This application claims the benefit of Korean Patent Application No. 2007-126249, filed on Dec. 12, 2006, the disclosure of which is hereby incorporated herein by reference in its entirety.
1. Technical Field
The present invention relates to an apparatus for manufacturing solid fuel using combustible waste and, more particularly, to an apparatus for manufacturing solid fuel using combustible waste, which manufactures RPF or RDF by melting general waste and combustible waste as well as the waste plastics, such as waste tires, waste vinyl and PET bottles, by use of heat generated in a combustion apparatus.
2. Discussion of Related Art
Synthetic resin products, such as tires, vinyl, plastics and the like are widely used in various industrial fields and daily life. Only parts of the synthetic resin products are recycled after use, and most synthetic resin products are classified as waste to be buried or burned out. Since plastic waste is bulky compared to weight, the cost of burying the plastic waste is higher than the cost of burying general waste. Moreover, even though the plastic waste is buried, since it is not biodegradable, it is regarded as a social problem.
In particular, a recycling rate of waste plastics is lower than that of the other waste. Specifically, during the period of one year of 2005, the recycling rates are respectively 55% for waste paper, 67% for waste tires, 58% for glass bottles and 43% for scrap iron while the recycling rate of plastics is about 15%. Moreover, waste plastics are generated by 4 to 5 million tons every year, and a generation rate thereof also remarkably increases every year. In these circumstances, to enhance the recognition that waste plastics are one of resources and to increase the recycling rate of waste plastics, the Ministry of Environment has notified the public of the quality and standard basis of solid fuel products using waste plastics and has positively supported people to use the solid fuel products as substitute fuel. As a result, in view of a long term, the recycling rate of waste plastics is expected to increase up to 50%, to have the economical effect of 500,000,000,000 Korea Won per year.
Meantime, considering the aforementioned reality, many techniques for manufacturing RDF (refuse derived fuel: solid fuel products using living waste) and RPF (refuse plastic fuel: solid fuel products using plastic waste) have been filed and registered. The RDF is manufactured by processing combustible waste among the living waste, and the RPF is manufactured by processing plastic waste.
For example, as a conventional technique, Korean Utility Model Registration No. 407,477 relates to the combustion apparatus for renewable energy, in which a fuel outlet is formed at a combustion burner. In this literature, the combustion apparatus of burning the renewable energy is described in detail. However, in the specification or drawings of this literature, there is not specified or illustrated a waste plastic extruder for producing reclaimed solid fuel using waste by thermal energy generated in the combustion apparatus, or the specific technical contents of manufacturing the reclaimed solid fuel.
As another conventional technique, Korean Patent Registration No. 321,378 relates to an apparatus for manufacturing solid fuel formed of combustible waste by using thermoplastics, which is illustrated in
However, since the aforementioned apparatus for manufacturing the solid fuel has the constitution of pushing out the solid fuel being press-molded, it cannot continuously produce the solid fuel so that the productivity is low. Moreover, since the waste inside the molding tube is melted by mounting the heating bands onto the outer circumference of the molding tube, a lot of energy, such as electric energy, for heating the heating bands is needed. Moreover, since the rotation supplier for supplying the combustible waste needs to be intermittently operated, another device for controlling the rotation supplier is needed, so that the entire constitution of the apparatus is very complicate.
Therefore, the present invention is directed to provide an apparatus for manufacturing solid fuel using combustible waste, which significantly reduces energy expenses for manufacturing the solid fuel, such as RPF or RDF, by manufacturing the solid fuel by melting combustible waste by use of heat of combustion in a combustion apparatus using renewable energy (RPF, RDF or combustible waste) as fuel.
Another object of the present invention is to provide an apparatus for manufacturing solid fuel using combustible waste, which improves the productivity of solid fuel and produces various kinds of the solid fuel with a maximized pressing force simultaneously, by improving the structure of a solid fuel extruder for manufacturing the solid fuel, such as RPF or RDF.
