US20050075423A1 - Biopolymer structures and components including column and rail system - Google Patents
Biopolymer structures and components including column and rail system Download PDFInfo
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- US20050075423A1 US20050075423A1 US10/868,276 US86827604A US2005075423A1 US 20050075423 A1 US20050075423 A1 US 20050075423A1 US 86827604 A US86827604 A US 86827604A US 2005075423 A1 US2005075423 A1 US 2005075423A1
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L89/00—Compositions of proteins; Compositions of derivatives thereof
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
- B29C48/40—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
- B29C48/40—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
- B29C48/405—Intermeshing co-rotating screws
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
- B29C48/40—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
- B29C48/41—Intermeshing counter-rotating screws
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/50—Details of extruders
- B29C48/76—Venting, drying means; Degassing means
- B29C48/765—Venting, drying means; Degassing means in the extruder apparatus
- B29C48/766—Venting, drying means; Degassing means in the extruder apparatus in screw extruders
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/10—Homopolymers or copolymers of propene
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L3/00—Compositions of starch, amylose or amylopectin or of their derivatives or degradation products
- C08L3/02—Starch; Degradation products thereof, e.g. dextrin
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L97/00—Compositions of lignin-containing materials
- C08L97/02—Lignocellulosic material, e.g. wood, straw or bagasse
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J123/00—Adhesives based on homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Adhesives based on derivatives of such polymers
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12F—RECOVERY OF BY-PRODUCTS OF FERMENTED SOLUTIONS; DENATURED ALCOHOL; PREPARATION THEREOF
- C12F3/00—Recovery of by-products
- C12F3/10—Recovery of by-products from distillery slops
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- E—FIXED CONSTRUCTIONS
- E04—BUILDING
- E04F—FINISHING WORK ON BUILDINGS, e.g. STAIRS, FLOORS
- E04F11/00—Stairways, ramps, or like structures; Balustrades; Handrails
- E04F11/18—Balustrades; Handrails
- E04F11/181—Balustrades
- E04F11/1842—Balusters; Grille-type elements
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L51/00—Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
- C08L51/06—Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers grafted on to homopolymers or copolymers of aliphatic hydrocarbons containing only one carbon-to-carbon double bond
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L93/00—Compositions of natural resins; Compositions of derivatives thereof
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L97/00—Compositions of lignin-containing materials
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- E—FIXED CONSTRUCTIONS
- E04—BUILDING
- E04F—FINISHING WORK ON BUILDINGS, e.g. STAIRS, FLOORS
- E04F11/00—Stairways, ramps, or like structures; Balustrades; Handrails
- E04F11/18—Balustrades; Handrails
- E04F2011/1885—Handrails or balusters characterized by the use of specific materials
- E04F2011/1897—Handrails or balusters characterized by the use of specific materials mainly of organic plastics with or without reinforcements or filling materials
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/249921—Web or sheet containing structurally defined element or component
- Y10T428/249953—Composite having voids in a component [e.g., porous, cellular, etc.]
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/28—Web or sheet containing structurally defined element or component and having an adhesive outermost layer
Definitions
- the present invention relates generally to structures formed from a biopolymer.
- the present invention more particularly relates to biopolymer structures and components formed from fermentation solids and thermoactive materials, including a column and rail system and the component parts of this system.
- plastics may be formed into lumber replacements, as described in U.S. Pat. No. 5,539,027; components of window and door assemblies, as described in U.S. Pat. No. 5,486,553; or siding for building structures, as described in U.S. Pat. No. 6,122,877.
- Fillers have been used in the plastic industry for almost 90 years. The reason most manufacturers use filled plastic is to reduce the price of the high cost of polypropylene and other plastics with lower cost fillers, such as wood flour, talc, and mica, and fiberglass. Filling plastic with fiberglass can improve its characteristics by creating higher thermal stability and higher bending and rupture strengths. However, low cost fillers like wood flour can degrade some of the qualities of plastics and make it harder to process. Talc and mica provide some increase in strength to plastic, but also add weight and decrease the life of the extruder due to abrasion. Fiberglass adds considerable strength of the product, but at a substantial cost.
- thermoactive materials that can reduce the cost and consumption of thermoactive materials and that performs better than a filler for products such as window and door assemblies, lumber replacements, siding for buildings, column and rail systems, and other goods.
- the present invention relates generally to structures formed from a biopolymer.
- the present invention more particularly relates to biopolymer structures and components formed from fermentation solids and thermoactive materials, including a column and rail system and the component parts of this system.
- the column system can include one or more independent panels and corner components that can be coupled to a base, a post, top cap, or any combination thereof.
- the rail system can include a top rail assembly including a top rail and a rail cover.
- the column can include a base, a pillar, and a post, where the post can be coupled to the base, the pillar, or both.
- the pillar can include a plurality of corners, and a plurality of panels coupled to the corners.
- a top cap can also be coupled to the pillar.
- the railing segment can comprise at least one baluster connected to rails, and can include a rail cover. The railing segment can then be coupled to the column.
- FIG. 1 is a front perspective view of a decking system.
- FIG. 2 is a front perspective view of a base component and a post.
- FIG. 3 is a front perspective view of a pillar and a base component.
- FIG. 4 is a front perspective view of a pillar, a base component, and a top cap.
- FIG. 5 is a front perspective view of components of a railing assembly.
- FIG. 6 is a side view of components a railing assembly.
- FIG. 7 is a side view of a railing assembly with a railing cover.
- FIG. 8 is a perspective view of a base.
- FIG. 9 is a top view of a panel component.
- FIG. 10 is a cross-sectional view of a corner.
- FIG. 11 is a perspective view of a top cap.
- FIG. 12 is a top view of a baluster.
- FIG. 13 is a side view of a bottom rail.
- FIG. 14 is a side view of a rail cover.
- FIG. 15 illustrates a method for processing a biopolymer composition.
- FIG. 16 illustrates a method for forming an article from a biopolymer.
- the present invention relates to articles fabricated from or including biopolymers including fermentation solid and thermoactive material.
- the present biopolymer can exhibit properties typical of plastic materials, properties advantageous compared to conventional plastic materials, and/or properties advantageous compared to aggregates including plastic and, for example, wood or cellulosic materials.
- the present biopolymer can be formed into useful articles using any of a variety of conventional methods for forming items from plastic.
- the present biopolymer can take any of a variety of forms.
- U.S. patent application Ser. No. ______ entitled “BIOPOLYMER AND METHODS OF MAKING IT” and filed evendate herewith describes the present biopolymer and related methods. This application is incorporated herein by reference.
- biopolymer refers to a material including a thermoactive material and a fermentation solid.
- fertilization solid refers to solid material recovered from a fermentation process, such as alcohol (e.g., ethanol) production.
- alcohol e.g., ethanol
- fermented protein solid refers to fermentation solid recovered from fermenting a material including protein.
- the fermented protein solid also includes protein.
- DDG distiller's dried grain
- grain e.g., corn
- DDG can include residual amounts of solubles, for example, about 2 wt-%.
- Distiller's dried grain includes compositions known as brewer's grain and spent solids.
- DDGS distalmost fine grain with solubles
- wet cake or “wet distiller's grain” refers to the coarse, wet residue remaining after the starch in grain (e.g., corn) has been fermented with selected yeasts and enzymes to produce products including ethanol and carbon dioxide.
- solvent washed wet cake refers to wet cake that has been washed with a solvent such as, water, alcohol, or hexane.
- gluten meal refers to a by-product of the wet milling of plant material (e.g., corn, wheat, or potato) for starch.
- Corn gluten meal can also be a by-product of the conversion of the starch in whole or various fractions of dry milled corn to corn syrups.
- Gluten meal includes prolamin protein and gluten (a mixture of water-insoluble proteins that occurs in most cereal grains) and also smaller amounts of fat and fiber.
- plant material refers to all or part of any plant (e.g., cereal grain), typically a material including starch.
- Suitable plant material includes grains such as maize (corn, e.g., whole ground corn), sorghum (milo), barley, wheat, rye, rice, millet, oats, soybeans, and other cereal or leguminous grain crops; and starchy root crops, tubers, or roots such as sweet potato and cassaya.
- the plant material can be a mixture of such materials and byproducts of such materials, e.g., corn fiber, corn cobs, stover, or other cellulose and hemicellulose containing materials such as wood or plant residues.
- Preferred plant materials include corn, either standard corn or waxy corn.
- Preferred plant materials can be fermented to produced fermentation solid.
- prolamin refers to any of a group of globular proteins which are found in plants, such as cereals. Prolamin proteins are generally soluble in 70-80 percent alcohol but insoluble in water and absolute alcohol. These proteins contain high levels of glutamic acid and proline. Suitable prolamin proteins include gliadin (wheat and rye), zein (corn), and kafirin (sorghum and millet). Suitable gliadin proteins include ⁇ -, ⁇ -, ⁇ -, and ⁇ -gliadins.
- zein refers to a prolamin protein found in corn, with a molecular weight of about 40,000 (e.g., 38,000), and not containing tryptophan and lysine.
- glass transition point refers to the temperature at which a particle of a material (such as a fermentation solid or thermoactive material) reaches a “softening point” so that it has a viscoelastic nature and can be more readily compacted. Below T g a material is in its “glass state” and has a form that can not be as readily deformed under simple pressure.
- melting point or “T m ” refers to the temperature at which a material (such as a fermentation solid or thermoactive material) melts and begins to flow. Suitable methods for measuring these temperatures include differential scanning calorimetry (DSC), dynamic mechanical thermal analysis (DTMA), and thermal mechanical analysis (TMA).
- DSC differential scanning calorimetry
- DTMA dynamic mechanical thermal analysis
- TMA thermal mechanical analysis
- weight percent (wt-%), percent by weight, % by weight, and the like are synonyms that refer to the concentration of a substance as the weight of that substance divided by the weight of the composition and multiplied by 100. Unless otherwise specified, the quantity of an ingredient refers to the quantity of active ingredient.
- the term “about” modifying any amount refers to the variation in that amount encountered in real world conditions of producing materials such as polymers or composite materials, e.g., in the lab, pilot plant, or production facility.
- an amount of an ingredient employed in a mixture when modified by about includes the variation and degree of care typically employed in measuring in a plant or lab producing a material or polymer.
- the amount of a component of a product when modified by about includes the variation between batches in a plant or lab and the variation inherent in the analytical method. Whether or not modified by about, the amounts include equivalents to those amounts. Any quantity stated herein and modified by “about” can also be employed in the present invention as the amount not modified by about.
- the present biopolymer includes fermentation solid and thermal active material.
- the biopolymer can take any of a variety of forms.
- the present biopolymer includes fermentation solid integrated with the thermoactive material, which form is referred to herein as an “integrated biopolymer”.
- the integrated biopolymer forms a uniform mass in which the fermentation solid has been blended into the thermoactive material.
- the present biopolymer includes features of the integrated biopolymer but has visible particles of remaining fermentation solid, which form is referred to herein as a “composite biopolymer”.
- a composite biopolymer can have a granite-like appearance with a matrix of thermoactive material with a first appearance surrounding particles of fermentation solid with a second appearance.
- the present biopolymer includes a significant portion of fermentation solid present as discrete particles surrounded by or embedded in the thermoactive material, which form is referred to herein as an “aggregate biopolymer”.
- the compounded fermentation solid and thermoactive material i.e., the soft or raw biopolymer
- the soft or raw biopolymer before hardening, takes the form of a dough, which can be largely homogeneous.
- “largely homogeneous” dough refers to a material with a consistency similar to baking dough (e.g., bread or cookie dough) with a major proportion of the fermentation solid blended into the thermoactive material and no longer appearing as distinct particles.
- the soft or raw biopolymer includes no detectable particles of fermentation solid, e.g., it is a homogeneous dough.
- the soft or raw biopolymer can include up to 95 wt-% (e.g., 90 wt-%) fermentation solid and take the form of a largely homogeneous or homogeneous dough. In an embodiment, the soft or raw biopolymer can include about 50 to about 70 wt-% fermentation solid and take the form of a largely homogeneous or homogeneous dough.
- the raw or soft biopolymer includes visible amounts of fermentation solid.
- visible amounts of fermentation solid refers to particles that are clearly visible to the naked eye and that provide a granite-like appearance to the cured biopolymer.
- Such visible fermentation solid can be colored for decorative effect in the cured biopolymer.
- the granite-like appearance can be produced by employing larger particles of fermentation solid than used to produce a homogeneous or largely homogeneous dough.
- the biopolymer can include fermentation solid at about 0.01 to about 95 wt-%, about 1 to about 95 wt-%, about 5 to about 95 wt-%, about 5 to about 80 wt-%, about 5 to about 70 wt-%, about 5 to about 20 wt-%, about 50 to about 95 wt-%, about 50 to about 80 wt-%, about 50 to about 70 wt-%, about 50 to about 60 wt-%, about 60 to about 80 wt-%, or about 60 to about 70 wt-%.
- the biopolymer can include fermentation solid at about 5 wt-%, about 10 wt-%, about 20 wt-%, about 50 wt-%, about 60 wt-%, about 70 wt-%, or about 75 wt-%.
- the present biopolymer can include any of these amounts or ranges not modified by about.
- the biopolymer can include thermoactive material at about 0.01 to about 95 wt-%, about 1 to about 95 wt-%, about 5 to about 30 wt-%, about 5 to about 40 wt-%, about 5 to about 50 wt-%, about 5 to about 85 wt-%, about 5 to about 95 wt-%, about 10 to about 30 wt-%, about 10 to about 40 wt-%, about 10 to about 50 wt-%, or about 10 to about 95 wt-%.
- the biopolymer can include thermoactive material at about 95 wt-%, about 75 wt-%, about 50 wt-%, about 45 wt-%, about 40 wt-%, about 35 wt-%, about 30 wt-%, about 25 wt-%, about 20 wt-%, about 15 wt-%, about 10 wt-%, or about 5 wt.
- the present biopolymer can include any of these amounts or ranges not modified by about.
- the biopolymer can include fermentation solid at about 5 to about 95 wt-% and thermoactive material at about 5 to about 95 wt-%, can include fermentation solid at about 50 to about 70 wt-% and thermoactive material at about 30 to about 70 wt-%, can include fermentation solid at about 50 to about 70 wt-% and thermoactive material at about 20 to about 70 wt-%, can include fermentation solid at about 50 to about 60 wt-% and thermoactive material at about 30 to about 50 wt-%, or can include fermentation solid at about 60 to about 70 wt-% and thermoactive material at about 20 to about 40 wt-%.
