JP2008208360A - Solid fuel and method for preparing the same - Google Patents

Solid fuel and method for preparing the same Download PDF

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JP2008208360A
JP2008208360A JP2008021275A JP2008021275A JP2008208360A JP 2008208360 A JP2008208360 A JP 2008208360A JP 2008021275 A JP2008021275 A JP 2008021275A JP 2008021275 A JP2008021275 A JP 2008021275A JP 2008208360 A JP2008208360 A JP 2008208360A
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solid fuel
rice husk
mixture
roller mill
biomass
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Kiyoshi Shimoide
潔 霜出
Shoichi Sakata
昌一 坂田
Toshinao Mitsuoka
利尚 満岡
Hiroshi Amano
宏 天野
Tadahiro Uesugi
忠弘 植杉
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Ube Corp
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Ube Industries Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

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  • Solid Fuels And Fuel-Associated Substances (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a solid fuel and a method for preparing the same that can be burned in a good state while being prepared with an improved crushing efficiency. <P>SOLUTION: The solid fuel is prepared by supplying a vertical-type roller mill 30 of an apparatus 100 for preparation and burning with a mixture of rice hulls and saw dust, and the mixture is crushed and introduced into a combustion boiler 25 as a solid fuel. The solid fuel is prepared by mixing 5-15 wt.% rice hulls with a 100 wt.% biomass other than the rice hulls. The solid fuel can be dried sufficiently in the course of crushing the mixture of rice hulls and saw dust because the inside of the vertical-type roller mill 30 is provided by a hot blast P taken out of an exhaust gas S of the combustion boiler 25 via a pressurizing fan 27. Crushing efficiency of the solid fuel can be improved because the amount of supply of saw dust can be increased while suppressing vibration by decreasing grinding resistance at the time of operating the vertical-type roller mill 30. <P>COPYRIGHT: (C)2008,JPO&amp;INPIT

Description

本発明は、バイオマスを細かく粉砕し乾燥させて微粉化した燃焼用の固体燃料およびその製造方法に関し、さらに詳しくは製造時の粉砕効率を向上させつつ良好に燃焼させることができる固体燃料およびその製造方法に関する。   The present invention relates to a solid fuel for combustion in which biomass is finely pulverized and dried to a fine powder, and a method for producing the same, and more specifically, a solid fuel that can be combusted satisfactorily while improving the pulverization efficiency during production, and the production thereof Regarding the method.

近年益々エネルギーの需要が増大していることに対応し、瀝青炭のような高品位の石炭に代えて、褐炭のような水分や揮発分を多く含んだ石炭を粉砕・乾燥させて生成した微粉炭や、木材などのバイオマスを粉砕・乾燥させて粉末状にした微粉バイオマス燃料などの固体燃料を使用して燃焼を行うボイラやキルンなどの工業用炉に用いる燃焼装置の開発が進められている。   In response to the increasing demand for energy in recent years, pulverized coal produced by crushing and drying coal containing a lot of moisture and volatiles such as brown coal instead of high-grade coal such as bituminous coal Further, development of a combustion apparatus for use in an industrial furnace such as a boiler or a kiln that uses a solid fuel such as a pulverized biomass fuel obtained by pulverizing and drying biomass such as wood into a powder form is underway.

このような燃焼装置を開示するものとして、例えば特許文献1に記載されたものが知られている。この特許文献1に記載された燃焼装置では、まず、ミルによって木材を粉砕し乾燥用気流により乾燥させて木粉を生成し排気ガスAとともに外部へ排出する。そして、集塵機によって排気ガスAにより搬送された木粉を捕集するとともに、排気ガスAから木粉を除いて排気ガスBを排出し、ボイラによってこの木粉を燃料として燃焼し排気ガスCを排出する。   As what discloses such a combustion apparatus, what was described in patent document 1, for example is known. In the combustion apparatus described in Patent Document 1, first, wood is pulverized by a mill and dried by an air flow for drying to generate wood powder, which is discharged together with exhaust gas A to the outside. The dust collector collects the wood powder conveyed by the exhaust gas A, removes the wood powder from the exhaust gas A, and discharges the exhaust gas B. The boiler burns the wood powder as fuel and exhausts the exhaust gas C. To do.

