Abstract:
This gasification melting facility includes: a fluidized bed gasification furnace that generates pyrolysis gas by thermally decomposing waste and discharges incombustibles; a vertical cyclone melting furnace that includes a pyrolysis gas duct through which the pyrolysis gas is introduced; a pyrolysis gas passage that connects the fluidized bed gasification furnace with the pyrolysis gas duct of the vertical cyclone melting furnace; pulverizer that pulverize the incombustibles into pulverized incombustibles so that the particle size of the incombustibles becomes fine; and airflow transporter that puts the pulverized incombustibles in the pyrolysis gas passage, and separating metal contained in the pulverized incombustibles by a difference in specific gravity while conveying the pulverized incombustibles together with airflow. The pyrolysis gas and the pulverized incombustibles are melted in the vertical cyclone melting furnace.

Description:
TECHNICAL FIELD 
       [0001]    The present invention relates to a gasification melting facility that gasifies and melts waste. 
       BACKGROUND ART 
       [0002]    In the past, a gasification and ash melting system has been known as a technique that can widely treat waste, such as incombustible waste, burned residue, and sludge in addition to municipal waste. The gasification and ash melting system includes: a gasification furnace that gasifies waste by thermally decomposing the waste; a melting furnace that is provided on the downstream side of the gasification furnace, combusts pyrolysis gas generated by the gasification furnace at high temperature, and converts ashes contained in the gas into molten slag; and a secondary combustion chamber that combusts flue gas discharged from the melting furnace. For the purpose of the recycling, volume reduction, and detoxification of waste, the gasification and ash melting system extracts slag from the melting furnace to reuse the slag as materials of construction such as base course materials or recovers waste heat from flue gas discharged from the secondary combustion chamber to generate electricity. 
         [0003]    A fluidized bed gasification furnace is widely used as the gasification furnace of such a gasification and ash melting system. A fluidized bed, in which a fluid medium is fluidized by the supply of combustion air, is formed at the bottom of the fluidized bed gasification furnace, and the fluidized bed gasification furnace is a device that partially combusts the waste put in the fluidized bed and thermally decomposes the waste in the fluidized bed maintained at high temperature by the combustion heat. 
         [0004]    Further, the fluidized bed gasification furnace is configured to discharge incombustibles from the bottom of the gasification furnace together with sand that is a fluid medium. Since the gasification melting facility requires volume reduction as described above, it is important to reduce the volume of incombustibles to be ultimately buried and treated. Means for reducing the volume of incombustibles, which are to be finally buried and treated, by recovering valuable metal, such as iron or aluminum, from incombustibles, and the like are known as means for reducing the volume of incombustibles. 
         [0005]    A gasification melting facility that pulverizes incombustibles from which valuable metal has been removed and introduces the pulverized incombustibles into a melting furnace to melt the pulverized incombustibles is disclosed in Patent Document 1 as means for reducing the volume of other wastes. This gasification melting facility can introduce the incombustibles into the melting furnace by pulverizing the incombustibles after further removing metals (metals other than valuable metal) from the incombustibles, from which valuable metal has been removed, using a vibrating screen and by cutting out a fixed amount of the pulverized incombustibles. 
       PRIOR ART DOCUMENT 
     Patent Document 
       [0000]    
       
         Patent Document 1: Japanese Unexamined Patent Application, First Publication No. 2008-69984 
       
