Patent Document

CROSS-REFERENCE TO RELATED APPLICATIONS  
       [0001]    This application is a continuation-in-part of patent application Ser. No. 09/919,128, entitled “Method for Making Composite Structures,” having Steve Slaughter and John C. Fish as inventors, which application is assigned to same assignee as the present application, and is hereby incorporated by reference. 
     
    
     
       BACKGROUND  
       DESCRIPTION OF RELATED ART  
         [0002]    Generally, vacuum assisted resin transfer molding (VARTM) processes include laying up layers of a material of any unimpregnated fiber and/or fabric on top of a mold. A vacuum bag is placed about the lay-up and sealed to the mold. A peel ply may be placed on top of the lay-up and between the layers and mold surface to insure that the vacuum bag can be removed from the completed part and that the part can be removed from the mold. Resin is introduced into the vacuum bag, while a vacuum is drawn from beneath the lay-up. This causes the resin to flow through the lay-up. Thereafter, the resin flow is terminated and the resin in the assembly is cured. This may require that the resin be heated to curing temperature. To insure even distribution of resin into the lay-up, a resin distribution medium is placed on top of the lay-up, which is designed to cause the resin to evenly distribute there across eliminating resin-starved areas.  
           [0003]    Many types of resin distribution have been proposed. Some inventions describe the use of a perforated film between the lay-up and vacuum bag. Resin is fed from the top through the vacuum bag, through the perforated film and into the lay-up. A spring is located at the periphery of the lay-up, but under the perforated film. The spring is coupled to a vacuum line, thus providing a channel such that resin can be more readily transferred into the lay-up. This reference is of interest for disclosing the use of a perforated film and the use of a spring to provide a channel to the perforated film. However, a special perforated film is required and there is still the problem of insuring that the resin reaches all parts of the perforated film. Other inventions use a wire mesh as a distribution medium in a vacuum assisted molding process. However, a wire mesh may not necessarily be made to conform to a complex contoured part. Furthermore, an open mesh may allow resin to flow too freely into the lay-up prior to the wire mesh becoming filled with resin, thus filling the lay-up near the inlet tube and creating resin starved area further away from the inlet tube.  
           [0004]    Other techniques use channels placed on the lay-up that act as resin distribution paths and become reinforcements on the finished part. This technique is generally not used on parts that do not require reinforcement.  
           [0005]    In general terms, the design of the distribution medium includes two parts: spaced apart lines and an array of raised pillars. In detail, the distribution medium can be a crisscrossed pattern of mono-filaments with raised segments at the intersection of the mono-filaments; a series of spaced apart strips forming a grid structure; or a knitted cloth with raised segments being areas of increased bulk. A central conduit in the form of a spring is positioned over the peel ply and is in communication with the resin inlet port and acts as a central distribution line. Other techniques use the distribution mediums on either side of the lay-up. These distribution mediums are specialized products and may unduly raise fabrication costs.  
           [0006]    A method also exists wherein multiple layers of fibrous reinforcements are assembled into a desired configuration on a support tool, with one of the layers of fibrous reinforcement defining a resin carrier fabric (distribution medium) that extends beyond the periphery of the other layers. The layers of fibrous reinforcements and tool are covered with a flexible layer to form an envelope that encapsulates the fibrous reinforcements. A vacuum source evacuates air from the envelope. Resin is introduced into the envelope and fibrous reinforcements by using a flow path through the one layer used as the resin carrier layer. After the fibrous reinforcements have been impregnated, the resin flow is terminated and the resin is cured. What is really happening is that an additional fibrous layer is added to the fiber reinforcements making up the part that extends there beyond and over flow channels at the periphery of the tool. In one embodiment, this extra fibrous layer is separated from the “part” by a release or peel ply. In a second embodiment, the fibrous layer is integral with the part. This distribution medium is designed for use in a process where the resin is introduced from the peripheral edges of the lay-up.  
