 
         FIGS. 4A and 4B  are schematic views depicting an alternative embodiment of the thermoformer of  FIGS. 3C through 3G . 
     
    
    
     DESCRIPTION OF THE PREFERRED EMBODIMENT 
     Referring now to the Drawing,  FIGS. 2 through 4B  depict various aspects of the thermoforming process  100  according to the present invention. In this regard,  FIG. 2  depicts the thermoforming process  100  as a block flow chart  102 , and  FIGS. 3A through 4B  depict schematic views of various steps of the flow chart of  FIG. 2 . 
     At Block  102  of the block flow chart  100 , a laminated thermoplastic sheet  200  (see  FIGS. 3A through 4B ) is provided and loaded, in a conventional manner, onto a frame at a first station of a thermoformer apparatus, which may be, for example, configured for rotational loading, sled loading, or other form of loading. 
     The laminated thermoplastic sheet  200  may, for example, be of the type described hereinabove. By way merely of preference and not limitation, the thermoplastic carrier sheet of the laminated thermoplastic sheet  200  may have the following specifications: the composition is a thermoplastic olefin (TPO) material, having a stock thickness ranging between 40 and 400 thousandths of an inch, more preferably between 60 and 180 thousandths of an inch, and most preferably between 100 and 160 thousandths of an inch. Further by way merely of preference and not limitation, the paint film of the laminated thermoplastic sheet  200  may have the following specifications: the paint film is laminated to the thermoplastic carrier sheet, and consists of a PVDF/PMMA dispersion with color matched to specific vehicle paint; a mask is incorporated with composition primarily of polyurethane, commonly referred to as a “Version 14” or a “Version 8” available, for example through Soliant, LLC. of Lancaster SC 29720. Other paint films are usable. 
     At Block  106 , the laminated thermoplastic sheet  200  is moved, via the frame, into one or more heating stations, preferably including (see  FIGS. 3A and 3B ) an optional pre-heating station  202  at Block  106   a  and a main heating station  204  at Block  106   b , wherein the pre-heating station, when present, provides partial heating to the sheet in advance of the main heating station. Preferably, both the class “A” side A of the sheet and the opposite class “B” side B of the sheet are each heated by respective heater banks  206   ap ,  206   bp ,  206   am ,  206   bm . The heaters of the heater banks may be, for example, quartz, calrod, ceramic and or halogen. The main heater station  204  heats the laminated thermoplastic sheet  200  into a moldably softened state so that is ready for being thermoformed. 
     If Block  106   a  is utilized, wherein pre-heating of the laminated thermoplastic sheet  200  is provided at the pre-heating station  202 , then the sheet is heated thereat for between about 1 and 3 minutes to attain a sheet temperature of about 250 degrees F. Thereupon, the laminated thermoplastic sheet  200  is shuttled to the main heating station  204 . 
     At Block  106   b , the laminated thermoplastic sheet  200  is heated in the main heating station  204  preferably as follows. The class “B” side B of the sheet is spaced from heater bank  206   bm  a distance between preferably 7 inches and 24 inches and is heated to about 400 degrees Fahrenheit (degrees F.). The class “A” side A of the sheet is spaced from heater bank  206   am  a distance preferably between 12 inches and 32 inches. The laminated thermoplastic sheet  200  is heated for a period of time of preferably between 1 and 5 minutes or until the class “A” side A of the sheet attains a temperature ranging from between about 280 and 350 degrees F., more preferably between about 290 and 330 degrees F., and yet more preferably between about 300 and 315 degrees F. The heater bank temperature is controlled by an infrared sensor indicating the temperature of the class “A” side A of the sheet. 
     At Block  108  the heated laminated thermoplastic sheet  200  is delivered, via the frame, to a thermoformer  208  (see  FIG. 3C ). The thermoformer  208  has two components which are mutually separable and sealable: a vacuum box component  210  and a pressure box component  212 . In this regard, the laminated thermoplastic sheet  200  is oriented such that the class “A” side A thereof faces toward the pressure box component  212 , and the class “B” side B thereof faces toward the mold surface  224 . 