また、制御部は、ミルの排気ガスAの出口付近に設置された温度センサの検出信号に基づき、排気ガスBの一部と排気ガスCの一部を適当な混合比で混合させ、排気ガスAの温度が95℃〜130℃になるように制御する。これにより、この燃焼装置は、木粉を燃料とした場合であっても、木材のミルでの発火や硫黄成分の露結などを防止しつつ、木粉を十分に細かく粉砕して乾燥させることができる構成となっている。
特開2005−48967号公報
Further, the control unit mixes a part of the exhaust gas B and a part of the exhaust gas C at an appropriate mixing ratio based on a detection signal of a temperature sensor installed near the outlet of the exhaust gas A of the mill. The temperature of A is controlled to be 95 ° C to 130 ° C. As a result, even when wood powder is used as a fuel, this combustion device can sufficiently pulverize and dry the wood powder while preventing ignition in the wood mill and condensation of sulfur components. It has a configuration that can.
JP 2005-48967 A

しかしながら、上述した特許文献1に記載されている燃焼装置では、ミルに投入される木材の粒度分布が粗粒側、あるいは細粒側に偏った場合、ミルにおける木材の粉砕時に機械的振動が発生するため、ミルに投入する木材の投入量を減少させざるを得ず、ミルの良好な運用ができなくなるという問題がある。   However, in the combustion apparatus described in Patent Document 1 described above, when the particle size distribution of the wood thrown into the mill is biased toward the coarse grain side or the fine grain side, mechanical vibration is generated during the grinding of the wood in the mill. Therefore, there is a problem that the amount of wood input to the mill must be reduced, and the mill cannot be operated satisfactorily.

また、ミルから排出される固体燃料の排出量を増加させるために、ミルに投入する木材の投入量を増加させると、粉砕抵抗が大きくなりミルの性能によっては木材の粉砕や乾燥が不十分となって、良好な燃焼性を有する固体燃料を製造できなくなる場合があるという問題もある。   Also, increasing the amount of wood input to the mill in order to increase the amount of solid fuel discharged from the mill increases the crushing resistance, and depending on the performance of the mill, crushing and drying of the wood may be insufficient. Therefore, there is a problem that it may become impossible to produce a solid fuel having good combustibility.

本発明は、このような問題点に鑑みてなされたもので、製造時における粉砕効率を向上させつつ良好に燃焼させることができる固体燃料およびその製造方法を提供することを目的とする。   The present invention has been made in view of such problems, and an object of the present invention is to provide a solid fuel that can be combusted satisfactorily while improving the pulverization efficiency during production, and a method for producing the same.

上記目的達成のため、本発明に係る固体燃料は、籾殻と該籾殻以外のバイオマスとを混合し粉砕してなることを特徴とする。   In order to achieve the above object, the solid fuel according to the present invention is characterized in that rice husk and biomass other than the rice husk are mixed and pulverized.

本発明に係る固体燃料は、上記のように籾殻とこの籾殻以外のバイオマスを混合し粉砕して構成されることにより、従来の固体燃料と比べてミルにおける粉砕抵抗が小さくなり粉砕時の機械的振動が抑えられるために製造時の粉砕効率を向上させることができる。また、粉砕抵抗が小さくなるため十分に粉砕されて良好な燃焼性を有することができる。   The solid fuel according to the present invention is configured by mixing and pulverizing rice husk and biomass other than the rice husk as described above, so that the pulverization resistance in the mill is smaller than that of the conventional solid fuel and mechanical at the time of pulverization. Since vibration is suppressed, the pulverization efficiency during production can be improved. Further, since the pulverization resistance is reduced, it can be sufficiently pulverized to have good combustibility.