In accordance with an embodiment of the present invention, there is provided an apparatus for manufacturing solid fuel using combustible waste, comprising: combustion equipment constituted by including a combustion apparatus, an ignition burner, a fuel throwing opening for throwing combustible waste into a combustion chamber, a ventilation unit for supplying air to the combustion chamber, and an outlet for discharging heat and gas generated upon combustion; and a heating chamber connected to the outlet and including a plurality of combustible waste supply pipes inside, and wherein an extruder with a spiral screw formed around a rotation shaft rotating by a motor is built in each combustible waste supply pipe, a hopper for supplying shredded combustible waste is positioned at an end of the extruder towards the motor, and an extrusion nozzle for extruding melted combustible waste is formed at the other end of the extruder.
Preferably, the outlet of the combustion equipment may be connected to a divided chamber, a number of divided pipes may be divided form the divided chamber, and each divided pipe may be connected to the heating chamber where the combustible waste supply pipe is installed.
Preferably, the rotation shaft of the extruder may have a diameter which progressively becomes bigger towards the end or the spiral screw formed about the rotation shaft may have a pitch interval which becomes narrower towards the end.
The above and other features and advantages of the present invention will become more apparent to those of ordinary skill in the art by describing in detail preferred embodiments thereof with reference to the attached drawings in which:
The present invention will now be described more fully hereinafter with reference to the accompanying drawings, in which preferred embodiments of the invention are shown. This invention may, however, be embodied in different forms and should not be construed as limited to the embodiments set forth herein.
An apparatus for manufacturing solid fuel using combustible waste according to the present invention will be described with reference to
As illustrated in
In the combustion equipment 100, the combustion apparatus 110 for burning the combustible waste will bed described. Rotating by a rotation force of a motor 111, the combustion apparatus 110 according to the first embodiment as illustrated in
The fuel used for burning in the combustion equipment 100 may be not only RDF and RPF but also anything that is the combustible waste. The fuel to be supplied to the combustion chamber 105 is stored in a hopper 131, rotated by a motor 133 and supplied to the combustion chamber 105 through an extruder 135 for transferring the fuel. Instead of the extruder 135, a cylinder (not shown) which intermittently operates may be used.
The fuel throwing opening 130 to supply the fuel to the combustion chamber 105 may be positioned at a sidewall of the combustion chamber 105 as illustrated in
The heat and gas generated when the fuel is burned in the combustion equipment 100 are discharged to the heating chamber 200 through the outlet 150 positioned around an upper end of the combustion chamber 105. Since the heat of combustion flowing out through the outlet 150 after the combustion generally has high temperature of about 1,200 to 1,300° C., the ventilation unit, such as the air blower, is positioned between the outlet 150 and the heating chamber 200, to provide cold air so that the temperature inside the heating chamber 200 drops to 400° C. or below. When a distribution chamber 160 is connected to the outlet 150, preferably, the ventilation unit may be positioned between the outlet 150 and the distribution chamber 160.
As illustrated in
Further, when each heating chamber 200′ is connected to each divided pipe 161, a number of the waste supply pipes 210 may be installed in each heating chamber 200′ but preferably one waste supply pipe 210 may be installed in each heating chamber 200′. Considering the facility capacity or the control and management capability and the field situation and others, preferably the number of the waste supply pipes 210 or divided pipes 161 may be twenty (20) or under. Reference numeral 170 denotes an exhaust chamber for collecting the discharged heat and gas and sending the collected heat and gas to the post-facility for removing pollutants before the collected heat and gas are exhausted to the air.