     
       SUMMARY OF INVENTION 
     Problem to be Solved by the Invention 
       [0007]    However, in the gasification melting facility disclosed in Patent Document 1, a vibrating screen that removes metals from incombustibles is needed in a process for treating the incombustibles. For this reason, there has been a problem in that the size of the gasification melting facility is increased. Further, since metals are insufficiently removed by the vibrating screen, there has been a problem in that metals are accidentally introduced into the melting furnace. 
         [0008]    The invention has been made in consideration of these circumstances and an object of the present invention is to provide a gasification melting facility that can be constructed at lower cost by the reduction of the number of devices forming the facility and can reliably remove metals. 
       Means for Solving the Problem 
       [0009]    In order to achieve the above-mentioned object, the present invention employs the following means. 
         [0010]    That is, a gasification melting facility according to the present invention includes: a fluidized bed gasification furnace that generates pyrolysis gas by thermally decomposing waste and discharges incombustibles; a vertical cyclone melting furnace that includes a pyrolysis gas duct through which the pyrolysis gas is introduced; a pyrolysis gas passage that connects the fluidized bed gasification furnace with the pyrolysis gas duct of the vertical cyclone melting furnace; pulverizer that pulverize the incombustibles, which are discharged from the fluidized bed gasification furnace, into pulverized incombustibles so that the particle size of the incombustibles becomes fine; and airflow transporter that conveys the pulverized incombustibles, which are generated by the pulverizer, together with airflow, puts the pulverized incombustibles in the pyrolysis gas passage, and separates metal contained in the pulverized incombustibles by a difference in specific gravity while conveying the pulverized incombustibles together with airflow. The pyrolysis gas and the pulverized incombustibles are melted in the vertical cyclone melting furnace. 
         [0011]    According to the gasification melting facility of the present invention, the pulverized incombustibles are conveyed together with airflow and metals contained in the pulverized incombustibles are separated while being conveyed together with airflow. Accordingly, a device that removes metal does not need to be provided, and therefore, it is possible to construct a gasification melting facility at lower cost. 
         [0012]    It is preferable that the particle size of the pulverized incombustibles be adjusted to a fine particle size smaller than 0.1 mm. 
         [0013]    According to the present invention, it is possible to reliably convey the pulverized incombustibles together with airflow and reliably remove metal. 
         [0014]    Further, the gasification melting facility according to the present invention preferably further includes, on a front stage of the pulverizer, classifier that classifies the incombustibles and a fluid medium that is discharged from the fluidized bed gasification furnace, separator that separates iron and aluminum from the incombustibles that are classified by the classifier, and fixed amount feeder that feeds the incombustibles, which have been subjected to the separation performed by the separator, to the pulverizer by a fixed amount. 
         [0015]    According to the present invention, it is possible to separate valuable metal from the incombustibles and to adjust the amount of the incombustibles to be fed to the pulverizer. 
         [0016]    Furthermore, it is preferable that the pyrolysis gas duct be provided with a premix burner. 
         [0017]    According to the present invention, since the pyrolysis gas and the pulverized incombustibles pass through the premix burner and are fed to the vertical cyclone melting furnace, it is possible to sufficiently preheat the pyrolysis gas and the pulverized incombustibles. Accordingly, smooth melting can be performed. 
         [0018]    Moreover, it is preferable that the gasification melting facility according to the present invention include a plurality of the pyrolysis gas passages and a plurality of the pyrolysis gas ducts. The pyrolysis gas and the pulverized incombustibles are blown into the vertical cyclone melting furnace to cause a swirling flow. 
         [0019]    According to the present invention, since the pyrolysis gas is introduced from the plurality of pyrolysis gas ducts, a swirling force of a gas flow in the vertical cyclone melting furnace can be increased and it is possible to prevent the pulverized incombustibles from carrying over in the flue gas without being caught in the vertical cyclone melting furnace. 
         [0020]    Further, the airflow transporter preferably includes a pneumatic transport pipe that is curved toward the downstream side, a blower that generates airflow in the pneumatic transport pipe, and a metal removal pipe that extends downward from a curved portion of the pneumatic transport pipe. 
         [0021]    According to the present invention, it is possible to remove metal by a simpler structure and to make the gasification melting facility compact. 
       Effect of the Invention 
       [0022]    According to the present invention, the pulverized incombustibles are conveyed together with airflow and metals contained in the pulverized incombustibles are separated while being conveyed together with airflow. Accordingly, a device that removes metal does not need to be provided, and therefore, it is possible to construct a gasification melting facility at lower cost. 
     
    
     
       BRIEF DESCRIPTION OF DRAWINGS 
         [0023]      FIG. 1  is a view showing the structure of a gasification melting facility of an embodiment of the present invention. 
           [0024]      FIG. 2  is a schematic view of a pneumatic transport pipe of the embodiment of the present invention. 
           [0025]      FIG. 3  is a cross-sectional view taken along line A-A of  FIG. 1 . 
       