また、籾殻と該籾殻以外のバイオマス100重量%に対して、5〜15重量%の籾殻を混合し粉砕してなる構成とされていてもよい。   Moreover, you may be set as the structure formed by mixing and grind | pulverizing rice husk and 5-15 weight% rice husk with respect to 100 weight% of biomass other than this rice husk.

また、バイオマスは、建築廃材、伐採木等からなる木質バイオマスであるとよい。   The biomass may be woody biomass composed of building waste, felled trees, and the like.

本発明に係る固体燃料の製造方法は、籾殻と該籾殻以外のバイオマスを混合して混合物を生成し、該混合物を竪型ローラミルにて粉砕することを特徴とする。   The method for producing a solid fuel according to the present invention is characterized in that a rice husk and biomass other than the rice husk are mixed to form a mixture, and the mixture is pulverized by a vertical roller mill.

本発明に係る固体燃料の製造方法では、上記のように籾殻とこの籾殻以外のバイオマスを混合して混合物を生成し、この混合物を竪型ローラミルにて粉砕することにより、従来の製造方法と比べてミルにおける粉砕抵抗を小さくして粉砕時の機械的振動を抑えることができるため、製造時の粉砕効率を向上させてミルの良好な運用を図ることができる。また、粉砕抵抗を小さくすることができるため、混合物を十分に粉砕して良好な燃焼性を有する固体燃料を製造することができる。   In the method for producing a solid fuel according to the present invention, a rice husk and biomass other than this rice husk are mixed to produce a mixture, and the mixture is pulverized by a vertical roller mill, as compared with the conventional production method. In addition, since the pulverization resistance in the mill can be reduced to suppress mechanical vibration during pulverization, the pulverization efficiency during production can be improved and the mill can be operated well. In addition, since the pulverization resistance can be reduced, the mixture can be sufficiently pulverized to produce a solid fuel having good combustibility.

また、竪型ローラミルに熱風を供給しながら混合物を粉砕する構成とされていてもよい。   Alternatively, the mixture may be pulverized while supplying hot air to the vertical roller mill.

バイオマスは、建築廃材、伐採木等からなる木質バイオマスであるとよい。   The biomass may be woody biomass composed of building waste, felled trees, and the like.

本発明によれば、製造時における粉砕効率を向上させつつ良好に燃焼させることができる固体燃料およびその製造方法を提供することが可能となるという効果を奏する。   According to the present invention, there is an effect that it is possible to provide a solid fuel that can be combusted satisfactorily while improving the pulverization efficiency during production, and a method for producing the same.

以下、添付の図面を参照して、本発明の実施の形態に係る固体燃料およびその製造方法を詳細に説明する。   Hereinafter, a solid fuel and a manufacturing method thereof according to embodiments of the present invention will be described in detail with reference to the accompanying drawings.

図1は、本発明の一実施形態に係る固体燃料の製造燃焼設備の全体構成の一例を説明するための説明図である。図1に示すように、製造燃焼設備100では、まず、例えば籾殻にこの籾殻以外のバイオマスを混合した固体燃料の材料となる混合物が、トラック11から受入ホッパ12に投入される。なお、混合物の投入に伴う受入ホッパ12内の空気中の塵などは、図示しない集塵機により集塵される。   FIG. 1 is an explanatory diagram for explaining an example of the entire configuration of a solid fuel production combustion facility according to an embodiment of the present invention. As shown in FIG. 1, in the production combustion facility 100, first, for example, a mixture that is a material of solid fuel obtained by mixing biomass other than the rice husk into the rice husk is input from the truck 11 to the receiving hopper 12. Note that dust in the air in the receiving hopper 12 accompanying the introduction of the mixture is collected by a dust collector (not shown).

投入される混合物は、籾殻と該籾殻以外のバイオマス100重量%に対して、5〜15重量%の籾殻が混合されたものである。ここで、混合物を構成するバイオマスは、建築廃材、伐採木などの木質バイオマスである木屑を使用し、籾殻は、米、麦、粟、稗などの穀物系籾殻を使用するとよい。   The mixture to be added is a mixture of rice husk and 5 to 15% by weight of rice husk with respect to 100% by weight of biomass other than the rice husk. Here, the biomass constituting the mixture may be wood waste, which is woody biomass such as building waste and felled wood, and the rice husk may be a grain-based rice husk such as rice, wheat, straw, and straw.

