The instant invention deals with a portable, vertical and horizontal extruding apparatus that is capable of densifying biomass to greater densities having higher British Thermal Unit (btu) potential than has been possible heretofore by using higher btu feed stock. This capability is possible through the use of a vented barrel that allows for the escape of any gasses that are built-up during the compression and densification process. The vents allow the compaction of high btu products by allowing the escape of gasses created by friction during the compression process
This invention deals with an extruding apparatus that is capable of densifying biomass to greater densities than has been possible heretofore. This invention allows the processing of material with heat content as high as 12,000 btu/lb., which is hotter than almost all coal used today, and, more importantly, much cleaner, that is, ultra low sulfur, low mercury and carbon dioxide neutral.
Pelletizing biomass, especially wood products, has been used in the United States for a long time. A high degree of compaction, that is, densification, and pellet toughness, that is, a pellet's resistance to disintegration, are the desired properties of a commercial pellet product.
Most prior art pelletizers and densification apparatii attempt to extrude particulate matter through a die of relative short barrel length. In such equipment, the particles are exposed to the compacting, shaping and densification forces in the barrel for only a short time.
As early as 1892, in U.S. Pat. No. 474,412, continuous production of pellets to bricks that were used as fuel was disclosed. This disclosure dealt with particulate matter that was coal dust mixed with a binder, such a mixture being fed between converging belts and compacted into briquettes that were ultimately transported and burned.
In 1940, U.S. Pat. No. 2,194,593 was issued to Graham and addressed a machine for compacting and densifying sawdust into briquettes for consumption in a heating apparatus. Very importantly, Graham recognized the now well-known principle that wood particulates contain sufficient natural resins, pitch and the like, that can be used for particle binding purposes, if enough heat and pressure are applied to activate them, that is, render the particulates “plastic”. Evenso, the briquettes derived by this method were not overly compacted owing to the fact that belts were used to do the compacting and had limited pressure on the particulate materials.
One of the main reasons that extruders have not been extensively used for highly densified materials is the fact that the extruder is “contained”, that is, relatively little air or other gasses can escape from the barrel of the extruder and this results in high and dangerous pressure within the barrel. It was thought that the barrel could not be vented because of the fact that it was believed that the material being extruded would exit from any vents or openings that were placed in the barrel to relieve pressure.
Contrary to this popular belief, it has been found that such openings can be placed in the extruder barrel to allow gasses to escape without the extruded material exiting through these openings. This results in highly densified materials without the dangers of high pressure.
This invention deals with an extruding apparatus that is capable of densifying biomass to greater densities than has been possible heretofore. Such an apparatus is an extruder having a barrel that has vents or openings cut through it to allow for the escape of gasses that are built up during the heating and extrusion process.
Thus, this invention deals with a densifying apparatus for densifying biomass. The apparatus comprises a support frame and mounted to the support frame is an extruder. The extruder has an extruder housing, a bearing housing having a front wall and a back wall, a feed hopper, and a vented barrel having a long axis. By “long axis” it is meant that the axis is centered in the barrel and runs the long length of the barrel. The extruder housing has mounted and supported therein, an extruder screw, the extruder screw comprising an extruder shaft, an auger segment mounted on the extruder shaft, a first end, a second end, and a middle zone.
The extruder shaft has mounted on the first end, a means for connecting to a drive means, and the extruder shaft terminates near the second end. The auger segment is mounted near the middle zone. The bearing housing is located between the extruder housing and the first end of the extruder shaft and the extruder shaft is supported by a thrust bearing located near the bearing housing front wall and a roller bearing located near the bearing housing back wall.
The vented barrel is mounted on a support wall and is centered such that it encloses the extruder shaft, the vent barrel being in linear alignment along the long axis with the extruder shaft.
There is a pressure clamp encircling the vented barrel and a hopper mounted on the extruder housing such that the biomass can be delivered to the auger segment of the extruder screw.