           [0007]    A system also exists wherein a pair of preforms with different permeabilities are installed in a mold separated by a separation layer. Different resins are injected into each preform by the vacuum assisted resin transfer method. The key to this process is the use of a separation layer having permeability lower than the permeability of either of the fiber preforms.  
           [0008]    Another invention uses a dual bag within a bag concept. Both bags are sealed to the mold surface with the lay-up within the inner bag. The outer bag incorporates protrusions. A vacuum is first drawn from between the inner and outer bag. This forces the protrusions into the inner bag creating a pattern of channels. A vacuum is then drawn from between the mold surface and inner bag. Resin is then flowed into the lay-up through the channels. Thus the inner bag acts as a resin distribution medium. This apparatus requires a custom vacuum bag, which may raise fabrication costs.  
           [0009]    Other devises in the general area of substance distribution provide systems wherein substance held in a reservoir is released to the surface of an applicator by rupturing a substantially fluid-impervious barrier layer in an interior cavity. The pressure provided to rupture the barrier is provided by manually squeezing and the material is then spread onto a third surface with the applicator. The apparatus does not contemplate a direct flow of material through the ruptured barrier onto the ultimate surface or build-up of pressure through a change in atmospheric pressure in the filling apparatus or through the weight of accumulating material.  
         SUMMARY  
         [0010]    An apparatus for controlling the flow of liquid, gaseous, or particulate solid substances from a substance distribution system and method for making same is provided. In some embodiments, a system for controlling the flow of a substance includes a distribution medium for receiving the substance, and a containment layer adjacent to the distribution medium. The containment layer substantially prevents the substance from flowing until the distribution medium is substantially filled with substance.  
           [0011]    In an alternate embodiment, a method for controlling the flow of a substance includes placing a distribution medium adjacent to a containment layer; introducing the substance into the distribution medium; configuring the containment layer to substantially prevent the substance from flowing from the distribution medium until the substance distribution medium is substantially filled with substance; and reconfiguring the containment layer to allow the substance to flow to an intended destination.  
           [0012]    In still another embodiment, a resin distribution system includes a resin distribution medium for receiving the resin. The resin distribution medium includes a first principle side facing the resin inflow and a second principle side facing the mold surface. A resin containment layer is positioned adjacent to the resin distribution medium. The resin containment layer is configured to substantially prevent the resin from entering the lay-up until the resin distribution medium is substantially filled with resin. 
       
    
    
     BRIEF DESCRIPTION OF THE DRAWINGS  
       [0013]    Embodiments of the present invention may be better understood, and their numerous objects, features, and advantages made apparent to those skilled in the art by referencing the accompanying drawings. The use of the same reference symbols in different drawings indicates similar or identical items.  
         [0014]    [0014]FIG. 1A is a cross-sectional view of an embodiment of a system for distributing layers of one or more substances.  
         [0015]    [0015]FIG. 1B is a cross-sectional view of another embodiment of a system for ting layers of one or more substances.  
         [0016]    [0016]FIG. 2 is an exploded perspective view of the system illustrated in FIG. 1A.  
         [0017]    [0017]FIG. 3 is an enlarged perspective view of an embodiment of the containment layer, wherein the containment layer is made of material that melts. FIG. 4 is an enlarged perspective view of another embodiment of the containment layer, wherein the containment layer is made of a perforated heat shrinkable material.  
         [0018]    [0018]FIG. 5 is an enlarged perspective view of another embodiment of the containment layer, wherein the containment layer is made of a highly perforated or highly embossed, frangible material.  
         [0019]    [0019]FIG. 5A is partial enlarged view of FIG. 5.  
     
    
     DETAILED DESCRIPTION  
       [0020]    Referring to FIGS. 1A and 2, an embodiment of a distribution system  10  for controlling and distributing the flow of liquid, gaseous, and particulate solid substances is shown including distribution medium  22  and containment layer  24 . Distribution medium  22  includes a first principle side facing an inflow of substance and a second principle side facing containment layer  24 . Containment layer  24  is designed to substantially prevent substance from flowing to an intended destination until distribution medium  22  is substantially filled with substance.  