そして、受入ホッパ12に投入された混合物は、スクリューフィーダ13によって所定の搬送速度で攪拌搬送されるとともに、ディスクスクリーン14を介して混合物中の夾雑物が取り除かれた後、ベルトコンベア16およびスクリューフィーダ17を介して供給ホッパ18に投入され貯蔵される。なお、ディスクスクリーン14から排出された混合物からは、さらにベルトコンベア16による搬送中に磁選機15によって鉄片などの磁性体が取り除かれる。   Then, the mixture charged into the receiving hopper 12 is stirred and conveyed by the screw feeder 13 at a predetermined conveying speed, and impurities in the mixture are removed via the disk screen 14, and then the belt conveyor 16 and the screw feeder. 17 is fed into the supply hopper 18 through the storage 17 and stored. The magnetic material such as iron pieces is removed from the mixture discharged from the disk screen 14 by the magnetic separator 15 during conveyance by the belt conveyor 16.

供給ホッパ18に貯蔵された混合物は、供給フィーダ19を介して所定量ずつ計量ベルトコンベア20に排出され、さらにこの計量ベルトコンベア20によって定量が量られた上でダブルフラップゲート21を介して竪型ローラミル30に供給される。   The mixture stored in the supply hopper 18 is discharged to the weighing belt conveyor 20 by a predetermined amount via the supply feeder 19, and after a fixed amount is measured by the weighing belt conveyor 20, the vertical shape is passed through the double flap gate 21. Supplied to the roller mill 30.

竪型ローラミル30では、投入された混合物が細かく粉砕される。この竪型ローラミル30内では、粉砕された混合物のうち、微粉化された軽量の粉体は竪型ローラミル30内に加圧ファン27によって供給される熱風Pにより上方へ空気搬送され、回転分級機31によって粒子径や密度、形状などに基づき区別されて本実施形態に係る固体燃料として粉体分離器であるサイクロン22に供給される。   In the vertical roller mill 30, the charged mixture is finely pulverized. In the vertical roller mill 30, among the pulverized mixture, the pulverized lightweight powder is pneumatically conveyed upward by the hot air P supplied by the pressure fan 27 into the vertical roller mill 30, and is a rotary classifier. 31 is distinguished based on particle diameter, density, shape, etc., and supplied to the cyclone 22 as a powder separator as a solid fuel according to the present embodiment.

このサイクロン22では、空気搬送された固体燃料が空気と分離され、分離された空気はミルファン28によってバグフィルタ29に供給されて、粉塵などが除去された後に図示しない環境設備へ送られるとともに、一部が加圧ファン27に送られる。   In the cyclone 22, the solid fuel transported by air is separated from the air, and the separated air is supplied to the bag filter 29 by the mill fan 28 and is sent to an environmental facility (not shown) after dust is removed. A part is sent to the pressure fan 27.

また、前述の分離された空気の一部は、図1に示すとおり燃焼熱ガスサイクロン26の出口または加圧ファン27の入口に送ることもできる。さらに、前述の分離された空気の一部は、加圧ファン27の排気側に送ることもできる。   A part of the separated air can be sent to the outlet of the combustion hot gas cyclone 26 or the inlet of the pressurized fan 27 as shown in FIG. Further, a part of the separated air can be sent to the exhaust side of the pressure fan 27.

一方、サイクロン22内で空気と分離された固体燃料は、下方に落下して搬送ブロア23により分配器24に送られた後、燃焼ボイラ25に備えられた図示しない燃焼バーナの数に応じて分配され、燃焼ボイラ25内で燃料として利用される。   On the other hand, the solid fuel separated from the air in the cyclone 22 falls downward and is sent to the distributor 24 by the transport blower 23 and then distributed according to the number of combustion burners (not shown) provided in the combustion boiler 25. And used as fuel in the combustion boiler 25.

