Fibrous materials and composites

Information

  • Patent Grant
  • 7980495
  • Patent Number
    7,980,495
  • Date Filed
    Thursday, April 29, 2010
    14 years ago
  • Date Issued
    Tuesday, July 19, 2011
    13 years ago
Abstract
Fibrous materials, compositions that include fibrous materials, and uses of the fibrous materials and compositions are disclosed. For example, the fibrous materials can be operated on by a microorganism to produce ethanol or a by-product, such as a protein or lignin.
Description
TECHNICAL FIELD

This invention relates to fibrous materials and to compositions.


BACKGROUND

Fibrous materials, e.g., cellulosic and lignocellulosic materials, are produced, processed, and used in large quantities in a number of applications. Often such fibrous materials are used once, and then discarded as waste.


Various fibrous materials, their uses and applications have been described in U.S. Pat. Nos. 6,448,307, 6,258,876, 6,207,729, 5,973,035 and 5,952,105. The entire disclosure of each of the patents of this paragraph is incorporated by reference herein.


SUMMARY

Generally, this invention relates to fibrous materials, methods of making fibrous materials, compositions that include fibrous materials (e.g., composites that include the fibrous materials and a resin, or compositions that include the fibrous materials and bacteria and/or an enzyme), and to uses of the same. For example, the compositions can be used to make ethanol, or a by-product, such as a protein or lignin, or applied to a structure as insulation.


Any of the fibrous materials disclosed herein can be used in combination with any of the fibrous materials, resins, additives, or other components disclosed in U.S. Pat. Nos. 6,448,307, 6,258,876, 6,207,729, 5,973,035 and 5,952,105. In turn, these fibrous materials and/or components can be used in any of the applications, products, procedures, et cetera disclosed in any of these patents or in this application.


The fibrous materials or compositions that include the fibrous materials can be, e.g., associated with, blended with, adjacent to, surrounded by, or within a structure or carrier (e.g., a netting, a membrane, a flotation device, a bag, a shell, or a biodegradable substance). Optionally, the structure or carrier may itself be made from a fibrous material, or of a composition that includes a fibrous material. In some embodiments, the fibrous material is combined with a material, such as a protic acid, that enhances the rate of biodegradation of the fibrous material. In some embodiments, the fibrous material is combined with a material that retards degradation of the fibrous material, such as a buffer.


The ratio of fibrous materials to the other components of the compositions will depend upon the nature of the components, and can be readily adjusted for a specific product application.


Any of the fibrous materials described herein, including any of the fibrous materials made by any of the methods described herein, can be used, e.g., to form composites with resin, or can be combined with bacteria and/or one or more enzymes to produce a valuable product, such as a fuel (e.g., ethanol, a hydrocarbon, or hydrogen).


In one aspect, the invention features methods of making fibrous materials. The methods include shearing a fiber source to provide a first fibrous material, and passing the first fibrous material through a first screen having an average opening size of 1.59 mm or less ( 1/16 inch, 0.0625 inch) to provide a second fibrous material. The fiber source can, e.g., be cut into pieces or strips of confetti-like material prior to the shearing.


In some embodiments, the average opening size of the first screen is less than 0.79 mm ( 1/32 inch, 0.03125 inch), e.g., less than 0.40 mm ( 1/64 inch, 0.015625 inch), less than 0.20 mm ( 1/128 inch, 0.0078125 inch), or even less than 0.10 mm ( 1/256 inch, 0.00390625 inch).


In specific implementations, the shearing is performed with a rotary knife cutter. If desired, the shearing can be performed while the fiber source is dry (e.g., having less than 0.25 percent by weight absorbed water), hydrated, or even while the fiber source is partially or fully submerged in a liquid, such as water or isopropanol.


The second fibrous material can, e.g., be collected in a bin having a pressure below nominal atmospheric pressure, e.g., at least 10 percent below nominal atmospheric pressure, at least 50 percent below nominal atmospheric pressure, or at least 75 percent below nominal atmospheric pressure.


The second fibrous material can, e.g., be sheared once or numerous times, e.g., twice, thrice, or even more, e.g., ten times. Shearing can “open up” and/or “stress” the fibrous materials, making the materials more dispersible, e.g., in a solution or in a resin.


The second fibrous material can be, e.g., sheared and the resulting fibrous material passed through the first screen.


The second fibrous material can be sheared, and the resulting fibrous material passed through a second screen having an average opening size less than the first screen, providing a third fibrous material.


A ratio of an average length-to-diameter ratio of the second fibrous material to an average length-to-diameter ratio of the third fibrous material can be, e.g., less than 1.5, less than 1.4, less than 1.25, or even less than 1.1.


The second fibrous can be, e.g., passed through a second screen having an average opening size less than the first screen.


The shearing and passing can be, e.g., performed concurrently.


The second fibrous material can have an average length-to-diameter ratio of, e.g., greater than 10/1, greater than 25/1, or even greater than 50/1.


For example, an average length of the second fibrous material can be between 0.5 mm and 2.5 mm, e.g., between 0.75 mm and 1.0 mm. For example, an average width of the second fibrous material can be between 5 μm and 50 μm, e.g., between 10 μm and 30 μm.


A standard deviation of a length of the second fibrous material can be less than 60 percent of an average length of the second fibrous material, e.g., less than 50 percent of an average length of the second fibrous material.


In some embodiments, a BET surface area of the second fibrous material is greater than 0.5 m2/g, e.g., greater than 1.0 m2/g, greater than 1.5 m2/g, greater than 1.75 m2/g, greater than 2.5 m2/g, greater than 10.0 m2/g, greater than 25.0 m2/g, greater than 50.0 m2/g, or even greater than 100.0 m2/g.


In some embodiments, a porosity of the second fibrous material is greater than 25 percent, e.g., greater than 50 percent, greater than 75 percent, greater than 85 percent, greater than 90 percent, greater than 92 percent, greater than 95 percent, or even greater than 99 percent.


In specific embodiments, the screen is formed by interweaving monofilaments.


The fiber source can include, e.g., a cellulosic material, a lignocellulosic material.


In some embodiments, the fiber source includes a blend of fibers, e.g., fibers derived from a paper source and fibers derived from a textile source, e.g., cotton.


In another aspect, the invention features methods of making fibrous materials that include shearing a fiber source to provide a first fibrous material; and passing the fibrous material through a first screen to provide a second fibrous material. A ratio of an average length-to-diameter ratio of the first fibrous material to an average length-to-diameter of the second fibrous material is less than 1.5.


In another aspect, the invention features methods of making fibrous materials that include shearing a fiber source to provide a first fibrous material; passing the fibrous material through a first screen to provide a second fibrous material; and then shearing the second fibrous material again to provide a third fibrous material.


In another aspect, the invention features composites or compositions made from any of the fibrous materials described herein. For example, compositions can include any of the fibrous materials described herein and a bacterium and/or an enzyme. The compositions that include any of the fibrous materials described herein and the bacterium and/or enzyme can be in a dry state, or they can include a liquid, such as water.


For example, the composite can be in the form of a stepping stool, pipes, panels, decking materials, boards, housings, sheets, blocks, bricks, poles, fencing, members, doors, shutters, awnings, shades, signs, frames, window casings, backboards, flooring, tiles, railroad ties, trays, tool handles, stalls, films, wraps, tapes, boxes, baskets, racks, casings, binders, dividers, walls, mats, frames, bookcases, sculptures, chairs, tables, desks, toys, games, pallets, wharves, piers, boats, masts, septic tanks, automotive panels, computer housings, above- and below-ground electrical casings, furniture, picnic tables, benches, shelters, trays, hangers, servers, caskets, book covers, canes and crutches.


In another aspect, the invention features fibrous materials having an average length-to-diameter ratio of greater than 5, and having a standard deviation of a fiber length of less than sixty percent of an average fiber length.


For example, the average length-to-diameter ratio can be greater than 10/1, e.g., greater than 15/1, greater than 25/1, greater than 35/1, greater than 45/1, or even greater than 50/1.


For example, the average length can be between 0.5 mm and 2.5 mm.


In another aspect, the invention features methods of making fibrous materials that include shearing a fiber source to provide a first fibrous material; collecting the first fibrous material; and then shearing the first fibrous to provide a second fibrous material.


In another aspect, the invention features methods of making a useful material, such as a fuel. The methods include shearing a fiber source to provide a first fibrous material; passing the first fibrous material through a first screen having an average opening size of about 1.59 mm or less ( 1/16 inch, 0.0625 inch) to provide a second fibrous material; and combining the second fibrous material with a bacterium and/or enzyme, the bacterium and/or enzyme utilizing the second fibrous material to produce a fuel that includes hydrogen, an alcohol, an organic acid and/or a hydrocarbon.


The alcohol can be, e.g., methanol, ethanol, propanol, isopropanol, butanol, ethylene glycol, propylene glycol, 1,4-butane diol, glycerin, or mixtures of these alcohols; the organic acid can be, e.g., malonic acid, succinic acid, glutaric acid, oleic acid, linoleic acid, glycolic acid, lactic acid, γ-hydroxybutyric acid, or mixtures of these acids; and the hydrocarbon can be, e.g., methane, ethane, propane, isobutene, pentane, n-hexane, or mixtures of these hydrocarbons.