- the biopolymer can include about 5 wt-% fermentation solid and about 70 to about 95 wt-% thermoactive material, about 10 wt-% fermentation solid and about 70 to about 90 wt-% thermoactive material, about 50 wt-% fermentation solid and about 30 to about 50 wt-% thermoactive material, about 55 wt-% fermentation solid and about 30 to about 45 wt-% thermoactive material, about 60 wt-% fermentation solid and about 20 to about 40 wt-% thermoactive material, about 65 wt-% fermentation solid and about 20 to about 40 wt-% thermoactive material, about 70 wt-% fermentation solid and about 10 to about 30 wt-% thermoactive material, about 90 wt-% fermentation solid and about 5 to about 10 wt-% thermoactive material.
- the present biopolymer can include any of these amounts or ranges not modified by about.
- the present biopolymer can include any of a variety of fermentation solids.
- Fermentation solid can be recovered from any of a variety of fermentation processes, such as alcohol (e.g., ethanol) production.
- a fermentation solid can be recovered from, for example, fermentation of plant material.
- Numerous fermentation solids have been characterized, primarily as animal feed.
- the fermentation solids that have been characterized include those known as distiller's dried grain (DDG), distiller's dried grain with solubles (DDGS), wet cake (WC), solvent washed wet cake (WWC), fractionated distiller's dried grain (FDDG), and gluten meal.
- Fermentation solid can include, for example, protein, fiber, and, optionally, fat. Fermentation solid can also include residual starch.
- Distiller's dried grains or other distiller's dried plant materials can be derived from any of a variety of agricultural products.
- “distiller's dried” followed by the name of a plant or type of plant refers to a fermentation solid derived from fermentation of that plant or type of plant.
- distiller's dried grain refers to a fermentation solid derived from fermentation of grain.
- distiller's dried corn refers to a fermentation solid derived from fermentation of corn.
- Distiller's dried sorghum refers to a fermentation solid derived from fermentation of sorghum (milo).
- Distiller's dried wheat refers to a fermentation solid derived from fermentation of wheat.
- a distiller's dried plant material need not be exclusively derived from the named plant material. Rather, the named plant material is the predominant plant material or the only plant material in the fermentation solid.
- the present biopolymer can include any of a variety of fermentation solids including, for example, distiller's dried grain, distiller's dried starchy root crop, distiller's dried tuber, and distiller's dried root.
- Suitable distiller's dried grains include distiller's dried cereal grain and distiller's dried legume.
- Suitable distiller's dried grains include distiller's dried maize (distiller's dried corn, e.g., distiller's dried whole ground corn or distiller's dried fractionated corn), distiller's dried sorghum (milo), distiller's dried barley, distiller's dried wheat, distiller's dried rye, distiller's dried rice, distiller's dried millet, distiller's dried oats, distiller's dried soybean.
- Suitable distiller's dried roots include distiller's dried sweet potato and distiller's dried cassaya.
- Suitable distiller's dried tubers include distiller's dried potato.
- distiller's dried fractionated plant material e.g., distiller's dried fractionated grain.
- the present biopolymer can include any of a variety of fractionated fermentation solids.
- the present biopolymer can include distiller's dried fractionated corn.
- the present biopolymer can include distiller's dried corn germ and/or distiller's dried corn endosperm.
- the present fermentation solid reached a temperature (e.g., at the exit from the dryer) of no higher than about 500° F., about 400° F., about 300° F., about 250° F., about 200° F., or about 180° F.
- the present fermentation solid reached a temperature (e.g., at the exit from the dryer) of no higher than about 500° F.
- the present fermentation solid reached a temperature (e.g., at the exit from the dryer) of no higher than about 400° F.
- the present fermentation solid reached a temperature (e.g., at the exit from the dryer) of no higher than about 300° F. In an embodiment, the present fermentation solid (e.g., fermented protein isolate) reached a temperature (e.g., at the exit from the dryer) of no higher than about 250° F. In an embodiment, the present fermentation solid (e.g., fermented protein isolate) reached a temperature (e.g., at the exit from the dryer) of no higher than about 200° F. In an embodiment, the present fermentation solid (e.g., fermented protein isolate) reached a temperature (e.g., at the exit from the dryer) of no higher than about 180° F. The present fermentation solid can include any of these temperatures not modified by about.
- distal's dried refers to a fermentation solid that reached a temperature (e.g., at the exit from the dryer) at or below that temperature.
- distiller's dried grain-200 refers to distiller's dried grain that reached a temperature (e.g., at the exit from the dryer) at or below 200° F.
- the plant material can also be ground. Grinding can subject plant material to elevated temperatures.
- distal's dried followed by a number with the suffix “gd” refers to a fermentation solid that was ground and dried reaching a temperature (e.g., at the exit from the dryer) at or below that temperature.
- distiller's dried grain-200gd refers to distiller's dried grain ground and dried and that reached a temperature (e.g., at the exit from the dryer) at or below 200° F.
- a fermentation solid that has been prepared by employing low temperature grinding and/or drying is referred to herein as “gently treated fermentation solid”.
- a fermented protein solid that has been prepared by employing low temperature grinding and/or drying is referred to herein as “proteinaceous fermentation solid”.
- Suitable gently treated fermentation solids include gently treated DDG and gently treated DDGS.
- Gently treated fermentation solids include those derived from fermentation processes lacking a cooking stage.
- the present biopolymer can include or can be made from a fermentation solid with any of broad range of sizes.
- the fermentation solid employed in the biopolymer has a particle size of about 2 mesh to less than about 1 micron, about 2 to about 10 mesh, about 12 to about 500 mesh, about 60 mesh to less than about 1 micron, about 60 mesh to about 1 micron, about 60 to about 500 mesh.
- the biopolymer can include any of a wide variety of thermoactive materials.
- the biopolymer can include any thermoactive material in which the fermentation solid can be embedded.
- the thermoactive material can be selected for its ability to form a homogeneous or largely homogeneous dough including the fermentation solid.
- the thermoactive material can be selected for its ability to covalently bond with the fermentation solid.
- the thermoactive material can be selected for its ability to flow when mixed or compounded with fermentation solid.
- the thermoactive material can set after being formed. Numerous such thermoactive materials are commercially available.
- thermoactive materials include thermoplastic, thermoset material, a resin and adhesive polymer, or the like.
- thermoplastic refers to a plastic that can once hardened be melted and reset.
- thermoset material refers to a material (e.g., plastic) that once hardened cannot readily be melted and reset.
- resin and adhesive polymer refers to more reactive or more highly polar polymers than thermoplastic and thermoset materials.
- Suitable thermoplastics include polyamide, polyolefin (e.g., polyethylene, polypropylene, poly(ethylene-copropylene), poly(ethylene-coalphaolefin), polybutene, polyvinyl chloride, acrylate, acetate, and the like), polystyrenes (e.g., polystyrene homopolymers, polystyrene copolymers, polystyrene terpolymers, and styrene acrylonitrile (SAN) polymers), polysulfone, halogenated polymers (e.g., polyvinyl chloride, polyvinylidene chloride, polycarbonate, or the like, copolymers and mixtures of these materials, and the like.
- polyamide e.g., polyethylene, polypropylene, poly(ethylene-copropylene), poly(ethylene-coalphaolefin), polybutene, polyvinyl chloride, acrylate, acetate, and
- Suitable vinyl polymers include those produced by homopolymerization, copolymerization, terpolymerization, and like methods.
- Suitable homopolymers include polyolefins such as polyethylene, polypropylene, poly-1-butene, etc., polyvinylchloride, polyacrylate, substituted polyacrylate, polymethacrylate, polymethylmethacrylate, copolymers and mixtures of these materials, and the like.
- Suitable copolymers of alpha-olefins include ethylene-propylene copolymers, ethylene-hexylene copolymers, ethylene-methacrylate copolymers, ethylene-methacrylate copolymers, copolymers and mixtures of these materials, and the like.
- suitable thermoplastics include polypropylene (PP), polyethylene (PE), and polyvinyl chloride (PVC), copolymers and mixtures of these materials, and the like.
- suitable thermoplastics include polyethylene, polypropylene, polyvinyl chloride (PVC), low density polyethylene (LDPE), copoly-ethylene-vinyl acetate, copolymers and mixtures of these materials, and the like.
- thermoset materials include epoxy materials, melamine materials, copolymers and mixtures of these materials, and the like.
- suitable thermoset materials include epoxy materials and melamine materials.
- suitable thermoset materials include epichlorohydrin, bisphenol A, diglycidyl ether of 1,4-butanediol, diglycidyl ether of neopentyl glycol, diglycidyl ether of cyclohexanedimethanol, aliphatic; aromatic amine hardening agents, such as triethylenetetraamine, ethylenediamine, N-cocoalkyltrimethylenediamine, isophoronediamine, diethyltoluenediamine, tris(dimethylaminomethylphe-nol); carboxylic acid anhydrides such as methyltetrahydrophthalic anhydride, hexahydrophthalic anhydride, maleic anhydride, polyazelaic polyanhydride and phthalic anhydr
- Suitable resin and adhesive polymer materials include resins such as condensation polymeric materials, vinyl polymeric materials, and alloys thereof.
- Suitable resin and adhesive polymer materials include polyesters (e.g., polyethylene terephthalate, polybutylene terephthalate, and the like), methyl diisocyanate (urethane or MDI), organic isocyanide, aromatic isocyanide, phenolic polymers, urea based polymers, copolymers and mixtures of these materials, and the like.
- Suitable resin materials include acrylonitrile-butadiene-styrene (ABS), polyacetyl resins, polyacrylic resins, fluorocarbon resins, nylon, phenoxy resins, polybutylene resins, polyarylether such as polyphenylether, polyphenylsulfide materials, polycarbonate materials, chlorinated polyether resins, polyethersulfone resins, polyphenylene oxide resins, polysulfone resins, polyimide resins, thermoplastic urethane elastomers, copolymers and mixtures of these materials, and the like.
- suitable resin and adhesive polymer materials include polyester, methyl diisocyanate (urethane or MDI), phenolic polymers, urea based polymers, and the like.
- Suitable thermoactive materials include polymers derived from renewable resources, such as polymers including polylactic acid (PLA) and a class of polymers known as polyhydroxyalkanoates (PHA).
- PHA polymers include polyhydroxybutyrates (PHB), polyhydroxyvalerates (PHV), and polyhydroxybutyrate-hydroxyvalerate copolymers (PHBV), polycaprolactone (PCL) (i.e. TONE), polyesteramides (i.e. BAK), a modified polyethylene terephthalate (PET) (i.e. BIOMAX), and “aliphatic-aromatic” copolymers (i.e. ECOFLEX and EASTAR BIO), mixtures of these materials and the like.
- PHA polymers include polyhydroxybutyrates (PHB), polyhydroxyvalerates (PHV), and polyhydroxybutyrate-hydroxyvalerate copolymers (PHBV), polycaprolactone (PCL) (i.e. TONE), polyesteramides (i.e. BAK),
- the present biopolymer can also include one or more additives.
- Suitable additives include one or more of dye, pigment, other colorant, hydrolyzing agent, plasticizer, filler, extender, preservative, antioxidants, nucleating agent, antistatic agent, biocide, fungicide, fire retardant, flame retardant, heat stabilizer, light stabilizer, conductive material, water, oil, lubricant, impact modifier, coupling agent, crosslinking agent, blowing or foaming agent, reclaimed or recycled plastic, and the like, or mixtures thereof.
- Suitable additives include plasticizer, light stabilizer, coupling agent, and the like, or mixtures thereof.
- additives can tailor properties of the present biopolymer for end applications.
- the present biopolymer can optionally include about 1 to about 20 wt-% additive.
- the present biopolymer can be made by any of a variety of methods that can mix thermoactive material and fermentation solid.
- the thermoactive material and fermentation solid are compounded.
- the verb “compound” refers to putting together parts so as to form a whole and/or forming by combining parts (e.g., thermoactive material and fermentation solid).
- the fermentation solid can be compounded with any of a variety of thermoactive materials, such as thermoset and thermoplastic materials. Any of a variety of additives or other suitable materials can be mixed or compounded with the fermentation solid and thermoactive material to make the present biopolymer.
- compounding fermentation solid and thermoactive material produces the dough-like material described hereinabove.
- Compounding can include one or more of heating the fermentation solid and thermoactive material, mixing (e.g., kneading) the fermentation solid and thermoactive material, and crosslinking the fermentation solid and thermoactive material.
- Compounding can include thermal kinetic compounding, extruding, high shear mixing compounding, or the like.
- the fermentation solid and thermoactive material are compounded in the presence of hydrolyzing agent.
- the biopolymer or biopolymer dough can be formed by melting together the fermentation solid and the thermoactive material.
- thermal kinetic compounding of wood particles and thermoactive material produces a material in which wood particles are easily seen as individual particles suspended in the plastic matrix or as wood particles coated with plastic.
- the compounded fermentation solid and thermoactive material can be an integrated mass that is homogenous or nearly so.
- the compounded, raw or soft biopolymer can be used directly or can be formed as pellets, granules, or another convenient form for converting to articles by molding or other processes.
- Thermal Kinetic Compounding can mix and compound employing high speed thermal kinetic principals.
- Thermal kinetic compounding includes mixing two or more components with high shear speeds using an impeller.
- Suitable thermal kinetic compounding apparatus are commercially available, for example, the Gelimat G1 (Draiswerke Company). Such a system can include a computer controlled metering and weight batch system.
- An embodiment of a thermal kinetic compounding apparatus includes a horizontally positioned mixer and compounding chamber with a central rotating shaft. Several staggered mixing elements are mounted to the shaft at different angles. The specific number and positions of the mixing blades varies with the size of the chamber.
- a pre-measured batch of thermoactive material and fermentation solid can be fed in to the compounder, for example, via an integrated screw that can be part of the rotor shaft. Alternatively, the thermoactive material and fermentation solid can be fed through a slide door, located on the mixer body.
- the apparatus can include an automatically operated discharge door at the bottom of the compounding chamber.
- thermoactive material and fermentation solid In the compounding chamber, the thermoactive material and fermentation solid is subject to high turbulence, due to high tip-speed of the mixing element.
- the thermoactive material and fermentation solid are well mixed and also subjected to temperature increase from impact against the chamber wall, mixing blades, and the material particles themselves. The friction in the moving particles can rapidly increase temperature and remove moisture.
- Thermal kinetic compounding can include compounding the quantities or concentrations listed above for the fermentation solid and thermoactive materials in batch size suitable for the apparatus.
- the compounded thermoactive material and fermentation solid, the biopolymer can then be run through a regrinding process to produce uniform granular materials.
- regrinding can employ a standard knife grinding system using a screen, which can create smaller uniform particles of a similar size and shape.
- Such granular materials can be used in, for example, extrusion, injection molding, and other plastic processing.
- the present biopolymer can be formed by any of a variety of extruding processes suitable for mixing or compounding fermentation solid and thermoactive material.
- extruding processes such as twin screw compounding
- Compounding by extruding can provide a higher internal temperature within the extruder and promote the interaction of thermoplastics with the fermentation solid.
- Twin screw compounding can employ co- or counter-rotating screws.
- the extruder can include vents that allow escape of moisture or volatiles from the mixture being compounded.