なお、バグフィルタ29にて除去された粉塵は、フィーダ29aによってサイクロン22からの固体燃料と合わせて分配器24に送られ、上述した固体燃料として利用される。また、本例の製造燃焼設備100では、分配器24を介して分配された固体燃料に対し、さらに微粉炭が混合されて燃焼ボイラ25にて燃料として利用される。   The dust removed by the bag filter 29 is sent to the distributor 24 together with the solid fuel from the cyclone 22 by the feeder 29a and used as the above-described solid fuel. Further, in the production combustion facility 100 of this example, pulverized coal is further mixed with the solid fuel distributed via the distributor 24 and used as fuel in the combustion boiler 25.

燃焼ボイラ25内の排気ガスSは、燃焼ボイラ25から排出されて燃焼熱ガスサイクロン26に供給され、この燃焼熱ガスサイクロン26にて熱風Pと煤塵とに分離され、分離された煤塵は図示しない環境設備へ送られるとともに、熱風Pは加圧ファン27に送られて竪型ローラミル30に供給される。   The exhaust gas S in the combustion boiler 25 is discharged from the combustion boiler 25 and supplied to the combustion hot gas cyclone 26, where it is separated into hot air P and soot dust, and the separated soot dust is not shown. While being sent to the environmental equipment, the hot air P is sent to the pressure fan 27 and supplied to the vertical roller mill 30.

したがって、本例の製造燃焼設備100においては、竪型ローラミル30内では、籾殻と木屑からなる混合物が細かく粉砕されるだけではなく、加圧ファン27からの熱風Pにより十分に乾燥される(粉砕乾燥)。   Therefore, in the production combustion facility 100 of this example, in the vertical roller mill 30, the mixture of rice husk and wood chips is not only finely pulverized but also sufficiently dried by the hot air P from the pressure fan 27 (pulverization). Dry).

図2は、上述した製造燃焼設備100における竪型ローラミル30の運転時の各種運用データを示す図である。なお、図2(a)は木屑供給量(縦軸の単位はt/h)の変移を、同図(b)はミルの差圧(縦軸の単位はkPa)の変移を、同図(c)はミルの振動(縦軸の単位はμm)の変移をそれぞれ示している。本例の竪型ローラミル30では、同図(a)に示すように、ダブルフラップゲート21を介して供給可能な木屑の供給量は、木屑に対して籾殻を投入する前よりも籾殻を投入した後の方が増加する。すなわち、籾殻と木屑を混合した場合の方が、木屑のみの場合よりも全体的に供給量を増加させることができることを示している。   FIG. 2 is a diagram showing various operation data during operation of the vertical roller mill 30 in the manufacturing combustion facility 100 described above. 2A shows the change in the amount of wood waste (the unit of the vertical axis is t / h), and FIG. 2B shows the change of the differential pressure of the mill (the unit of the vertical axis is kPa). c) shows the transition of the vibration of the mill (the unit of the vertical axis is μm). In the vertical roller mill 30 of the present example, as shown in FIG. 3A, the supply amount of wood chips that can be supplied through the double flap gate 21 is more than that before the rice husks are added to the wood chips. The latter increases. That is, it is shown that the supply amount can be increased as a whole when the rice husk and the wood waste are mixed, compared with the case of the wood waste alone.

また、同図(b)に示すように、竪型ローラミル30への排ガス供給側と固体燃料排出側の圧力差(差圧)は、木屑に対して籾殻を投入する前よりも籾殻を投入した後の方が減少する。このことは、籾殻と木屑を混合した場合の方が木屑のみの場合よりも竪型ローラミル30内での木屑の粉砕効率が向上し、粉砕物のローラミル30内部での循環量が減少したことを示している。   Further, as shown in FIG. 5B, the pressure difference (differential pressure) between the exhaust gas supply side and the solid fuel discharge side to the vertical roller mill 30 is greater than that before the rice husks are added to the wood chips. The latter will decrease. This indicates that the wood crushing efficiency is improved in the vertical roller mill 30 when the rice husk and the wood waste are mixed, and the amount of pulverized material circulated within the roller mill 30 is reduced. Show.