     The vacuum box component  210  includes a vacuum box wall  214  which defines a vacuum box  230 , a selectively movable inner support, a selectively movable mold  218 , and a vacuum source  220  connected to the vacuum box via a vacuum conduit  222  which passes through the vacuum box wall. The mold  218  is, for example, composed of poured aluminum which is cut back to size, surface treated and sand blasted, and includes a mold surface  224  of a predetermined shape to which the laminated thermoplastic sheet  200  is to be formingly shaped. The mold further has a plurality of coolant lines  228  through which a liquid coolant flows, wherein the coolant lines may be in multiple zones, preferably between 2 and 4 zones, for cooling the mold surface. The vacuum source is preferably capable of providing a vacuum of at least 30 inches of mercury (inches of Hg). 
     The pressure box component  212  includes a pressure box wall  240  which defines a pressure box  260 , a source of compressed air  242 , an air valve  244 , an air chiller  246 , an air port  262  at the pressure box wall, an air pressure regulation valve  264 , which may be incorporated with a dump valve  248 , in the pressure box wall, and, preferably, an auxiliary source of compressed air  250 , an auxiliary air valve  252  and an auxiliary air port  254  at the pressure box wall. The air chiller  246  cools the compressed air exiting from the source of compressed air  242 , and may, for nonlimiting example, be a refrigeration device (as for example an air conditioning unit and/or a heat exchanger)  246   a  and/or a throttling valve  246   b  for cooling by the well-known Joule-Thomson effect in which rapid expansion of a gas produces cooling thereof. The dump valve  248  is preferably in the form of a 4 inch air actuated ball valve. The source of compressed air  242  and the auxiliary source of compressed air  250  are preferably capable of providing a high cubic foot per minute air flow at a pressure of at least 50 pounds per square inch above atmospheric pressure (psi). In this regard, the airflow rate of the chilled compressed air is sufficient to maintain a predetermined chilled temperature, discussed hereinbelow, within the pressure box. 
     The vacuum box and pressure box components  210 ,  212  are movable toward and away from each other, preferably the vacuum box component being stationary, wherein when in a mutually separated state, as shown at  FIGS. 3C and 3G , the laminated thermoplastic sheet is movable into and out of the thermoformer  208 , and wherein when in a mutually closed state, the mutual perimeters  214   p ,  240   p  of the vacuum box wall  214  and the pressure box wall  240 , respectively provide an air tight seal therebetween. 
     Operation of the aforementioned components is preferably controlled by a programmable microprocessor Mp, shown at  FIG. 2 . 
     Returning to Block  108 , at  FIG. 3D  the vacuum box and pressure box components  210 ,  212  are bought together into the aforementioned closed state, whereat the perimeters  214   p ,  240   p  provide an air tight seal therebetween inclusive of the laminated thermoplastic sheet  200 . With the laminated thermoplastic sheet  200  still in the aforementioned heated state provided by Block  106 , thermoforming of the sheet is then performed at the thermoformer  208 , as follows. 
     At Block  108   a , cooling liquid (as for example water) is circulated through the coolant lines  228 . 
     Next, at Block  108   b , the vacuum source  220  is activated, drawing down a vacuum in the vacuum box  230  of from between zero and 30 inches of Hg, more preferably of between 10 and 25 inches of Hg, and most preferably of between 18 and 22 inches of Hg. As shown sequentially at  FIGS. 3D and 3E , the vacuum causes the laminated thermoplastic sheet  200  to be sucked onto the mold surface  224  and thereupon assume the shape of the mold surface. 
     Simultaneously with execution of Block  108   b , at Block  108   c  the auxiliary air valve  252  is opened and the auxiliary source of compressed air  250  thereupon delivers compressed air CA to the pressure box  260  of the pressure box component  212 . The auxiliary source of compressed air  250  provides a rapid pressurization in the pressure box  260  of between zero to 40 psi, more preferably of between 5 and 30 psi, and yet more preferably between 10 and 25 psi. The pressure of the compressed air CA in the pressure box  260  is regulated by the pressure regulation valve  264 , which may be incorporated in the air valve  244 , in the auxiliary air valve  252 , in the dump valve  248  (as mentioned and shown merely by way of example) or be a separate pressure regulation valve in the pressure box wall  240 . 
     As shown sequentially at  FIGS. 3D and 3E , the pressure of the compressed air CA pressing the laminated thermoplastic sheet  200  onto the mold surface  224  simultaneously acts with the sucking action of the vacuum source  220  drawing the laminated thermoplastic sheet onto the mold surface in Block  108   b , to thereby enhance the forming detail of the laminated thermoplastic sheet with respect to surface details of the mold surface. The pressure of the compressed air CA at Block  108   c  is held in the pressure box  260  for between zero and 40 seconds, more preferably for between 5 and 30 seconds, and yet more preferably for between 7 and 15 seconds. 
