SYNTHETIC FABRIC HAVING SLIP RESISTANT PROPERTIES AND METHOD OF MAKING SAME
20230096881 · 2023-03-30
Inventors
Cpc classification
B32B38/004
PERFORMING OPERATIONS; TRANSPORTING
B29C59/025
PERFORMING OPERATIONS; TRANSPORTING
B32B27/12
PERFORMING OPERATIONS; TRANSPORTING
E04D12/002
FIXED CONSTRUCTIONS
B32B2305/20
PERFORMING OPERATIONS; TRANSPORTING
B32B5/028
PERFORMING OPERATIONS; TRANSPORTING
B32B37/20
PERFORMING OPERATIONS; TRANSPORTING
B32B11/10
PERFORMING OPERATIONS; TRANSPORTING
B32B37/15
PERFORMING OPERATIONS; TRANSPORTING
International classification
E04D12/00
FIXED CONSTRUCTIONS
B29C59/02
PERFORMING OPERATIONS; TRANSPORTING
B32B11/10
PERFORMING OPERATIONS; TRANSPORTING
B32B27/12
PERFORMING OPERATIONS; TRANSPORTING
B32B37/15
PERFORMING OPERATIONS; TRANSPORTING
B32B38/00
PERFORMING OPERATIONS; TRANSPORTING
B32B5/02
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A synthetic nonwoven fabric having bonded fibers forming channels surrounding unbonded fibers forming raised slip resistant spots. The fabric is made by extruding hot polymer through a spinneret die onto a moving belt to form a sheet of random fibers, which sheet undergoes a calendering process between a pair of heated rollers, one of which rollers having a plurality of cavities defined in its surface. The resulting fabric can be laminated and otherwise combined with other layers as desired to provide an end product having good slip resistant properties.
Claims
1.-20. (canceled)
21. A roofing membrane comprising: a calendered sheet; a resin lamination layer; and a scrim layer; wherein the calendered sheet comprises a polymer resin; wherein the calendered sheet comprises: a) a plurality of elevated portions of random unbonded fibers, and b) bonded fibers in channels between the plurality of elevated portions; wherein the resin lamination layer: a) is between the calendered sheet and scrim layer, and b) extends at least from a first end of the calendered sheet to a second end of the calendered sheet opposite the first end, and wherein the scrim layer extends at least from the first end of the calendered sheet to the second end of the calendered sheet
22. The roofing membrane of claim 21, wherein the polymer resin comprises polypropylene, polyethylene, polyester, or nylon.
23. The roofing membrane of claim 21, wherein the scrim layer comprises a woven material.
24. The roofing membrane of claim 23, wherein the woven material comprises at least one of polyethylene or polypropylene.
25. The roofing membrane of claim 21, wherein the resin lamination layer comprises a polymer.
26. The roofing membrane of claim 21, wherein the resin lamination layer comprises a combination of polyethylene and polypropylene.
27. The roofing membrane of claim 21, wherein the resin lamination layer comprises: between 5% and 30% low-density polyethylene, and polypropylene.
28. The roofing membrane of claim 21, further comprising: a resin coating layer, wherein the resin coating layer is on the scrim layer, and extends at least from the first end of the calendered sheet to the second end of the calendered sheet.
29. The roofing membrane of claim 28, wherein the resin coating layer comprises a film.
30. The roofing membrane of claim 29, wherein the film comprises at least one of polyethylene and polypropylene.
31. A system, comprising: a roof deck; and a roofing membrane installed above the roof deck, wherein the roofing membrane comprises: a calendered sheet; a resin lamination layer; and a scrim layer; and wherein the calendered sheet comprises a polymer resin; wherein the calendered sheet comprises: a) a plurality of elevated portions of random unbonded fibers, and b) bonded fibers in channels between the plurality of elevated portions; wherein the resin lamination layer: a) is between the calendered sheet and scrim layer, and b) extends at least from a first end of the calendered sheet to a second end of the calendered sheet opposite the first end, and wherein the scrim layer extends at least from the first end of the calendered sheet to the second end of the calendered sheet.
32. The system of claim 31, wherein the polymer resin comprises polypropylene, polyethylene, polyester, or nylon.
33. The system of claim 31, wherein the scrim layer comprises a woven material.
34. The system of claim 33, wherein the woven material comprises at least one of polyethylene or polypropylene.
35. The system of claim 31, wherein the resin lamination layer comprises a polymer.
36. The system of claim 31, wherein the resin lamination layer comprises: between 5% and 30% low-density polyethylene, and polypropylene.
37. The system of claim 31, wherein the roofing membrane further comprises: a resin coating layer, wherein the resin coating layer is on the scrim layer, and extends at least from the first end of the calendered sheet to the second end of the calendered sheet.