Prior to combining with the bacterium and/or enzyme, any of the fibrous materials described herein can be hydrolyzed to break down higher molecular weight carbohydrates into lower molecular weight carbohydrates.


In another aspect, the invention features methods of making a useful material, such as a fuel, by shearing a fiber source or a fibrous material, and then combining it with a bacterium and/or an enzyme. For example, the fiber source can be sheared once to provide a fibrous material, and then the fibrous material can be combined with a bacterium and/or an enzyme to make the useful material.


In another aspect, the invention features methods of densifying fibrous compositions. The methods include shearing a fiber source to provide a fibrous material; combining the fibrous material with a bacterium and/or enzyme to provide a fibrous material composition; encapsulating the composition in a substantially gas impermeable material; and removing entrapped gas from the encapsulated composition to densify the composition. For example, the gas impermeable material can be in the form of a bag, and the composition can be densified by evacuating air from the bag, and then sealing the bag.


In another aspect, the invention features composites that include a fibrous material, a resin and a dye.


For example, the fibrous material can have an average length-to-diameter ratio of greater than 5, and a standard deviation of a fiber length of less than sixty percent of an average fiber length.


In some embodiments, the composite additionally includes a pigment.


In some implementations, the dye soaked into or surfaced on the fibers.


In another aspect, the invention features methods of making composites that include dyeing a fibrous material; combining the fibrous material with a resin; and forming a composite from the combination.


In another aspect, the invention features methods of making composite that include adding a dye to a resin to provide a dye/resin combination; combining the dye/resin combination with a fibrous material; and forming a composite from the dye/resin combination and fibrous material.


The term “fibrous material”, as used herein, is a material that includes numerous loose, discrete and separable fibers. For example, a fibrous material can be prepared from a polycoated paper or a bleached Kraft paper fiber source by shearing, e.g., with a rotary knife cutter.


The term “screen”, as used herein, means a member capable of sieving material according to size, e.g., a perforated plate, cylinder or the like, or a wire mesh or cloth fabric.


Embodiments and/or aspects can have any one of, or combinations of, the following advantages. The fibrous materials are opened up and/or stressed, making the materials more dispersible, e.g., in a solution or in a resin, and making them more susceptible to chemical, enzymatic or biological attack. The fibrous materials can have, e.g., a relatively narrow length and/or length-to-diameter ratio distribution, such that their properties are consistently defined. For example, when blended with a molten resin or a solution, the fibers of the fibrous materials can modify the rheology of the molten resin or solution in a consistent and predicable manner, e.g., resulting in resin/fibrous material combinations that are, e.g., easier to mold and extrude. For example, the fibrous materials can easily pass through small openings or channels, such as those found in or associated with injection molds, e.g., gates or hot runners. Parts molded from such fibrous materials can exhibit a good surface finish, e.g., with few visible speckles of large particles and/or agglomerated particles.


All publications, patent applications, patents, and other references mentioned herein are incorporated by reference in their entirety for all that they contain.


Other features and advantages of the invention will be apparent from the following detailed description, and from the claims.





DESCRIPTION OF DRAWINGS


FIG. 1 is block diagram illustrating conversion of a fiber source into a first and second fibrous material.



FIG. 2 is a cross-sectional view of a rotary knife cutter.



FIGS. 3-8 are top views of a variety of screens made from monofilaments.



FIG. 9 is block diagram illustrating conversion of a fiber source into a first, second and third fibrous material.



FIGS. 10A and 10B are photographs of fiber sources; FIG. 10A being a photograph of a polycoated paper container, and FIG. 10B being a photograph of unbleached Kraft paper rolls.



FIGS. 11 and 12 are scanning electron micrographs of a fibrous material produced from polycoated paper at 25× magnification and 1000× magnification, respectively. The fibrous material was produced on a rotary knife cutter utilizing a screen with ⅛ inch openings.



FIGS. 13 and 14 are scanning electron micrographs of a fibrous material produced from bleached Kraft board paper at 25× magnification and 1000× magnification, respectively. The fibrous material was produced on a rotary knife cutter utilizing a screen with ⅛ inch openings.



FIGS. 15 and 16 are scanning electron micrographs of a fibrous material produced from bleached Kraft board paper at 25× magnification and 1000× magnification, respectively. The fibrous material was twice sheared on a rotary knife cutter utilizing a screen with 1/16 inch openings during each shearing.



FIGS. 17 and 18 are scanning electron micrographs of a fibrous material produced from bleached Kraft board paper at 25× magnification and 1000× magnification, respectively. The fibrous material was thrice sheared on a rotary knife cutter. During the first shearing, a ⅛ inch screen was used; during the second shearing, a 1/16 inch screen was used, and during the third shearing a 1/32 inch screen was used.



FIG. 19 is a block diagram illustrating revertible bulk densification of a fibrous material composition.





DETAILED DESCRIPTION

Referring to FIG. 1, a fiber source 10 is sheared, e.g., in a rotary knife cutter, to provide a first fibrous material 12. The first fibrous material 12 is passed through a first screen 16 having an average opening size of 1.59 mm or less ( 1/16 inch, 0.0625 inch) to provide a second fibrous material 14. If desired, fiber source 10 can be cut prior to the shearing, e.g., with a shredder. For example, when a paper is used as the fiber source 10, the paper can be first cut into strips that are, e.g., ¼- to ½-inch wide, using a shredder, e.g., a counter-rotating screw shredder, such as those manufactured by Munson (Utica, N.Y.). As an alternative to shredding, the paper can be reduced in size by cutting to a desired size using a guillotine cutter. For example, the guillotine cutter can be used to cut the paper into sheets that are, e.g., 10 inches wide by 12 inches long.


In some embodiments, the shearing of fiber source 10 and the passing of the resulting first fibrous material 12 through first screen 16 are performed concurrently. The shearing and the passing can also be performed in a batch-type process.


For example, a rotary knife cutter can be used to concurrently shear the fiber source 10 and screen the first fibrous material 12. Referring to FIG. 2, a rotary knife cutter 20 includes a hopper 22 that can be loaded with a shredded fiber source 10′ prepared by shredding fiber source 10. Shredded fiber source 10′ is sheared between stationary blades 24 and rotating blades 26 to provide a first fibrous material 12. First fibrous material 12 passes through screen 16 having the dimensions described above, and the resulting second fibrous material 14 is captured in bin 30. To aid in the collection of the second fibrous material 14, bin 30 can have a pressure below nominal atmospheric pressure, e.g., at least 10 percent below nominal atmospheric pressure, e.g., at least 25 percent below nominal atmospheric pressure, at least 50 percent below nominal atmospheric pressure, or at least 75 percent below nominal atmospheric pressure. In some embodiments, a vacuum source 50 (FIG. 2) is utilized to maintain the bin below nominal atmospheric pressure.


Shearing can be advantageous for “opening up” and “stressing” the fibrous materials, making the materials more dispersible, e.g., in a solution or in a resin, and making them more susceptible to chemical, enzymatic or biological attack. Without wishing to be bound by any particular theory, it is believed, at least in some embodiments, that shearing can functionalize fiber surfaces with functional groups, such as hydroxyl or carboxylic acid groups, which can, e.g., help disperse the fibers in a molten resin or enhance chemical or biological attack.


The fiber source can be sheared in a dry state, a hydrated state (e.g., having up to ten percent by weight absorbed water), or in a wet state, e.g., having between about 10 percent and about 75 percent by weight water. The fiber source can even be sheared while partially or fully submerged under a liquid, such as water, ethanol, isopropanol.


The fiber source can also be sheared in under a gas (such as a stream or atmosphere of gas other than air), e.g., oxygen or nitrogen, or steam.


Other methods of making the fibrous materials include stone grinding, mechanical ripping or tearing, pin grinding or air attrition milling.


If desired, the fibrous materials can be separated, e.g., continuously or in batches, into fractions according to their length, width, density, material type, or some combination of these attributes. For example, for forming composites, it is often desirable to have a relatively narrow distribution of fiber lengths. In addition, e.g., when making compositions that include bacteria and/or an enzyme, it is often desirable to use a substantially single material as a feedstock.


For example, ferrous materials can be separated from any of the fibrous materials by passing a fibrous material that includes a ferrous material past a magnet, e.g., an electromagnet, and then passing the resulting fibrous material through a series of screens, each screen having different sized apertures.


The fibrous materials can also be separated, e.g., by using a high velocity gas, e.g., air. In such an approach, the fibrous materials are separated by drawing off different fractions, which can be characterized photonically, if desired. Such a separation apparatus is discussed in Lindsey et al, U.S. Pat. No. 6,883,667, the entire disclosure of which is hereby incorporated by reference herein in its entirety.


The fibrous materials can be used immediately following their preparation, or they can may be dried, e.g., at approximately 105° C. for 4-18 hours, so that the moisture content is, e.g., less than about 0.5% before use.


