Abstract:
The above objective are accomplished by providing a filter medium for use in manufacturing of hydraulic fluid and air filters comprising: an upstream layer comprised of nonwoven fiber having a denier between about 5.0 and 7.0 and a weight of between about 3.0 and 5.0 ounces a scrim and a cap layer comprising a fiber having a denier between about 0.1 and 5.0 denier and a weight between about 2.0 and 4.0 ounces carried by said upstream layer and disposed downstream from said upstream layer. The upstream layer, scrim and cap layer can have a weight of about 4.0 ounces, 2.0 ounces and 3.0 ounces respectively. A downstream layer can be disposed between said upstream layer and said cap layer.

Description:
FIELD OF THE INVENTION 
       [0001]    This invention is directed to a manufacturing part for a filter used to remove particles from a stream. More specifically, the filter media is a high efficiency and durable filter media for removing particles from a hydraulic fluid stream. 
       BACKGROUND 
       [0002]    During the development of many machines, the use of fluids is an integral part of the operation of the machine. For example, many machines rely upon a power source and a transmission system to provide controlled application of power. Transmissions can be a set of cooperating gears for speed and torque conversions from a power source (such as a rotating power source) to another device (such as a drive axle or propeller). In operation, the transmission uses transmission fluid to provide hydraulic power to move the gears from one location to another to perform the power redirection, and speed and torque conversions. 
         [0003]    One of the operational realities with transmission fluid is that transmissions can create a high temperature environment. The internal friction can increase the operational temperature to over 250° F., significantly above the normal operating temperature of about 175° F. At temperatures higher than the normal operating temperature, the transmission fluid can oxidize which can destroy the lubricating properties and can result in contaminates entering the fluid stream. High operating temperatures cause seals to breakdown which can result in dirt and other contaminates entering the fluid. Further, the normal operation can cause contaminates to become present in the fluid. 
         [0004]    Transmission filters are used to help remove these contaminants from the transmission fluid itself. The filter can hold metal particles, debris and other foreign material to prevent the material from continued circulation in the fluid stream. Characteristics of filter media include the ability to remove a certain percentage of particulate of a certain size, durability, porosity, high temperature operations and the like. It can be desirable to have various layers of filter material which operate to provide certain physical characteristic. Further, multiple layers can provide for mechanical stability of the filter medium itself. 
         [0005]    There are several types of filter media that have been previously attempted for use with hydraulic fluid filtration, and include air-laid and wet-laid processing which can provide filtration for both air and fluid streams. However, most of these materials, especially non-woven material, can suffer from a lack of mechanical strength and shortened operational life when in contact with a fluid, including transmission fluids. Further, pressures from the fluid stream can exceed the burst threshold of these materials rendering the medium useless in such environments if the filter material has a structural failure (e.g. bursts). 
         [0006]    There have been several attempts to produce a non-woven filter media with sufficient physical properties to be used in filter media. For example, U.S. Pat. No. 6,695,148 is directed to a transmission fluid filter felt. However, these attempts fail to provide a filter media with sufficient particulate removal, strength and filtration life using a layered arrangement of materials with different densities to provide the desired filtering characteristics. Additional attempts to provide for a high strength, high capacity filter media include U.S. Pat. Nos. 4,161,422; 4,274,914; 4,713,285; 4,765,812; 5,068,141 and 5,283,106. 
         [0007]    It would be advantageous for the manufacturing of hydraulic filters to have a filter media that was a high strength, high capacity filter without the limitations existing in the prior art such as lack of burst strength when used in wet, high pressure fluid streams and air streams. 
         [0008]    Therefore, it is an object of the current invention to provide a high strength filter medium that can be used in the filtration of fluids capable of operating in a high pressure, high temperature environment. 
         [0009]    It is another object of the present invention to provide for a layered filter material for use in a filter medium having different fiber types carried by a scrim to provide mechanical support for the filter material. 
       SUMMARY OF THE INVENTION 
       [0010]    The above objectives are accomplished by providing a filter medium for use in manufacturing of hydraulic fluid filters comprising: an upstream layer of non-woven fiber wherein the fibers of the upstream layer having a thickness greater than about 50% of the overall thickness of the filter media, a weight in the range of 20% to 60% of the total weight of the filter media and an average fiber diameter between about 10 to 40 microns; a scrim disposed adjacent to the upstream layer, arranged downstream from the upstream layer, the scrim being between about 10% to 40% of the total weight of the filter medium; and a cap layer of non-woven fiber carried by the scrim disposed downstream of the upstream layers having a denier between about 0.1 to 5, about 10% to 30% of the total weight of the filter medium and a fiber diameter between about 1 to 21 microns. 
         [0011]    The filter medium can also include a downstream layer disposed between the scrim and the cap layer having about 10% to 50% of the total weight of the filter medium and an average fiber diameter between about 10 to 40 microns and between about 1 to 15 denier. The upstream layer, downstream layer, scrim and cap layer can include material selected from the group consisting of: polyethylene, polypropylene, nylon, polyester, acrylic, PPS, meta-aramid, para-aramid, PTFE, glass and any combination thereof. 
         [0012]    The scrim should be selected from the group consisting of: a woven scrim, a leno scrim, mock leno scrim, locking leno scrim, a knit scrim, made from filament or spun yarn and any combination thereof. 
     
