The present invention relates generally to systems and methods for creating extruded products while venting steam and/or gases during the extrusion process.
The pressure to use biodegradable disposable packaging has been steadily increasing in the last decade. As recently as March, 2003, Taiwan has outlawed the use of Styrofoam in disposable packaging. Even China's major cities such as Beijing and Shanghai have outlawed the use of Styrofoam materials in disposable packaging. Various attempts have been made in the prior art to manufacture starch based disposables for use in food service items such as trays, plates, and bowls. Some methods include producing starch based packaging that has materials vented in excess of the final product as can be evidenced when one inspects the finished product. However, these technologies use male and female molds and not extrusion dies. Attempts to extrude starch do not include venting during the extrusion process, and instead include injection gases in an attempt to foam the starch.
Further, the majority of the existing extrusion processes using starch are geared towards producing thick sheeted materials that are then bonded together to form packaging materials that replace thick Styrofoam. Examples are protective packaging for shipping television sets or other similar electronic or heavy systems. Unfortunately, existing efforts have not been successful for producing articles such as toilet paper rolls, chop sticks, or straws primarily due to the inability to reduce pressures during the baking-extrusion process.
Accordingly, there is a need for improved systems and methods for extruding materials while continually venting gases during the extrusion process without any substantial material losses.
In one embodiment of the present invention a method of extruding a material is provided comprising the steps of providing an extrusion head having a plurality of venting gaps for venting a gas; providing an extrusion mixture comprising fibers and water to the extrusion head; extruding the mixture through the extrusion head wherein the step of extruding comprises heating the mixture within the extrusion head such that the gas is released from the mixture; venting the gas from the extrusion head through the plurality of venting gaps such that the remaining mixture is substantially retained by the extrusion head.
In another embodiment, an extrusion head is provided comprising a plurality of venting gaps, wherein the venting gaps are dimensioned to allow for the venting of a gas but substantial retention of the remaining material to be extruded during extrusion and wherein the venting gaps are both radial and axial and the extrusion head is multi-piece.
In order to fully understand the manner in which the above-recited details and other advantages and objects of the invention are obtained, a more detailed description of the invention will be rendered by reference to specific embodiments thereof which are illustrated in the included drawings. Understanding that these drawings depict only typical embodiments of the invention and are not therefore to be considered as limiting of its scope, the invention will be described and explained with additional specificity and detail through the use of accompanying drawings in which:
The following description of the invention is intended to illustrate various embodiments of the invention. As such, the specific modifications discussed are not to be construed as limitations on the scope of the invention. It will be apparent to one skilled in the art that various equivalents, changes, and modifications may be made without departing from the scope of the invention, and it is understood that such equivalent embodiments are to be included herein.
In an embodiment of the present invention, the characteristics of baked goods are used to provide high efficiency systems and methods for extruding starch-based articles as well as similar behavior materials. The systems and methods of the present embodiment accomplish the ability to extrude thin and thick walled extrusions that could not previously be produced due to the inability to vent gases during the extrusion process.
In the present embodiment, vents may be added within an extrusion tunnel, axially and/or through a cross section. Thus, referring to
In one aspect of the present embodiment the composition to be extruded can be water, alcohol or other liquid based. The composition may or may not contain additives such as fibers to improve the properties of the composition.
According to another embodiment of the invention, during the extrusion process, fibers can be chopped up and mixed in an extrusion mixture or fibers can be continuous and pulled through as is performed in composite pulltrusions. For pulltrusions, the fibers are pulled through a material flow opening of the extruder and are baked directly into the starch mixture. This can form a very axially strong product since the fibers are continuous.
According to another embodiment of the invention, the fibers can be knitted together to form different shapes that are then pulled through the extruder and baked into the starch. This method allows for biaxially strong extrusions. It also allows the user to customize required strength solutions by producing a fiber matrix that is then baked into the starch matrix.
According to another embodiment of the invention, the addition of a center mandrel with or without venting features on this mandrel and heated or unheated which would allow for the formation of tupes such as paper roll centers, toilet paper centers, and straws.
