The present disclosure relates to the manufacture of molded polyurethane foam products and, more particularly, to a method of manufacture incorporating a post-cure step according to which such polyurethane products are, in an energy efficient manner, made more robust and better suited to shipping.
It is generally known to provide a molded polyurethane foam cushion for the comfort of an occupant of a seat, whether the seat is for a piece of furniture, a piece of equipment, or a vehicle, such as an automobile.
Molded polyurethane foams (both of the soft and firm varieties) may be formed by the so-called “one shot” process of mixing two streams—a first (or isocyanate) stream and a second (or polyol) stream—essentially comprised of the following components: A base polyol resin material, a copolymer polyol resin material, water, a catalyst (or catalyst package), typically an isocyanate such as, for instance, TDI, MDI or blends thereof (generally, such blends are not less than 5% of either TDI or MDI; e.g., TM20, a blend of 80% TDI and 20% MDI), and a surfactant. Various additives can, as known, be used to provide different properties.
It is generally understood to mix the above components by pouring two streams of the materials into a mold, closing the mold, and allowing the components to react. This reaction is exothermic, although auxiliary heat (approximately 150°-170° F., using an isocyanate catalyst) is typically applied to the mold to help reduce the amount of time to cure the foam and thereby more quickly produce the foam product.
Optionally, the resultant foam product is crushed in the mold using a time pressure release process (TPR process). TPR includes reducing the sealing pressure of the mold to allow gas to escape the foam and mold during cure and/or prior to being removed from the mold (i.e. “demold”). As a further option (and preferably), the demolded foam product may also be mechanically crushed (and may be repeatedly crushed) using a crushing apparatus such as a vacuum, a hard roller, or a brush crusher. This conventionally occurs as soon as 2 minutes following demold. The mechanical crushing apparatus applies a predetermined force to obtain a predetermined amount of reduction in thickness of the foam product at a particular time (e.g. from 15 seconds to 8 minutes, and more preferably from 90 seconds to 2 minutes) after demold and for a given period of crush time. Conventionally, mechanical crushing proceeds sequentially, with a first stage performing a 50% compression (i.e., compression to 50% of the original thickness of the foam), followed by a second stage performing a 90% compression, and a third stage also performing a 90% compression. The post-demold crushing operation is advantageous in providing an improved dampening of vibration through the foam product (such as, in the case of an automobile seat, the dampening of road vibration), as well as in creating improved perceived comfort of the product when employed as a seat.
Crushing is an important part of the process in manufacturing molded polyurethane seats in particular. In the absence of proper crushing, the foam product will exhibit a false hardness and, in subsequent use, will suffer height loss under compression. In the automobile industry specifically, the height at which a driver has adequate visibility (the H-point) is a critical design specification which must be accounted for in the manufacture of polyurethane seats. Improperly crushed foam seats can result in unwanted variation of the H-point. Additionally, an improperly crushed seat which later loses height under compression can cause an undesirable alteration in the seat's cosmetic appearance as the seat cover may become loose.
In a mass-production environment for the manufacture of polyurethane foam products, such as seats, crushed foam products may be placed on a monorail or other conveyor to cure for a period of time (e.g., 30-120 minutes). Afterwards, the foam products may be bagged or otherwise collectively packaged for shipment to another location for the performance of further operations (such as seat assembly, for instance). Because the foam product is generally not fully cured at demolding, if the time during which the foam products are allowed to cure on the monorail or other conveyor is too short, the foam products may still be warm enough so that, upon bagging/packaging, they may impinge on and form semi-permanent or even permanent dents or compressions in adjacent foam products. This is known as set damage. Such damaged foam products are typically rejected as waste or scrap.
Shipping costs for molded polyurethane foam products is relatively very high since the products are essentially air and so take up a relatively large volume with a relatively low mass. As fuel costs increase, these shipping costs likewise increase. The greater the degree to which polyurethane foam products may be compressed, the greater the numbers of such products which can be shipped and, thus, the more economical shipping becomes.
Previously, a post-cure step has been used in the production of molded polyurethane foam products in order to reduce set damage. As shown in
While beneficial in producing a molded foam product whose more dense superficial layer protected from set damage during shipping, the post-cure operation of the prior art was time-consuming. A more prevalent method for the conventional manufacture of molded polyurethane foam products, as shown in
A method of manufacturing a foam product comprising molding the foam product by injecting liquid material into a mold cavity; de-molding the foam product by removing the foam product from the mold cavity; post-curing the foam product, after de-molding and prior to crushing the foam product, to reduce set damage and form a superficial layer thereon by applying auxiliary heat; and crushing the foam product to obtain a predetermined reduction in thickness of the foam product by mechanically compressing the foam product. The method further comprising cooling the foam product, after post-curing and prior to crushing the foam product, by removing the auxiliary heat applied to the foam product.
Referring generally to the FIGURES, and in particular to
Post-cure step 20 takes place as soon as possible following demolding 11 so that the core temperature of the polyurethane product is kept elevated to reduce/eliminate the time and energy required to perform the post-cure operation. Preferably, the post-cure step 20 stakes place within no more than a few minutes of demolding.