    
    
     DESCRIPTION OF EMBODIMENTS 
       [0026]    An embodiment of the present invention will be described below with reference to the drawings. An embodiment of the present invention will be described below with reference to the drawings. 
         [0027]    As shown in  FIG. 1 , a gasification melting facility  1  of this embodiment includes a fluidized bed gasification furnace  2  and a melting apparatus  4 . The gasification melting facility  1  introduces pyrolysis gas  52 , which is generated by the thermal decomposition of waste  51  in the fluidized bed gasification furnace  2 , to the melting apparatus  4  through a pyrolysis gas passage  3 . 
         [0028]    The fluidized bed gasification furnace  2  includes a gasification furnace body  5  having a rectangular cylindrical shape, and a waste inlet  6  including a waste discharge device  6   a  is provided on one side wall of the gasification furnace body  5 . Further, a pyrolysis gas outlet  23  through which the pyrolysis gas generated in the gasification furnace is discharged is provided at the top portion of the gasification furnace body  5 , and an incombustible outlet  7  is provided at the lower portion of the gasification furnace body  5 . Furthermore, a fluid medium  8  (mainly, silica sand) is circulated and supplied to the bottom portion of the fluidized bed gasification furnace  2 . 
         [0029]    Incombustibles and a fluid medium  53 , which are discharged from the incombustible outlet  7 , are fed to a sand classifier  9 , and are separated into incombustibles  54  and a fluid medium  55 . The fluid medium  55 , which is separated here, is returned to the fluidized bed gasification furnace  2  by means such as a sand circulating elevator. 
         [0030]    The incombustibles  54 , which are discharged from the sand classifier  9 , are fed to a separation device (separator) that includes a magnetic separator  10  and an aluminum sorter  11 . First, the incombustibles  54  are fed to the magnetic separator  10 , and iron is then separated. Next, incombustibles  56 , which are discharged from the magnetic separator  10 , are fed to the aluminum sorter  11 , and aluminum is separated. Accordingly, valuable metal including iron and aluminum is separated. 
         [0031]    Incombustibles  57 , which are discharged from the aluminum sorter  11 , are fed to a fixed amount feeding device  13  that includes a hopper  12 . A fixed amount of the incombustibles  57 , which are stored in the hopper  12 , is cut out in the fixed amount feeding device  13 . The cut incombustibles  58  are fed to a powdering machine  14  and are pulverized to have a particle size of 0.1 mm or less, so that the particle size of the incombustibles  58  is adjusted. Hereinafter, the incombustibles, which have been pulverized, are referred to as pulverized incombustibles  59 . Since the particle size of the incombustibles  58  is adjusted to 0.1 mm or less, the incombustibles  58  are appropriately scattered by airflow when the pulverized incombustibles  59  are introduced into a pneumatic transport pipe  31  of an airflow conveyor  30  to be described below. 
         [0032]    The airflow conveyor  30  is provided below the powdering machine  14 . The airflow conveyor  30  includes a pneumatic transport pipe  31  on which a curved portion  35  is formed, a blower  32  that generates airflow in the pneumatic transport pipe  31 , and a metal removal pipe  33  that is provided on the curved portion  35 . The blower  32  is installed so as to generate airflow toward the downstream side from an upstream end of the pneumatic transport pipe  31 . 
         [0033]    As shown in  FIG. 2 , an introduction portion  34  and the curved portion  35  are formed on the pneumatic transport pipe  31  in this order from the upstream side. Since the introduction portion  34  is connected to an outlet of the powdering machine  14 , the pulverized incombustibles  59  having been pulverized by the powdering machine  14  are introduced into the pneumatic transport pipe  31  from the introduction portion  34 . The pneumatic transport pipe  31  is curved on the downstream side of the introduction portion  34 , so that the curved portion  35  is formed. The pneumatic transport pipe  31  is curved upward at the curved portion  35 . Further, the metal removal pipe  33  extends downward from the curved portion  35 . 
         [0034]    The pneumatic transport pipe  31  is branched into two pipes on the downstream side of the curved portion  35 . The pneumatic transport pipe  31 , which is branched into two pneumatic transport pipes, is connected to branched pyrolysis gas passage  3  to be described below. 
         [0035]    Next, the detail of the melting apparatus  4  will be described. 