One feature of some embodiments of the invention is that the number of venting gaps can be customized, i.e., increased or reduced in numbers or size, to better control the steam and gas release process. It is important to note that not only round shapes but squares, rectangles, octagonal, namely, any cross-section that can be extruded, could be developed for this process. As previously mentioned, the addition of center mandrels could help in forming tube like sections instead of purely solid shapes.
Methods according to some embodiments of the invention generally comprise the steps of mixing at least water and starch together to form a starch-based composition then extruding the composition through the special die heads. The heat starts to bake the starch which in turn forms a skin wherever it comes into contact with the heated extruder surfaces. In addition, the heat turns the water in the composition to steam which is allowed to escape via the venting features. The mixture can have premixed fibers in it or continuous fibers that can also be stitched together or weaved in a shape to improve the overall strength of the finished product.
These and other features of embodiments of the present invention will become more fully apparent from the following description and appended claims, or may be learned by the practice of the invention as set forth hereinafter.
In another embodiment of the present invention mold systems and methods of use are provided such that aqueous starch-based compositions and baked goods articles that use the conversion of water to steam may be produced using an extruder that allows the venting of such gases and/or steam. The extruder is vented in such a way as to allow steam to escape, but retain the composition until the exit end.
More particularly, some embodiments use the physical property of starch and other baked goods to allow the release of steam without releasing the composition. When the mixture first contacts the heated surfaces of the extruder, they form a skin and the water in the mixture starts to turn to steam. This method of allowing the venting of the steam at multiple areas along the extrusion path allows for more dense products that can withstand much higher forces. By adding steam release gaps using the several different methods describes herein, the baking time can be reduced thus increasing output.
By methods of the present embodiment one may produce tube and other extruded shapes that would be cheaper than existing paper and plastic products. Moreover, the overall process tends to be relatively benign and does not use the harsh chemicals normally associated with paper or plastic products.
In another embodiment of the present invention, the above extrusion concept may be applied to any material that can be placed in a cavity which when exposed to the heated surface produces a skin that is semi-permeable to the liquid being turned to gas and is not limited to aqueous based mixtures. Moreover, the mixtures can be edible or non-edible and could include various components for modifying the properties of the mixture, such as the addition of scents or other materials.
Referring to
Referring to
Referring to
Referring to
Referring to
As stated above, the foregoing is merely intended to illustrate various embodiments of the present invention. The specific modifications discussed above are not to be construed as limitations on the scope of the invention. It will be apparent to one skilled in the art that various equivalents, changes, and modifications may be made without departing from the scope of the invention, and it is understood that such equivalent embodiments are to be included herein. All references cited herein are incorporated by reference as if fully set forth herein.
This application is a continuation-in-part of U.S. patent application Ser. No. 10/608,441 filed Jun. 27, 2003 now U.S. Pat. No. 7,481,645, entitled “Method for Use in Baking Articles of Manufacture and Mold for Use in Said Method,” and U.S. patent application Ser. No. 10/928,602 filed Aug. 26, 2004, entitled “Composition for Use in Biodegradable Articles and Method of Use,” which claims the benefit of U.S. Provisional Patent Application No. 60/498,129 filed Aug. 26, 2003, entitled Provisional Patent Application No. 60/498,396 filed Aug. 27, 2003, entitled “Mix Formulation for Use in Biodegradable Articles and Method of Use.” The entirety of each of these applications is incorporated herein by reference.