さらに、同図(c)に示すように、竪型ローラミル30における機械的振動は、木屑に対して籾殻を投入する前よりも籾殻を投入した後の方が減少する。このことは、籾殻と木屑を混合した場合の方が木屑のみの場合よりも竪型ローラミル30内での粉砕物の粉砕ローラへの噛み込みが向上し、粉砕抵抗が少なく機械的負荷が減少することを示している。   Furthermore, as shown in FIG. 3C, the mechanical vibration in the vertical roller mill 30 is reduced after the rice husks are added to the wood chips than before the rice husks are added. This means that the mixture of rice husk and wood waste improves the biting of the pulverized material into the grinding roller in the vertical roller mill 30 compared to the case of wood waste alone, reduces the pulverization resistance, and reduces the mechanical load. It is shown that.

なお、本例の製造燃焼設備100にて用いた籾殻、木屑および籾殻と木屑の混合物(固体燃料)それぞれの組成は、次の表1に示すようなものとなった。籾殻は米の籾殻を、木屑は建築廃材を用いた。建築廃材と米の籾殻の総重量100重量%に対して、10重量%の米の籾殻が混合された。   The composition of each of the rice husks, wood chips, and the mixture of the rice husks and the wood chips (solid fuel) used in the production combustion facility 100 of this example is as shown in Table 1 below. Rice husks were made from rice husks, and wood chips were made from construction waste. 10% by weight of rice husk was mixed with 100% by weight of the total weight of building waste and rice husk.

Figure 2008208360
また、本例の製造燃焼設備100の燃焼ボイラ25における固体燃料として、木屑のみを用いた場合と籾殻と木屑の混合物を用いた場合の各種運用データは、次の表2に示すようなものとなった。表2によれば、籾殻を混合した場合とそうでない場合を比べると、発電量等のボイラ性能や、排ガス濃度は同程度であった。
Figure 2008208360
In addition, as shown in Table 2 below, various operation data when using only wood waste and a mixture of rice husk and wood waste as solid fuel in the combustion boiler 25 of the production combustion facility 100 of this example are as follows. became. According to Table 2, when the case where the rice husk was mixed was compared with the case where the rice husk was not mixed, the boiler performance such as the amount of power generation and the exhaust gas concentration were comparable.

Figure 2008208360
このように、図2、表1および表2からも明らかなように、籾殻と木屑を混合して粉砕した本実施形態に係る固体燃料は、木屑のみからなる固体燃料と比較しても、同等あるいはそれ以上の燃焼性を備えつつ竪型ローラミル30の運用を良好にすることが可能であるといえる。したがって、この固体燃料によれば、製造時における粉砕効率を向上させつつ良好に燃焼させることが可能となる。
Figure 2008208360
Thus, as is clear from FIG. 2, Table 1 and Table 2, the solid fuel according to the present embodiment obtained by mixing and pulverizing rice husk and wood waste is equivalent even when compared with the solid fuel consisting only of wood waste. Alternatively, it can be said that it is possible to improve the operation of the vertical roller mill 30 while having more combustibility. Therefore, according to this solid fuel, it becomes possible to burn well while improving the pulverization efficiency at the time of manufacture.

なお、上述した製造燃焼設備100では、トラック11から受入ホッパ12に投入される固体燃料の材料が、籾殻と木屑とを混合した混合物であるため、これら籾殻と木屑との混合については、次のような方法を採用することが可能である。   In the above-described production combustion facility 100, the material of the solid fuel input from the truck 11 to the receiving hopper 12 is a mixture obtained by mixing rice husks and wood chips. It is possible to adopt such a method.