If desired, lignin can be removed from any of the fibrous materials that include lignin, such as lignocellulosic materials. Also, if desired, the fibrous material can be sterilized to kill any microorganisms that may be on the fibrous material. For example, the fibrous material can be sterilized by exposing the fibrous material to radiation, such as infrared radiation, ultraviolet radiation, or an ionizing radiation, such as gamma radiation. The fibrous materials can also be sterilized by temperature adjustment, e.g., heating or cooling the fibrous material under conditions and for a sufficient time to kill any microorganisms, or by employing a chemical sterilant, such as bleach (e.g., sodium hypochlorite), chlorhexidine, or ethylene oxide. The fibrous materials can also be sterilized by using a competitive organism, such as yeast against bacteria.


Referring to FIGS. 3-8, in some embodiments, the average opening size of the first screen 16 is less than 0.79 mm ( 1/32 inch, 0.03125 inch), e.g., less than 0.51 mm ( 1/50 inch, 0.02000 inch), less than 0.40 mm ( 1/64 inch, 0.015625 inch), less than 0.23 mm (0.009 inch), less than 0.20 mm ( 1/128 inch, 0.0078125 inch), less than 0.18 mm (0.007 inch), less than 0.13 mm (0.005 inch), or even less than less than 0.10 mm ( 1/256 inch, 0.00390625 inch). Screen 16 is prepared by interweaving monofilaments 52 having an appropriate diameter to give the desired opening size. For example, the monofilaments can be made of a metal, e.g., stainless steel. As the opening sizes get smaller, structural demands on the monofilaments may become greater. For example, for opening sizes less than 0.40 mm, it can be advantageous to make the screens from monofilaments made from a material other than stainless steel, e.g., titanium, titanium alloys, amorphous metals, nickel, tungsten, rhodium, rhenium, ceramics, or glass. In some embodiments, the screen is made from a plate, e.g. a metal plate, having apertures, e.g., cut into the plate using a laser.


In some embodiments, the second fibrous 14 is sheared and passed through the first screen 16, or a different sized screen. In some embodiments, the second fibrous material 14 is passed through a second screen having an average opening size equal to or less than that of first screen 16.


Referring to FIG. 9, a third fibrous material 62 can be prepared from the second fibrous material 14 by shearing the second fibrous material 14 and passing the resulting material through a second screen 60 having an average opening size less than the first screen 16.


Fiber sources include cellulosic fiber sources, including paper and paper products like those shown in FIGS. 10A (polycoated paper) and 10B (Kraft paper), and lignocellulosic fiber sources, including wood, and wood-related materials, e.g., particle board. Other suitable fiber sources include natural fiber sources, e.g., grasses, rice hulls, bagasse, cotton, jute, hemp, flax, bamboo, sisal, abaca, straw, corn cobs, rice hulls, coconut hair; fiber sources high in α-cellulose content, e.g., cotton; synthetic fiber sources, e.g., extruded yarn (oriented yarn or un-oriented yarn) or carbon fiber sources; inorganic fiber sources; and metal fiber sources. Natural or synthetic fiber sources can be obtained from virgin scrap textile materials, e.g., remnants or they can be post consumer waste, e.g., rags. When paper products are used as fiber sources, they can be virgin materials, e.g., scrap virgin materials, or they can be post-consumer waste. Aside from virgin raw materials, post-consumer, industrial (e.g., offal), and processing waste (e.g., effluent from paper processing) can also be used as fiber sources. Also, the fiber source can be obtained or derived from human (e.g., sewage), animal or plant wastes. Additional fiber sources have been described in U.S. Pat. Nos. 6,448,307, 6,258,876, 6,207,729, 5,973,035 and 5,952,105, each of which is incorporated by reference herein in its entirety.


Blends of any of the above fibrous sources may be used.


Generally, the fibers of the fibrous materials can have a relatively large average length-to-diameter ratio (e.g., greater than 20-to-1), even if they have been sheared more than once. In addition, the fibers of the fibrous materials described herein may have a relatively narrow length and/or length-to-diameter ratio distribution. Without wishing to be bound by any particular theory, it is currently believed that the relatively large average length-to-diameter ratio and the relatively narrow length and/or length-to-diameter ratio distribution are, at least in part, responsible for the ease at which the fibrous materials are dispersed in a resin, e.g., a molten thermoplastic resin. It is also believed that the relatively large average length-to-diameter ratio and the relatively narrow length and/or length-to-diameter ratio distribution are, at least in part, responsible for the consistent properties of the fibrous materials, the predictable rheology modification the fibrous materials impart on a resin, the ease at which the combinations of the fibrous materials and resins are cast, extruded and injection molded, the ease in which the fibrous materials pass through small, often torturous channels and openings, and the excellent surface finishes possible with molded parts, e.g., glossy finishes and/or finishes substantially devoid of visible speckles.


As used herein, average fiber widths (i.e., diameters) are those determined optically by randomly selecting approximately 5,000 fibers. Average fiber lengths are corrected length-weighted lengths. BET (Brunauer, Emmet and Teller) surface areas are multi-point surface areas, and porosities are those determined by mercury porosimetry.


The average length-to-diameter ratio of the second fibrous material 14 can be, e.g. greater than 8/1, e.g., greater than 10/1, greater than 15/1, greater than 20/1, greater than 25/1, or greater than 50/1. An average length of the second fibrous material 14 can be, e.g., between about 0.5 mm and 2.5 mm, e.g., between about 0.75 mm and 1.0 mm, and an average width (i.e., diameter) of the second fibrous material 14 can be, e.g., between about 5 μm and 50 μm, e.g., between about 10 μm and 30 μm.


In some embodiments, a standard deviation of the length of the second fibrous material 14 is less than 60 percent of an average length of the second fibrous material 14, e.g., less than 50 percent of the average length, less than 40 percent of the average length, less than 25 percent of the average length, less than 10 percent of the average length, less than 5 percent of the average length, or even less than 1 percent of the average length.


In some embodiments, a BET surface area of the second fibrous material 14 is greater than 0.1 m2/g, e.g., greater than 0.25 m2/g, greater than 0.5 m2/g, greater than 1.0 m2/g, greater than 1.5 m2/g, greater than 1.75 m2/g, greater than 5.0 m2/g, greater than 10 m2/g, greater than 25 m2/g, greater than 35 m2/g, greater than 50 m2/g, greater than 60 m2/g, greater than 75 m2/g, greater than 100 m2/g, greater than 150 m2/g, greater than 200 m2/g, or even greater than 250 m2/g. A porosity of the second fibrous material 14 can be, e.g., greater than 20 percent, greater than 25 percent, greater than 35 percent, greater than 50 percent, greater than 60 percent, greater than 70 percent, e.g., greater than 80 percent, greater than 85 percent, greater than 90 percent, greater than 92 percent, greater than 94 percent, greater than 95 percent, greater than 97.5 percent, greater than 99 percent, or even greater than 99.5 percent.


In some embodiments, a ratio of the average length-to-diameter ratio of the first fibrous material 12 to the average length-to-diameter ratio of the second fibrous material 14 is, e.g., less than 1.5, e.g., less than 1.4, less than 1.25, less than 1.1, less than 1.075, less than 1.05, less than 1.025, or even substantially equal to 1.


In particular embodiments, the second fibrous material 14 is sheared again and the resulting fibrous material passed through a second screen having an average opening size less than the first screen to provide a third fibrous material 62. In such instances, a ratio of the average length-to-diameter ratio of the second fibrous material 14 to the average length-to-diameter ratio of the third fibrous material 62 can be, e.g., less than 1.5, e.g., less than 1.4, less than 1.25, or even less than 1.1.


In some embodiments, the third fibrous material 62 is passed through a third screen to produce a fourth fibrous material. The fourth fibrous material can be, e.g., passed through a fourth screen to produce a fifth material. Similar screening processes can be repeated as many times as desired to produce the desired fibrous material having the desired properties.


In some embodiments, the desired fibrous material includes fibers having an average length-to-diameter ratio of greater than 5 and having a standard deviation of the fiber length that is less than sixty percent of the average length. For example, the average length-to-diameter ratio can be greater than 10/1, e.g., greater than 25/1, or greater than 50/1, and the average length can be between about 0.5 mm and 2.5 mm, e.g., between about 0.75 mm and 1.0 mm. An average width of the fibrous material can be between about 5 μm and 50 μm, e.g., between about 10 μm and 30 μm. For example, the standard deviation can be less than 50 percent of the average length, e.g., less than 40 percent, less than 30 percent, less than 25 percent, less than 20 percent, less than 10 percent, less than 5 percent, or even less than 1 percent of the average length. A desirable fibrous material can have, e.g., a BET surface area of greater than 0.5 m2/g, e.g., greater than 1.0 m2/g, greater than 1.5 m2/g, greater than 1.75 m2/g., greater than 5 m2/g, greater than 10 m2/g, greater than 25.0 m2/g, greater than 50.0 m2/g, greater than 75.0 m2/g, or even greater than 100.0 m2/g. A desired material can have, e.g., a porosity of greater than 70 percent, e.g., greater than 80 percent, greater than 87.5 percent, greater than 90 percent, greater than 92.5, greater than 95, greater than 97.5, or even greater than 99 percent. A particularly preferred embodiment has a BET surface area of greater than 1.25 m2/g and a porosity of greater than 85 percent.