- Biopolymer material can be formed into a variety of objects and structures.
- raw biopolymer can be formed into pellets which are fed into machinery configured to injection mold, extrude, or otherwise form or process the biopolymer.
- pellets can be formed by first urging polymer and fermentation solids through a die to produce a linear extrusion and then cutting the extrusion into a pellet shape.
- the pellets have a substantially uniform size and shape.
- the cross-section of the pellet can be any of a variety of shapes, such as square, circular, oval, rectangular, pentagonal, hexagonal, etc., as determined by depending on the shape of the extrusion die.
- a circular cross section can be preferred in many applications, typically with a radius of several millimeters and length of about two to four time the radius.
- biopolymer can be used in boat hulls, playground sets, storage containers, crown molding, and the like.
- Embodiments of the present biopolymer can be injection molded.
- compounded biopolymer can be ground to form uniform pellets for use in an injection molding process.
- the present polymer can be processed using less energy per pound than conventional thermoplastics.
- the present biopolymer can exhibit faster heating and cooling times during injection molding compared to conventional thermoplastics.
- the present biopolymer maintains the melt index of the plastic and allows flowability characteristics that allows high speed injection molding. For example, biopolymer including fermentation solid and polypropylene was observed to have higher thermal conductivity than pure polypropylene. Higher thermal conductivity provides faster heating and/or cooling, which can which can speed processes such as injection molding.
- machinery can be configured to injection mold biopolymer into a desired shape.
- a mold defines a shape, into which heated thermoactive material is injected. The material is then allowed to cool and subsequently ejected from the mold.
- the present biopolymer can be extruded to form an article of manufacture employing any of a number of conventional extrusion processes.
- the present biopolymer can be extruded by dry process extrusion.
- the present biopolymer can be extruded using any of a variety of conventional die designs.
- extruding the present biopolymer to form an article can include feeding the biopolymer into a material preparation auger and converting it to a size suitable for extruding.
- Extruding can employ any of a variety of conventional dies and any of a variety of conventional temperatures. Compounding by extruding can provide a higher internal temperature within the extruder and promote the interaction of thermoplastics with the fermentation solid.
- An extruder having one or more dies can be configured to form the biopolymer into a shape.
- the biopolymer can be urged through a die to produce a desired cross section.
- the extruded biopolymer can then be cut to a desired length as necessary.
- the biopolymer can also be allowed to harden or otherwise cured to preserve the cross-sectional shape. Extruded biopolymer can later be cut into shorter lengths as desired.
- the biopolymer material can be heated above the melting point.
- the biopolymer can then be moved through a converging die that is heated to reduce shear stress in the biopolymer near the wall and then through a forming section to provide a desired cross section.
- the biopolymer can then be passed through a low-friction unheated or thermally insulated section that has a cross section that is the same or similar to the cross section of the forming section to establish a cross sectional memory in the polymer and reduce swelling after extrusion.
- the biopolymer material can then be quenched to form a shell below the melting point. In embodiments, the shell can substantially maintain the biopolymer in the desired shape.
- the biopolymer material can be moved through a heated converging die and then a forming section to provide a desired cross section.
- the biopolymer material can then be quenched to form a shell to maintain the desired shape.
- machinery can be configured to move biopolymer through a transition die and then through a stranding die to produce strands of biopolymer.
- Machinery can further be configured to move the strands through a molding die that combines the strands into a desired extrusion.
- this stranding and re-bonding process can produce a product having a structure and/or appearance that is similar to the grain in wood.
- Methods and apparatus for stranding and re-bonding thermoactive materials are further described in U.S. Pat. No. 5,516,472, which is incorporated herein by reference. This patent discloses methods and apparatus employed for processing plastics with wood fillers or other shredded cellulosic material. These methods and apparatus can also be employed to process and form embodiments of the present biopolymer.
- Additional materials can be co-extruded with the biopolymer.
- a layer or sheet of another material e.g., a coating or thermoactive material
- the co-extruded layer or sheet can provide desired surface properties, structural properties, and/or appearance.
- the present biopolymer can be foamed either from its soft, raw form or upon melting without addition of foaming or blowing agents. Surprisingly, the present biopolymer can foam upon extruding even in the absence of foaming agents to produce a rigid, strong hardened foam. Although not limiting the present invention, it is believed that the present foam can result from foaming of protein in the fermentation solid.
- the stiff or solid foam can exhibit greater strength (e.g., flexural modulus) compared to conventional foamed plastics at the same density. Conventional plastics decrease in strength when foamed.
- the present biopolymer foam may include denatured protein interacting with the thermoactive material to create an advantageously strong biopolymer foam.
- the present biopolymer (e.g., in the form of pellets) can be converted to a biopolymer foam by injection molding, extrusion, and like methods employed for forming plastics. Although not limiting to the present invention, it is believed that the heat and kinetic energy applied in these processes, such as by a mixing screw, is sufficient to foam the present biopolymer.
- injection molding the mold can be partially filled to allow the foaming action of the biopolymer to fill the cavity. This can decrease the density of the molded article without using chemical foaming or blowing agents.
- Extruding can also be employed to foam the present biopolymer. The dies used in extruding can form the foamed biopolymer.
- a foamed biopolymer can be produced by mixing a foaming agent with fermentation solids and thermoactive material.
- biopolymer can be foamed without pre-fabrication into pellets by mixing fermentation solids and thermoactive material with a powdered foaming agent, heating and compounding the mixture and then extruding the biopolymer.
- vacuum can be used to remove vapors.
- greater expansion occurs in the center of an extruded profile than at the perimeter of the profile, such that the extruded product has a higher density near the exterior than on the interior.
- ingredients can first be processed into a biopolymer product and then the biopolymer can be re-ground into fine particles to facilitate foaming into a foamed product shape.
- foamed biopolymer can be created by creating discontinuities in a biopolymer material.
- the discontinuities are expanded and the biopolymer is then stabilized to preserve the discontinuities by cooling or crosslinking.
- biopolymer can be made using foaming agents such as an inert gases (e.g. nitrogen or carbon dioxide, hydrocarbons, chlorinated hydrocarbons, chlorofluorocarbons) or a decomposing chemical blowing agent that dissolves or disperses into biopolymer in liquid form and which decomposes to an inert gas at elevated temperatures.
- foaming agents such as an inert gases (e.g. nitrogen or carbon dioxide, hydrocarbons, chlorinated hydrocarbons, chlorofluorocarbons) or a decomposing chemical blowing agent that dissolves or disperses into biopolymer in liquid form and which decomposes to an inert gas at elevated temperatures.
- the expansion associate with foaming agents or decomposing chemical blowing agents cause expansion of cell structures to develop a foamed
- An embodiment of a foamed component includes a solid outer layer or shell and an interior formed of foamed biopolymer.
- Foamed biopolymer components can be configured to offer relatively low weight and high stiffness compared to solid components.
- Foamed biopolymer can be formed for example into components such as sized lumber, posts, beams, trim, shaped structural members, furniture board, and trim components. It can be desirable to form components with a specific gravity lower than water, so the components float, or to approximate the density of wood lumber.
- Window or door components can also be formed from foamed biopolymer.
- Components of a column and rail system can be formed from foamed biopolymer. Components combining hollow and foamed cores are also possible.
- biopolymer admixture can provide a higher flow or lower viscosity compared to typical mixtures that use dried fibers with a thermoactive material. This can allow for processing with significantly lower pressures during extrusion or injection molding. For example, pressures of compression molding a conventional fiber/polymer material can typically fall in the 500-1000 psi range. In contrast, in an embodiment, the present biopolymer can reach maximum density at less than 150 psi. In an embodiment, motor load for processing the present biopolymer can be decreased from 50% for conventional polymer to 10% for the present polymer.
- the lower compression pressure requirement of embodiments of the present biopolymer can allow for significant changes to the engineering and structure of pressing or extrusion equipment for the biopolymer and lower the costs of such equipment.
- equipment for processing the biopolymer can also be configured with lower processing temperature.
- processing temperature can be reduced from 400 degrees Fahrenheit for conventional polymer to 320 degrees Fahrenheit for an embodiment of the present biopolymer.
- Biopolymer ingredients and manufacturing processes can be manipulated to achieve desired combinations of properties. Properties that can be considered include density, surface hardness, shear strength and bending properties, retention force (for retaining nails, screws, or other fasteners), strip-out properties, coefficient of thermal expansion, and Young's modulus.
- structural parameters can be manipulated by altering the percentage of fermentation solids in the biopolymer.
- Embodiments of structural members that include biopolymer material can be used to build a variety of structures, including pillars, rails, and decking systems, and can be used in a variety of places, including porches, patios, entryways, gardens, lawns, or as accents.
- pillars and rails can be used as a component of a decking system.
- a pillar is made from a base, corners, panels, and a top cap.
- a base can be configured to slide over a post that is coupled or secured to the ground or another structure.
- a post is not required, it can provide advantageous structural support.
- a plurality of panels can be interconnected by a plurality of corners to form a pillar.
- four panels and four pillars can be used to create a rectangular pillar.
- other pillar shapes can be formed, such as triangles, pentagons, hexagons, heptagons, octagons, and so on. Irregular pillars are also possible: Neither the panels nor the corners that shape the pillar need to be the same size.
- a pillar can be configured to slide over or otherwise couple to a post.
- the pillar can further be coupled to the base.
- the pillar can be secured to the post, or the base can be secured to the post.
- a top cap can then be mounted or otherwise coupled to the post and/or to the pillar.
- the top cap can be in a variety of different forms, including functional or aesthetically pleasing forms.
- the top cap is shaped as a generally horizontal member having an inner body portion and first and second outer ends and first and second generally vertical members that are spaced apart and disposed inwardly from said first and second ends of the horizontal member.
- the column can be hollow, filled, partially filled, or internally foamed.
- the column can have a hollow interior.
- the column can have a partially filled interior, such as when the post is secured to the top cap but there is a distance or void between one or more panels and the post.
- the column can have an entirely filled interior, such as when the post is secured to the top cap and is also touching the panels.
- the column can include a solid shell and a foamed, webbed, or strutted interior, or a combination thereof. The invention is not limited to these possible embodiments.
- the panel can be a decorative element, with a desirable color, material, texture, or the like.
- the panel can be a transparent or translucent material, such as stained glass or a printed glass or plastic material that gives the appearance of stained glass.
- a light source can be positioned within the pillar or column and can be configured to illuminate the transparent or translucent panel.
- the light source is in the space between the pillar and the post.
- the corner component can form a frame for the decorative panel.
- the railing is formed from balusters and rails.
- a plurality of balusters are placed between a top rail and a bottom rail and then secured to the top and bottom rails.
- a rail cover can then be secured to the top rail to make the railing.
- the structural members can be made in whole or in part of a variety of materials, including biopolymer, wood, glass, and composite materials, and can be metalized with brass, bronze, chrome, or gun metal for unique looks and styles.
- the top caps can also made of glass or other transparent or translucent material and lighted from the inside. Other lighting arrangements are also possible.
- the structural members can take a variety of shapes. For example, the structural members can have rounded or sharp edges, and can be circular or polygons.
- the structural members can be made in a variety of ways, including injection molding or extrusion.
- the structural members can also be secured in a variety of ways, including by being screwed, nailed, glued, snapped, or fastened. Biopolymer components can be thermowelded together. Thermowelds can be smoothed or otherwise featured with a knife, router or other tool to provide a pleasing appearance.
- FIGS. 1-14 illustrate examples of structural embodiments that can be formed from or include the present biopolymer.
- FIG. 1 is a front perspective view of an embodiment of a decking system that can be made of a corner 1 , a panel 2 , a baluster 3 , a rail 4 , a rail cover 5 , a base 6 , and a top cap 7 .
- a pillar can include a corner 1 , a panel 2 , a base 6 , and a top cap 7 , and can be secured to a railing, which can be made up of a baluster 3 , rail 4 , and rail cover 5 , as shown in FIG. 1 .
- FIG. 2 shows a front view of a base component where a base 6 can slide over a post 8 .
- a fastener such as screw 9 , can secure a base 6 to a post 8 .
- a plurality of panels 2 can be interconnected by a plurality of corners 1 to form a rectangular pillar.
- a pillar can slide over a post 8 and can be mounted on a base 6 as shown in FIG. 3 .
- a top cap 7 can be mounted to a post 8 to form the pillar as shown in FIG. 4 .
- FIG. 5 is a front view of a railing assembly.
- a plurality of balusters 3 can be placed between a top rail 4 and a bottom rail 4 as shown in FIG. 5 .
- a baluster 3 can be connected to a top rail 4 and a bottom rail 4 by, for example, a screw 10 , as shown in FIG. 6 .
- a rail cover 5 can be mounted on a top rail 4 of an assembling railing to make a railing as shown in FIG. 7 .
- FIGS. 8-14 Embodiments of structural components that can be used to form the structure in FIGS. 1-7 are shown in FIGS. 8-14 .
- FIG. 8 is a perspective view of a base 6 .
- FIG. 9 is a top view of a panel component 2 .
- FIG. 10 is a cross-sectional view of a corner 1 .
- FIG. 11 is a perspective view of a top cap 7 .
- FIG. 12 is a top view of a baluster 3 .
- FIG. 13 is a side view of a bottom rail 4 .
- FIG. 14 s a side view of a rail cover 5 .
- the biopolymer can be treated for appearance during or after forming.
- the die or other surface used in forming can form a textured surface on the biopolymer article. Extruding can co-extrude an appearance layer of polymer or other material with a biopolymer core.
- the formed biopolymer can be treated with a multi roller printing process to impart the look of real wood or other desired printed textures or colors.
- the formed biopolymer can be treated with a thermosetting powder.
- the thermosetting powder can be, for example, clear, semi-transparent, or fully pigmented.
- the powder can be heat cured, which can form a coating suitable for interior or exterior uses.
- the powder can also be textured to provide, for example, a natural wood look and texture.
- the biopolymer products can be powder coated, embossed, and/or printed to provide desired surface properties such as weatherability and UV-resistance and/or surface effects such as wood grain colors and textures.
- a biopolymer product can be formed with a protective layer.
- a biopolymer product can be coated with a thermosetting powder that is baked on to cure the powder into a high performance coating.
- the powder can for example be polyester, epoxy, acrylates, or other polymers or thermoactive material, or a combination thereof.
- the coating can be clear, semi-transparent, or fully pigmented.
- the powder coated biopolymer product can be baked in an infrared or IR/UV oven. Such a coated product can be appropriate for both internal and exterior use.
- a thin layer of resin or other material can be added to a surface.
- An embodiment of one or more components of a column and rail system for example, can be fabricated with a protective resin layer to enhance weatherability. Addition of a surface layer can also be useful in other applications, including for example interior applications where exposure to cleaning agents can occur (e.g. tub or shower areas), and exterior applications such as building trim, shutters, lawn and garden equipment, decorative panels and signs, patio furniture, or column and rail system.