         [0021]    In some embodiments, distribution system  10  can be utilized to fabricate composite materials. System  10  includes mold  12  and mold surface  14 . For purposes of illustration a flat mold surface  14  is shown, however, mold surface  14  can be curved, can include a moving conveyor belt, or any other surface for evenly distributing resin over one or more layers of material  16 A through  16 D to form lay-up  16 . In some embodiments, peel ply layers  18 A,  18 B can be positioned adjacent one or both of the outer sides of lay-up  16 . Peel ply layers  18 A,  18 B are typically made of a porous material to allow resin to easily pass through without bonding to mold surface  14  or containment layer  24  as resin-impregnated lay-up  16  equilibrates into its final state. In other embodiments, peel ply layers  18 A,  18 B may not be included.  
         [0022]    In some embodiments, outer sheet  26 , also referred to as a vacuum bag, includes inlet port  28  positioned adjacent distribution system  10  and sealed at its marginal edges  30  to mold surface  14  by sealant tape  32  or other suitable means to form chamber  34 . An example of a sealant tape  32  that can be utilized is Tacky Tape™ manufactured by Schnee-Moorehead, Irving, Tex. Vacuum outlet port  35  can be installed between mold surface  14  and marginal edge  30  of outer sheet  26  for drawing a vacuum in chamber  34 .  
         [0023]    In some embodiments, substance enters inlet port  28 , while a vacuum is drawn from outlet port  35 . The vacuum causes outer sheet  26  to collapse down around distribution medium  22 . Without distribution medium  22 , it would be difficult to evenly distribute resin over lay-up  16 , and substance starved areas or even voids could be created in the cured lay-up  16 . With substance distribution medium  22 , however, resin can flow evenly lay-up  16 , greatly reducing the chance of forming voids and the like in the final product.  
         [0024]    [0024]FIG. 1B shows another embodiment of distribution system  10  that include vacuum outlet ports  35 ′ in mold  12 . Outlet ports  35 ′ can be positioned in one or more locations in mold  12 . Portions of outlet ports  35 ′ extending from mold  12  can be fitted to a vacuum source to draw outer sheet  26  to collapse around distribution medium  22  and lay-up  16 . In some embodiments, one or more outlet ports  35 ′ are positioned around the periphery of lay-up  16  in areas where there are likely to be gaps between lay-up and outer sheet  26 . As many inlet ports  28  and outlet ports  35 ′ as necessary can be utilized, thereby enabling distribution system  10  to be utilized to fabricate components in a variety of shapes and sizes. Further, a combination of one or more outlet ports  35  (FIG. 1A) and outlet ports  35 ′ can be utilized in the same distribution system  10 .  
         [0025]    Lay-up  16  can comprise one or more layers of material, such as woven fiberglass, graphite or other composite reinforcement material. Peel plies  18 A and  18 B can be made of a material such as coated fiberglass, which is porous to resin so that resin can easily pass through without bonding to mold surface  14  or containment layer  24  as the resin cures. A suitable peel ply material is Release Ease 234TFP, manufactured by Airtech Products, Incorporated, Huntington Beach, Calif.  
         [0026]    In some embodiments of distribution system  10 , a material suitable for use as outer sheet  26  is impregnated Nylon, which can be obtained from numerous suppliers such as the previously mentioned Airtech Products. When the substance being distributed is resin, distribution medium  22  can be comprised of any suitable material. For example, a knitted mono-filament UV stabilized high density polyethylene can used as distribution medium  22 , such as commercially available SolarGuard™ manufactured by Roxford Fordell Company, Greenville, S.C. Anther suitable product for distribution medium  22  is Colbond 7004 manufactured by Colbond, Incorporated, Enka, N.C. Colbond 7004 is a random orientated, heat fused mono-filament material.  