Fibrous Material/Resin Composites


Composites including any of the fibrous materials or blends of any of the fibrous materials described herein (including any of the fibrous materials disclosed in U.S. Pat. Nos. 6,448,307, 6,258,876, 6,207,729, 5,973,035 and 5,952,105), e.g., the first 12 or second fibrous material 14, and a resin, e.g., a thermoplastic resin or a thermosetting resin, can be prepared by combining the desired fibrous material and the desired resin. The desired fibrous material can be combined with the desired resin, e.g., by mixing the fibrous material and the resin in an extruder or other mixer. To form the composite, the fibrous material can be combined with the resin as the fibrous material itself or as a densified fibrous material that can be re-opened during the combining Such a densified material is discussed in International Application No. PCT/US2006/010648, filed on Mar. 23, 2006, the disclosure of which is incorporated herein by reference in its entirety.


Examples of thermoplastic resins include rigid and elastomeric thermoplastics. Rigid thermoplastics include polyolefins (e.g., polyethylene, polypropylene, or polyolefin copolymers), polyesters (e.g., polyethylene terephthalate), polyamides (e.g., nylon 6, 6/12 or 6/10), and polyethyleneimines. Examples of elastomeric thermoplastic resins include elastomeric styrenic copolymers (e.g., styrene-ethylene-butylene-styrene copolymers), polyamide elastomers (e.g., polyether-polyamide copolymers) and ethylene-vinyl acetate copolymer.


In some embodiments, the thermoplastic resin has a melt flow rate of between 10 g/10 minutes to 60 g/10 minutes, e.g., between 20 g/10 minutes to 50 g/10 minutes, or between 30 g/10 minutes to 45 g/10 minutes, as measured using ASTM 1238.


In some embodiments, compatible blends of any of the above thermoplastic resins can be used.


In some embodiments, the thermoplastic resin has a polydispersity index (PDI), i.e., a ratio of the weight average molecular weight to the number average molecular weight, of greater than 1.5, e.g., greater than 2.0, greater than 2.5, greater than 5.0, greater than 7.5, or even greater than 10.0.


In specific embodiments, polyolefins or blends of polyolefins are utilized as the thermoplastic resin.


Examples of thermosetting resins include natural rubber, butadiene-rubber and polyurethanes.


In addition to the desired fibrous material and resin, additives, e.g., in the form of a solid or a liquid, can be added to the combination of the fibrous material and resin. For example, suitable additives include fillers such as calcium carbonate, graphite, wollastonite, mica, glass, fiber glass, silica, and talc; inorganic flame retardants such as alumina trihydrate or magnesium hydroxide; organic flame retardants such as chlorinated or brominated organic compounds; ground construction waste; ground tire rubber; carbon fibers; or metal fibers or powders (e.g., aluminum, stainless steel). These additives can reinforce, extend, or change electrical, mechanical or compatibility properties. Other additives include fragrances, coupling agents, compatibilizers, e.g., maleated polypropylene, processing aids, lubricants, e.g., fluorinated polyethylene, plasticizers, antioxidants, opacifiers, heat stabilizers, colorants, foaming agents, impact modifiers, polymers, e.g., degradable polymers, photostabilizers, biocides, antistatic agents, e.g., stearates or ethoxylated fatty acid amines. Suitable antistatic compounds include conductive carbon blacks, carbon fibers, metal fillers, cationic compounds, e.g., quaternary ammonium compounds, e.g., N-(3-chloro-2-hydroxypropyl)-trimethylammonium chloride, alkanolamides, and amines. Representative degradable polymers include polyhydroxy acids, e.g., polylactides, polyglycolides and copolymers of lactic acid and glycolic acid, poly(hydroxybutyric acid), poly(hydroxyvaleric acid), poly[lactide-co-(e-caprolactone)], poly[glycolide-co-(e-caprolactone)], polycarbonates, poly(amino acids), poly(hydroxyalkanoate)s, polyanhydrides, polyorthoesters and blends of these polymers.


In some embodiments, the fibrous material is sterilized prior to combining with a resin to kill any microorganisms that may be on the fibrous material. For example, the fibrous material can be sterilized by exposing the fibrous material to radiation; by heating the fibrous material under conditions and for a sufficient time to kill any microorganisms, e.g., boiling at normal atmospheric pressure; or by employing chemical sterilants.


It can be advantageous to make the composite smell and/or look like natural wood, e.g., cedarwood. For example, the fragrance, e.g., natural wood fragrance, can be compounded into the resin used to make the composite. In some implementations, the fragrance is compounded directly into the resin as an oil. For example, the oil can be compounded into the resin using a roll mill, e.g., a Banbury® mixer or an extruder, e.g., a twin-screw extruder with counter-rotating screws. An example of a Banbury® mixer is the F-Series Banbury® mixer, manufactured by Farrel. An example of a twin-screw extruder is the WP ZSK 50 MEGAcompunder™, manufactured by Krupp Werner & Pfleiderer. After compounding, the scented resin can be added to the fibrous material and extruded or molded. Alternatively, master batches of fragrance-filled resins are available commercially from International Flavors and Fragrances, under the tradename PolyIff™ or from the RTP Company. In some embodiments, the amount of fragrance in the composite is between about 0.005% by weight and about 10% by weight, e.g., between about 0.1% and about 5% or 0.25% and about 2.5%.


Other natural wood fragrances include evergreen or redwood. Other fragrances include peppermint, cherry, strawberry, peach, lime, spearmint, cinnamon, anise, basil, bergamot, black pepper, camphor, chamomile, citronella, eucalyptus, pine, fir, geranium, ginger, grapefruit, jasmine, juniperberry, lavender, lemon, mandarin, marjoram, musk, myrhh, orange, patchouli, rose, rosemary, sage, sandalwood, tea tree, thyme, wintergreen, ylang ylang, vanilla, new car or mixtures of these fragrances. In some embodiments, the amount of fragrance in the fibrous material-fragrance combination is between about 0.005% by weight and about 20% by weight, e.g., between about 0.1% and about 5% or 0.25% and about 2.5%. Even other fragrances and methods are described U.S. Provisional Application Ser. No. 60/688,002, filed Jun. 7, 2005, the entire disclosure of which is hereby incorporated by reference herein.


Any of the fibrous material described above, e.g., the first 12 or second fibrous material 14, together with a resin, can be used to form articles such as pipes, panels, decking materials, boards, housings, sheets, blocks, bricks, poles, fencing, members, doors, shutters, awnings, shades, signs, frames, window casings, backboards, flooring, tiles, railroad ties, trays, tool handles, stalls, films, wraps, tapes, boxes, baskets, racks, casings, binders, dividers, walls, mats, frames, bookcases, sculptures, chairs, tables, desks, toys, games, pallets, wharves, piers, boats, masts, septic tanks, automotive panels, computer housings, above- and below-ground electrical casings, furniture, picnic tables, benches, shelters, trays, hangers, servers, caskets, book covers, canes, crutches, insulation, thread, cloth, novelties, house wares and structures.


The fibrous material may be dyed before combining with the resin and compounding to form the composites described above. In some embodiments, this dyeing can be helpful in masking or hiding the fibrous material, especially large agglomerations of the fibrous material, in molded or extruded parts. Such large agglomerations, when present in relatively high concentrations, can show up as speckles in the surfaces of the molded or extruded parts.


For example, the desired fibrous material can be dyed using an acid dye, direct dye or a reactive dye. Such dyes are available from Spectra Dyes, Kearny, N.J. or Keystone Aniline Corporation, Chicago, Ill. Specific examples of dyes include SPECTRA™ LIGHT YELLOW 2G, SPECTRACID™ YELLOW 4GL CONC 200, SPECTRANYL™ RHODAMINE 8, SPECTRANYL™ NEUTRAL RED B, SPECTRAMINE™ BENZOPERPURINE, SPECTRADIAZO™ BLACK OB, SPECTRAMINE™ TURQUOISE G, and SPECTRAMINE™ GREY LVL 200%, each being available from Spectra Dyes.


In some embodiments, resin color concentrates containing pigments are blended with dyes. When such blends are then compounded with the desired fibrous material, the fibrous material may be dyed in-situ during the compounding. Color concentrates are available from Clariant.


EXAMPLES

Scanning electron micrographs were obtained on a JEOL 65000 field emission scanning electron microscope. Fiber lengths and widths (i.e., diameters) were determined by Integrated Paper Services, Inc., Appleton, Wis., using an automated analyzer (TAPPI T271). BET surface area was determined by Micromeritics Analytical Services, as were porosity and bulk density.