Number | Name | Date | Kind |
---|---|---|---|
1875482 | Nanna | Sep 1932 | A |
2488189 | Hanson | Nov 1949 | A |
3031030 | Rodenacker | Apr 1962 | A |
3169272 | Maxson | Feb 1965 | A |
3772076 | Keim | Nov 1973 | A |
4491417 | Hold et al. | Jan 1985 | A |
4545752 | Hanamoto et al. | Oct 1985 | A |
4639341 | Hanamoto et al. | Jan 1987 | A |
4900242 | Maus et al. | Feb 1990 | A |
5100586 | Jennings et al. | Mar 1992 | A |
5169566 | Stucky et al. | Dec 1992 | A |
5205863 | Elion et al. | Apr 1993 | A |
5209880 | Miwa | May 1993 | A |
5232496 | Jennings et al. | Aug 1993 | A |
5352111 | Selback | Oct 1994 | A |
5354621 | Liebermann | Oct 1994 | A |
5356579 | Jennings et al. | Oct 1994 | A |
5358676 | Jennings et al. | Oct 1994 | A |
5376320 | Tiefenbacher et al. | Dec 1994 | A |
5385764 | Andersen et al. | Jan 1995 | A |
5412005 | Bastioli et al. | May 1995 | A |
5453310 | Andersen et al. | Sep 1995 | A |
5506046 | Andersen et al. | Apr 1996 | A |
5508072 | Andersen et al. | Apr 1996 | A |
5514430 | Andersen et al. | May 1996 | A |
5523293 | Jane et al. | Jun 1996 | A |
5527387 | Andersen et al. | Jun 1996 | A |
5543186 | Andersen et al. | Aug 1996 | A |
5545297 | Andersen et al. | Aug 1996 | A |
5545450 | Andersen et al. | Aug 1996 | A |
5549859 | Andersen et al. | Aug 1996 | A |
5580409 | Andersen et al. | Dec 1996 | A |
5580624 | Andersen et al. | Dec 1996 | A |
5582670 | Andersen et al. | Dec 1996 | A |
5614307 | Andersen et al. | Mar 1997 | A |
5618341 | Anderson et al. | Apr 1997 | A |
5626954 | Andersen et al. | May 1997 | A |
5631052 | Andersen et al. | May 1997 | A |
5631053 | Andersen et al. | May 1997 | A |
5631097 | Andersen et al. | May 1997 | A |
5635292 | Jennings et al. | Jun 1997 | A |
5637412 | Jennings et al. | Jun 1997 | A |
5641584 | Andersen et al. | Jun 1997 | A |
5654048 | Andersen et al. | Aug 1997 | A |
5658603 | Andersen et al. | Aug 1997 | A |
5658624 | Anderson et al. | Aug 1997 | A |
5660900 | Andersen et al. | Aug 1997 | A |
5660903 | Andersen et al. | Aug 1997 | A |
5660904 | Andersen et al. | Aug 1997 | A |
5662731 | Anderson et al. | Sep 1997 | A |
5665152 | Bassi et al. | Sep 1997 | A |
5665439 | Andersen et al. | Sep 1997 | A |
5665442 | Andersen et al. | Sep 1997 | A |
5676905 | Andersen et al. | Oct 1997 | A |
5679145 | Anderson et al. | Oct 1997 | A |
5679381 | Andersen et al. | Oct 1997 | A |
5683772 | Andersen et al. | Nov 1997 | A |
5691014 | Andersen et al. | Nov 1997 | A |
5693355 | Haas | Dec 1997 | A |
5695811 | Andersen et al. | Dec 1997 | A |
5702787 | Andersen et al. | Dec 1997 | A |
5705203 | Andersen et al. | Jan 1998 | A |
5705237 | Andersen et al. | Jan 1998 | A |
5705238 | Andersen et al. | Jan 1998 | A |
5705239 | Andersen et al. | Jan 1998 | A |
5705242 | Andersen et al. | Jan 1998 | A |
5707474 | Andersen et al. | Jan 1998 | A |
5709827 | Andersen et al. | Jan 1998 | A |
5709913 | Andersen et al. | Jan 1998 | A |
5711908 | Tiefenbacher et al. | Jan 1998 | A |
5714217 | Andersen et al. | Feb 1998 | A |