         [0027]    Referring to FIGS. 1A and 3, in other embodiments, temperature sensitive containment layer  24 A has a melting point such that containment layer  24 A dissolves or melts after substance is at least partially distributed in distribution medium  22 . Once containment layer  24 A melts, the substance can flow to its intended destination. Distribution system  10  can include means for applying heat to temperature sensitive containment layer  24 A. Heating can be done either directly by means such as raising the ambient temperature, blowing heated air, conducting electricity through a metallic frame, chemical reaction, or other suitable means. Heat can also be applied to substance containment layer  24 A by heating the substance before, during, or after the substance contacts containment layer  24 A. Other materials that dissolve can be used for containment layer  24 A in addition to, or instead of, containment layers  24 A that dissolve when heated.  
         [0028]    In some embodiments, a temperature sensitive containment layer  24 A includes a meltable substance layer  36  and porous veil material  37 . An example of a suitable material for temperature sensitive containment layer  24 A for use with resin is Blue Max Tak Tu on Reemay (a polyester non-woven veil), manufactured by The Blue Max Company, Anaheim, Calif. The Blue Max Tak Tu material is a low temperature melting resin  36  that is applied to a porous veil material  37 .  
         [0029]    Referring to FIG. 4, another embodiment of containment layer  24 B includes a plurality of holes  40  in a heat shrinkable material. Holes  40  are a size such that substance will not readily flow there through at ambient temperatures. Upon heating, the material of containment layer  24 B will shrink, causing holes  40  to increase in size, shown in dotted lines and indicated by numeral  40 ′, allowing substance to flow from substance distribution medium  22 . A suitable heat shrinkable material for use with resin substances includes Intercept Shrink film manufactured by FPM, Incorporated, Brownstone, Me.  
         [0030]    Referring to FIGS. 1, 5 and  5 A, in some embodiments, containment layer  24 C is a porous film  42  includes a plurality of holes or very closely spaced perforations  44 . The size of the perforations is selected to prevent or greatly reduce substance flow through substance containment layer  24 C. Holes  44  having a size such that substance will not flow there through when a vacuum is drawn to outlet port  35  at a first rate and will flow there through when a vacuum is drawn from outlet port  35  at a higher second rate. Calculating the size of holes  44  in substance containment layer  24 C can be accomplished as follows. For a layer of substance above substance containment layer  24 C, the hydrostatic pressure at the layer is by the equation:  
         PH=ρhg  
         [0031]    Where: ρ is the density of the substance,  
         [0032]    h is the depth (height) of the substance, and  
         [0033]    g is the gravitational constant  
         [0034]    The “excess pressure” developed by the surface tension of the substance and the openings (perforations) in substance containment layer  24 C can be expressed as:  
           PE= 2  T/d    
         [0035]    where T is the surface tension of the substance and  
         [0036]    d is the perforation diameter (assumes circular perforation)  
         [0037]    The governing equation for substance containment sets the hydrostatic pressure equal to the excess pressure:  
           ρhg= 2  T/d    
         [0038]    Properties of a typical resin, such as Derakane  411  C- 50  resin by Dow Chemical Company, Midland, Mich. are:  
         ρ=1265 kg/ m 3  
           T= 0.032 Newtons/meter  
         [0039]    The maximum perforation size that overcomes the hydrostatic pressure is then:  
           d= 2  T /((hg)=2(0.032)/(1265 ×h× 9.8)  
           d= 0.000005163 /h  meters.  
         [0040]    Using a typical thickness of a substance distribution medium, where the substance is resin, the substance height becomes 0.00635 m (0.25 in) and the maximum perforation size is:  
           d   max =8.13×10 −4  meters (0.032 in).  