Example 1

Preparation of Fibrous Material from Polycoated Paper


A 1500 pound skid of virgin, half-gallon juice cartons made of un-printed polycoated white Kraft board having a bulk density of 20 lb/ft3 was obtained from International Paper. The material was cut into pieces 8¼ inches by 11 inches using a guillotine cutter and fed to a Munson rotary knife cutter, Model SC30. Model SC30 is equipped with four rotary blades, four fixed blades, and a discharge screen having ⅛ inch openings. The gap between the rotary and fixed blades was set to approximately 0.020 inch. The rotary knife cutter sheared the confetti-like pieces across the knife-edges, tearing the pieces apart and releasing a fibrous material at a rate of about one pound per hour. The fibrous material had a BET surface area of 0.9748 m2/g +/−0.0167 m2/g, a porosity of 89.0437 percent and a bulk density (@0.53 psia) of 0.1260 g/mL. An average length of the fibers was 1.141 mm and an average width of the fibers was 0.027 mm, giving an average L/D of 42:1. Scanning electron micrographs of the fibrous material are shown in FIGS. 11 and 12 at 25× magnification and 1000× magnification, respectively.


Example 2

Preparation of Fibrous Material from Bleached Kraft Board


A 1500 pound skid of virgin bleached white Kraft board having a bulk density of 30 lb/ft3 was obtained from International Paper. The material was cut into pieces 8¼ inches by 11 inches using a guillotine cutter and fed to a Munson rotary knife cutter, Model SC30. The discharge screen had ⅛ inch openings. The gap between the rotary and fixed blades was set to approximately 0.020 inch. The rotary knife cutter sheared the confetti-like pieces, releasing a fibrous material at a rate of about one pound per hour. The fibrous material had a BET surface area of 1.1316 m2/g +/−0.0103 m2/g, a porosity of 88.3285 percent and a bulk density (@0.53 psia) of 0.1497 g/mL. An average length of the fibers was 1.063 mm and an average width of the fibers was 0.0245 mm, giving an average L/D of 43:1. Scanning electron micrographs of the fibrous material are shown in FIGS. 13 and 14 at 25× magnification and 1000× magnification, respectively.


Example 3

Preparation of Twice Sheared Fibrous Material from Bleached Kraft Board


A 1500 pound skid of virgin bleached white Kraft board having a bulk density of 30 lb/ft3 was obtained from International Paper. The material was cut into pieces 8¼ inches by 11 inches using a guillotine cutter and fed to a Munson rotary knife cutter, Model SC30. The discharge screen had 1/16 inch openings. The gap between the rotary and fixed blades was set to approximately 0.020 inch. The rotary knife cutter the confetti-like pieces, releasing a fibrous material at a rate of about one pound per hour. The material resulting from the first shearing was fed back into the same setup described above and sheared again. The resulting fibrous material had a BET surface area of 1.4408 m2/g +/−0.0156 m2/g, a porosity of 90.8998 percent and a bulk density (@0.53 psia) of 0.1298 g/mL. An average length of the fibers was 0.891 mm and an average width of the fibers was 0.026 mm, giving an average L/D of 34:1. Scanning electron micrographs of the fibrous material are shown in FIGS. 15 and 16 at 25× magnification and 1000× magnification, respectively.


Example 4

Preparation of Thrice Sheared Fibrous Material from Bleached Kraft Board


A 1500 pound skid of virgin bleached white Kraft board having a bulk density of 30 lb/ft3 was obtained from International Paper. The material was cut into pieces 8¼ inches by 11 inches using a guillotine cutter and fed to a Munson rotary knife cutter, Model SC30. The discharge screen had ⅛ inch openings. The gap between the rotary and fixed blades was set to approximately 0.020 inch. The rotary knife cutter sheared the confetti-like pieces across the knife-edges. The material resulting from the first shearing was fed back into the same setup and the screen was replaced with a 1/16 inch screen. This material was sheared. The material resulting from the second shearing was fed back into the same setup and the screen was replaced with a 1/32 inch screen. This material was sheared. The resulting fibrous material had a BET surface area of 1.6897 m2/g +/−0.0155 m2/g, a porosity of 87.7163 percent and a bulk density (@0.53 psia) of 0.1448 g/mL. An average length of the fibers was 0.824 mm and an average width of the fibers was 0.0262 mm, giving an average L/D of 32:1. Scanning electron micrographs of the fibrous material are shown in FIGS. 17 and 18 at 25× magnification and 1000× magnification, respectively.


Other Compositions and Uses of the Fibrous Materials


Compositions can be prepared that include any of the fibrous materials described herein, including any of the fibrous materials, resins, additives or other components disclosed in U.S. Pat. Nos. 6,448,307, 6,258,876, 6,207,729, 5,973,035 and 5,952,105). For example, any of the fibrous materials described herein can be combined with a solid, a liquid or a gas, e.g., a chemical or chemical formulation (in the solid or liquid state), such as a pharmaceutical (e.g., an antibiotic), an agricultural material (e.g., plant seeds, a fertilizer, herbicide or pesticide), or an enzyme or a formulation that includes enzymes. Compositions that include one or more type of bacteria or bacteria in combination with one or more enzymes can also be prepared.


Such compositions can take advantage of the fibrous material's desirable properties. For example, any of the fibrous materials can be used to absorb chemicals, potentially absorbing many times their own weight. For example, the fibrous materials can be used to absorb spilled oil, or other chemicals. Combining these fibrous materials with a microorganism, such as a bacterium, that can metabolize the oil or chemical can aid in cleanup. For example, the fibrous materials can be combined with solutions of enzymes, dried, and then used in pet bedding, or combined with a pharmaceutical and used for delivering a therapeutic agent, such as a drug. If desired, the fibrous materials can be combined with a degradable polymer, e.g., polyglycolic acid, polylactic acid and copolymers of glycolic and lactic acid. Other degradable materials that can be used have been discussed above.


Compositions that include fibrous materials, e.g., cellulosic or lignocellulosic materials and, e.g., chemicals or chemical formulations in the solid, liquid or gaseous state, can be prepared, e.g., in various immersion, spraying, or blending apparatuses. For example, the compositions can be prepared using ribbon blenders, cone blenders, double cone blenders, and Patterson-Kelly “V” blenders.


If desired, lignin can be removed from any of the fibrous materials that include lignin, such as lignocellulosic materials. Also, if desired, the fibrous material can be sterilized to kill any microorganisms that may be on the fibrous material. For example, the fibrous material can be sterilized by exposing the fibrous material to radiation, such as infrared radiation, ultraviolet radiation, or an ionizing radiation, such as gamma radiation. The fibrous materials can also be sterilized by heating the fibrous material under conditions and for a sufficient time to kill any microorganisms, or by employing a chemical sterilant, such as bleach (e.g., sodium hypochlorite), chlorhexidine, or ethylene oxide.


Any of the fibrous materials can be washed, e.g., with a liquid such as water, to remove any undesirable impurities and/or contaminants.


In a specific application, the fibrous materials can be used as a feedstock for various microorganisms, such as yeast and bacteria, that can ferment or otherwise work on the fibrous materials to produce a useful material, such as a fuel, e.g., an alcohol, an organic acid, a hydrocarbon or hydrogen, or a protein.


The alcohol produced can be a monohydroxy alcohol, e.g., ethanol, or a polyhydroxy alcohol, e.g., ethylene glycol or glycerin. Examples of alcohols that can be produced include methanol, ethanol, propanol, isopropanol, butanol, ethylene glycol, propylene glycol, 1,4-butane diol, glycerin or mixtures of these alcohols. The organic acid produced can a monocarboxylic acid or a polycarboxylic acid. Examples of organic acids include formic acid, acetic acid, propionic acid, butyric acid, valeric acid, caproic, palmitic acid, stearic acid, oxalic acid, malonic acid, succinic acid, glutaric acid, oleic acid, linoleic acid, glycolic acid, lactic acid, γ-hydroxybutyric acid or mixtures of these acids. The hydrocarbon produced can be, e.g., an alkane or an alkene. Examples of hydrocarbons that can be produced include methane, ethane, propane, isobutene, pentane, n-hexane or mixtures of these hydrocarbons.


In a particular embodiment, a fiber source that includes a cellulosic and/or lignocellulosic fiber source is sheared to provide a first fibrous material. The first fibrous material is then passed through a first screen having an average opening size of about 1.59 mm or less ( 1/16 inch, 0.0625 inch) to provide a second fibrous material. The second fibrous material is combined with a bacterium and/or enzyme. In this particular embodiment, the bacterium and/or enzyme is capable of utilizing the second fibrous material directly without pre-treatment to produce a fuel that includes hydrogen, an alcohol, an organic acid and/or a hydrocarbon.


In some embodiments, prior to combining the bacteria and/or enzyme, the fibrous material is sterilized to kill any microorganisms that may be on the fibrous material. For example, the fibrous material can be sterilized by exposing the fibrous material to radiation, such as infrared radiation, ultraviolet radiation, or an ionizing radiation, such as gamma radiation. The microorganisms can also be killed using chemical sterilants, such as bleach (e.g., sodium hypochlorite), chlorhexidine, or ethylene oxide.