- a biopolymer product can be vinyl wrapped or metal wrapped.
- Biopolymer products can be given a wood appearance and/or texture (or other texture/appearance) through processing such as embossing or printing, or by co-extruding an outer layer with the biopolymer.
- Column and rail system assemblies for example, can be patterned with a wood grain appearance or texture.
- Other wood-replacement products can similarly be processed to resemble particular woods (or stained woods) in texture and color.
- the biopolymer product can be run through a multiroller printing process to impart the look of real wood or other desired printed textures or colors, such as stucco, concrete, bricks, stone, tile, clay, or metal.
- an extrusion can be directly printed using a gravure printing process or an embossing wheel.
- the combination of color and texture can create a natural wood look and feel.
- Other printing process also can be used, including direct computer imagery.
- printing or other methods can create realistic wood textures such as maple, oak, cherry, cedar or other desired prints and textures.
- the biopolymer material can be placed in a thermal plated press during the curing process both to impart faster curing and to impress a texture onto the surface of the end product.
- an exterior product can be formed using fermentation solids in conjunction with a powder coating for exterior products.
- the exterior product can be printed with a desired appearance and/or textured in a press with a texture plate to form an exterior grade textured surface.
- similar processes can be employed to generate a rough-service product.
- the biopolymer can be printed and then coated to protect the printed surface.
- the biopolymer may be digitally printed for example, to impart a desired appearance such as the grain of a particular wood, such as cherry.
- the biopolymer may then be powder coated to protect the printed surface.
- the biopolymer may be powder coated with a clear layer to allow the printed surface to show through.
- an outer layer is applied to the product.
- the outer layer can for example be a veneer, a wood grain covering, a pigmented covering, or another type of co-extruded layer.
- the outer layer can provide a desired color, appearance, texture, weatherability, or other property.
- the biopolymer can be made to look like granite.
- the biopolymer can include visible particles of remaining fermentation solid.
- Such a composite biopolymer can result in a matrix of one appearance surrounding particles with a different appearance, giving the appearance of granite.
- a significant fraction of the fermentation solid can be blended into and/or bonded with the thermoactive material.
- particulate matter can be added to the biopolymer.
- Embodiments including particulate matter can be formed to simulate the appearance of granite or other stones, or natural wood grains such as burled wood.
- particulate can be fused into a biopolymer product for example by mixing in the particular during extrusion molding or compression molding.
- particulate does not dissolve into the polymer but remains distinct, so that the particulate matter is visible to the naked eye.
- particulate can be combined in a polymer to give a desired aggregate appearance.
- the biopolymer with aggregate matter can be machined, cut, drilled, or otherwise processed. Further description of polymer-particulate material is provided in U.S. Pat. No. 5,635,123, which is incorporated by reference.
- the phrase “adapted and configured” describes a system, apparatus, or other structure that is constructed or configured to perform a particular task or adopt a particular configuration to.
- the phrase “adapted and configured” can be used interchangeably with other similar phrases such as arranged and configured, constructed and arranged, adapted, constructed, manufactured and arranged, and the like.
Abstract
The present invention relates generally to structures formed from a biopolymer. The present invention more particularly relates to biopolymer structures and components formed from fermentation solids and thermoactive materials, including a column and rail system and the component parts of this system.
Description
- This application claims priority to U.S. Provisional Patent Application Ser. No. 60/478,247 filed Jun. 13, 2003, 60/478,248 filed Jun. 13, 2003, and 60/478,601 filed Jun. 13, 2003.
- The present invention relates generally to structures formed from a biopolymer. The present invention more particularly relates to biopolymer structures and components formed from fermentation solids and thermoactive materials, including a column and rail system and the component parts of this system.
- A variety of products may be formed from filled plastics. For example, plastics may be formed into lumber replacements, as described in U.S. Pat. No. 5,539,027; components of window and door assemblies, as described in U.S. Pat. No. 5,486,553; or siding for building structures, as described in U.S. Pat. No. 6,122,877.
- Fillers have been used in the plastic industry for almost 90 years. The reason most manufacturers use filled plastic is to reduce the price of the high cost of polypropylene and other plastics with lower cost fillers, such as wood flour, talc, and mica, and fiberglass. Filling plastic with fiberglass can improve its characteristics by creating higher thermal stability and higher bending and rupture strengths. However, low cost fillers like wood flour can degrade some of the qualities of plastics and make it harder to process. Talc and mica provide some increase in strength to plastic, but also add weight and decrease the life of the extruder due to abrasion. Fiberglass adds considerable strength of the product, but at a substantial cost.
- There are many disadvantages associated with existing plastics filled with plant material, such, such as wood or straw. A principal problem associated with the extrusion and injection of such plastics is that the particle size of the plant material used in this process is very small and is primarily ground wood. Otherwise, the viscosity of the mixture is too high to be extruded or molded efficiently. Moreover, extrusion or injection processes are further limited by the ratio of filler materials, such as wood, to the plastic that can be used. This puts undesirable constraints on the products that can be produced. Wood plastic composites typically use between 30% to 65% wood flour or fine wood saw dust mixed with simple plastics. Ratios higher than this cause both processing problems and overall performance degradation in areas of moisture absorption, rot, decay, moisture stability, and so on.
- There remains a need for an inexpensive, biologically derived material that can reduce the cost and consumption of thermoactive materials and that performs better than a filler for products such as window and door assemblies, lumber replacements, siding for buildings, column and rail systems, and other goods.
- The present invention relates generally to structures formed from a biopolymer. The present invention more particularly relates to biopolymer structures and components formed from fermentation solids and thermoactive materials, including a column and rail system and the component parts of this system. The column system can include one or more independent panels and corner components that can be coupled to a base, a post, top cap, or any combination thereof. The rail system can include a top rail assembly including a top rail and a rail cover. The column can include a base, a pillar, and a post, where the post can be coupled to the base, the pillar, or both. The pillar can include a plurality of corners, and a plurality of panels coupled to the corners. A top cap can also be coupled to the pillar. The railing segment can comprise at least one baluster connected to rails, and can include a rail cover. The railing segment can then be coupled to the column.
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FIG. 1 is a front perspective view of a decking system. -
FIG. 2 is a front perspective view of a base component and a post. -
FIG. 3 is a front perspective view of a pillar and a base component. -
FIG. 4 is a front perspective view of a pillar, a base component, and a top cap. -
FIG. 5 is a front perspective view of components of a railing assembly. -
FIG. 6 is a side view of components a railing assembly. -
FIG. 7 is a side view of a railing assembly with a railing cover. -
FIG. 8 is a perspective view of a base. -
FIG. 9 is a top view of a panel component. -
FIG. 10 is a cross-sectional view of a corner. -
FIG. 11 is a perspective view of a top cap. -
FIG. 12 is a top view of a baluster. -
FIG. 13 is a side view of a bottom rail. -
FIG. 14 is a side view of a rail cover. -
FIG. 15 illustrates a method for processing a biopolymer composition. -
FIG. 16 illustrates a method for forming an article from a biopolymer. - Overview
- The present invention relates to articles fabricated from or including biopolymers including fermentation solid and thermoactive material. The present biopolymer can exhibit properties typical of plastic materials, properties advantageous compared to conventional plastic materials, and/or properties advantageous compared to aggregates including plastic and, for example, wood or cellulosic materials. The present biopolymer can be formed into useful articles using any of a variety of conventional methods for forming items from plastic.
- The present biopolymer can take any of a variety of forms. U.S. patent application Ser. No. ______ entitled “BIOPOLYMER AND METHODS OF MAKING IT” and filed evendate herewith describes the present biopolymer and related methods. This application is incorporated herein by reference.
- Definitions
- As used herein, the term “biopolymer” refers to a material including a thermoactive material and a fermentation solid.
- As used herein, the phrase “fermentation solid” refers to solid material recovered from a fermentation process, such as alcohol (e.g., ethanol) production.
- As used herein, the phrase “fermented protein solid” refers to fermentation solid recovered from fermenting a material including protein. The fermented protein solid also includes protein.
- As used herein, the phrase “distiller's dried grain” (DDG) refers to the dried residue remaining after the starch in grain (e.g., corn) has been fermented with selected yeasts and enzymes to produce products including ethanol and carbon dioxide. DDG can include residual amounts of solubles, for example, about 2 wt-%. Distiller's dried grain includes compositions known as brewer's grain and spent solids.
- As used herein, the phrase “distiller's dried grain with solubles” (DDGS) refers to a dried preparation of the coarse material remaining after the starch in grain (e.g., corn) has been fermented plus the soluble portion of the residue remaining after fermentation, which has been condensed by evaporation to produce solubles. The solubles can be added to the DDG to form DDGS.
- As used herein, the phrase “wet cake” or “wet distiller's grain” refers to the coarse, wet residue remaining after the starch in grain (e.g., corn) has been fermented with selected yeasts and enzymes to produce products including ethanol and carbon dioxide.
- As used herein, the phrase “solvent washed wet cake” refers to wet cake that has been washed with a solvent such as, water, alcohol, or hexane.
- As used herein, the phrase “gluten meal” refers to a by-product of the wet milling of plant material (e.g., corn, wheat, or potato) for starch. Corn gluten meal can also be a by-product of the conversion of the starch in whole or various fractions of dry milled corn to corn syrups. Gluten meal includes prolamin protein and gluten (a mixture of water-insoluble proteins that occurs in most cereal grains) and also smaller amounts of fat and fiber.
- As used herein, the phrase “plant material” refers to all or part of any plant (e.g., cereal grain), typically a material including starch. Suitable plant material includes grains such as maize (corn, e.g., whole ground corn), sorghum (milo), barley, wheat, rye, rice, millet, oats, soybeans, and other cereal or leguminous grain crops; and starchy root crops, tubers, or roots such as sweet potato and cassaya. The plant material can be a mixture of such materials and byproducts of such materials, e.g., corn fiber, corn cobs, stover, or other cellulose and hemicellulose containing materials such as wood or plant residues. Preferred plant materials include corn, either standard corn or waxy corn. Preferred plant materials can be fermented to produced fermentation solid.
- As used herein, the term “prolamin” refers to any of a group of globular proteins which are found in plants, such as cereals. Prolamin proteins are generally soluble in 70-80 percent alcohol but insoluble in water and absolute alcohol. These proteins contain high levels of glutamic acid and proline. Suitable prolamin proteins include gliadin (wheat and rye), zein (corn), and kafirin (sorghum and millet). Suitable gliadin proteins include α-, β-, γ-, and ω-gliadins.
- As used herein, the term “zein” refers to a prolamin protein found in corn, with a molecular weight of about 40,000 (e.g., 38,000), and not containing tryptophan and lysine.
- As used herein, the phrase “glass transition point” or “Tg” refers to the temperature at which a particle of a material (such as a fermentation solid or thermoactive material) reaches a “softening point” so that it has a viscoelastic nature and can be more readily compacted. Below Tg a material is in its “glass state” and has a form that can not be as readily deformed under simple pressure. As used herein, the phrase “melting point” or “Tm” refers to the temperature at which a material (such as a fermentation solid or thermoactive material) melts and begins to flow. Suitable methods for measuring these temperatures include differential scanning calorimetry (DSC), dynamic mechanical thermal analysis (DTMA), and thermal mechanical analysis (TMA).
- As used herein, weight percent (wt-%), percent by weight, % by weight, and the like are synonyms that refer to the concentration of a substance as the weight of that substance divided by the weight of the composition and multiplied by 100. Unless otherwise specified, the quantity of an ingredient refers to the quantity of active ingredient.
- As used herein, the term “about” modifying any amount refers to the variation in that amount encountered in real world conditions of producing materials such as polymers or composite materials, e.g., in the lab, pilot plant, or production facility. For example, an amount of an ingredient employed in a mixture when modified by about includes the variation and degree of care typically employed in measuring in a plant or lab producing a material or polymer. For example, the amount of a component of a product when modified by about includes the variation between batches in a plant or lab and the variation inherent in the analytical method. Whether or not modified by about, the amounts include equivalents to those amounts. Any quantity stated herein and modified by “about” can also be employed in the present invention as the amount not modified by about.
- The Biopolymer
- The present biopolymer includes fermentation solid and thermal active material. The biopolymer can take any of a variety of forms. In an embodiment, the present biopolymer includes fermentation solid integrated with the thermoactive material, which form is referred to herein as an “integrated biopolymer”. In an embodiment, the integrated biopolymer forms a uniform mass in which the fermentation solid has been blended into the thermoactive material. In an embodiment, the present biopolymer includes features of the integrated biopolymer but has visible particles of remaining fermentation solid, which form is referred to herein as a “composite biopolymer”. A composite biopolymer can have a granite-like appearance with a matrix of thermoactive material with a first appearance surrounding particles of fermentation solid with a second appearance. In yet another embodiment, the present biopolymer includes a significant portion of fermentation solid present as discrete particles surrounded by or embedded in the thermoactive material, which form is referred to herein as an “aggregate biopolymer”.
- In an embodiment, the compounded fermentation solid and thermoactive material (i.e., the soft or raw biopolymer), before hardening, takes the form of a dough, which can be largely homogeneous. As used herein, “largely homogeneous” dough refers to a material with a consistency similar to baking dough (e.g., bread or cookie dough) with a major proportion of the fermentation solid blended into the thermoactive material and no longer appearing as distinct particles. In an embodiment, the soft or raw biopolymer includes no detectable particles of fermentation solid, e.g., it is a homogeneous dough. In an embodiment, the soft or raw biopolymer can include up to 95 wt-% (e.g., 90 wt-%) fermentation solid and take the form of a largely homogeneous or homogeneous dough. In an embodiment, the soft or raw biopolymer can include about 50 to about 70 wt-% fermentation solid and take the form of a largely homogeneous or homogeneous dough.
- In an embodiment, the raw or soft biopolymer includes visible amounts of fermentation solid. As used herein, visible amounts of fermentation solid refers to particles that are clearly visible to the naked eye and that provide a granite-like appearance to the cured biopolymer. Such visible fermentation solid can be colored for decorative effect in the cured biopolymer. The granite-like appearance can be produced by employing larger particles of fermentation solid than used to produce a homogeneous or largely homogeneous dough.
- In certain embodiments, the biopolymer can include fermentation solid at about 0.01 to about 95 wt-%, about 1 to about 95 wt-%, about 5 to about 95 wt-%, about 5 to about 80 wt-%, about 5 to about 70 wt-%, about 5 to about 20 wt-%, about 50 to about 95 wt-%, about 50 to about 80 wt-%, about 50 to about 70 wt-%, about 50 to about 60 wt-%, about 60 to about 80 wt-%, or about 60 to about 70 wt-%. In certain embodiments, the biopolymer can include fermentation solid at about 5 wt-%, about 10 wt-%, about 20 wt-%, about 50 wt-%, about 60 wt-%, about 70 wt-%, or about 75 wt-%. The present biopolymer can include any of these amounts or ranges not modified by about.