         [0041]    For thicker substance distribution mediums, the maximum perforation size will decrease. Perforations larger than this maximum value may not contain the substance during infusion. Similarly, the minimum perforation size can be estimated by equating the excess pressure to the sum of the hydrostatic pressure and the vacuum pressure in the bagged assembly:  
           ρhg+PV =2  T/d    
         [0042]    where PV will be on the order of one atmosphere. At sea level, PV is approximately 100 kiloPascals (kPa) and dominates the left side of the equation above. The minimum perforation size is then estimated by:  
           d   min =2  T/PV= 2(0.032)/(100×10 3 )  
           d   min =6.4×10 −7  meters=2.5×10 −5  inches  
         [0043]    Perforations smaller than this minimum value may not permit substance to pass through the substance containment layer  24 C under vacuum pressure. The substance containment layer  24 C perforation size is then bounded by:  
         [0044]    2.5×10 −5  inch&lt; d&lt; 0.032 inch  
         [0045]    A suitable material for containment layer  24 C for use with resin substances is Easy Gardner Tree Wrap having round holes with a 0.015 inch diameter or Easy Gardner Weed Block with square holes of a similar size. Both of these materials are manufactured by Easy Gardner, Incorporated, Waco, Tex. This method of calculation can also be used to design the perforations for temperature sensitive containment layers  24 B (FIG. 4).  
         [0046]    In still other embodiments of distribution system  10  (FIG. 1), containment layer  24  can be comprised of a layer of perforated material including a plurality of embossed holes. Sufficient pressure can be applied to containment layer  24  to cause the perforations to release and allow the substance to flow once it is distributed in distribution layer  22 . Distribution system  10  can be modified to include means for applying pressure to the substance in distribution layer  24  to induce tearing of the holes in containment layer  24 . Such means include physically applying pressure to the substance, applying vacuum pressure, such as by drawing a vacuum on chamber  34 , or other suitable means. Containment layer  24  can also be configured to tear upon application of sufficient weight of the substance. Distribution medium  22  can be configured to allow sufficient substance to accumulate to apply the required weight to containment layer  24 .  
         [0047]    Other embodiments include containment layer  24  fabricated from materials whose porosity properties change under application of different rates of vacuum, different rates of atmospheric pressure, and varying heat. Substances that can be distributed with distribution system  10  include any amounts of liquid, solid, and/or gaseous substances. Distribution layer  22  can be fabricated from any suitable material or combination of materials, and can include grids or other suitable openings to distribute the substance.  
         [0048]    Various embodiments can include two or more distribution systems  10  that are configured to allow substances to be combined automatically at desired pre-selected time intervals, or upon application of means to at least partially remove containment layer  24  to allow the substance to flow toward its intended destination. For example, containment layer  24  in one distribution system  10  can be configured to release the substance when activated by an operator. The distributed substance can flow onto and chemically react with another substance in a second distribution system  10 . Containment layer  24  can be configured to release the combined substances either manually or automatically once the chemical reaction is complete.  
         [0049]    Distribution medium  22  can be configured to accumulate all or a portion of the substance to be distributed by increasing the depth of the grid, including side walls around the perimeter of distribution medium  22 , or other suitable structure. Further, distribution system  10  can be oriented to allow substance to flow in any desired direction. Additionally, the substance can be forced to flow in any desired direction through the use pressure, pumps, or other suitable mechanism for inducing flow through distribution medium  22 .  
         [0050]    While the present disclosure describes various embodiments, these embodiments are to be understood as illustrative and do not limit the claim scope. Many variations, modifications, additions and improvements of the described embodiments are possible. For example, those having ordinary skill in the art will readily implement the structures and methods disclosed herein, and will understand that any process parameters, materials, and dimensions are given by way of example only. The parameters, materials, and dimensions can be varied to achieve the desired structure as well as modifications, which are within the scope of the claims. Variations and modifications of the embodiments disclosed herein may also be made while remaining within the scope of the following claims. In the claims, unless otherwise indicated the article “a” is to refer to “one or more than one”.

Technology Category: 7