     Once the aforesaid time of pressurization at Block  108   c  has expired, the auxiliary source of compressed air  250  is shut-off by the auxiliary air valve  252  being closed and the dump valve  248  being opened so as to dump the compressed air CA from the pressure box, as shown at  FIG. 3E , to environs outside the thermoformer  208 . 
     Next, at Block  108   d , the dump valve  248  is closed and chilled compressed air CCA is introduced into the pressure box, via opening of the air valve  244 , to allow, as shown at  FIG. 3F , compressed air from the compressed air source to pass through the air chiller  246  flushingly into the pressure box  260 . The pressure value of the chilled compressed air CCA is basically the same as that indicated hereinabove for the compressed air CA. The chilled compressed air CCA flushes at a flow rate into and out of the pressure box  260  so that, at maintained pressure, the temperature of the chilled compressed air in the pressure box is maintained at between 32 and 70 degrees F., more preferably between 32 and 60 degrees F., and yet more preferably between 32 and 50 degrees F. 
     The chilled compressed air CCA is applied for between 1 and 15 seconds, more preferably between 5 and 10 seconds, the time being determined by the desire to chill the class “A” side A of the laminated thermoplastic sheet  200  to a temperature of 200 degrees F., more preferably to below 190 degrees F., wherein an infrared temperature sensor senses the temperature of the class “A” side of the sheet, and the microprocessor controls the rate of temperature lowering of the sheet to ensure retention of gloss of the class “A” side thereof. In this regard, critical to the success of forming a class “A” part is the rate of cooling of the class “A” side (or surface) A of the laminated thermoplastic sheet  200 . The class “A” side temperature needs to be reduced to less than 190 degrees F. within 30 seconds of initial forming on the mold, more preferably within 20 seconds and still more preferably within 15 seconds. Once forming of the laminated thermoplastic sheet is completed, the air valve  244  is closed. 
     At Block  110 , the laminated thermoplastic sheet  200  has fully formed on the mold surface and has now become cooled, whereupon, as shown at  FIG. 3G , the vacuum box and pressure box components  210 ,  212  are again separated, so that the formed laminated thermoplastic sheet  200 ′ can be removed from the thermoformer  208 . 
     Once the formed laminated thermoplastic sheet is removed from the thermoformer, it is moved to a next station where it is removed, in a conventional manner, from the frame, put onto a cooling fixture, and then moved to a trimming station which trims it to size to provide a completed part at Block  112 . 
     While the above described method of thermoforming involved an auxiliary source of compressed air  250 , it is possible to alternatively use the source of compressed air  242  as a singular source of compressed air to the pressure box, as for example depicted at  FIGS. 4A and 4B . In this regard, the air from the source of compressed air  242  may be chilled through the air chiller  246  initially as the singular source of compressed air  242  supplies at all times chilled compressed air to the pressure box  260 , as shown at  FIG. 4A  (in this case, the compressed air comprises chilled compressed air). Alternatively in this regard, an initial shot of compressed air may be delivered as described hereinabove using only the source of compressed air  242 , wherein a switch valve  244 ′ directs the compressed air initially through an alternate conduit with a port  254 ′, then after the laminated thermoplastic sheet has initially formed, the switch valve directs the compressed air through the refrigeration device  246  to provide the chilled compressed air at the portal  262 ′ in the manner described hereinabove, as shown at  FIG. 4B . 
     Utilizing the aforedescribed thermoforming process  100  according to the present invention, a laminated thermoplastic sheet can be thermoformed into a part with a retained gloss above 70 and distinctness of image (DOI) greater than 80, the requirement for class “A” parts for automotive industry. 
     The following examples were performed and are provided for illustrative purposes. Gloss was measured using a BYK-Gardner (of Columbia, Md. 21046) micro tri-gloss meter model 4524 at a 60 degrees surface angle. In each example, the laminated thermoplastic sheet was a TPO sheet having a composition similar to that shown in  FIG. 1 , and having a total thickness of about 140 thousandths of an inch. 
     EXAMPLE 1 
     