- In certain embodiments, the biopolymer can include thermoactive material at about 0.01 to about 95 wt-%, about 1 to about 95 wt-%, about 5 to about 30 wt-%, about 5 to about 40 wt-%, about 5 to about 50 wt-%, about 5 to about 85 wt-%, about 5 to about 95 wt-%, about 10 to about 30 wt-%, about 10 to about 40 wt-%, about 10 to about 50 wt-%, or about 10 to about 95 wt-%. In certain embodiments, the biopolymer can include thermoactive material at about 95 wt-%, about 75 wt-%, about 50 wt-%, about 45 wt-%, about 40 wt-%, about 35 wt-%, about 30 wt-%, about 25 wt-%, about 20 wt-%, about 15 wt-%, about 10 wt-%, or about 5 wt. The present biopolymer can include any of these amounts or ranges not modified by about.
- In certain embodiments, the biopolymer can include fermentation solid at about 5 to about 95 wt-% and thermoactive material at about 5 to about 95 wt-%, can include fermentation solid at about 50 to about 70 wt-% and thermoactive material at about 30 to about 70 wt-%, can include fermentation solid at about 50 to about 70 wt-% and thermoactive material at about 20 to about 70 wt-%, can include fermentation solid at about 50 to about 60 wt-% and thermoactive material at about 30 to about 50 wt-%, or can include fermentation solid at about 60 to about 70 wt-% and thermoactive material at about 20 to about 40 wt-%. In certain embodiments, the biopolymer can include about 5 wt-% fermentation solid and about 70 to about 95 wt-% thermoactive material, about 10 wt-% fermentation solid and about 70 to about 90 wt-% thermoactive material, about 50 wt-% fermentation solid and about 30 to about 50 wt-% thermoactive material, about 55 wt-% fermentation solid and about 30 to about 45 wt-% thermoactive material, about 60 wt-% fermentation solid and about 20 to about 40 wt-% thermoactive material, about 65 wt-% fermentation solid and about 20 to about 40 wt-% thermoactive material, about 70 wt-% fermentation solid and about 10 to about 30 wt-% thermoactive material, about 90 wt-% fermentation solid and about 5 to about 10 wt-% thermoactive material. The present biopolymer can include any of these amounts or ranges not modified by about.
- Fermentation Solids
- The present biopolymer can include any of a variety of fermentation solids. Fermentation solid can be recovered from any of a variety of fermentation processes, such as alcohol (e.g., ethanol) production. A fermentation solid can be recovered from, for example, fermentation of plant material. Numerous fermentation solids have been characterized, primarily as animal feed. The fermentation solids that have been characterized include those known as distiller's dried grain (DDG), distiller's dried grain with solubles (DDGS), wet cake (WC), solvent washed wet cake (WWC), fractionated distiller's dried grain (FDDG), and gluten meal. Fermentation solid can include, for example, protein, fiber, and, optionally, fat. Fermentation solid can also include residual starch.
- Distiller's dried grains or other distiller's dried plant materials can be derived from any of a variety of agricultural products. As used herein, “distiller's dried” followed by the name of a plant or type of plant refers to a fermentation solid derived from fermentation of that plant or type of plant. For example, distiller's dried grain refers to a fermentation solid derived from fermentation of grain. By way of a more specific example, distiller's dried corn refers to a fermentation solid derived from fermentation of corn. Distiller's dried sorghum refers to a fermentation solid derived from fermentation of sorghum (milo). Distiller's dried wheat refers to a fermentation solid derived from fermentation of wheat. A distiller's dried plant material need not be exclusively derived from the named plant material. Rather, the named plant material is the predominant plant material or the only plant material in the fermentation solid.
- The present biopolymer can include any of a variety of fermentation solids including, for example, distiller's dried grain, distiller's dried starchy root crop, distiller's dried tuber, and distiller's dried root. Suitable distiller's dried grains include distiller's dried cereal grain and distiller's dried legume. Suitable distiller's dried grains include distiller's dried maize (distiller's dried corn, e.g., distiller's dried whole ground corn or distiller's dried fractionated corn), distiller's dried sorghum (milo), distiller's dried barley, distiller's dried wheat, distiller's dried rye, distiller's dried rice, distiller's dried millet, distiller's dried oats, distiller's dried soybean. Suitable distiller's dried roots include distiller's dried sweet potato and distiller's dried cassaya. Suitable distiller's dried tubers include distiller's dried potato.
- A fermentation solid derived from fractionated plant material is referred to herein as distiller's dried fractionated plant material, e.g., distiller's dried fractionated grain. The present biopolymer can include any of a variety of fractionated fermentation solids. For example, the present biopolymer can include distiller's dried fractionated corn. For example, the present biopolymer can include distiller's dried corn germ and/or distiller's dried corn endosperm.
- In certain embodiments, the present fermentation solid (e.g., fermented protein isolate) reached a temperature (e.g., at the exit from the dryer) of no higher than about 500° F., about 400° F., about 300° F., about 250° F., about 200° F., or about 180° F. In an embodiment, the present fermentation solid (e.g., fermented protein isolate) reached a temperature (e.g., at the exit from the dryer) of no higher than about 500° F. In an embodiment, the present fermentation solid (e.g., fermented protein isolate) reached a temperature (e.g., at the exit from the dryer) of no higher than about 400° F. In an embodiment, the present fermentation solid (e.g., fermented protein isolate) reached a temperature (e.g., at the exit from the dryer) of no higher than about 300° F. In an embodiment, the present fermentation solid (e.g., fermented protein isolate) reached a temperature (e.g., at the exit from the dryer) of no higher than about 250° F. In an embodiment, the present fermentation solid (e.g., fermented protein isolate) reached a temperature (e.g., at the exit from the dryer) of no higher than about 200° F. In an embodiment, the present fermentation solid (e.g., fermented protein isolate) reached a temperature (e.g., at the exit from the dryer) of no higher than about 180° F. The present fermentation solid can include any of these temperatures not modified by about.
- As used herein, “distiller's dried” followed by a number refers to a fermentation solid that reached a temperature (e.g., at the exit from the dryer) at or below that temperature. For example, distiller's dried grain-200 refers to distiller's dried grain that reached a temperature (e.g., at the exit from the dryer) at or below 200° F. In certain distillation processes, the plant material can also be ground. Grinding can subject plant material to elevated temperatures. As used herein, “distiller's dried” followed by a number with the suffix “gd” refers to a fermentation solid that was ground and dried reaching a temperature (e.g., at the exit from the dryer) at or below that temperature. For example, distiller's dried grain-200gd refers to distiller's dried grain ground and dried and that reached a temperature (e.g., at the exit from the dryer) at or below 200° F. A fermentation solid that has been prepared by employing low temperature grinding and/or drying is referred to herein as “gently treated fermentation solid”. A fermented protein solid that has been prepared by employing low temperature grinding and/or drying is referred to herein as “proteinaceous fermentation solid”. Suitable gently treated fermentation solids include gently treated DDG and gently treated DDGS. Gently treated fermentation solids include those derived from fermentation processes lacking a cooking stage.
- The present biopolymer can include or can be made from a fermentation solid with any of broad range of sizes. In certain embodiments, the fermentation solid employed in the biopolymer has a particle size of about 2 mesh to less than about 1 micron, about 2 to about 10 mesh, about 12 to about 500 mesh, about 60 mesh to less than about 1 micron, about 60 mesh to about 1 micron, about 60 to about 500 mesh.
- Thermoactive Material
- The biopolymer can include any of a wide variety of thermoactive materials. For example, the biopolymer can include any thermoactive material in which the fermentation solid can be embedded. In an embodiment, the thermoactive material can be selected for its ability to form a homogeneous or largely homogeneous dough including the fermentation solid. In an embodiment, the thermoactive material can be selected for its ability to covalently bond with the fermentation solid. In an embodiment, the thermoactive material can be selected for its ability to flow when mixed or compounded with fermentation solid. In an embodiment, the thermoactive material can set after being formed. Numerous such thermoactive materials are commercially available.
- Suitable thermoactive materials include thermoplastic, thermoset material, a resin and adhesive polymer, or the like. As used herein, the term “thermoplastic” refers to a plastic that can once hardened be melted and reset. As used herein, the term “thermoset” material refers to a material (e.g., plastic) that once hardened cannot readily be melted and reset. As used herein, the phrase “resin and adhesive polymer” refers to more reactive or more highly polar polymers than thermoplastic and thermoset materials.
- Suitable thermoplastics include polyamide, polyolefin (e.g., polyethylene, polypropylene, poly(ethylene-copropylene), poly(ethylene-coalphaolefin), polybutene, polyvinyl chloride, acrylate, acetate, and the like), polystyrenes (e.g., polystyrene homopolymers, polystyrene copolymers, polystyrene terpolymers, and styrene acrylonitrile (SAN) polymers), polysulfone, halogenated polymers (e.g., polyvinyl chloride, polyvinylidene chloride, polycarbonate, or the like, copolymers and mixtures of these materials, and the like. Suitable vinyl polymers include those produced by homopolymerization, copolymerization, terpolymerization, and like methods. Suitable homopolymers include polyolefins such as polyethylene, polypropylene, poly-1-butene, etc., polyvinylchloride, polyacrylate, substituted polyacrylate, polymethacrylate, polymethylmethacrylate, copolymers and mixtures of these materials, and the like. Suitable copolymers of alpha-olefins include ethylene-propylene copolymers, ethylene-hexylene copolymers, ethylene-methacrylate copolymers, ethylene-methacrylate copolymers, copolymers and mixtures of these materials, and the like. In certain embodiments, suitable thermoplastics include polypropylene (PP), polyethylene (PE), and polyvinyl chloride (PVC), copolymers and mixtures of these materials, and the like. In certain embodiments, suitable thermoplastics include polyethylene, polypropylene, polyvinyl chloride (PVC), low density polyethylene (LDPE), copoly-ethylene-vinyl acetate, copolymers and mixtures of these materials, and the like.
- Suitable thermoset materials include epoxy materials, melamine materials, copolymers and mixtures of these materials, and the like. In certain embodiments, suitable thermoset materials include epoxy materials and melamine materials. In certain embodiments, suitable thermoset materials include epichlorohydrin, bisphenol A, diglycidyl ether of 1,4-butanediol, diglycidyl ether of neopentyl glycol, diglycidyl ether of cyclohexanedimethanol, aliphatic; aromatic amine hardening agents, such as triethylenetetraamine, ethylenediamine, N-cocoalkyltrimethylenediamine, isophoronediamine, diethyltoluenediamine, tris(dimethylaminomethylphe-nol); carboxylic acid anhydrides such as methyltetrahydrophthalic anhydride, hexahydrophthalic anhydride, maleic anhydride, polyazelaic polyanhydride and phthalic anhydride, mixtures of these materials, and the like.
- Suitable resin and adhesive polymer materials include resins such as condensation polymeric materials, vinyl polymeric materials, and alloys thereof. Suitable resin and adhesive polymer materials include polyesters (e.g., polyethylene terephthalate, polybutylene terephthalate, and the like), methyl diisocyanate (urethane or MDI), organic isocyanide, aromatic isocyanide, phenolic polymers, urea based polymers, copolymers and mixtures of these materials, and the like. Suitable resin materials include acrylonitrile-butadiene-styrene (ABS), polyacetyl resins, polyacrylic resins, fluorocarbon resins, nylon, phenoxy resins, polybutylene resins, polyarylether such as polyphenylether, polyphenylsulfide materials, polycarbonate materials, chlorinated polyether resins, polyethersulfone resins, polyphenylene oxide resins, polysulfone resins, polyimide resins, thermoplastic urethane elastomers, copolymers and mixtures of these materials, and the like. In certain embodiments, suitable resin and adhesive polymer materials include polyester, methyl diisocyanate (urethane or MDI), phenolic polymers, urea based polymers, and the like.
- Suitable thermoactive materials include polymers derived from renewable resources, such as polymers including polylactic acid (PLA) and a class of polymers known as polyhydroxyalkanoates (PHA). PHA polymers include polyhydroxybutyrates (PHB), polyhydroxyvalerates (PHV), and polyhydroxybutyrate-hydroxyvalerate copolymers (PHBV), polycaprolactone (PCL) (i.e. TONE), polyesteramides (i.e. BAK), a modified polyethylene terephthalate (PET) (i.e. BIOMAX), and “aliphatic-aromatic” copolymers (i.e. ECOFLEX and EASTAR BIO), mixtures of these materials and the like.
- Additives
- The present biopolymer can also include one or more additives. Suitable additives include one or more of dye, pigment, other colorant, hydrolyzing agent, plasticizer, filler, extender, preservative, antioxidants, nucleating agent, antistatic agent, biocide, fungicide, fire retardant, flame retardant, heat stabilizer, light stabilizer, conductive material, water, oil, lubricant, impact modifier, coupling agent, crosslinking agent, blowing or foaming agent, reclaimed or recycled plastic, and the like, or mixtures thereof. Suitable additives include plasticizer, light stabilizer, coupling agent, and the like, or mixtures thereof. In certain embodiments, additives can tailor properties of the present biopolymer for end applications. In an embodiment, the present biopolymer can optionally include about 1 to about 20 wt-% additive.
- Methods of Making the Biopolymer
- The present biopolymer can be made by any of a variety of methods that can mix thermoactive material and fermentation solid. In an embodiment, the thermoactive material and fermentation solid are compounded. As used herein, the verb “compound” refers to putting together parts so as to form a whole and/or forming by combining parts (e.g., thermoactive material and fermentation solid). The fermentation solid can be compounded with any of a variety of thermoactive materials, such as thermoset and thermoplastic materials. Any of a variety of additives or other suitable materials can be mixed or compounded with the fermentation solid and thermoactive material to make the present biopolymer. In an embodiment, compounding fermentation solid and thermoactive material produces the dough-like material described hereinabove.
- Compounding can include one or more of heating the fermentation solid and thermoactive material, mixing (e.g., kneading) the fermentation solid and thermoactive material, and crosslinking the fermentation solid and thermoactive material. Compounding can include thermal kinetic compounding, extruding, high shear mixing compounding, or the like. In an embodiment, the fermentation solid and thermoactive material are compounded in the presence of hydrolyzing agent.
- The biopolymer or biopolymer dough can be formed by melting together the fermentation solid and the thermoactive material. In contrast, thermal kinetic compounding of wood particles and thermoactive material produces a material in which wood particles are easily seen as individual particles suspended in the plastic matrix or as wood particles coated with plastic. Advantageously, the compounded fermentation solid and thermoactive material can be an integrated mass that is homogenous or nearly so.
- The compounded, raw or soft biopolymer can be used directly or can be formed as pellets, granules, or another convenient form for converting to articles by molding or other processes.