The RDF or RPF melts the combustible waste to different extent, depending on a manufacturing temperature. Since the quality of the RDF or RPF varies according to the melted extent, preferably, the RDF or RPF may be manufactured at the temperature of about 150 to 400° C. To control the manufacturing temperature, it is desirable to control the temperature of the heating chamber 200 or 200′. Thus, preferably, a separate cooling chamber 300 may be installed at the front end of the heating chamber 200 or 200′, that is, around the combustible waste supply pipe 210 at the portion where the extrusion nozzle 230 is positioned, to provide the cold air through a separate ventilation unit (not shown) so that the waste supply pipe 210 is cooled down. Preferably, a temperature checking unit (not shown) for checking the temperature inside the heating chamber 200 or 200′, such as a temperature sensor or a thermometer, may be installed in the heating chamber 200 or 200′. More preferably, the operation of the ventilation unit may be controlled to be intermittent, according to the temperature inside the heating chamber 200 or 200′.
The waste supply pipe 210 is installed inside the heating chamber 200 or 200′. The extruder 211 is installed in each waste supply pipe 210. The extruder 211 is rotated by the rotation force of the motor 215. In the extruder 211, the spiral screw 214 is formed around the rotation shaft 213. When the waste shredded in small size (about the length of 1 to 3 ca) is supplied into the extruder 211 inside the waste supply pipe 210 through the hopper 220 positioned nearby the motor 215, the waste is melted by the heat of the heating chamber 200 or 200′ surrounding the waste supply pipe 210 at a predetermined space and the waste is pressed and transferred. The transferred waste is extruded through an extrusion opening 231 of the extrusion nozzle 230 installed at the end of the waste supply pipe 210. The melted and extruded waste is cut in a predetermined size by a cutting unit 217 installed at a front end of the extrusion nozzle 230 of the waste supply pipe 210, to be manufactured as solid fuel. Reference number 219 denotes a support for holding the solid fuel when the cutting unit 271 cuts the solid fuel.
Preferably, the number of the extrusion opening 231 formed in the extrusion nozzle 230 may be about 1 to 20, considering the size of the apparatus for manufacturing the solid fuel. The sectional shape of the extrusion opening 231 is round as illustrated in
In the extruder 211, when a pitch interval of the spiral screw 214 formed on the outer circumferential surface of the rotation shaft 213 is formed so as to be narrower towards the end in a rotation direction, or when a diameter of the rotation shaft 213 is formed to be greater towards the end in the rotation direction, the melted and transferred waste can be more efficiently pressed to be transferred and extruded, so that the quality of the manufactured solid fuel is improved.
In
As described above, in the apparatus for manufacturing fuel solid using combustible waste according to the present invention, since the fuel solid is manufactured by melting the combustible waste by using only the heat of combustion of the combustion apparatus using the renewable energy (RPF, RDF or combustible waste) as the fuel, without using any additional heating unit, the energy expenses for manufacturing the solid fuel, such as RPF or RDF, can be sharply reduced.
Furthermore, in the apparatus for manufacturing the fuel solid, the extruder on which the spiral screw is formed is used as the unit for transferring the combustible waste. Therefore, since the combustible waste is transferred not intermittently but continuously, the productivity of manufacturing the solid fuel, such as RPF or RDF, is improved. Further, since the structures of the extruder and the extrusion nozzle are improved, various kinds of quality solid fuel with a maximized pressing force can be produced simultaneously.
Furthermore, as the solid fuel, such as RPF or RDF, which is manufactured by the apparatus for manufacturing solid fuel according to the present invention substitutes for heavy oil or light oil which has been used as the heating oil in the central heating of a large-scale public housing complex or in the places where large-scale heating is needed, such as a cement factory, a dye house, an electric power generation plant, an iron mill, an industrial boiler factory, an inland water farm, a flowering and gardening farm and the like, tremendous energy can be saved.
The invention has been described using preferred exemplary embodiments. However, it is to be understood that the scope of the invention is not limited to the disclosed embodiments. On the contrary, the scope of the invention is intended to include various modifications and alternative arrangements within the capabilities of persons skilled in the art using presently known or future technologies and equivalents. The scope of the claims, therefore, should be accorded the broadest interpretation so as to encompass all such modifications and similar arrangements.
Number | Date | Country | Kind |
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10-2006-0126249 | Dec 2006 | KR | national |