US2007023954A1PendingUtilityA1
Method for low-density cellular wood plastic composites
Individually held — no corporate assignee on recordPriority: Apr 26, 2001Filed: Jun 24, 2006Published: Feb 1, 2007
Est. expiryApr 26, 2021(expired)· nominal 20-yr term from priority
B29C 2793/009B29C 2948/92704B29C 48/2886B29K 2105/12B29C 48/905B27N 3/005B29C 48/875B29C 48/2556B29K 2105/06B29C 44/22B29K 2711/14B29C 48/07B29C 48/919B29C 44/3446B29C 2948/92904B29K 2311/10B29C 2791/006B29K 2105/16B29C 48/90B29C 48/916B29C 48/908B29C 48/355B27N 3/28B29C 48/06B29C 48/12B29C 48/09B29C 48/288B29C 48/022B29C 48/295B29K 2105/04B29C 48/793B29C 48/904B29K 2105/0005B29C 48/903B29C 48/285B29C 48/912B29C 48/885
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Claims
Abstract
A low-pressure CO 2 tank or an air compressor with a refrigerated air dryer is attached either at or after the vent zone of a standard twin-screw extruder. During or after extrusion, the gas is dissolved in the wood-plastic melt. The CO 2 expands which foams the wood-plastic material.
Claims
exact text as granted — not AI-modified1 - 24 . (canceled)
25 . A method of manufacturing a plank comprising the steps of: a) placing a material in a hopper; b) mixing and then extruding the material from an extruder; c) injecting gas from a device located outside of the extruder, said gas being injected into the material to create foaming in the material d) shaping the extruded material with at least one die into a plank; e) tempering the plank in a controlled environment to maximize foaming; f) calibrating the shape and size of the plank through at least heating; g) cooling the plank further; and h) conveying the plank to a saw for further sizing.
26 . A process of making a composite comprising the steps of: a mixing finely ground wood flour with plastic in an extruder to form a plasticated mixture; introducing a blowing agent into the plasticated material outside of the extruder under low pressure; developing sufficient pressure to drive the blowing agent into the plasticated mixture to form cells within the plasticated mixture, wherein the blowing agent is incorporated under a pressure gradient in the extruder sufficient to increase the solubility of the blowing agent in the plasticated mixture and under a temperature sufficient to prevent collapse of the cells; and reducing the pressure prior to removing the plasticated mixture from the extruder.
27 . The process of claim 26 wherein the wood flour is selected from the group consisting of wood flour, sawdust, pond sludge, newspapers, alfalfa, wheat pulp, wood chips, wood flakes, wood fibers, ground wood, wood veneers, wood laminates, kenaf, paper, cardboard, and straw.
28 . The process of claim 26 wherein the wood flour is selected from hard and soft wood and has a particle size no greater than about 40 mesh.
29 . The process of claim 26 wherein the wood flour has a particle size no greater than about 60 mesh.
30 . The process of claim 26 wherein the moisture content of the wood flour is between about 1% and 9%.
31 . The process of claim 26 wherein the moisture content of the wood flour is no more than about 2%.
32 . The process of claim 26 wherein the thermoplastic materials are selected from the group consisting of polyethylene, polypropylene, poly-vinyl chloride, low-density polyethylene, ethyl-vinyl acetate and waste plastic sawdust.
33 . The process of claim 26 wherein the thermoplastic materials are selected from the group consisting of high-density polyethylene and polypropylene.
34 . The process of claim 26 wherein the ratio of wood fibers to the thermoplastic material is between approximately 3:2 and 1:4.
35 . The process of claim 26 wherein the ratio of wood fibers to the thermoplastic material is approximately 2:3.
36 . The process of claim 26 wherein the blowing agent is selected from the group consisting of air and carbon dioxide.
37 . The process of claim 26 , wherein the pressure gradient is 5 between 1400 psi and 3800 psi.
38 . The process of claim 3 , where the temperature of the extrudate is controlled at a level between about 5 and 15° F. (2.7 and 8.3° C.) above the crystallization temperature of the plasticated mixture.
39 . A process for producing plastic/wood fiber composite foamed structures comprising the steps of: pre-drying wood fiber filler to produce dried wood fiber filler; mixing the dried wood fiber filler with plastic to produce a plastic/wood fiber mixture; feeding the plastic/wood fiber mixture into an extruder; mixing a physical blowing agent into the plastic/wood fiber mixture after the extruder to produce a plastic/wood fiber/gas mixture; subjecting the plastic/wood fiber/gas mixture to high shear forces in the presence of high pressures; and producing a plastic/wood fiber composite foamed structure.
40 . The process of claims 39 , further comprising the steps of: maintaining the pre-drying temperature below the degradation temperature to produce dried wood fiber filler which has a degradation temperature and an active volatization temperature; maintaining the mixing temperature below an active volatilizing temperature; maintaining the processing temperature below an active volatilizing temperature.Join the waitlist — get patent alerts
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