    
     
       DESCRIPTION OF THE DRAWINGS 
         [0013]    The following description of the invention will be better understood by reference to the following drawings that are incorporated and made part of the written specification: 
           [0014]      FIG. 1  is a perspective view of aspects of the invention; 
           [0015]      FIG. 2  is a perspective view of aspects of the invention; 
           [0016]      FIG. 3  is a perspective view of aspects of the invention; 
           [0017]      FIG. 4  is a side view of aspects of the invention; and 
           [0018]      FIG. 5  is test results displayed in graphical format related to the present invention. 
       
    
    
     DESCRIPTION OF THE INVENTION 
       [0019]    Referring to  FIG. 1 , the invention will be discussed in more detail. A fluid stream, i.e. hydraulic fluid such as transmission fluid, is flowing in a direction shown as  10 . The portion of the stream  12  that is upstream to the filter medium  14  can include contaminates  16 . The filter medium can trap these contaminates thereby removing them from the portion of the stream  18  that is downstream the filter medium thereby removing these contaminates from recirculating. The stream can be aqueous or non-aqueous. The stream can be hydraulic fluid such as transmission fluid, oil and the like. In one embodiment, the filter medium is suited for filtering transmission fluid such as used with the power train of a vehicle. 
         [0020]    Further, the filter medium can be arranged in layers which include an upstream layer  20 , a scrim  22  and a cap layer  24 . In one embodiment, a downstream layer  26  can be included and disposed between the scrim and the cap layer. 
         [0021]    The various layers can be seen in  FIGS. 2 and 3 . The upstream layer can be a non-woven fiber with a denier of between about 1 and 15 and have an open porous arrangement. In one embodiment, the upstream layer has a thickness between about 50% to 70% of the overall thickness of the filter material  14 . For example, if the thickness of the filter material  14  is 10 mm, the thickness of the upstream layer would be between about 5 mm and 7 mm. In one embodiment, the denier of the upstream layer is between about 1 to 15. In one embodiment, the upstream layer is between about 20% and 60% of the overall weight of the filter medium. In one embodiment, the upstream layer is between about 10 to 40 microns. The upstream layer can be made from material including polyethylene, polypropylene, nylon, polyester, acrylic, PPS, meta-aramid, para-aramid, PTFE, glass and any combination thereof. 
         [0022]    The cap layer can be made from a non-woven fiber and disposed adjacent to the scrim. In one embodiment, the scrim supports the upstream layer. In one embodiment, the cap layer has an average fiber diameter of between about 1 to 21 microns. In one embodiment, the cap layer has a fiber of between about 0.1 and 5.0 denier. In one embodiment, the cap layer is between about 10% and 30% of the total weight of the filter medium. In one embodiment, the cap layer is between about 5% and 25% of the overall thickness of the filter medium. 
         [0023]    The cap layer can also be made from a light weight nonwoven material and need not necessarily be made from a needle felt. The cap layer can be made from or include any of the following: hydroentangled nonwoven using staple splitable fiber such as a 60 gsm non-woven with 2.25 denier 16 pie PET/PA fiber; spunbond hydroentangled nonwoven using splitable continuous filaments such as distributed under the trademark Evolon; thermal bonded nonwoven such as provided by the company Bondex, Inc.; spubond nonwoven; melt blown nonwoven; a combination of layers comprising a combination of spunbond (S) and melt blown (M) fabrics such as a SMS or SM combinations; wetlaid; wetlaid containing glass fibers; laminate combination of any of the proceeding materials. The cap layer can be attached to the upstream layer through methods taken from the group comprising: needling, heat lamination, chemical lamination such as spaced adhesives, resins, epoxy and any combination of these. 
         [0024]    Evolon is a fabric which is manufactured by Freudenberg and includes a microfilament fabric with a dense compact fiber structure. It has good textile and mechanical properties, and is soft, drapable and lightweight with good strength. It is has good barrier and filtration properties, and is very absorbent with quick dry properties and is breathable. 
         [0025]    In one embodiment, the scrim is disposed adjacent to said cap layer and upstream from said cap layer. The scrim can be 10% to 40% of the total weight of the filter medium. The scrim can be between about 2% and 10% of the total thickness of the filter medium. The scrim can be a woven scrim, a leno scrim, a mock leno scrim, a locking lens scrim, a knit scrim, made from filaments or spun yarn and any combination thereof. The scrim can be a nonwoven material and can include: polyethylene, polypropylene, nylon, polyester, acrylic, PPS, meta-aramid, para-aramid, PTFE, glass and any combination thereof. In the manufacturer of the filter medium, referring to  FIG. 4 , an upstream layer  20  can be placed in a needle punch machine or carding machine with a scrim  22   a  placed along the outside of upstream layer  20 . When the needles  30  move in the direction  32 , the scrim can be forced into the upstream layer and shown as  22  disposed within the upstream layer. The scrim begins to dispose at a location shown as  22   a  and is forced into the interior of the upstream layer shown as  22 . This defines a downstream layer  26  adjacent to cap layer  24 . Further, the needle punching process causes the cap layer, downstream layer, scrim and upstream layer to form a laminated filter medium. 
         [0026]    The downstream layer can be a nonwoven material and can include: polyethylene, polypropylene, nylon, polyester, acrylic, PPS, meta-aramid, para-aramid, PTFE, glass and any combination thereof. In one embodiment, the downstream layer is between about 10% and 30% of the total weight of the filter medium. The downstream layer can have an average fiber diameter of between about 10 to 40 microns. The downstream layer can have fiber of between about 1 and 15 denier. The downstream layer can be between about 10% and 40% of the overall thickness of the filter medium. 
         [0027]    In one embodiment, the upstream layer and the downstream layer combined have about 50% to 80% of the thickness of the overall thickness of the filter medium. 
         [0028]    The following Table 1 illustrates some of the properties of on embodiment and its various aspects: 
         [0000]    
       