       
         
               
               
             
           
               
                   
               
               
                 PROCESSING CONDITIONS: 
                 VALUES: 
               
               
                   
               
             
             
               
                 Class “A” side temp. 
                 330 degrees F. 
               
               
                 Class “B” side temp. 
                 430 degrees F. 
               
               
                 Compressed air temp. 
                 Not applicable 
               
               
                 Chilled compressed air temp. 
                 Not applicable 
               
               
                 Air pressure in pressure box 
                 None 
               
               
                 Vacuum 
                 20 inches of Hg 
               
               
                 Vacuum time 
                 about 60 seconds 
               
               
                 Mold coolant temp. 
                 75 to 90 degrees F. 
               
               
                 60° gloss reading before molding 
                 at or above 70 
               
               
                 60° gloss reading after molding 
                 50 
               
               
                 Mold cooling temperature 
                 75 to 90 degrees F. 
               
               
                 Quality of part, comments 
                 Webbing, poor quality, lost gloss 
               
               
                   
               
             
          
         
       
     
     Example 1 illustrates prior art thermoforming process conditions, wherein the hoped for outcome should a high gloss class “A” part; however, poor part quality and low gloss resulted. There was no compressed air in the pressure box. 
     EXAMPLE 2 
     
       
         
               
               
               
             
           
               
                   
                   
               
               
                   
                 PROCESSING CONDITIONS: 
                 VALUES: 
               
               
                   
                   
               
             
             
               
                   
                 Class “A” side temp. 
                 320 degrees F. 
               
               
                   
                 Class “B” side temp. 
                 420 degrees F. 
               
               
                   
                 Compressed air temp. 
                 about 90 degrees F. 
               
               
                   
                 Chilled compressed air temp. 
                 Not applicable 
               
               
                   
                 Air pressure in pressure box 
                 20 psi 
               
               
                   
                 Compressed air time 
                 about 60 seconds 
               
               
                   
                 Vacuum 
                 20 inches of Hg 
               
               
                   
                 Vacuum time 
                 about 60 seconds 
               
               
                   
                 Mold coolant temp. 
                 75 to 90 degrees F. 
               
               
                   
                 60° gloss reading before molding 
                 at or above 70 
               
               
                   
                 60° gloss reading after molding 
                 50 
               
               
                   
                 Mold cooling temperature 
                 75 to 90 degrees F. 
               
               
                   
                 Quality of part, comments 
                 poor forming, lost gloss 
               
               
                   
                   
               
             
          
         
       
     
     Example 2 illustrates a second example of the prior art which is an adjustment of the process illustrated in Example 1, wherein ambient temperature compressed air was introduced into the pressure box. Although temperatures were lowered, the results were as in Example 1, poor part quality and low gloss. 
     EXAMPLE 3 
     
       
         
               
               
               
             
           
               
                   
                   
               
               
                   
                 PROCESSING CONDITIONS: 
                 VALUES: 
               
               
                   
                   
               
             
             
               
                   
                 Class “A” side temp. 
                 310 degrees F. 
               