         [0036]    The melting apparatus  4  includes a vertical cyclone melting furnace  15 , a secondary combustion chamber  17  that is connected to an upper portion of the vertical cyclone melting furnace  15  through a connecting portion  16 , and a boiler portion  18  that is connected to a downstream portion of the secondary combustion chamber  17 . 
         [0037]    The vertical cyclone melting furnace  15  has a circular cross-section, and a flue gas outlet  19  having a throttling structure is formed at the upper portion of the vertical cyclone melting furnace  15 . In other words, the diameter of the vertical cyclone melting furnace  15  is reduced once at the flue gas outlet  19 , and the vertical cyclone melting furnace  15  extends upward in a conical shape so as to be widened and is connected to the secondary combustion chamber  17 . Further, a slag outlet  20  is provided at the lower portion of the vertical cyclone melting furnace  15 . 
         [0038]    As shown in  FIG. 3 , the vertical cyclone melting furnace  15  includes a substantially cylindrical furnace wall  15   a  and a pair of pyrolysis gas ducts  21  through which the pyrolysis gas  52  is introduced are horizontally provided on the cross-section of the furnace wall  15   a  at predetermined positions in the up and down direction. The pyrolysis gas ducts  21  are disposed so that the pyrolysis gas  52  introduced from the pyrolysis gas ducts  21  is ejected in the tangential direction of a circle C formed in the vertical cyclone melting furnace. Furthermore, premix burners  22  are installed at portions of the pyrolysis gas ducts  21  that are connected to the vertical cyclone melting furnace  15 . 
         [0039]    Combustion air is blown into the premix burners  22  from nozzle holes that are formed on the circumferential surfaces of the premix burners  22 . Air, oxygen, oxygen-enriched air, or the like may be used as the combustion air. In this case, an air ratio of the combustion air may be in the range of 0.9 to 1.1, and preferably about 1.0. It is possible to stably maintain the temperature in the furnace high by setting the air ratio as described above. 
         [0040]    Since the pyrolysis gas  52  and the combustion air are blown into the vertical cyclone melting furnace  15  after being mixed with each other in the premix burners  22  in advance in this way, the pyrolysis gas  52  and the combustion air are sufficiently mixed with each other. Accordingly, it is possible to instantly combust the pyrolysis gas  52  in the furnace. 
         [0041]    The secondary combustion chamber  17  is formed to have a square cross-section. The connecting portion  16  of which the diameter is reduced toward the flue gas outlet  19  of the vertical cyclone melting furnace  15  is provided at the lower end portion of the secondary combustion chamber  17 . Since the boiler portion  18  is provided on the flue gas-downstream side of the secondary combustion chamber  17 , heat is recovered by a superheater (not shown) or the like installed on a flue. Flue gas  62 , which has passed through the boiler portion  18 , passes through a reaction dust collector, a catalytic reaction device, and the like, which are provided on the rear stage, and is discharged to the atmosphere through a chimney. 
         [0042]    Next, the pyrolysis gas passage  3 , which connects the fluidized bed gasification furnace  2  with the vertical cyclone melting furnace  15 , will be described in detail. 
         [0043]    As described above, the pyrolysis gas  52  is introduced into the vertical cyclone melting furnace  15  through the pyrolysis gas passage  3 . Specifically, the pyrolysis gas outlet  23  of the fluidized bed gasification furnace  2  and the pyrolysis gas ducts  21  of the vertical cyclone melting furnace  15  are connected to each other through the pyrolysis gas passage  3 . The pyrolysis gas passage  3  is branched into two passages at a predetermined position from the upstream side (the fluidized bed gasification furnace  2 ) toward the downstream side (the vertical cyclone melting furnace  15 ), and the two branched pyrolysis gas passages  3  are connected to the pair of pyrolysis gas ducts  21 , respectively. 
         [0044]    Further, the two branched pneumatic transport pipes  31   a  are connected to the two branched pyrolysis gas passages  3  as described above. Accordingly, the pulverized incombustibles  59  are introduced into the vertical cyclone melting furnace  15  together with the pyrolysis gas  52 . 
         [0045]    Next, the function of the gasification melting facility  1  of the embodiment will be described. 