         
               
               
               
               
               
             
           
               
                 TABLE 1 
               
               
                   
               
               
                   
                   
                   
                   
                 Fiber 
               
               
                   
                 Thickness vs. 
                   
                 Weight vs. 
                 Diameter 
               
               
                 Layer 
                 Overall Thickness 
                 Denier 
                 Overall Weight 
                 (microns) 
               
               
                   
               
             
             
               
                 Upstream 
                 50% to 70% 
                 1 to 15 
                 20% to 60% 
                 10 to 40 
               
               
                 Cap 
                  5% to 25% 
                 0.1 to 5   
                 10% to 30% 
                  1 to 21 
               
               
                 Scrim 
                 10% to 40% 
                   
                 10% to 40% 
               
               
                 Downstream 
                 20% to 40% 
                 1 to 15 
                 10% to 50% 
                 10 to 40 
               
               
                 Upstream +− 
                 50% to 70% 
                   
                 20% to 60% 
               
               
                 Downstream 
               
               
                   
               
             
          
         
       
     
         [0029]    The filter medium of the present invention can have a particle removal rate as shown in the following Table 2: 
         [0000]    
       
         
               
               
               
             
               
               
               
             
               
               
               
             
           
               
                   
                 TABLE 2 
               
             
             
               
                   
                   
               
               
                   
                 Efficiency Percentage (%) 
                   
               
             
          
           
               
                 Particle Size (μm) 
                 @ 132 cfm 
                 @ 149 cfm 
               
               
                   
               
             
          
           
               
                 30.0 
                 58.76 
                 54.64 
               
               
                 40.0 
                 83.04 
                 79.65 
               
               
                 50.0 
                 92.96 
                 91.08 
               
               
                 60.0 
                 97.44 
                 96.03 
               
               
                 70.0 
                 98.51 
                 97.33 
               
               
                 80.0 
                 99.21 
                 98.92 
               
               
                 90.0 
                 99.23 
                 99.22 
               
               
                 100.0 
                 99.35 
                 100.00 
               
               
                   
               
             
          
         
       
     