In a particular embodiment, the cellulosic and/or lignocellulosic material of the fibrous material is first broken down into lower molecular weight sugars, which are then added to a solution of yeast and/or bacteria that ferment the lower molecular weight sugars to produce ethanol. The cellulosic and/or lignocellulosic material can be broken down using chemicals, such as acids or bases, by enzymes, or by a combination of the two. Chemical hydrolysis of cellulosic materials is described by Bjerre, in Biotechnol. Bioeng., 49:568 (1996) and Kim in Biotechnol. Prog., 18:489 (2002), which are each hereby incorporated by reference herein in their entirety.


Bioethanol strategies are discussed by DiPardo in Journal of Outlook for Biomass Ethanol Production and Demand (EIA Forecasts), 2002; Sheehan in Biotechnology Progress, 15:8179, 1999; Martin in Enzyme Microbes Technology, 31:274, 2002; Greer in BioCycle, 61-65, April 2005; Lynd in Microbiology and Molecular Biology Reviews, 66:3, 506-577, 2002; Ljungdahl et al. in U.S. Pat. No. 4,292,406; and Bellamy in U.S. Pat. No. 4,094,742, which are each hereby incorporated by reference herein in their entirety.


Referring now to FIG. 19, a fibrous material having a low bulk density can be combined with a microorganism, e.g., freeze-dried yeast or bacteria, and/or a enzyme, and then revertibly densified to a fibrous material composition having a higher bulk density. For example, a fibrous material composition having a bulk density of 0.05 g/cm3 can be densified by sealing the fibrous material in a relatively gas impermeable structure, e.g., a bag made of polyethylene or a bag made of alternating layers of polyethylene and a nylon, and then evacuating the entrapped gas, e.g., air, from the structure. After evacuation of the air from the structure, the fibrous material can have, e.g., a bulk density of greater than 0.3 g/cm3, e.g., 0.5 g/cm3, 0.6 g/cm3, 0.7 g/cm3 or more, e.g., 0.85 g/cm3. This can be advantageous when it is desirable to transport the fibrous material to another location, e.g., a remote manufacturing plant, where the fibrous material composition can be added to a solution, e.g., to produce ethanol. After piercing the substantially gas impermeable structure, the densified fibrous material reverts to nearly its initial bulk density, e.g., greater than 60 percent of its initial bulk density, e.g., 70 percent, 80 percent, 85 percent or more, e.g., 95 percent of its initial bulk density. To reduce static electricity in the fibrous material, an anti-static agent can be added to the fibrous material. For example, a chemical anti-static compound, e.g., a cationic compound, e.g., quaternary ammonium compound, can be added to the fibrous material.


In some embodiments, the structure, e.g., bag, is formed of a material that dissolves in a liquid, such as water. For example, the structure can be formed from a polyvinyl alcohol so that it dissolves when in contact with a water-based system. Such embodiments allow densified structures to be added directly to solutions, e.g., that include a microorganism, without first releasing the contents of the structure, e.g., by cutting.


Other Embodiments


While certain embodiments have been described, other embodiments are possible.


While some embodiments use screens to provide a desired fibrous material, in some embodiments, no screens are used to make the desired fibrous. For example, in some embodiments, a fiber source is sheared between a first pair of blades that defines a first gap, resulting in a first fibrous material. The first fibrous material is then sheared between a second pair of blades that define a second gap that is smaller than the first gap, resulting in a second fibrous material. Similar screening processes can be repeated as many times as desired to produce the desired fibrous material having the desired properties.


In some embodiments, a ratio of an average length-to-diameter ratio of the first fibrous material to an average length-to-diameter of the second fibrous material is less than 1.5.


Still other embodiments are within the scope of the following claims.

Claims
  • 1. A method of making a fuel, the method comprising: mechanically treating a fiber source to provide a first fibrous material;passing the first fibrous material through a first screen having an average opening size of about 1.59 mm or less to provide a second fibrous material; andcombining the second fibrous material with a microorganism, the microorganism utilizing the second fibrous material to produce a fuel selected from the group consisting of hydrogen, alcohols, organic acids, hydrocarbons, and mixtures thereof.
  • 2. The method of claim 1, wherein the alcohol is selected from the group consisting of methanol, ethanol, propanol, isopropanol, butanol, ethylene glycol, propylene glycol, 1, 4-butane diol, glycerin, and mixtures thereof.
  • 3. The method of claim 1, wherein the organic acid is selected from the group consisting of formic acid, acetic acid, propionic acid, butyric acid, valeric acid, caproic, palmitic acid, stearic acid, oxalic acid, malonic acid, succinic acid, glutaric acid, oleic acid, linoleic acid, glycolic acid, lactic acid, γ-hydroxybutyric acid and mixtures thereof.
  • 4. The method of claim 1, wherein the hydrocarbon is selected from the group consisting of methane, ethane, propane, isobutene, pentane, n-hexane, and mixtures thereof
  • 5. The method of claim 1, further comprising sterilizing the second fibrous material prior to combining with the microorganism.
  • 6. The method of claim 5, wherein the sterilizing is performed by exposing the second fibrous material to a radiation source.
  • 7. The method of claim 1, wherein the fiber source comprises a cellulosic or lignocellulosic material.
  • 8. The method of claim 7, wherein the cellulosic or lignocellulosic material is selected from the group consisting of wood, grasses, rice hulls, bagasse, cotton, jute, hemp, flax, bamboo, sisal, abaca, straw, corn cobs, coconut hair, and paper.
  • 9. The method of claim 1, wherein utilizing the second fibrous material comprises fermenting a low molecular weight sugar derived from the second fibrous material.
  • 10. The method of claim 9 wherein the microorganism comprises a yeast.
  • 11. The method of claim 1 wherein the microorganism hydrolyzes the second fibrous material to provide a hydrolyzed material.
  • 12. The method of claim 11 wherein the hydrolyzed material comprises one or more low molecular weight sugars.
  • 13. The method of claim 11, wherein the alcohol is selected from the group consisting of methanol, ethanol, propanol, isopropanol, butanol, ethylene glycol, propylene glycol, 1, 4-butane diol, glycerin, and mixtures thereof.
  • 14. The method of claim 11, wherein the organic acid is selected from the group consisting of formic acid, acetic acid, propionic acid, butyric acid, valeric acid, caproic, palmitic acid, stearic acid, oxalic acid, malonic acid, succinic acid, glutaric acid, oleic acid, linoleic acid, glycolic acid, lactic acid, γ-hydroxybutyric acid and mixtures thereof.
  • 15. The method of claim 11, wherein the hydrocarbon is selected from the group consisting of methane, ethane, propane, isobutene, pentane, n-hexane, and mixtures thereof.
  • 16. The method of claim 11, further comprising sterilizing the second fibrous material prior to combining with the microorganism.
  • 17. The method of claim 16, wherein the sterilizing is performed by exposing the second fibrous material to a radiation source.
  • 18. The method of claim 11, wherein the fiber source comprises a cellulosic or lignocellulosic material.
  • 19. The method of claim 18, wherein the cellulosic or lignocellulosic material is selected from the group consisting of wood, grasses, rice hulls, bagasse, cotton, jute, hemp, flax, bamboo, sisal, abaca, straw, corn cobs, coconut hair, and paper.
  • 20. The method of claim 11, further comprising combining the hydrolyzed material with a microorganism and allowing the combination to ferment.
  • 21. The method of claim 20 wherein the microorganism combined with the hydrolyzed material comprises a yeast.
  • 22. The method of claim 11 wherein the microorganism comprises a bacterium or an enzyme.
  • 23. The method of claim 1 wherein mechanically treating comprises shearing.
  • 24. The method of claim 1 wherein mechanically treating comprises grinding or milling.
  • 25. The method of claim 1 wherein the microorganism comprises a bacterium or an enzyme.
CROSS REFERENCE TO RELATED APPLICATIONS

This application is a divisional (and claims benefit of priority under 35 U.S.C. §121) of U.S. Ser. No. 11/453,951, filed on Jun. 15, 2006, which was a continuation-in-part (CIP) of, and claimed the benefit of priority from, International Application No. PCT/US2006/010648, filed on Mar. 23, 2006, which claimed priority from U.S. Provisional Patent Application Ser. No. 60/711,057, filed Aug. 24, 2005. The entire content of each application is hereby incorporated by reference herein.