- Thermal Kinetic Compounding
- Thermal Kinetic Compounding (“TKC”) can mix and compound employing high speed thermal kinetic principals. Thermal kinetic compounding includes mixing two or more components with high shear speeds using an impeller. Suitable thermal kinetic compounding apparatus are commercially available, for example, the Gelimat G1 (Draiswerke Company). Such a system can include a computer controlled metering and weight batch system.
- An embodiment of a thermal kinetic compounding apparatus includes a horizontally positioned mixer and compounding chamber with a central rotating shaft. Several staggered mixing elements are mounted to the shaft at different angles. The specific number and positions of the mixing blades varies with the size of the chamber. A pre-measured batch of thermoactive material and fermentation solid can be fed in to the compounder, for example, via an integrated screw that can be part of the rotor shaft. Alternatively, the thermoactive material and fermentation solid can be fed through a slide door, located on the mixer body. The apparatus can include an automatically operated discharge door at the bottom of the compounding chamber.
- In the compounding chamber, the thermoactive material and fermentation solid is subject to high turbulence, due to high tip-speed of the mixing element. The thermoactive material and fermentation solid are well mixed and also subjected to temperature increase from impact against the chamber wall, mixing blades, and the material particles themselves. The friction in the moving particles can rapidly increase temperature and remove moisture. Thermal kinetic compounding can include compounding the quantities or concentrations listed above for the fermentation solid and thermoactive materials in batch size suitable for the apparatus.
- The compounded thermoactive material and fermentation solid, the biopolymer, can then be run through a regrinding process to produce uniform granular materials. Such regrinding can employ a standard knife grinding system using a screen, which can create smaller uniform particles of a similar size and shape. Such granular materials can be used in, for example, extrusion, injection molding, and other plastic processing.
- Compounding by Extruding
- The present biopolymer can be formed by any of a variety of extruding processes suitable for mixing or compounding fermentation solid and thermoactive material. For example, conventional extruding processes, such as twin screw compounding, can be employed to make the present biopolymer. Compounding by extruding can provide a higher internal temperature within the extruder and promote the interaction of thermoplastics with the fermentation solid. Twin screw compounding can employ co- or counter-rotating screws. The extruder can include vents that allow escape of moisture or volatiles from the mixture being compounded.
- Forming Biopolymer into Products
- Biopolymer material can be formed into a variety of objects and structures. In one embodiment, raw biopolymer can be formed into pellets which are fed into machinery configured to injection mold, extrude, or otherwise form or process the biopolymer. In an embodiment, pellets can be formed by first urging polymer and fermentation solids through a die to produce a linear extrusion and then cutting the extrusion into a pellet shape. In an embodiment, the pellets have a substantially uniform size and shape. The cross-section of the pellet can be any of a variety of shapes, such as square, circular, oval, rectangular, pentagonal, hexagonal, etc., as determined by depending on the shape of the extrusion die. A circular cross section can be preferred in many applications, typically with a radius of several millimeters and length of about two to four time the radius. U.S. Pat. Nos. 5,441,801, 6,280,667, and 5,746,958, which are incorporated herein by reference, further discuss processing of pellets of polymer materials. These patents disclose methods and apparatus employed for processing plastics with wood fillers. These methods and apparatus can also be employed to process and form embodiments of the present biopolymer.
- While specific biopolymer products are described hereinbelow, other products are also possible. For example, biopolymer can be used in boat hulls, playground sets, storage containers, crown molding, and the like.
- Injection Molding the Biopolymer
- Embodiments of the present biopolymer can be injection molded. In an embodiment, compounded biopolymer can be ground to form uniform pellets for use in an injection molding process. In an embodiment, the present polymer can be processed using less energy per pound than conventional thermoplastics. In an embodiment, the present biopolymer can exhibit faster heating and cooling times during injection molding compared to conventional thermoplastics. In an embodiment, the present biopolymer maintains the melt index of the plastic and allows flowability characteristics that allows high speed injection molding. For example, biopolymer including fermentation solid and polypropylene was observed to have higher thermal conductivity than pure polypropylene. Higher thermal conductivity provides faster heating and/or cooling, which can which can speed processes such as injection molding.
- Injection molding techniques are known to those skilled in the art. In an embodiment, machinery can be configured to injection mold biopolymer into a desired shape. A mold defines a shape, into which heated thermoactive material is injected. The material is then allowed to cool and subsequently ejected from the mold.
- Extruding the Biopolymer
- The present biopolymer can be extruded to form an article of manufacture employing any of a number of conventional extrusion processes. For example, the present biopolymer can be extruded by dry process extrusion. For example, the present biopolymer can be extruded using any of a variety of conventional die designs. In an embodiment, extruding the present biopolymer to form an article can include feeding the biopolymer into a material preparation auger and converting it to a size suitable for extruding. Extruding can employ any of a variety of conventional dies and any of a variety of conventional temperatures. Compounding by extruding can provide a higher internal temperature within the extruder and promote the interaction of thermoplastics with the fermentation solid. An extruder having one or more dies can be configured to form the biopolymer into a shape. The biopolymer can be urged through a die to produce a desired cross section. The extruded biopolymer can then be cut to a desired length as necessary. The biopolymer can also be allowed to harden or otherwise cured to preserve the cross-sectional shape. Extruded biopolymer can later be cut into shorter lengths as desired.
- In an embodiment, the biopolymer material can be heated above the melting point. The biopolymer can then be moved through a converging die that is heated to reduce shear stress in the biopolymer near the wall and then through a forming section to provide a desired cross section. In an embodiment, the biopolymer can then be passed through a low-friction unheated or thermally insulated section that has a cross section that is the same or similar to the cross section of the forming section to establish a cross sectional memory in the polymer and reduce swelling after extrusion. The biopolymer material can then be quenched to form a shell below the melting point. In embodiments, the shell can substantially maintain the biopolymer in the desired shape. In another embodiment, the biopolymer material can be moved through a heated converging die and then a forming section to provide a desired cross section. The biopolymer material can then be quenched to form a shell to maintain the desired shape. Further description of methods and apparatus for fabricating extrusions of thermoactive material is provided by U.S. Pat. No. 6,527,532, which is incorporated herein by reference. This patent discloses methods and apparatus employed for processing and forming plastics with wood fillers. These methods and apparatus can also be employed to process and form embodiments of the present biopolymer.
- In another embodiment, machinery can be configured to move biopolymer through a transition die and then through a stranding die to produce strands of biopolymer. Machinery can further be configured to move the strands through a molding die that combines the strands into a desired extrusion. In one embodiment, this stranding and re-bonding process can produce a product having a structure and/or appearance that is similar to the grain in wood. Methods and apparatus for stranding and re-bonding thermoactive materials are further described in U.S. Pat. No. 5,516,472, which is incorporated herein by reference. This patent discloses methods and apparatus employed for processing plastics with wood fillers or other shredded cellulosic material. These methods and apparatus can also be employed to process and form embodiments of the present biopolymer.
- Co-Extruding Materials with the Biopolymer
- Additional materials can be co-extruded with the biopolymer. In an embodiment, a layer or sheet of another material (e.g., a coating or thermoactive material) can be co-extruded with the biopolymer. In an embodiment, the co-extruded layer or sheet can provide desired surface properties, structural properties, and/or appearance.
- Foaming the Biopolymer
- In an embodiment, the present biopolymer can be foamed either from its soft, raw form or upon melting without addition of foaming or blowing agents. Surprisingly, the present biopolymer can foam upon extruding even in the absence of foaming agents to produce a rigid, strong hardened foam. Although not limiting the present invention, it is believed that the present foam can result from foaming of protein in the fermentation solid.
- The stiff or solid foam can exhibit greater strength (e.g., flexural modulus) compared to conventional foamed plastics at the same density. Conventional plastics decrease in strength when foamed. Although not limiting to the present invention, it is believed that the present biopolymer foam may include denatured protein interacting with the thermoactive material to create an advantageously strong biopolymer foam.
- The present biopolymer (e.g., in the form of pellets) can be converted to a biopolymer foam by injection molding, extrusion, and like methods employed for forming plastics. Although not limiting to the present invention, it is believed that the heat and kinetic energy applied in these processes, such as by a mixing screw, is sufficient to foam the present biopolymer. In injection molding, the mold can be partially filled to allow the foaming action of the biopolymer to fill the cavity. This can decrease the density of the molded article without using chemical foaming or blowing agents. Extruding can also be employed to foam the present biopolymer. The dies used in extruding can form the foamed biopolymer.
- In an embodiment, a foamed biopolymer can be produced by mixing a foaming agent with fermentation solids and thermoactive material. In an embodiment, biopolymer can be foamed without pre-fabrication into pellets by mixing fermentation solids and thermoactive material with a powdered foaming agent, heating and compounding the mixture and then extruding the biopolymer. In an embodiment, vacuum can be used to remove vapors. In an embodiment, greater expansion occurs in the center of an extruded profile than at the perimeter of the profile, such that the extruded product has a higher density near the exterior than on the interior. Methods for combining particulate and polymer with a foaming agent to produce a foamed product with a desired density are described in U.S. Pat. No. 6,153,293, which is incorporated by reference. This patent discloses methods and apparatus employed for processing plastics with wood fillers. These methods and apparatus can also be employed to process and form embodiments of the present biopolymer.
- It may be desirable to process biopolymer ingredients into fine particulate to allow for effective foaming. In an embodiment, ingredients can first be processed into a biopolymer product and then the biopolymer can be re-ground into fine particles to facilitate foaming into a foamed product shape.
- In an embodiment, foamed biopolymer can be created by creating discontinuities in a biopolymer material. The discontinuities are expanded and the biopolymer is then stabilized to preserve the discontinuities by cooling or crosslinking. In an embodiment biopolymer can be made using foaming agents such as an inert gases (e.g. nitrogen or carbon dioxide, hydrocarbons, chlorinated hydrocarbons, chlorofluorocarbons) or a decomposing chemical blowing agent that dissolves or disperses into biopolymer in liquid form and which decomposes to an inert gas at elevated temperatures. The expansion associate with foaming agents or decomposing chemical blowing agents cause expansion of cell structures to develop a foamed biopolymer. The foaming process can be control through control of the extrusion temperature and other parameters.
- An embodiment of a foamed component includes a solid outer layer or shell and an interior formed of foamed biopolymer. Foamed biopolymer components can be configured to offer relatively low weight and high stiffness compared to solid components. Foamed biopolymer can be formed for example into components such as sized lumber, posts, beams, trim, shaped structural members, furniture board, and trim components. It can be desirable to form components with a specific gravity lower than water, so the components float, or to approximate the density of wood lumber. Window or door components can also be formed from foamed biopolymer. Components of a column and rail system can be formed from foamed biopolymer. Components combining hollow and foamed cores are also possible.
- U.S. Pat. Nos. 6,054,207, 6,153,293, 6,280,667, and 6,342,172 which are incorporated herein by reference, further describe processes and apparatus for fabricating thermoactive material into foamed products. These patents disclose methods and apparatus employed for processing plastics with wood fillers. These methods and apparatus can also be employed to process and form embodiments of the present biopolymer.
- Processing Parameters and Structural Parameters
- In an embodiment, biopolymer admixture can provide a higher flow or lower viscosity compared to typical mixtures that use dried fibers with a thermoactive material. This can allow for processing with significantly lower pressures during extrusion or injection molding. For example, pressures of compression molding a conventional fiber/polymer material can typically fall in the 500-1000 psi range. In contrast, in an embodiment, the present biopolymer can reach maximum density at less than 150 psi. In an embodiment, motor load for processing the present biopolymer can be decreased from 50% for conventional polymer to 10% for the present polymer.
- The lower compression pressure requirement of embodiments of the present biopolymer can allow for significant changes to the engineering and structure of pressing or extrusion equipment for the biopolymer and lower the costs of such equipment. In an embodiment, equipment for processing the biopolymer can also be configured with lower processing temperature. In an embodiment, processing temperature can be reduced from 400 degrees Fahrenheit for conventional polymer to 320 degrees Fahrenheit for an embodiment of the present biopolymer.
- Mechanical properties for lumber replacements (or other structures) can be quantified and tested for a variety of parameters. Biopolymer ingredients and manufacturing processes can be manipulated to achieve desired combinations of properties. Properties that can be considered include density, surface hardness, shear strength and bending properties, retention force (for retaining nails, screws, or other fasteners), strip-out properties, coefficient of thermal expansion, and Young's modulus. In an embodiment, structural parameters can be manipulated by altering the percentage of fermentation solids in the biopolymer.
- U.S. Pat. No. 5,539,027, which is incorporated herein by reference, further describes fabrication of structural polymer members. Testing of mechanical properties for structural members is described in U.S. Pat. No. 6,342,172, which is incorporated herein by reference. These patents disclose methods relating to processing plastics with wood fillers. These methods can also be employed to process and form embodiments of the present biopolymer.
- Column and Rail System
- Embodiments of structural members that include biopolymer material can be used to build a variety of structures, including pillars, rails, and decking systems, and can be used in a variety of places, including porches, patios, entryways, gardens, lawns, or as accents. In one embodiment, pillars and rails can be used as a component of a decking system.
- In a preferred embodiment, a pillar is made from a base, corners, panels, and a top cap. In an embodiment, a base can be configured to slide over a post that is coupled or secured to the ground or another structure. Although a post is not required, it can provide advantageous structural support. In an embodiment, a plurality of panels can be interconnected by a plurality of corners to form a pillar. In one embodiment, four panels and four pillars can be used to create a rectangular pillar. In other embodiments, other pillar shapes can be formed, such as triangles, pentagons, hexagons, heptagons, octagons, and so on. Irregular pillars are also possible: Neither the panels nor the corners that shape the pillar need to be the same size.
- In an embodiment, a pillar can be configured to slide over or otherwise couple to a post. The pillar can further be coupled to the base. Alternatively, the pillar can be secured to the post, or the base can be secured to the post. A top cap can then be mounted or otherwise coupled to the post and/or to the pillar. The top cap can be in a variety of different forms, including functional or aesthetically pleasing forms. In one embodiment, the top cap is shaped as a generally horizontal member having an inner body portion and first and second outer ends and first and second generally vertical members that are spaced apart and disposed inwardly from said first and second ends of the horizontal member.
- The column can be hollow, filled, partially filled, or internally foamed. In one embodiment, the column can have a hollow interior. In another embodiment, the column can have a partially filled interior, such as when the post is secured to the top cap but there is a distance or void between one or more panels and the post. In a third embodiment, the column can have an entirely filled interior, such as when the post is secured to the top cap and is also touching the panels. In other embodiments, the column can include a solid shell and a foamed, webbed, or strutted interior, or a combination thereof. The invention is not limited to these possible embodiments.