As is known, the molding step 10 is conventionally performed with the application of auxiliary heat at temperatures (typically, approximately 130°-170° F.) sufficient to accelerate curing. During this step, which is an exothermic reaction, the polyurethane product's core temperature is raised to a temperature of approximately 180°-200° F., depending upon mass. Following demolding 11, the molded foam product is heated during the post-cure step 20. The temperature at which the post-cure step 20 is performed is sufficient to effect a melting of the foam at the outer surface thereof, such as depicted diagrammatically in
The crushing step 40 forces the exchange of gases generated in the foam product during molding with the ambient air, and so rapidly lowers the core temperature of the foam. The energy inefficiency of performing the prior art post-cure operation after crushing is manifest (
While the post-cure step 20 may be performed using any device and/or means suited to further curing of the foam product and formation of a denser superficial layer thereon, exemplary devices include any one or more of thermal curing devices, such as in a conventional industrial oven, induction heating, dielectric heating (such as with microwaves), gas-fired infrared radiant heating, UV heating, plasma heating, or electron-beam processing (which uses high-energy electrons, instead of heat, to initiate cross-linking reactions in polymers). With UV heating, plasma heating, and electron-beam processing, it will be understood that the frequency and wavelength will be material to their successful utilization.
To expedite heat transfer removal during the cooling 30 of the foam product before crushing, an auxiliary cooling device and/or cooling means, such as, by way of example, a high-speed fan, cooling tower, etc., may be utilized.
While the time of the post-cure step in the embodiment of
The utilization of induction heating in the post-cure step 20′ will depend on the presence of electrically conducting material, also known as a susceptor, in the polyurethane foam product. It is contemplated that the susceptor may comprise a structural metal framework about which the foam product is molded.
Where the molded polyurethane product comprises a structural metal framework, one or more of the heating means exemplified above may, depending upon the type of metal, be unsuited to the post-cure step 20 if scorching results. Under such circumstances, a heating means for the post-cure step 20 which avoids scorching is preferred.
Preferably, though not necessarily, the heating means are adapted to the in-line performance of the post-cure step 20 when the disclosed method is performed in a mass-production environment, in order to further enhance the efficiency of the method.
By post-curing the foam product immediately (at zero time after de-molding) or as soon as possible after de-molding the foam product and continuing the heating of the foam product, significant productivity/manufacturing advantages (e.g., cost, etc.) over the prior art may be realized. Therefore, starting the post-curing step as soon as possible enables the foam product to require minimum heating going forward in the process of manufacturing the foam product. For example, approximately 10 seconds from de-mold to the heat source would require approximately 3 minutes of heating; approximately 30 seconds from de-mold to the heat source would require approximately 9 minutes of heating; and approximately 3 minutes from the de-mold to the heat source would require 15 minutes of heating at a higher rate of heating.
As will be understood from the foregoing description, by implementing the post-cure step as soon as possible following demolding, and before crushing, the core temperature of the polyurethane product is kept relatively high and the beneficial further curing of the molded foam product and formation of a denser superficial layer on the polyurethane product are realized in a more energy efficient manner. The superficial layer not only prevents set damage when the foam products are bagged or otherwise packaged for shipment following crushing, it may also facilitate the application of pads or other components on the product with adhesives. Further curing permits greater compression of the foam product during the crush operation, thereby yielding foam products of relatively smaller volume/higher density. Such foam products thus lend themselves to shipment in greater quantities and so improve shipping economy. Furthermore, and depending on the heating means used in the post-cure step, the post-cure step may be rendered relatively shorter and the energy efficiency thereof even further increased as compared to the method of the prior art.
The foregoing description of embodiments of the disclosure has been presented for purposes of illustration and description. It is not intended to be exhaustive or to limit the disclosure to the precise form disclosed, and modifications and variations are possible in light of the above teachings or may be acquired from practice of the innovation. The embodiments are shown and described in order to explain the principals of the innovation and its practical application to enable one skilled in the art to utilize the innovation in various embodiments and with various modifications as are suited to the particular use contemplated.
Although only a few embodiments of the present innovations have been described in detail in this disclosure, those skilled in the art who review this disclosure will readily appreciate that many modifications are possible without materially departing from the novel teachings and advantages of the subject matter recited. Accordingly, all such modifications are intended to be included within the scope of the present innovations. Other substitutions, modifications, changes and omissions may be made in the design, operating conditions and arrangement of the exemplary embodiments without departing from the spirit of the present innovations.
This application claims the benefit of and priority to U.S. Provisional Patent Application No. 61/099,142, filed Sep. 22, 2008, titled: POST-CURE OF MOLDED POLYURETHANE FOAM PRODUCTS, in the name of McEvoy et al. which is incorporated by reference herein.
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/US09/57868 | 9/22/2009 | WO | 00 | 10/26/2009 |
Number | Date | Country | |
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61099142 | Sep 2008 | US |