US Referenced Citations (351)
Number Name Date Kind
1824221 Mason Sep 1931 A
2516847 Boehm Aug 1950 A
2519442 Delorme et al. Aug 1950 A
2558378 Petry Jun 1951 A
2635976 Meiler et al. Apr 1953 A
2658828 Pattilloch Nov 1953 A
2665261 Baker Jan 1954 A
2680102 Becher Jun 1954 A
2757150 Heritage Jul 1956 A
2789903 Lukman et al. Apr 1957 A
2935763 Newman et al. May 1960 A
3308218 Wiegand et al. Mar 1967 A
3309444 Schueler Mar 1967 A
3493527 Schueler Feb 1970 A
3516953 Wood Jun 1970 A
3596314 Krugler Aug 1971 A
3645939 Gaylord Feb 1972 A
3671615 Price Jun 1972 A
3697364 Boustany Oct 1972 A
3709845 Boustany Jan 1973 A
3718536 Downs et al. Feb 1973 A
3836412 Boustany et al. Sep 1974 A
3878143 Baumann et al. Apr 1975 A
3888810 Shinomura Jun 1975 A
3943079 Hamed Mar 1976 A
3956541 Pringle May 1976 A
3956555 McKean May 1976 A
4005162 Bucking Jan 1977 A
4016232 Pringle Apr 1977 A
4020212 Erickson Apr 1977 A
4033913 Sunden Jul 1977 A
4045603 Smith Aug 1977 A
4056591 Goettler et al. Nov 1977 A
4058580 Flanders Nov 1977 A
4097648 Pringle Jun 1978 A
4112038 Garner Sep 1978 A
4113908 Shinomura Sep 1978 A
4115497 Halmo et al. Sep 1978 A
4145389 Smith Mar 1979 A
4168251 Schinzel et al. Sep 1979 A
4187352 Klobbie Feb 1980 A
4188259 Mamers et al. Feb 1980 A
4203876 Dereppe et al. May 1980 A
4204010 Kramm et al. May 1980 A
4228116 Colombo et al. Oct 1980 A
4239679 Rolls et al. Dec 1980 A
4244847 Posiviata et al. Jan 1981 A
4244903 Schnause Jan 1981 A
4248743 Goettler Feb 1981 A
4248820 Haataja Feb 1981 A
4250222 Mavel et al. Feb 1981 A
4263184 Leo et al. Apr 1981 A
4265846 Shen et al. May 1981 A
4273688 Porzel et al. Jun 1981 A
4277428 Luck et al. Jul 1981 A
4279790 Nakajima Jul 1981 A
4281039 Miura et al. Jul 1981 A
4290988 Nopper et al. Sep 1981 A
4303019 Haataja et al. Dec 1981 A
4305901 Prince et al. Dec 1981 A
4311554 Herr Jan 1982 A
4311621 Nishizawa et al. Jan 1982 A
4318351 Munk Mar 1982 A
4323625 Coran et al. Apr 1982 A
4328136 Blount May 1982 A
4359534 Kurtzman et al. Nov 1982 A
4368268 Gong Jan 1983 A
4376144 Goettler Mar 1983 A
4382108 Carroll et al. May 1983 A
4393020 Li et al. Jul 1983 A
4400470 Zeikus et al. Aug 1983 A
4414267 Coran et al. Nov 1983 A
4420351 Lussi et al. Dec 1983 A
4426470 Wessling et al. Jan 1984 A
4433813 Whatton et al. Feb 1984 A
4440708 Haataja et al. Apr 1984 A
4454091 Chion et al. Jun 1984 A
4455709 Zanini Jun 1984 A
4480035 Roychodhury Oct 1984 A
4481701 Hewitt Nov 1984 A
4491553 Yamada et al. Jan 1985 A
4503115 Hemels et al. Mar 1985 A
4505869 Nishibori Mar 1985 A
4506037 Suzuki et al. Mar 1985 A
4508595 Gasland Apr 1985 A
4511656 Gong Apr 1985 A
4520530 Pinto Jun 1985 A
4551294 Wottka et al. Nov 1985 A
4559376 Kubat Dec 1985 A
4562218 Fornadel et al. Dec 1985 A
4594372 Natov et al. Jun 1986 A
4597928 Terentiev et al. Jul 1986 A
4608922 Pohl Sep 1986 A
4609624 Rothlisberger Sep 1986 A
4610900 Nishibori Sep 1986 A
4612286 Sherman et al. Sep 1986 A
4624890 Lloyd et al. Nov 1986 A
4632170 Pohl Dec 1986 A
4645631 Hegenstaller et al. Feb 1987 A
4659754 Edwards et al. Apr 1987 A
4663225 Farley et al. May 1987 A
4674414 Nülle et al. Jun 1987 A
4686251 Ostermann et al. Aug 1987 A
4687793 Motegi et al. Aug 1987 A
4713291 Sasaki et al. Dec 1987 A
4716062 Klein Dec 1987 A
4717742 Beshay Jan 1988 A
4734236 Davis Mar 1988 A
4737532 Fujita et al. Apr 1988 A
4738723 Frizzell et al. Apr 1988 A
4746688 Bistak et al. May 1988 A
4769109 Tellvik et al. Sep 1988 A
4769274 Tellvik et al. Sep 1988 A
4791020 Kokta Dec 1988 A
4810445 Lamb, Sr. et al. Mar 1989 A
4812410 Lawford Mar 1989 A
4818604 Tock Apr 1989 A
4833181 Narukawa et al. May 1989 A
4840902 Lawford Jun 1989 A
4840903 Wu Jun 1989 A
4851458 Hopperdietzel Jul 1989 A
4865788 Davis Sep 1989 A
4874095 Warych Oct 1989 A
4894192 Warych Jan 1990 A
4911700 Makoui et al. Mar 1990 A
4915764 Miani Apr 1990 A
4927579 Moore May 1990 A
4929498 Suskind et al. May 1990 A
4935182 Ehner et al. Jun 1990 A
4960548 Ikeda et al. Oct 1990 A
4963603 Felegi, Jr. et al. Oct 1990 A
4968463 Levasseur Nov 1990 A
4973440 Tamura et al. Nov 1990 A
4978489 Radvan et al. Dec 1990 A
4988478 Held Jan 1991 A
5002713 Palardy et al. Mar 1991 A
5008310 Beshay Apr 1991 A
5009586 Pallmann Apr 1991 A
5028266 Rettenmaier Jul 1991 A
5028539 Ingram et al. Jul 1991 A
5057167 Gersbeck Oct 1991 A
5064692 Hofmann et al. Nov 1991 A
5075057 Hoedl Dec 1991 A
5075359 Castagna et al. Dec 1991 A
5082605 Brooks et al. Jan 1992 A
5084135 Brooks et al. Jan 1992 A
5087400 Theuveny Feb 1992 A
5088910 Goforth et al. Feb 1992 A
5093058 Harmon et al. Mar 1992 A
5096046 Goforth et al. Mar 1992 A
5096406 Brooks et al. Mar 1992 A
5100545 Brooks Mar 1992 A
5100603 Neefe Mar 1992 A
5100791 Spindler et al. Mar 1992 A
5102055 Buschmann et al. Apr 1992 A
5104411 Makoui et al. Apr 1992 A
5120776 Raj et al. Jun 1992 A
5124519 Roy et al. Jun 1992 A
5134023 Hsu Jul 1992 A
5134944 Keller et al. Aug 1992 A
5137668 Lamb, Sr. Aug 1992 A
5155147 Dietz et al. Oct 1992 A
5173257 Pearson Dec 1992 A
5177009 Kampen Jan 1993 A
5183837 Lepori et al. Feb 1993 A
5194461 Berquist et al. Mar 1993 A
5196069 Cullingford et al. Mar 1993 A
5198074 Villavicencio et al. Mar 1993 A
5213021 Goforth et al. May 1993 A
5254617 Inoue et al. Oct 1993 A
5268074 Brooks et al. Dec 1993 A
5277758 Brooks et al. Jan 1994 A
5284610 Tai Feb 1994 A
5285973 Goforth et al. Feb 1994 A
5298102 Pohl Mar 1994 A
5331087 Menges Jul 1994 A
5348871 Scott et al. Sep 1994 A
5350370 Jackson et al. Sep 1994 A
5351895 Brooks et al. Oct 1994 A
5366790 Liebel Nov 1994 A
5370999 Stuart Dec 1994 A
5372878 Saito Dec 1994 A
5372939 Lastick et al. Dec 1994 A
5374474 Pratt et al. Dec 1994 A
5380180 Lamb, Sr. Jan 1995 A
5406768 Giuseppe et al. Apr 1995 A
5421205 Pohl Jun 1995 A
5424202 Ingram et al. Jun 1995 A
5432000 Young, Sr. et al. Jul 1995 A
5437766 Van Phan et al. Aug 1995 A
5439542 Liebel Aug 1995 A
5439749 Klasell et al. Aug 1995 A
5441801 Deaner et al. Aug 1995 A
5480602 Nagaich Jan 1996 A
5486553 Deaner et al. Jan 1996 A
5487989 Fowler et al. Jan 1996 A
5497594 Giuseppe et al. Mar 1996 A
5498478 Hansen et al. Mar 1996 A
5498766 Stuart et al. Mar 1996 A
5516472 Laver May 1996 A
5516585 Young, Sr. et al. May 1996 A
5518677 Deaner et al. May 1996 A
5539027 Deaner et al. Jul 1996 A
5540244 Brooks et al. Jul 1996 A
5543205 Liebel Aug 1996 A
5547745 Hansen et al. Aug 1996 A