5716675 | Andersen et al. | Feb 1998 | A |
5720913 | Andersen et al. | Feb 1998 | A |
5736209 | Andersen et al. | Apr 1998 | A |
5738921 | Andersen et al. | Apr 1998 | A |
5753308 | Andersen et al. | May 1998 | A |
5766525 | Andersen et al. | Jun 1998 | A |
5776388 | Andersen et al. | Jul 1998 | A |
5783126 | Andersen et al. | Jul 1998 | A |
5783240 | Wenger et al. | Jul 1998 | A |
5786080 | Andersen et al. | Jul 1998 | A |
5798151 | Andersen et al. | Aug 1998 | A |
5800647 | Andersen et al. | Sep 1998 | A |
5800756 | Andersen et al. | Sep 1998 | A |
5810961 | Andersen et al. | Sep 1998 | A |
5830305 | Andersen et al. | Nov 1998 | A |
5830548 | Andersen et al. | Nov 1998 | A |
5843544 | Andersen et al. | Dec 1998 | A |
5851634 | Andersen et al. | Dec 1998 | A |
5868824 | Andersen et al. | Feb 1999 | A |
5928741 | Andersen et al. | Jul 1999 | A |
5973082 | Elmore | Oct 1999 | A |
5976235 | Andersen et al. | Nov 1999 | A |
6030673 | Andersen et al. | Feb 2000 | A |
6083586 | Andersen et al. | Jul 2000 | A |
6090195 | Andersen et al. | Jul 2000 | A |
6146573 | Shogren et al. | Nov 2000 | A |
6158883 | Hepke | Dec 2000 | A |
6168857 | Andersen et al. | Jan 2001 | B1 |
6180037 | Andersen et al. | Jan 2001 | B1 |
6200404 | Andersen et al. | Mar 2001 | B1 |
6214399 | Garbo | Apr 2001 | B1 |
6220849 | Atake | Apr 2001 | B1 |
6228898 | Nakanishi | May 2001 | B1 |
6231970 | Andersen et al. | May 2001 | B1 |
6240836 | Garbo | Jun 2001 | B1 |
6277899 | Bastioli et al. | Aug 2001 | B1 |
6347934 | Andersen et al. | Feb 2002 | B1 |
6379446 | Andersen et al. | Apr 2002 | B1 |
6413069 | Oono et al. | Jul 2002 | B2 |
6494704 | Andersen et al. | Dec 2002 | B1 |
6585859 | Hakansson | Jul 2003 | B1 |
6589327 | Snidow | Jul 2003 | B1 |
6846573 | Seydel | Jan 2005 | B2 |
6878199 | Bowden et al. | Apr 2005 | B2 |
7004616 | Murakami et al. | Feb 2006 | B2 |
7083673 | Bowden et al. | Aug 2006 | B2 |
7196124 | Parker et al. | Mar 2007 | B2 |
20030047110 | Poovarodom et al. | Mar 2003 | A1 |
20030143417 | Kesselring et al. | Jul 2003 | A1 |
20030216492 | Bowden et al. | Nov 2003 | A1 |
20040265453 | Helou, Jr. et al. | Dec 2004 | A1 |
20050089606 | Dellinger et al. | Apr 2005 | A1 |
20060057319 | Gleich et al. | Mar 2006 | A1 |
20060075544 | Kriesel et al. | Apr 2006 | A1 |
20060110498 | Dellinger et al. | May 2006 | A1 |
20070021534 | Glenn et al. | Jan 2007 | A1 |
Number | Date | Country |
---|---|---|
0752209 | Jan 1997 | EP |
0880896 | Dec 1998 | EP |
57-110150 | Jul 1982 | JP |
09-028274 | Apr 1997 | JP |
10-245792 | Sep 1998 | JP |
11-222794 | Aug 1999 | JP |
9210938 | Jul 1992 | WO |
9945073 | Sep 1999 | WO |
0039215 | Jul 2000 | WO |
2005021633 | Oct 2005 | WO |
Number | Date | Country | |
---|---|---|---|
20070202228 A1 | Aug 2007 | US |
Number | Date | Country | |
---|---|---|---|
60498129 | Aug 2003 | US | |
60498396 | Aug 2003 | US |
Number | Date | Country | |
---|---|---|---|
Parent | 10608441 | Jun 2003 | US |
Child | 11648129 | US | |
Parent | 10928602 | Aug 2004 | US |
Child | 10608441 | US |