Plant-based flexible material, process for preparation, and uses thereof
US-2024158638-A1 · May 16, 2024 · US
US2016108243A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016108243-A1 |
| Application number | US-201514971419-A |
| Country | US |
| Kind code | A1 |
| Filing date | Dec 16, 2015 |
| Priority date | Mar 16, 2010 |
| Publication date | Apr 21, 2016 |
| Grant date | — |
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Members including components of windows and doors are formed by a method that includes obtaining a biopolymer and a filler, feeding them into an extruder, controlling at least the temperature of the biopolymer and the filler within the extruder to promote the initiation of nucleation of the biopolymer, extruding the composite through a die of the extruder to form an extruded member and controlling at least the cooling rate of the extruded member after it leaves the die to promote crystallization of the biopolymer. Methods are disclosed for compounding and pelletizing as well as direct extrusion of the composite. In a preferred embodiment, the biopolymer is polylactic acid (PLA) and the filler is wood fiber. In addition, neat PLA formulations are also disclosed. Further, the heat distortion temperature and the hydrolysis resistance of these members are greatly increased through specific processing conditions and the addition of strategic quantities of additives.
Opening claim text (preview).
What is claimed is: 1 . A method of forming a member comprising the steps of: (a) obtaining a biopolymer and a filler; (b) feeding the biopolymer and the filler to an extruder; (c) controlling at least the temperature of the biopolymer and the filler within the extruder to promote the initiation of nucleation of the biopolymer; (d) forcing the biopolymer and the filler through a die of the extruder to form an extruded member; and (e) controlling at least the cooling rate of the extruded member after it leaves the die to promote crystallization of the biopolymer. 2 . A method of forming a member as claimed in claim 1 and wherein the step (b) includes the mixing together of the biopolymer and the filler within the extruder to form the composite. 3 . A method of forming a member as claimed in claim 1 and further comprising the step following step (a) of compounding the biopolymer and the filler to form a composite having a predetermined weight percent biopolymer and a predetermined weight percent filler and wherein step (b) comprises feeding the compounded composite to the extruder. 4 . A method of forming a member as claimed in claim 3 and further comprising the step of pelletizing the compounded composite before step (b) and wherein step (b) comprises feeding the pelletized composite to the extruder. 5 . A profile extrusion process comprising: feeding polylactic acid and at least one nucleating agent to an extruder to form a mixture; moving the mixture through a profile extrusion die to form a base extrusion; and providing conditions effective to crystallize the polylactic acid during the profile extrusion process. 6 . The method of claim 5 further comprising providing conditions effective to initiate nucleation of the polylactic acid before the mixture exits the profile extrusion die. 7 . The method of claim 6 wherein providing conditions effective to initiate nucleation of the polylactic acid comprises controlling the melt temperature of the polylactic acid before the mixture exits the profile extrusion die. 8 . The method of claim 5 wherein providing conditions effective to crystallize the polylactic acid comprises controlling the cooling conditions to maintain the temperature of the base extrusion after exiting the profile extrusion die within a predetermined temperature range for a predetermined length of time. 9 . The method of claim 8 wherein the predetermined temperature range is from 100 degrees Celsius to 120 degrees Celsius. 10 . The method of claim 8 wherein the predetermined length of time is 20 seconds to 275 seconds. 11 . The method of claim 5 wherein the at least one nucleating agent comprises an organic nucleating agent, an inorganic nucleating agent, or a combination thereof. 12 . The method of claim 5 wherein feeding polylactic acid and at least one nucleating agent to an extruder to form a mixture comprises feeding polylactic acid, a filler, and at least one nucleating agent to an extruder to form a mixture. 13 . The method of claim 12 wherein the filler comprises wood particulate. 14 . The method of claim 12 wherein feeding polylactic acid, a filler, and at least one nucleating agent to an extruder to form a mixture comprises feeding a compounded composite of two or more components to the extruder, wherein the components comprise polylactic acid, a filler, and at least one nucleating agent. 15 . The method of claim 14 wherein the compounded composite is in the form of pellets. 16 . The method of claim 14 wherein the method further comprises: compounding polylactic acid, a filler, and at least one nucleating agent in determined weight percentages to form a compounded composite; wherein feeding polylactic acid, a filler, and at least one nucleating agent to an extruder to form a mixture comprises feeding the compounded composite to the extruder. 17 . The method of claim 16 wherein the method further comprises: pelletizing the compounded composite; wherein feeding polylactic acid, a filler, and at least one nucleating agent to an extruder to form a mixture comprises feeding the pelletized compounded composite to the extruder. 18 . The method of claim 5 further comprising moving a capping material through an extrusion die onto at least part of the base extrusion. 19 . The method of claim 18 wherein moving a capping material through an extrusion die onto at least part of the base extrusion occurs during or after formation of the base extrusion. 20 . The method of claim 5 wherein feeding polylactic acid and at least one nucleating agent to an extruder to form a mixture comprises feeding polylactic acid, a hydrolysis inhibitor, and at least one nucleating agent to an extruder to form a mixture. 21 . The method of claim 20 wherein the hydrolysis inhibitor comprises a carbodiimide. 22 . The method of claim 5 wherein feeding polylactic acid and at least one nucleating agent to an extruder to form a mixture comprises feeding polylactic acid, a filler, a hydrolysis inhibitor, and at least one nucleating agent to an extruder to form a mixture. 23 . The method of claim 22 wherein feeding polylactic acid, a filler, a hydrolysis inhibitor, and at least one nucleating agent to an extruder to form a mixture comprises feeding a compounded composite of two or more components to the extruder, wherein the components comprise polylactic acid, a filler, a hydrolysis inhibitor, and at least one nucleating agent. 24 . The method of claim 5 further comprising devolatilizing prior to moving the polylactic acid and at least one nucleating agent through an extrusion die. 25 . A profile extrusion process comprising: feeding polylactic acid and at least one nucleating agent to an extruder to form a mixture; moving the mixture through a profile extrusion die to form a base extrusion; controlling the melt temperature of the polylactic acid before the mixture exits the profile extrusion die; and controlling the cooling conditions to maintain the temperature of the base extrusion after the profile extrusion die within a temperature range from 100 degrees Celsius to 120 degrees Celsius for 20 seconds to 275 seconds.
Filamentary, e.g. strands · CPC title
containing compounding ingredients (releasing, lubricating or separating agents B29C33/56, fibers B29K2105/08, B29K2105/12; fillers B29K2105/16, recycled material B29K2105/26) · CPC title
Temperature · CPC title
Lignocellulosic material, e.g. wood, straw or bagasse {(manufacture of articles made from lignocellulosic material by dry processes B27N)} · CPC title
Measuring, controlling or regulating · CPC title
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