               
                   
                 Class “B” side temp. 
                 400 degrees F. 
               
               
                   
                 Compressed air temp. 
                 about 90 degrees F. 
               
               
                   
                 Chilled compressed air temp. 
                 70 degrees F. 
               
               
                   
                 Air pressure in pressure box 
                 20 psi 
               
               
                   
                 Compressed air time 
                 7 to 12 seconds 
               
               
                   
                 Chilled compressed air time 
                 53 to 48 seconds 
               
               
                   
                 Vacuum 
                 20 inches of Hg 
               
               
                   
                 Vacuum time 
                 about 60 seconds 
               
               
                   
                 Mold coolant temp. 
                 75 to 90 degrees F. 
               
               
                   
                 60° gloss reading before molding 
                 at or above 70 
               
               
                   
                 60° gloss reading after molding 
                 60 
               
               
                   
                 Mold cooling temperature 
                 75 to 90 degrees F. 
               
               
                   
                 Quality of part, comments 
                 good forming, lost gloss 
               
               
                   
                   
               
             
          
         
       
     
     In Example 3, by adding some chilled compressed air into the pressure box, the definition of the formed part was improved, but the gloss was still inferior. 
     EXAMPLE 4 
     
       
         
               
               
             
           
               
                   
               
               
                 PROCESSING CONDITIONS: 
                 VALUES: 
               
               
                   
               
             
             
               
                 Class “A” side temp. 
                 310 degrees F. 
               
               
                 Class “B” side temp. 
                 400 degrees F. 
               
               
                 Compressed air temp. 
                 about 90 degrees F. 
               
               
                 Chilled compressed air temp. 
                 50 degrees F. 
               
               
                 Air pressure in pressure box 
                 20 psi 
               
               
                 Compressed air time 
                 7 to 12 seconds 
               
               
                 Chilled compressed air time 
                 53 to 48 seconds 
               
               
                 Vacuum 
                 20 inches of Hg 
               
               
                 Vacuum time 
                 about 60 seconds 
               
               
                 Mold coolant temp. 
                 75 to 90 degrees F. 
               
               
                 60° gloss reading before molding 
                 at or above 70 
               
               
                 60° gloss reading after molding 
                 at or above 70 
               
               
                 Mold cooling temperature 
                 75 to 90 degrees F. 
               
               
                 Quality of part, comments 
                 good forming, retained gloss 
               
               
                   
               
             
          
         
       
     
     Example 4 was carried out according to the thermoforming method  100  of the present invention, as outlined hereinabove. The forming detail and retention of gloss of the class “A” side was excellent. 
     EXAMPLE 5 
     The process as described above in Example 4 was followed, but the class “A” side of the laminated thermoplastic sheet was cooled such that the class “A” side did not reach 190 degrees F. within 15 seconds. By not switching to chilled air for greater than 15 seconds, the gloss of the part was reduced to less than a value of 70. This illustrates the importance of cooling the class “A” side of the laminated thermoplastic sheet below 190 degrees F. within 15 seconds. Not achieving this timing causes the gloss of the class “A” side to fall below 70. 
     By contrast, the process as described in Example 4 involved the chilled compressed air being introduced in less than 7 to 12 seconds into the pressure box, resulting a gloss value being retained above 70. Accordingly, it is anticipated that incorporating the chilled compressed air initially at the pressurization stage will further enhance or sustain the final gloss of the class “A” side of the laminated thermoplastic sheet. 
     To those skilled in the art to which this invention appertains, the above described preferred embodiment may be subject to change or modification. Such change or modification can be carried out without departing from the scope of the invention, which is intended to be limited only by the scope of the appended claims.

Technology Classification (CPC): 1