5554520 Fowler et al. Sep 1996 A
5558933 Anthony Sep 1996 A
5571618 Hansen et al. Nov 1996 A
5574094 Malucelli et al. Nov 1996 A
5582682 Ferretti Dec 1996 A
5582847 Peterson et al. Dec 1996 A
5585155 Heikkila et al. Dec 1996 A
5614570 Hansen et al. Mar 1997 A
5628830 Brink May 1997 A
5637502 Scott et al. Jun 1997 A
5643359 Soroushian et al. Jul 1997 A
5643635 Ahn et al. Jul 1997 A
5663216 Tomka Sep 1997 A
5677154 Van Draanen et al. Oct 1997 A
5682015 Harben Oct 1997 A
5695874 Deaner et al. Dec 1997 A
5705216 Tyson Jan 1998 A
5733758 Nguyen Mar 1998 A
5735916 Lucas et al. Apr 1998 A
5746958 Gustafsson et al. May 1998 A
5753474 Ramey May 1998 A
5759680 Brooks et al. Jun 1998 A
5767177 Omente et al. Jun 1998 A
5773138 Seethamraju et al. Jun 1998 A
5779164 Chieffalo et al. Jul 1998 A
5791262 Knight et al. Aug 1998 A
5819491 Davis Oct 1998 A
5821111 Grady et al. Oct 1998 A
5824246 Reetz Oct 1998 A
5827607 Deaner et al. Oct 1998 A
5837506 Lynd et al. Nov 1998 A
5851469 Muller et al. Dec 1998 A
5871161 Nishibori Feb 1999 A
5874263 Holtzapple et al. Feb 1999 A
5876641 LeClair et al. Mar 1999 A
5882564 Puppin Mar 1999 A
5882905 Saha et al. Mar 1999 A
5888806 Nguyen Mar 1999 A
5932334 Deaner et al. Aug 1999 A
5932456 Van Drannen et al. Aug 1999 A
5942424 Woodward et al. Aug 1999 A
5948505 Puppin Sep 1999 A
5948524 Seethamraju et al. Sep 1999 A
5952105 Medoff et al. Sep 1999 A
5962307 Holtzapple et al. Oct 1999 A
5973035 Medoff et al. Oct 1999 A
5981067 Seethamraju et al. Nov 1999 A
5985429 Plummer et al. Nov 1999 A
6004668 Deaner et al. Dec 1999 A
6007656 Heikkilä et al. Dec 1999 A
6015611 Deaner et al. Jan 2000 A
6015612 Deaner et al. Jan 2000 A
6015703 White et al. Jan 2000 A
6043392 Holtzapple et al. Mar 2000 A
6054207 Finley Apr 2000 A
6090595 Foody et al. Jul 2000 A
6102690 Ingram et al. Aug 2000 A
6106944 Heikkila et al. Aug 2000 A
6122877 Hendrickson et al. Sep 2000 A
6130076 Ingram Oct 2000 A
6207729 Medoff et al. Mar 2001 B1
6210792 Seethamraju et al. Apr 2001 B1
6258175 Lightner Jul 2001 B1
6258876 Medoff et al. Jul 2001 B1
6270883 Sears et al. Aug 2001 B1
6270893 Young, Sr. et al. Aug 2001 B1
6333181 Ingram et al. Dec 2001 B1
6346160 Puppin Feb 2002 B1
6357197 Serino et al. Mar 2002 B1
6409841 Lombard Jun 2002 B1
6410302 Träff et al. Jun 2002 B1
6419828 Russo, Jr. Jul 2002 B1
6420626 Erspamer et al. Jul 2002 B1
6425979 Hansen et al. Jul 2002 B1
6448307 Medoff et al. Sep 2002 B1
6509180 Verser et al. Jan 2003 B1
6521087 Hansen et al. Feb 2003 B2
6555350 Ahring et al. Apr 2003 B2
6620503 Qin et al. Sep 2003 B2
6660506 Nguyen et al. Dec 2003 B2
6670035 Pittman et al. Dec 2003 B2
6692825 Qin et al. Feb 2004 B2
6703227 Jakel et al. Mar 2004 B2
6730249 Sears et al. May 2004 B2
6743507 Barlow et al. Jun 2004 B2
6746976 Urankar et al. Jun 2004 B1
6824682 Branson Nov 2004 B2
6824729 Oin et al. Nov 2004 B2
6835560 Greene Dec 2004 B2
6846657 Heikkilä et al. Jan 2005 B2
6855180 Pinatti et al. Feb 2005 B1
6855182 Sears Feb 2005 B2
6908995 Blount Jun 2005 B2
6927048 Verser et al. Aug 2005 B2
6962722 Dawley et al. Nov 2005 B2
6969781 Graef et al. Nov 2005 B2
7026152 Ingram et al. Apr 2006 B2
7074603 Verser et al. Jul 2006 B2
7135308 Bush et al. Nov 2006 B1
7138257 Galli et al. Nov 2006 B2
7160714 Matano Jan 2007 B2
7169821 Branson Jan 2007 B2
7307108 Medoff et al. Dec 2007 B2
20020010229 Medoff et al. Jan 2002 A1
20020019614 Woon et al. Feb 2002 A1
20020137154 Ingram et al. Sep 2002 A1
20030021915 Rohatgi et al. Jan 2003 A1
20030032702 Medoff et al. Feb 2003 A1
20030054500 Ingram et al. Mar 2003 A1
20030109011 Hood et al. Jun 2003 A1
20030121380 Cowell et al. Jul 2003 A1
20030125688 Keane et al. Jul 2003 A1
20030157675 Otero et al. Aug 2003 A1
20030178365 Zha et al. Sep 2003 A1
20030187102 Medoff et al. Oct 2003 A1
20030207064 Bunyan et al. Nov 2003 A1
20040005461 Nagel et al. Jan 2004 A1
20040040906 Jagtoyen et al. Mar 2004 A1
20040172878 Krylowicz et al. Sep 2004 A1
20040187863 Langhauser Sep 2004 A1
20040219649 Olsen et al. Nov 2004 A1
20040231661 Griffin et al. Nov 2004 A1
20040253696 Grichko Dec 2004 A1
20050069998 Perdices et al. Mar 2005 A1
20050106734 Richard et al. May 2005 A1
20050112739 Golubkov May 2005 A1
20050136520 Kinley et al. Jun 2005 A1
20050164355 Vlasenko et al. Jul 2005 A1
20050191736 Brown et al. Sep 2005 A1
20050272134 Hughes Dec 2005 A1
20050277574 Niedbala et al. Dec 2005 A1
20060005279 Dotson et al. Jan 2006 A1
20060014260 Fan et al. Jan 2006 A1
20060026715 Hood et al. Feb 2006 A1
20060053514 Wu et al. Mar 2006 A1
20060057264 Hughes et al. Mar 2006 A1
20060088922 Yang et al. Apr 2006 A1
20060105442 Wu et al. May 2006 A1
20060127999 Verser et al. Jun 2006 A1
20060234364 Rajgarhia et al. Oct 2006 A1
20060246563 Eroma et al. Nov 2006 A1
20060251764 Abbas et al. Nov 2006 A1
20060292677 Ostrander Dec 2006 A1
20070031953 Dunson, Jr. et al. Feb 2007 A1
20070045456 Medoff Mar 2007 A1
Foreign Referenced Citations (52)
Number Date Country
4781190 Jan 1989 AU
43 31 747 Mar 1995 DE
0 161 766 Nov 1985 EP
0 161 766 Nov 1985 EP
0 330 729 Sep 1988 EP
0 409 525 Jul 1990 EP
2104903 Mar 1983 GB
2171953 Sep 1986 GB
60-168611 Feb 1985 JP
61-243805 Oct 1986 JP
61-273805 Feb 1988 JP
63-033441 Feb 1988 JP
63-033442 Feb 1988 JP
63-033448 Feb 1988 JP
10-130672 May 1998 JP
WO 9207022 Oct 1991 WO
WO 9303135 Feb 1993 WO
WO 9305186 Mar 1993 WO
WO 9408027 Apr 1994 WO
WO 9613468 May 1996 WO
WO 9613551 May 1996 WO
WO 9637627 Nov 1996 WO
WO 9706942 Feb 1997 WO
WO 9710352 Mar 1997 WO
WO 9718173 May 1997 WO
WO 9742307 Nov 1997 WO
WO 9858071 Dec 1998 WO
WO 9911453 Mar 1999 WO
WO 9923138 May 1999 WO
WO 0029183 May 2000 WO
WO 0034567 Jun 2000 WO
WO 0132715 May 2001 WO
WO 0202559 Jan 2002 WO
WO 0214039 Feb 2002 WO
WO 0238786 May 2002 WO
WO 02057317 Jul 2002 WO
WO 03062430 Jul 2003 WO
WO 2005003319 Jan 2005 WO
WO 2005054487 Jun 2005 WO
WO 2005069849 Aug 2005 WO
WO 2005079190 Sep 2005 WO
WO 2005111214 Nov 2005 WO
WO 2005113459 Dec 2005 WO
WO 2005118828 Dec 2005 WO
WO 2006031757 Mar 2006 WO
WO 2006096527 Sep 2006 WO
WO 2006101584 Sep 2006 WO
WO 2006114095 Nov 2006 WO
WO 2006119052 Nov 2006 WO
WO 2006128304 Dec 2006 WO
WO 2007005646 Jan 2007 WO
WO 2007009463 Jan 2007 WO
Related Publications (1)
Number Date Country
20100267097 A1 Oct 2010 US
Divisions (1)
Number Date Country
Parent 11453951 Jun 2006 US
Child 12769931 US