         [0030]    In obtaining the results shown in Table 2, the filter media in a six inch disk exhibited a retention capacity of 5.27 grams at 132 cfm and 5.48 grams at 162 cfm. The life of the filter media was 25.10 minutes for 132 cfm and 26.12 minutes for 162 cfm. 
         [0031]    In another test for flow vs. pressure drop, a six inch disk in a pump filled with automatic transmission fluid (Dexro VI ATF) was used. Dexro VI is an automatic transmission fluid (ATF) that is distributed by the Exxon Moblie Corporation, and is a high performance, synthetic blend ATF made from severely hydrotreated and hydrocracked base oil such as petroleum. The base oil may be a mixture of the following CAS#s: 8042-47-5, 64742-46-7, 64742-52-5, 64742-54-7, 72623-84-8, 72623-85-9, 72623-86-0, 72623-87-1, 178603-64-0, 178603-65-1, 178603-66-2, or 445411-73-4 and assigned by the Chemical Abstracts Service (CAS). 
         [0032]    The fluid was pulled through the filter media by a downstream pump and the pressure drop measured over a range of flow rates with the results shown in Table 3. This test is designed to measure the media&#39;s ability to flow oil at a cool and ambient temperature. This test method is referred to as the Filtertek TM536 (24° C.). 
         [0000]    
       
         
               
               
               
             
               
               
               
             
               
               
               
             
           
               
                   
                 TABLE 3 
               
             
             
               
                   
                   
               
               
                   
                 Pressure Drop (″Hg) @ 24° C. 
                   
               
             
          
           
               
                 Flow Rate (lpm) 
                 @ 141 cfm 
                 @ 162 cfm 
               
               
                   
               
             
          
           
               
                 3.5 
                 1.20 
                 1.15 
               
               
                 6.9 
                 1.85 
                 1.65 
               
               
                 10.3 
                 2.55 
                 2.35 
               
               
                 13.7 
                 3.40 
                 2.90 
               
               
                 17.1 
                 4.20 
                 3.66 
               
               
                 20.4 
                 5.00 
                 4.20 
               
               
                 23.8 
                 5.80 
                 4.90 
               
               
                 27.2 
                 6.60 
                 5.75 
               
               
                 30.6 
                 7.70 
                 6.50 
               
               
                 34.0 
                 8.65 
                 7.20 
               
               
                 37.4 
                 9.50 
                 7.90 
               
               
                 40.7 
                 10.40 
                 8.70 
               
               
                   
               
             
          
         
       
     
         [0033]    The invention has also been tested for chemical compatibility. This test measures the effects of prolonged exposure to hot ATF. Using a 2 inch by 6 inch filter media section, the media is exposed to ATF at 302° F. for 24 to 168 hours. Every 24 hours, 4 strips are removed and are pulled starting with pneumatic grips 2 inches apart. The pull rate is 1.00″ per minute. This test is referred to as the TM 659 test. In one embodiment, an Instrom 4201 gauge is used to obtain measurements. The results are shown in graphical form in  FIG. 5 . 
         [0034]    In one embodiment, the upstream layer is a 3.5 to 4.5 ounce layer made from about 6 denier fibers. In one embodiment, the upstream layer is 100% 6 denier fiber. The scrim is a filament polyester scrim having a fiber weight of between 1 and 3 ounces. The cap layer can be a 2 to 4 ounce blend including about 75% of about 1.5 denier fiber and about 25% of 2.25 denier fiber. In one embodiment, the upstream layer is 4 ounces, the scrim is 2 ounces and the cap is 3 ounces. In the event that the layers are treated with a liquid bath, the bath can add 0.5 to 1.5 ounces of chemicals to the layers. In one embodiment, the chemicals are 0.9% by weight. The upstream layer can include fiber having between about 1 denier to about 15 denier and the cap layer can include fiber having between about 1.0 denier to about 5.0 denier. This embodiment provides air permeability of about 150 cfm. Once the upstream layer and cap have been manufactured into a single layered material, the material is treated with a chemical bath that can include: a phenol formaldehyde resin, a polymer having high molecular weight, acrylic acid chains in a liquid state, ammonia and water. The acrylic acid chains can be cross-linked. In one embodiment, the chemical bath comprises 7% to 30% by weight of a phenol formaldehyde resin, 2% to 9% polymer, 0% to 1% ammonia and 40% to 91% water. In one embodiment, the polymer is available under the trademark Carbopolceloffered by Lubrizol. In one embodiment, the phenol formaldehyde is offered under the brand designation 510 D 50 by Georgia-Pacific. 
         [0035]    It is understood that the above descriptions and illustrations are intended to be illustrative and not restrictive. Many embodiments as well as many applications besides the examples provided will be apparent to those of skill in the art upon reading the above description. The scope of the invention should, therefore, be determined not with reference to the above description, but should instead be determined with reference to the appended claims, along with the full scope of equivalents to which such claims are entitled. The disclosures of all articles and references, including patent applications and publications, are incorporated by reference for all purposes. The omission in the following claims of any aspect of subject matter that is disclosed herein is not a disclaimer of such subject matter, nor should it be regarded that the inventor did not consider such subject matter to be part of the disclosed inventive subject matter.