- The panel can be a decorative element, with a desirable color, material, texture, or the like. In an embodiment, the panel can be a transparent or translucent material, such as stained glass or a printed glass or plastic material that gives the appearance of stained glass. In an embodiment, a light source can be positioned within the pillar or column and can be configured to illuminate the transparent or translucent panel. In an embodiment, the light source is in the space between the pillar and the post. In an embodiment, the corner component can form a frame for the decorative panel.
- In a preferred embodiment, the railing is formed from balusters and rails. A plurality of balusters are placed between a top rail and a bottom rail and then secured to the top and bottom rails. A rail cover can then be secured to the top rail to make the railing.
- The structural members can be made in whole or in part of a variety of materials, including biopolymer, wood, glass, and composite materials, and can be metalized with brass, bronze, chrome, or gun metal for unique looks and styles. The top caps can also made of glass or other transparent or translucent material and lighted from the inside. Other lighting arrangements are also possible. The structural members can take a variety of shapes. For example, the structural members can have rounded or sharp edges, and can be circular or polygons. The structural members can be made in a variety of ways, including injection molding or extrusion. The structural members can also be secured in a variety of ways, including by being screwed, nailed, glued, snapped, or fastened. Biopolymer components can be thermowelded together. Thermowelds can be smoothed or otherwise featured with a knife, router or other tool to provide a pleasing appearance.
- Illustrated Embodiments of the Column and Rail System
-
FIGS. 1-14 illustrate examples of structural embodiments that can be formed from or include the present biopolymer. -
FIG. 1 is a front perspective view of an embodiment of a decking system that can be made of acorner 1, apanel 2, abaluster 3, arail 4, arail cover 5, abase 6, and atop cap 7. A pillar can include acorner 1, apanel 2, abase 6, and atop cap 7, and can be secured to a railing, which can be made up of abaluster 3,rail 4, andrail cover 5, as shown inFIG. 1 . -
FIG. 2 shows a front view of a base component where abase 6 can slide over apost 8. A fastener, such asscrew 9, can secure abase 6 to apost 8. A plurality ofpanels 2 can be interconnected by a plurality ofcorners 1 to form a rectangular pillar. A pillar can slide over apost 8 and can be mounted on abase 6 as shown inFIG. 3 . Atop cap 7 can be mounted to apost 8 to form the pillar as shown inFIG. 4 . -
FIG. 5 is a front view of a railing assembly. A plurality ofbalusters 3 can be placed between atop rail 4 and abottom rail 4 as shown inFIG. 5 . Abaluster 3 can be connected to atop rail 4 and abottom rail 4 by, for example, ascrew 10, as shown inFIG. 6 . Arail cover 5 can be mounted on atop rail 4 of an assembling railing to make a railing as shown inFIG. 7 . - Embodiments of structural components that can be used to form the structure in
FIGS. 1-7 are shown inFIGS. 8-14 .FIG. 8 is a perspective view of abase 6.FIG. 9 is a top view of apanel component 2.FIG. 10 is a cross-sectional view of acorner 1.FIG. 11 is a perspective view of atop cap 7.FIG. 12 is a top view of abaluster 3.FIG. 13 is a side view of abottom rail 4.FIG. 14 s a side view of arail cover 5. - Coatings, Textures, and Appearance
- The biopolymer can be treated for appearance during or after forming. For example, the die or other surface used in forming can form a textured surface on the biopolymer article. Extruding can co-extrude an appearance layer of polymer or other material with a biopolymer core. After forming, the formed biopolymer can be treated with a multi roller printing process to impart the look of real wood or other desired printed textures or colors. After forming, the formed biopolymer can be treated with a thermosetting powder. The thermosetting powder can be, for example, clear, semi-transparent, or fully pigmented. The powder can be heat cured, which can form a coating suitable for interior or exterior uses. The powder can also be textured to provide, for example, a natural wood look and texture.
- In an embodiment, the biopolymer products can be powder coated, embossed, and/or printed to provide desired surface properties such as weatherability and UV-resistance and/or surface effects such as wood grain colors and textures.
- In an embodiment, a biopolymer product can be formed with a protective layer. In an embodiment, a biopolymer product can be coated with a thermosetting powder that is baked on to cure the powder into a high performance coating. The powder can for example be polyester, epoxy, acrylates, or other polymers or thermoactive material, or a combination thereof. The coating can be clear, semi-transparent, or fully pigmented. In one embodiment, the powder coated biopolymer product can be baked in an infrared or IR/UV oven. Such a coated product can be appropriate for both internal and exterior use.
- In an embodiment, a thin layer of resin or other material can be added to a surface. An embodiment of one or more components of a column and rail system, for example, can be fabricated with a protective resin layer to enhance weatherability. Addition of a surface layer can also be useful in other applications, including for example interior applications where exposure to cleaning agents can occur (e.g. tub or shower areas), and exterior applications such as building trim, shutters, lawn and garden equipment, decorative panels and signs, patio furniture, or column and rail system.
- In an embodiment, a biopolymer product can be vinyl wrapped or metal wrapped.
- Biopolymer products can be given a wood appearance and/or texture (or other texture/appearance) through processing such as embossing or printing, or by co-extruding an outer layer with the biopolymer. Column and rail system assemblies, for example, can be patterned with a wood grain appearance or texture. Other wood-replacement products can similarly be processed to resemble particular woods (or stained woods) in texture and color.
- In one embodiment, the biopolymer product can be run through a multiroller printing process to impart the look of real wood or other desired printed textures or colors, such as stucco, concrete, bricks, stone, tile, clay, or metal. In other embodiments, an extrusion can be directly printed using a gravure printing process or an embossing wheel. The combination of color and texture can create a natural wood look and feel. Other printing process also can be used, including direct computer imagery. In an embodiment, printing or other methods can create realistic wood textures such as maple, oak, cherry, cedar or other desired prints and textures. In one embodiment, the biopolymer material can be placed in a thermal plated press during the curing process both to impart faster curing and to impress a texture onto the surface of the end product.
- In an embodiment, an exterior product can be formed using fermentation solids in conjunction with a powder coating for exterior products. In an embodiment, the exterior product can be printed with a desired appearance and/or textured in a press with a texture plate to form an exterior grade textured surface. In another embodiment, similar processes can be employed to generate a rough-service product.
- In another embodiment, the biopolymer can be printed and then coated to protect the printed surface. The biopolymer may be digitally printed for example, to impart a desired appearance such as the grain of a particular wood, such as cherry. The biopolymer may then be powder coated to protect the printed surface. In an embodiment, the biopolymer may be powder coated with a clear layer to allow the printed surface to show through.
- In another embodiment, an outer layer is applied to the product. The outer layer can for example be a veneer, a wood grain covering, a pigmented covering, or another type of co-extruded layer. The outer layer can provide a desired color, appearance, texture, weatherability, or other property.
- In another embodiment, the biopolymer can be made to look like granite. In an embodiment, the biopolymer can include visible particles of remaining fermentation solid. Such a composite biopolymer can result in a matrix of one appearance surrounding particles with a different appearance, giving the appearance of granite. In such a composite biopolymer, a significant fraction of the fermentation solid can be blended into and/or bonded with the thermoactive material.
- In another embodiment, particulate matter can be added to the biopolymer. Embodiments including particulate matter can be formed to simulate the appearance of granite or other stones, or natural wood grains such as burled wood. In an embodiment, particulate can be fused into a biopolymer product for example by mixing in the particular during extrusion molding or compression molding. In an embodiment, particulate does not dissolve into the polymer but remains distinct, so that the particulate matter is visible to the naked eye. In an embodiment, particulate can be combined in a polymer to give a desired aggregate appearance. In an embodiment, the biopolymer with aggregate matter can be machined, cut, drilled, or otherwise processed. Further description of polymer-particulate material is provided in U.S. Pat. No. 5,635,123, which is incorporated by reference.
- It should be noted that, as used in this specification and the appended claims, the singular forms “a,” “an,” and “the” include plural referents unless the content clearly dictates otherwise. Thus, for example, reference to a composition containing “a compound” includes a mixture of two or more compounds. It should also be noted that the term “or” is generally employed in its sense including “and/or” unless the content clearly dictates otherwise.
- It should also be noted that, as used in this specification and the appended claims, the phrase “adapted and configured” describes a system, apparatus, or other structure that is constructed or configured to perform a particular task or adopt a particular configuration to. The phrase “adapted and configured” can be used interchangeably with other similar phrases such as arranged and configured, constructed and arranged, adapted, constructed, manufactured and arranged, and the like.
- All publications and patent applications in this specification are indicative of the level of ordinary skill in the art to which this invention pertains. All publications and patent applications are herein incorporated by reference to the same extent as if each individual publication or patent application was specifically and individually indicated by reference.
- The invention has been described with reference to various specific and preferred embodiments and techniques. However, it should be understood that many variations and modifications may be made while remaining within the spirit and scope of the invention.
Claims (46)
1. An article of manufacture comprising a biopolymer, the biopolymer comprising thermoactive material and fermentation solid.
2. The article of claim 1 , wherein the biopolymer comprises:
about 5 to about 95 wt-% fermentation solid; and
about 1 to about 95 wt-% thermoactive material.
3. The article of claim 1 , wherein the fermentation solid comprises at least one of distiller's dried grain, distiller's dried starchy root crop, distiller's dried tuber, and distiller's dried root.
4. The article of claim 3 , wherein the fermentation solid comprises at least one of distiller's dried cereal grain and distiller's dried legume.
5. The article of claim 4 , wherein the fermentation solid comprises distiller's dried corn, distiller's dried sorghum (milo), distiller's dried barley, distiller's dried wheat, distiller's dried rye, distiller's dried rice, distiller's dried millet, distiller's dried oats, and distiller's dried soybean.
6. The article of claim 1 , wherein the article is configured for use as a replacement for a wood structural member.
7. The article of claim 1 wherein the article comprises a board.
8. The article of claim 1 wherein the article comprises a deck plank.
9. The article of claim 1 , wherein the article is configured as a column, the column comprising:
a base;
a pillar coupled to the base, wherein the pillar comprises:
plurality of corners; and
plurality of panels, wherein each panel is coupled to a corner on each side; and
a top cap coupled to the pillar;
wherein at least one of the base, the corners, the panels, and the top cap comprises an article comprising the biopolymer.
10. The article of claim 1 , wherein the article is configured as a column, the column comprising:
a post;
a base coupled to the post;
a pillar coupled to the base, the post, or both, wherein the pillar comprises:
a plurality of corners; and
a plurality of panels, wherein the panels are coupled to the corners forming a pillar; and
a top cap, coupled to the pillar, the post, or both;
wherein at least one of the base, the corners, the panels, and the top cap comprises an article comprising biopolymer.
11. The article of claim 1 , wherein the article is configured as a rail system, the rail system comprising:
a plurality of balusters, each baluster comprising a top end and a bottom end;
a top rail coupled to the top ends of the balusters;
a bottom rail coupled to the bottom ends of the balusters; and
a rail cover coupled to the top rail;
wherein at least one of the balusters, the top rail, the bottom rail, the base, the corners, the panels, and the top cap comprises an article comprising biopolymer.
12. The article of claim 1 , wherein the article is configured as a column and rail system, the column and rail system comprising:
a plurality of columns, each of the columns comprising:
a post;
a base coupled to the post;
a pillar coupled to the base, the post, or both, wherein the pillar comprises:
a plurality of corners; and
a plurality of panels, wherein the panels are coupled to the corners forming a pillar; and
a top cap coupled to the pillar, the post, or both;
a railing segment comprising:
at least one baluster, each baluster a top end and a bottom end;
a top rail coupled to at least one baluster top end;
a bottom rail coupled to at least one baluster bottom end; and
a rail cover coupled to the top rail;
the railing segment extending between two of the columns;
wherein at least one of the baluster, the top rail, the bottom rail, the base, the corners, the panels, and the top cap comprises an article comprising biopolymer.
13. The article of claim 1 , wherein the article comprises a corner configured for being a component of a column and rail system.
14. The article of claim 1 , wherein the article comprises a panel configured for being a component of a column and rail system.
15. The article of claim 1 , wherein the article comprises a column configured for being a configured for being a component of a column and rail system.
16. The article of claim 1 , wherein the article comprises a baluster configured for being a component of a column and rail system.
17. The article of claim 1 , wherein the article comprises a rail configured for being a component of a column and rail system.
18. The article of claim 1 , wherein the article comprises a rail cover configured for being a component of a column and rail system.
19. The article of claim 1 , wherein the article comprises a base configured for being a component of a column and rail system.
20. The article of claim 1 , wherein the article comprises a top cap configured for being a component of a column and rail system.
21. The article of claim 1 , wherein the article comprises a decorative cap configured for being a component of a column and rail system.
22. The article of claim 1 , further comprising a layer of a second material on the biopolymer.
23. The article of claim 22 , wherein the layer of second material comprises impression-formed features.
24. The article of claim 22 , wherein the layer of second material comprises a coextruded material.
25. The article of claim 22 , wherein the layer of second material comprises a powder coating.
26. The article of claim 1 , wherein the fermentation solid comprises fermented protein solid.
27. The article of claim 26 , wherein the fermentation solid comprises distiller's dried grain.
28. The article of claim 27 , wherein the distiller's dried grain further comprises solubles.
29. The article of claim 27 , wherein the distiller's dried grain comprises distiller's dried grain-200.
30. The article of claim 27 , wherein the distiller's dried grain comprises distiller's dried corn.
31. The article of claim 1 , wherein the biopolymer comprises:
about 50 to about 70 wt-% fermentation solid; and
about 20 to about 50 wt-% thermoactive material.
32. The article of claim 1 , wherein the thermoactive material comprises at least one of thermoplastic, thermoset material, and resin and adhesive polymer.
33. The article of claim 1 , wherein the thermoactive material comprises at least one of polyethylene, polypropylene, and polyvinyl chloride.
34. The article of claim 1 , wherein the thermoactive material comprises at least one of epoxy material and melamine.
35. The article of claim 1 , wherein the thermoactive material comprises at least one of polyester, phenolic polymer, and urea containing polymer.
36. The article of claim 1 , wherein the article is in the form of an integral biopolymer, a composite biopolymer, or an aggregate biopolymer.
37. The article of claim 1 , wherein the article is in the form of a composite biopolymer and the composite biopolymer has a granite-like appearance.
38. The article of claim 1 , further comprising at least one of dye, pigment, hydrolyzing agent, plasticizer, filler, preservative, antioxidants, nucleating agent, antistatic agent, biocide, fungicide, fire retardant, flame retardant, heat stabilizer, light stabilizer, conductive material, water, oil, lubricant, impact modifier, coupling agent, crosslinking agent, blowing or foaming agent, and reclaimed or recycled plastic.
39. The article of claim 1 , further comprising at least one of plasticizer, light stabilizer, and coupling agent.
40. A method of making an article, the method comprising:
forming the article from a composition comprising:
about 5 to about 95 wt-% fermentation solid; and
about 0.1 to about 95 wt-% thermoactive material.