38. The system of claim 37, wherein the resin coating layer comprises a film.
39. The system of claim 38, wherein the film comprises at least one of polyethylene and polypropylene.
40. The system of claim 31, further comprising: a roofing shingle installed above the roofing membrane.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0032] These and other features of the invention will become more apparent from the following description in which reference is made to the appended drawings and wherein:
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[0044]
DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0045] Nonwoven fabrics are commonly used in the manufacture of products, including roofing underlays. A regular nonwoven fabric is made by extruding a heated thermoplastic resin through a spinneret die unto a moving surface. The term “nonwoven” refers to the individual fibers which are randomly interlaid and entangled to form a web including a multitude of randomly distributed fibers. The web of fibers can be bonded to each other or unbonded. Known methods for bonding include thermal calendering, air bonding, and passing the web through a saturated steam chamber at an elevated pressure. Bonding by thermal calendering is done by “spot bonding”, where one calender roll has a plurality of fine points which apply heat and pressure to the web to bond spots.
[0046] The present invention employs a novel calendering process to produce a spunbond nonwoven fabric 16 as shown in
[0047] The elevated high spots in combination with the channels provide good traction even in wet conditions. Foreign material such as debris, dust, water and snow is diverted in the channels, leaving the high spots to provide a gripping surface.
[0048] Production of the nonwoven high spot fabric is shown in
[0049] An example of suitable dimensions for a cavity roller are shown in
[0050] As a further example, the oval “high spots” 120 shown in
[0051] Product thickness must be sufficient to create the key requirements of the product:
[0052] The high spots must be suitably elevated relative to the channels, in the case of this example, preferably greater than 0.5 mm, and most specifically between 0.7 mm and 1 mm.
[0053] The top of the high spot must have non-bonded fibers to grip a roofer's shoes.
[0054] Proper width of the channels, preferably greater than 0.5 mm.
[0055] The calendering process is carefully controlled to ensure that the top surface of the high spots 20 remains a rough surface comprised of loose, unbonded fibers which create a slip resistant surface. While the presence of a high spot with bonded fibers does provide some traction, it is the presence of the unbonded fibers that provides additional traction.
[0056] When commencing production, the sheet of fibers is hand fed from the moving belt 34 to the rollers 36 and 38. Once fed through the nip (the gap between the rollers 36 and 38) and fed around the remaining rollers, the process can proceed uninterrupted. Both rollers 36 and 38 are heated, however need not be heated to the same temperature. The temperature of the rollers is important in the overall process and can be adjusted depending on the materials used and the thickness of the product. The rollers must be hot enough to ensure that the channel area is fused well, but not overheated. If overheated, the material will burn and lose its strength. For the product illustrated in
[0057] After passing between the calendering cavity roll 36 and the standard roll 38, the fabric sheet continues along a series of rollers and is wound in a Jumbo Roll form. When it first exits the calender rolls, the sheet is air cooled by adjusting the line speed to give the non-woven enough time to cool down slightly then it is run over water cooled stainless steel rollers to ensure it is cooled and takes its final shape before winding it to form the Jumbo roll.
[0058] In order to provide a waterproofing layer, the nonwoven high spot fabric must be bonded with a waterproofing membrane. These could form a number of different combinations. For example, the high spot nonwoven can be laminated to a regular nonwoven, the lamination layer forming a waterproof barrier as discussed in more detail below. Such a combination is illustrated in
[0059] The lamination process consists of taking the high spot nonwoven and combining it with another membrane material.
[0060] As discussed in more detail below, in the lamination process, temperature, pressure and cooling is controlled to achieve the best physical properties of the product and to ensure that the grip (“high”) spot pattern remains effective. The product is also trimmed to the desired width prior to being wound on the paper core.
[0061] The product may also undergo further processing, such as a printing process in order to place product logo and other necessary information on it. Once processing has been completed, the product goes through “rewinding”, where the Jumbo rolls are rewound into small 250 foot rolls and then packaged onto skids for shipping.
[0062] Additional manufacturing details are set out below.
Manufacturing Process
[0063] During production, the major focus was put on developing the “high spot” nonwoven manufacturing process, followed by the lamination process. Various trials were conducted as set out below.
Trial 1—Top Layer Nonwoven Thickness vs. Weight
[0064] A number of trials were conducted during which changes to the fiber density and weight were made. As the layer of nonwoven fibers passes through the calendering process, it is important that the cavities (inverted cups) 37 of the newly designed rollers 36 are not overfilled, as this would result in the creation of a solid surface. Accordingly, a variety of product weights were tested, from 150 grams per square meter (gsm) down to 50 gsm and the resulting effect on the non-slip surface and “angel hair” pattern (the random, unbonded fibers) was measured and observed.
[0065] Trials were conducted by reducing the weight per square meter from 150 gsm to 50 gsm in increments of 10 gsm. After running the various increments, it was determined that the heavier weights resulted in an end product that was too thick and expensive. Ultimately, four weights were selected for producing standard end weight products (15 and 30 lb): 50, 70, 80 & 90 gsm. These were tested with a slope tester and a magnifying glass to confirm the presence of sufficient unbonded fibers for grip stop requirements.