Turning now to
There is shown the frame 3, on which the extruder 4 is mounted. Shown in this Figure are an electric motor 5 (this motor can also be a fuel driven motor, such as a gasoline or diesel driven motor), drive belts 6 configured to a drive pulley 7 for the electric motor 5, a drive pulley 8 for the belts 6 on the shaft connector 9, a hopper 10 for feeding biomass to the extruder 4, a support plate 11 and support rods 12, and attached to the front of the plate 11 is a barrel 13 that has elongated openings 14 in it, and an extension 15 that is attached to the barrel 13 to aid in the removal of the densified mass from the barrel.
In more detail, and with reference to
The Extruder 4 also comprises a feed hopper 10 for feeding biomass to the extruder 4. The extruder housing 16 has mounted in it and supports an extruder shaft 20. The extruder shaft 20 has a first end 22 and a second end 21, the first end 22 being the lead end of the extruder shaft 20 and the second end 21 being the trailing or back end of the extruder shaft 20. The extruder shaft 20 has at its middle zone 23, an auger segment 24.
The first end 21 has mounted on it a means for connecting to a drive means. The drive means can be for example a motor, such as the electric motor 5 shown in
The extruder shaft 20 is supported near the first end 21 by a set of bearings, namely, a thrust bearing 27 and a roller bearing 28, all of which is housed in and supported by the bearing housing 17. The thrust bearing 27 is located near the front wall 18 of the bearing housing and the roller bearing 28 is located near the back wall 19 of the bearing housing 17.
Turning now to
As shown in
It should be noted that the clamp 30 is configured such that the pressure exerted by the auger segment 24 of the extruder screw can be balanced such that there is some back pressure on the forming material, without the barrel 13 exploding and such that the pressure is sufficient to form the densified material according to the invention.
At the first end 22 of the extruder shaft 20 is a connector 31 that connects the connector for the drive means 26 to the extruder shaft 20. The connector 31 surrounds the ends of the extruder shaft 20 and the connector for the drive means 26 and is pinned in place by a shear pin 32. In the event that the extruder gets bogged down because of overload of material, the shear pin 32 will shear rather than twisting the shaft 20. The power take-off is conventional state of the art in power equipment and is not shown.
Turning now to
Comminuted, chipped, or otherwise small-sized biomass is fed into the hopper 10 with the extruder screw 20 operating, and the extruder screw 20 conveys the biomass towards the barrel 13 and slowly compresses the material. As the biomass material feeds into the barrel 13, it is further compacted such that it is densified and because of the vent holes in the barrel 13, the material is highly compressed. The apparatus of this invention can yield densities on the order of about 100 pounds/cubic foot, while prior art devices can produce materials having densities only in the range of about 70 pounds/cubic foot. As the biomass compresses, there is heat generated and this heat is sufficient under the pressures of the extruder to furnish the high density material while venting the gasses generated from such heating. Such temperatures can be as high as 160° C. No additional heating means is required.
It should be noted that even though the apparatus 1 of
Biomass that is conventionally used in prior art devices can easily be used in the apparatus of the instant invention. Such materials as waste wood products, such as slashing, sawdust, bark, and the like, grasses, weeds, tree branches and twigs, leaves, grain stalks, grains, starch containing grain products, pine needles, pine cones, nut shells, and lumber scraps to mention a few.
The apparatus of this invention is lightweight and is portable to the extent that it can be moved from site to site and can accommodate clean up proceedings. The portability of the unit is such that it is economically maintainable. The portable nature of the device allows finished product to be manufactured in forest or field thus greatly reducing transportation costs. It reduces the cost of using wood chips by a factor of eight if the densification can be done on site where the chips are produced. The high wear components can easily be replaced in the field for efficient maintenance.
This application claims priority from U.S. Provisional Patent Application No. 60/841,461 filed Aug. 30, 2006.
Number | Date | Country | |
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60841461 | Aug 2006 | US |