         [0046]    The waste  51 , which is put in from the waste inlet  6 , is fed to the fluidized bed gasification furnace  2  through the waste discharge device  6   a  in a fixed amount and then is thermally decomposed and gasified. Accordingly, the waste  51  is decomposed into gas, tar, and char (carbide). Tar is a component that is liquid at room temperature, but is present in the form of gas in the gasification furnace. Char is gradually and finely powdered in a fluidized bed, and is introduced into the melting apparatus  4  as the pyrolysis gas  52  together with gas and tar. 
         [0047]    In addition, a fluid medium is classified from the incombustibles and the fluid medium  53 , which are discharged from the incombustible outlet  7  of the fluidized bed gasification furnace  2 , by the sand classifier  9 , iron is separated by the magnetic separator  10 , and aluminum is separated by the aluminum sorter  11 . After that, the incombustibles  57 , which are put in the hopper  12 , are cut out by the fixed amount feeding device  13  and are introduced into the powdering machine  14 . 
         [0048]    When the pulverized incombustibles  59 , which are pulverized by the powdering machine  14  to have a particle size of 0.1 mm or less, are introduced into the pneumatic transport pipe  31  from the introduction portion  34 , the pulverized incombustibles  59  are conveyed toward the downstream side together with airflow. After that, the pulverized incombustibles  59  reach the curved portion  35 , and are conveyed upward along the curved portion  35  as shown by an arrow  59   a . In this case, materials having a high specific gravity, such as metals, to be mixed in the pulverized incombustibles  59  fall without being conveyed together with airflow, and fall along the metal removal pipe  33  as shown by an arrow  59   b . Accordingly, metals are removed from the pulverized incombustibles  59 , and only the pulverized incombustibles  59  from which metals have been removed are introduced into the pyrolysis gas passage  3 . 
         [0049]    After being mixed with the pyrolysis gas  52  fed from the fluidized bed gasification furnace  2 , the pulverized incombustibles  59  introduced into the pyrolysis gas passage  3  pass through the premix burners  22 , are fed to the vertical cyclone melting furnace  15 , and are converted into molten slag. 
         [0050]    According to the embodiment, the pulverized incombustibles  59  are conveyed together with airflow and metals contained in the pulverized incombustibles  59  are separated while being conveyed together with airflow. Accordingly, for example, a device that removes metal such as a vibrating screen does not need to be provided, so that it is possible to construct a gasification melting facility at lower cost. 
         [0051]    Further, since the pyrolysis gas  52  and the pulverized incombustibles  59  pass through the premix burners  22  and are fed to the vertical cyclone melting furnace, it is possible to sufficiently preheat the pyrolysis gas  52  and the pulverized incombustibles  59 . Furthermore, since the particle size of the pulverized incombustibles  59  is adjusted to 0.1 mm or less, smooth melting can be performed. 
         [0052]    Moreover, since the pyrolysis gas  52  and the pulverized incombustibles  59  are introduced from the two pyrolysis gas ducts  21 , a swirling force of a gas flow in the vertical cyclone melting furnace  15  can be increased. Further, it is possible to prevent the pulverized incombustibles  59  from carrying over in the flue gas without being caught in the vertical cyclone melting furnace  15  by the throttling structure of the flue gas outlet  19  of the vertical cyclone melting furnace  15 . 
         [0053]    In addition, the scope of the invention is not limited by the above-mentioned embodiment, and the invention may have various modifications without departing from the gist of the invention. For example, the number of the branches of the pyrolysis gas passage and the number of the pyrolysis gas ducts are not limited to two, and may be three or more. 
       REFERENCE SIGNS LIST 
       [0000]    
       
         
           
               1 : gasification melting facility 
               2 : fluidized bed gasification furnace 
               3 : pyrolysis gas passage 
               9 : sand classifier (classifier) 
               10 : magnetic separator (separator) 
               11 : aluminum sorter (separator) 
               13 : fixed amount feeding device (fixed amount feeder) 
               14 : powdering machine (pulverizer) 
               15 : vertical cyclone melting furnace 
               19 : flue gas outlet (throttling structure) 
               21 : pyrolysis gas duct 
               22 : premix burner 
               30 : airflow conveyor (airflow transporter) 
               31 : pneumatic transport pipe 
               32 : blower 
               33 : metal removal pipe 
               51 : waste 
               52 : pyrolysis gas 
               59 : pulverized incombustibles