Trial 2—Calendering Temperature
[0066] As the weight trials were completed, the temperature of the calendaring process was also adjusted to ensure fusion of the thermoplastic fibers only occurs in the desired areas (the channels). If the temperature is too high, the high spot area fibers fuse together creating a slippery surface. Accordingly, trials were conducted for the calendaring process with the cavity roll heated to temperatures between 150 degrees Celsius to 130 degrees Celsius in increments of 2 degrees Celsius. After each test run, the bonding of the nonwoven fibers was observed in both the channel and high spot areas. A temperature of 142 degrees Celsius was observed to be the best for the required weights, with a range of approximately 142-146. At this temperature, the high spots remain unfused (unbonded) and the channel area was fused to create the desired pattern. In addition the bottom of the fabric is fused creating a smooth surface.
Trial 3—Resin Blend & Melt Selection
[0067] Various trials were conducted for the polypropylene melt flow properties. Polypropylene resin was selected from 22 MI to 35 MI for the trials. High melt flow resins are easier to process but produce a lower strength fiber. Testing started with a 35 MI resin which produced a good even profile fiber, but a lower strength fabric. Finally, a 25 MI polypropylene resin was selected in combination with 2% UV stabilizer masterbatch and 2% color additive to create an even flow and even profile of high spun nonwoven fabric. It was found that a higher colour ratio also tends to change the material flow and consequently the physical appearance and evenness of the resulting nonwoven fabric. A colour ratio of 1.5 to 2.5% was found to work best with the blend to produce the desired results.
Trial 4—Manufacturing Speed and Winding Tension
[0068] Various trials were conducted to ensure a stable process is maintained to achieve the right grip spot structure. Higher speeds resulted in warm fabric being wound with a resulting distortion to the high spot structure. Line speed trials from 80 to 40 meters per minute were conducted. As a result of these trials, it was determined that a line speed of 45-55 meters per minute produced satisfactory results along with the parameters determined from the first 3 trials discussed above.
[0069] The winding tension was also reduced to ensure the rolls were not wound too tight such that the high spots were flattened. Once the fabric cools down sufficiently and takes its final shape, the winding tension or pressure does not seem to affect the grip spots. Lower line speed also creates better annealing time for the nonwoven to settle in its desired design.
Lamination Process
[0070] The lamination process is critical to ensure the final product has suitable water proofing characteristics. The lamination process takes two separate nonwovens (one regular and one high spot) and laminates them together with the lamination layer acting as a water barrier. Type I products contain a mono lamination layer & Type II products contain two separate layers of polymer for lamination and antiskid properties. For example, for a type II product, the nonwoven high spot fabric 16 was laminated to a scrim and then an antiskid film was laminated to it.
[0071] The following trials were conducted to ensure the final product had the desired characteristics.
1. Product Blends
[0072] The product blends were optimized to ensure good lamination, water barrier properties, pliability, and softness for installation. The obvious choice for the lamination layer was polypropylene as the nonwoven fabrics are made of polypropylene. However, 100% polypropylene used for lamination created a very stiff and hard to work product. A low density polyethylene was added in increments of 5% up to 30%. At 30% some poor lamination effects were observed and it was reduced to 25% where good lamination was achieved with a resulting softer, and easier to work with, product. Water ponding and rain tests were conducted to ensure the product has suitable water barrier properties. A 2% UV additive was added to ensure UV stability of the product.
2. Process Parameter Optimization
[0073] A temperature profile was created for the above blend to maximize lamination and reduce degradation of the polymer. A high temperature results in higher polymer flow, which in turn results in penetration of the polymer through the nonwoven creating a slippery surface and poor water barrier properties. A temperature range of 260-265 degrees Celsius was established to ensure the desired physical and barrier properties of the fabric.
3. NIP Pressure
[0074] Along with resin blend and temperature of extrudate, the NIP pressure plays an important role. Higher NIP pressure will damage the high spot surface, impregnate laminate polymer into the nonwoven layers, and create an uneven lamination film layer, which in turn can damage the water barrier properties of the product. Trials were conducted from 90 PSI down to 30 PSI on Nip rollers of laminate. It was determined that a range of 40-50 PSI performed the best for lamination and film integrity. Both water ponding and rain tests were conducted to ensure the desired physical outcome. The NIP rollers selected for this process were a steel “chill” roller and a silicone “rubber” roller with greater than 60 durometer hardness to achieve the best results.
[0075] It is contemplated that the high spot non woven product produced with our new cavity calendar roll can be used in more than just roofing applications. For example, it could be used as a housewrap, as a breathable underlayer should this be desired, or as a house enveloped membrane.
[0076] As discussed above, the high spot nonwoven can be combined with a plurality of different types of membrane layers depending on the desired characteristics for the end product. For example, the high spot nonwoven could be laminated to an antislip film with a lamination layer of polypropylene or polyethylene, or it could be coated directly with an antislip coating to improve the back side (bottom surface) slip resistance. A further example would be the type II product discussed above where the high spot nonwoven is laminated to a woven scrim (preferably formed of polyethylene or polypropylene) with a lamination layer of polyethylene or polypropylene. If desired, the back side of the woven scrim may be further coated with an antislip/antiskid coating.
[0077] It will be readily appreciated by those skilled in the art that various modifications and variations of the present invention may be devised without departing from the scope or spirit of the invention