41. The method of claim 40 , wherein forming comprises one or more of extrusion molding, injection molding, blow molding, compression molding, transfer molding, thermoforming, casting, calendering, low-pressure molding, high-pressure laminating, reaction injection molding, foam molding, and coating.
42. The method of claim 40 , further comprising coating the article.
43. The method of claim 40 , wherein forming the composition comprises extruding the biopolymer through a die to produce an extrusion.
44. The method of claim 43 , further comprising applying a surface texture to the article.
45. The method of claim 44 , wherein applying comprises pressing the article.
46. The method of claim 45 , wherein pressing the article promotes extraction of water from the mixture.
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WO (1) | WO2004113435A1 (en) |
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Citations (21)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4284652A (en) * | 1977-01-24 | 1981-08-18 | The Quaker Oats Company | Matrix, product therewith, and process |
US4466889A (en) * | 1981-08-20 | 1984-08-21 | Pfizer Inc. | Polyvalent metal ion chelating agents for xanthan solutions |
US5397834A (en) * | 1993-09-03 | 1995-03-14 | Iowa State University Research Foundation, Inc. | Biodegradable thermoplastic composition of aldehyde starch and protein |
US5406768A (en) * | 1992-09-01 | 1995-04-18 | Andersen Corporation | Advanced polymer and wood fiber composite structural component |
US5441801A (en) * | 1993-02-12 | 1995-08-15 | Andersen Corporation | Advanced polymer/wood composite pellet process |
US5486553A (en) * | 1992-08-31 | 1996-01-23 | Andersen Corporation | Advanced polymer/wood composite structural member |
US5516472A (en) * | 1993-11-12 | 1996-05-14 | Strandex Corporation | Extruded synthetic wood composition and method for making same |
US5596080A (en) * | 1994-10-03 | 1997-01-21 | E. I. Du Pont De Nemours And Company | Crosslinking processes/agents for zein |
US5635123A (en) * | 1992-08-11 | 1997-06-03 | Phenix Biocomposites, Inc. | Biocomposite material and method of making |
US5725939A (en) * | 1994-02-10 | 1998-03-10 | Ein Engineering Co., Ltd. | Synthetic wood meal, method and apparatus for manufacturing the same; synthetic wood board including the synthetic wood meal, method and apparatus of extrusion molding therefor |
US5739015A (en) * | 1997-03-10 | 1998-04-14 | Board Of Supervisors Of Louisiana State University And Agricultural And Mechanical College | Biotransformation of chitin to chitosan |
US5746958A (en) * | 1995-03-30 | 1998-05-05 | Trex Company, L.L.C. | Method of producing a wood-thermoplastic composite material |
US5851469A (en) * | 1995-12-27 | 1998-12-22 | Trex Company, L.L.C. | Process for making a wood-thermoplastic composite |
US5914367A (en) * | 1996-10-10 | 1999-06-22 | Biotechnology Research & Development Corp. | Polymer protein composites and methods for their preparation and use |
US5948524A (en) * | 1996-01-08 | 1999-09-07 | Andersen Corporation | Advanced engineering resin and wood fiber composite |
US6054207A (en) * | 1998-01-21 | 2000-04-25 | Andersen Corporation | Foamed thermoplastic polymer and wood fiber profile and member |
US6122877A (en) * | 1997-05-30 | 2000-09-26 | Andersen Corporation | Fiber-polymeric composite siding unit and method of manufacture |
US6313105B1 (en) * | 1997-07-09 | 2001-11-06 | Aventis Research And Technologies Gmbh & Co Kg | Thermoplastic mixtures containing dialdehyde starch and natural polymers |
US6323265B1 (en) * | 1997-07-09 | 2001-11-27 | Aventis Research & Technologies Gmbh & Co Kg | Thermoplastic mixture containing 1,4-α-D-polyglucane, method for making the same and use thereof |
US6593625B2 (en) * | 2001-06-12 | 2003-07-15 | International Business Machines Corporation | Relaxed SiGe layers on Si or silicon-on-insulator substrates by ion implantation and thermal annealing |
US20050019545A1 (en) * | 2003-06-13 | 2005-01-27 | Agri-Polymerix, Llc | Biopolymer structures and components |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CH503576A (en) | 1969-02-06 | 1971-02-28 | Jetzer Raimund | Process for the production of pellets from household, agricultural and forestry waste |
JPS5159953A (en) * | 1974-11-22 | 1976-05-25 | Sumitomo Bakelite Co | TANPAKUSHITSUKEISEIKEIZAIRYOSOSEIBUTSU |
NL8105881A (en) | 1981-12-29 | 1983-07-18 | Unilever Nv | FERMENTED MILK PRODUCTS CONTAINING LACTIC ACID BACTERIA AND METHOD OF PREPARATION THEREOF. |
JPH10145055A (en) * | 1996-11-08 | 1998-05-29 | Daiko:Kk | Body for communication equipment such as portable telephone comprising food-material waste and the like and manufacturing method thereof |
JP4509328B2 (en) * | 2000-08-07 | 2010-07-21 | 紀伊産業株式会社 | Plastic molded products for cosmetic containers |
US7241832B2 (en) * | 2002-03-01 | 2007-07-10 | bio-tec Biologische Naturverpackungen GmbH & Co., KG | Biodegradable polymer blends for use in making films, sheets and other articles of manufacture |
PT102888B (en) * | 2002-12-23 | 2005-04-29 | Filipe Manuel Rodrigues Aguiar | INDUSTRIAL PROCESS OF PRODUCTION OF POLYLACTIC ACID (PLA) OBTAINED BY ESTERIFICATION AND POLYMERIZATION OF PURIFIED LACTIC ACID, THE ACID IS REFERRED TO BE PRODUCED THROUGH A FERMENTATION PROCESS |
-
2004
- 2004-06-14 WO PCT/US2004/018774 patent/WO2004113435A1/en active Application Filing
- 2004-06-14 CA CA 2528936 patent/CA2528936A1/en not_active Abandoned
- 2004-06-14 AU AU2004249706A patent/AU2004249706A1/en not_active Abandoned
- 2004-06-14 BR BRPI0411323 patent/BRPI0411323A/en not_active IP Right Cessation
- 2004-06-14 US US10/868,424 patent/US7625961B2/en active Active
- 2004-06-14 US US10/868,263 patent/US7332119B2/en not_active Expired - Fee Related
- 2004-06-14 MX MXPA05013451A patent/MXPA05013451A/en not_active Application Discontinuation
- 2004-06-14 KR KR1020057023983A patent/KR20060061301A/en not_active Application Discontinuation
- 2004-06-14 US US10/868,276 patent/US20050075423A1/en not_active Abandoned
- 2004-06-14 EP EP20040755122 patent/EP1639040A1/en not_active Withdrawn
- 2004-06-14 JP JP2006533765A patent/JP2007517078A/en active Pending
Patent Citations (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4284652A (en) * | 1977-01-24 | 1981-08-18 | The Quaker Oats Company | Matrix, product therewith, and process |
US4466889A (en) * | 1981-08-20 | 1984-08-21 | Pfizer Inc. | Polyvalent metal ion chelating agents for xanthan solutions |
US5635123A (en) * | 1992-08-11 | 1997-06-03 | Phenix Biocomposites, Inc. | Biocomposite material and method of making |
US5486553A (en) * | 1992-08-31 | 1996-01-23 | Andersen Corporation | Advanced polymer/wood composite structural member |
US5539027A (en) * | 1992-08-31 | 1996-07-23 | Andersen Corporation | Advanced polymer/wood composite structural member |
US5406768A (en) * | 1992-09-01 | 1995-04-18 | Andersen Corporation | Advanced polymer and wood fiber composite structural component |
US5497594A (en) * | 1992-09-01 | 1996-03-12 | Andersen Corporation | Advanced polymer and wood fiber composite structural component |
US5441801A (en) * | 1993-02-12 | 1995-08-15 | Andersen Corporation | Advanced polymer/wood composite pellet process |
US5518677A (en) * | 1993-02-12 | 1996-05-21 | Andersen Corporation | Advanced polymer/wood composite pellet process |
US5397834A (en) * | 1993-09-03 | 1995-03-14 | Iowa State University Research Foundation, Inc. | Biodegradable thermoplastic composition of aldehyde starch and protein |
US5516472A (en) * | 1993-11-12 | 1996-05-14 | Strandex Corporation | Extruded synthetic wood composition and method for making same |
US5725939A (en) * | 1994-02-10 | 1998-03-10 | Ein Engineering Co., Ltd. | Synthetic wood meal, method and apparatus for manufacturing the same; synthetic wood board including the synthetic wood meal, method and apparatus of extrusion molding therefor |
US5596080A (en) * | 1994-10-03 | 1997-01-21 | E. I. Du Pont De Nemours And Company | Crosslinking processes/agents for zein |
US5746958A (en) * | 1995-03-30 | 1998-05-05 | Trex Company, L.L.C. | Method of producing a wood-thermoplastic composite material |
US5851469A (en) * | 1995-12-27 | 1998-12-22 | Trex Company, L.L.C. | Process for making a wood-thermoplastic composite |
US6527532B1 (en) * | 1995-12-27 | 2003-03-04 | Trex Company, L.L.C. | Apparatus for making a wood-plastic profile |
US5948524A (en) * | 1996-01-08 | 1999-09-07 | Andersen Corporation | Advanced engineering resin and wood fiber composite |
US5914367A (en) * | 1996-10-10 | 1999-06-22 | Biotechnology Research & Development Corp. | Polymer protein composites and methods for their preparation and use |
US5739015A (en) * | 1997-03-10 | 1998-04-14 | Board Of Supervisors Of Louisiana State University And Agricultural And Mechanical College | Biotransformation of chitin to chitosan |
US6122877A (en) * | 1997-05-30 | 2000-09-26 | Andersen Corporation | Fiber-polymeric composite siding unit and method of manufacture |
US6323265B1 (en) * | 1997-07-09 | 2001-11-27 | Aventis Research & Technologies Gmbh & Co Kg | Thermoplastic mixture containing 1,4-α-D-polyglucane, method for making the same and use thereof |
US6313105B1 (en) * | 1997-07-09 | 2001-11-06 | Aventis Research And Technologies Gmbh & Co Kg | Thermoplastic mixtures containing dialdehyde starch and natural polymers |
US6054207A (en) * | 1998-01-21 | 2000-04-25 | Andersen Corporation | Foamed thermoplastic polymer and wood fiber profile and member |
US6593625B2 (en) * | 2001-06-12 | 2003-07-15 | International Business Machines Corporation | Relaxed SiGe layers on Si or silicon-on-insulator substrates by ion implantation and thermal annealing |
US20050019545A1 (en) * | 2003-06-13 | 2005-01-27 | Agri-Polymerix, Llc | Biopolymer structures and components |
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US20050215672A1 (en) * | 2004-02-11 | 2005-09-29 | Board Of Trustees Of Michigan State University | Anhydride functionalized polyhydroxyalkanoates, preparation and use thereof |
US20100301254A1 (en) * | 2004-06-23 | 2010-12-02 | University Of Maine System Board Of Trustees | Barrier compositions and articles produced with the compositions |
US20050287248A1 (en) * | 2004-06-23 | 2005-12-29 | Jabar Anthony Jr | Barrier compositions and articles produced with the compositions |
US7737200B2 (en) * | 2004-06-23 | 2010-06-15 | University Of Maine System Board Of Trustees | Barrier compositions and articles produced with the compositions |
US20070020476A1 (en) * | 2005-06-03 | 2007-01-25 | Kintzley Tom G | Wood composites, methods of production, and methods of manufacture thereof |
US7803855B2 (en) * | 2005-06-03 | 2010-09-28 | Hexion Specialty Chemicals, Inc. | Wood composites, methods of production, and methods of manufacture thereof |
US20090206507A1 (en) * | 2005-08-31 | 2009-08-20 | J Wayne Martin | Method and apparatus for pelletizing biomaterial composites |
US8765827B2 (en) | 2008-03-05 | 2014-07-01 | Gs Cleantech Corporation | Multifunctional biocomposite additive compositions and methods |
US9587098B2 (en) | 2008-03-05 | 2017-03-07 | Gs Cleantech Corporation | Multifunctional biocomposite additive compositions and methods |
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US8449986B2 (en) | 2008-03-05 | 2013-05-28 | Scout Materials Llc | Multifunctional biocomposite additive compositions and methods |
US8598256B2 (en) | 2008-03-05 | 2013-12-03 | Gs Cleantech Corporation | Multifunctional biocomposite additive compositions and methods |
US20090281203A1 (en) * | 2008-03-05 | 2009-11-12 | Riebel Michael J | Multifunctional biocomposite additive compositions and methods |
US8772379B2 (en) | 2008-03-05 | 2014-07-08 | Gs Cleantech Corporation | Multifunctional biocomposite additive compositions and methods |
US8809425B2 (en) | 2008-03-05 | 2014-08-19 | Gs Cleantech Corporation | Multifunctional biocomposite additive compositions and methods |
US9034954B2 (en) | 2008-03-05 | 2015-05-19 | Gs Cleantech Corporation | Multifunctional biocomposite additive compositions and methods |
US9346955B2 (en) | 2008-03-05 | 2016-05-24 | Gs Cleantech Corporation | Multifunctional biocomposite additive compositions and methods |
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US10851560B2 (en) | 2008-10-20 | 2020-12-01 | Vision Extrusions Ltd. | Fence system |
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US9156209B2 (en) * | 2010-07-22 | 2015-10-13 | Green Bubble Technologies Llc | Biooptical and biofunctional properties, applications and methods of polylactic acid films |
US20120019917A1 (en) * | 2010-07-22 | 2012-01-26 | Riebel Michael J | Biooptical and Biofunctional Properties, Applications and Methods of Polylactic Acid Films |
US20120291377A1 (en) * | 2011-04-26 | 2012-11-22 | Michael Riebel | Fire retardant biolaminate composite and related assembly |
US11268284B2 (en) | 2017-11-14 | 2022-03-08 | Vision Extrusions Group Limited | Railing system |
US11499337B2 (en) | 2017-11-14 | 2022-11-15 | Vision Extrusions Group Limited | Fence panel system |
Also Published As
Publication number | Publication date |
---|---|
US20050101700A1 (en) | 2005-05-12 |
EP1639040A1 (en) | 2006-03-29 |
US20050019545A1 (en) | 2005-01-27 |
KR20060061301A (en) | 2006-06-07 |
CA2528936A1 (en) | 2004-12-29 |
US7625961B2 (en) | 2009-12-01 |
BRPI0411323A (en) | 2006-07-25 |
MXPA05013451A (en) | 2006-06-23 |
JP2007517078A (en) | 2007-06-28 |
WO2004113435A1 (en) | 2004-12-29 |
US7332119B2 (en) | 2008-02-19 |
AU2004249706A1 (en) | 2004-12-29 |
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