図3は、製造燃焼設備100における籾殻と木屑との混合方法を説明するための図である。籾殻と木屑との混合は、例えば図3(a)に示すように、まず、ショベルローダ41により混合ヤード50の籾殻受入ホッパ42へあらかじめ籾殻を貯蔵しておく。そして、図示しないセンサによって受入ホッパ45近傍へのトラック47の進入が検知されると、籾殻切出しコンベア43および籾殻投入コンベア44を起動して籾殻の受入ホッパ45への投入を開始するとともに、トラック47に積載した木屑を受入ホッパ45へ投入する。   FIG. 3 is a diagram for explaining a method of mixing rice husks and wood chips in the production combustion facility 100. For example, as shown in FIG. 3 (a), the rice husk is first stored in advance in the rice husk receiving hopper 42 of the mixing yard 50 by the shovel loader 41. When the sensor 47 (not shown) detects the entry of the truck 47 into the vicinity of the receiving hopper 45, the rice husk cutting conveyor 43 and the rice husk charging conveyor 44 are activated to start feeding the rice husk into the receiving hopper 45, and the truck 47 The wood chips loaded on the hopper 45 are put into the receiving hopper 45.

このとき、籾殻切出しコンベア43および籾殻投入コンベア44による籾殻の搬送投入量をスクリューフィーダ46の切出し能力に基づいてあらかじめ最適な混合割合となるように調整しておくとよい。受入ホッパ45においては、それぞれ投入された籾殻と木屑とがスクリューフィーダ46により攪拌されつつ混合され、竪型ローラミル30側へ排出されて供給される。したがって、このような混合方法によれば、スクリューフィーダ46を、竪型ローラミル30への払い出し機のみならず籾殻と木屑との混合機としても利用することが可能となるとともに、籾殻と木屑とを容易に混合することが可能となる。   At this time, the amount of rice husk transported and fed by the rice husk cutting conveyor 43 and the rice husk feeding conveyor 44 may be adjusted in advance so as to obtain an optimum mixing ratio based on the cutting ability of the screw feeder 46. In the receiving hopper 45, the rice husks and wood chips that are respectively charged are mixed while being agitated by the screw feeder 46, and are discharged and supplied to the vertical roller mill 30 side. Therefore, according to such a mixing method, the screw feeder 46 can be used not only as a dispenser to the vertical roller mill 30 but also as a mixer of rice husk and wood waste, and the rice husk and wood waste can be used. It can be easily mixed.

また、籾殻と木屑との混合は、例えば図3(b)に示すように、籾殻を積載したトラック48と木屑を積載したトラック49のそれぞれの積載量を、あらかじめ最適な混合割合となるように設定しておく。そして、各トラック48,49を混合ヤード50へ進入させ、受入ホッパ45へ籾殻および木屑を投入し、スクリューフィーダ46により攪拌混合して竪型ローラミル30側へ排出する。この場合、図示しないセンサによって受入ホッパ45近傍へのトラック48,49の進入が検知されると、スクリューフィーダ46が起動して籾殻と木屑を受入ホッパ45経由で混合することも可能である。この場合においても、上述したように容易に籾殻と木屑とを混合することができる。なお、図3に示した受入ホッパ45およびスクリューフィーダ46は、図1に示した受入ホッパ12およびスクリューフィーダ13として用いることができる。   Further, for example, as shown in FIG. 3B, the mixing of rice husks and wood chips is performed so that the loading amounts of the truck 48 loaded with rice husks and the truck 49 loaded with wood chips become optimum mixing ratios in advance. Set it. Then, the trucks 48 and 49 are made to enter the mixing yard 50, and the rice husks and wood chips are put into the receiving hopper 45, stirred and mixed by the screw feeder 46, and discharged to the vertical roller mill 30 side. In this case, when the entry of the trucks 48 and 49 to the vicinity of the receiving hopper 45 is detected by a sensor (not shown), the screw feeder 46 is activated and the rice husk and the wood waste can be mixed via the receiving hopper 45. Even in this case, rice husk and wood chips can be easily mixed as described above. The receiving hopper 45 and the screw feeder 46 shown in FIG. 3 can be used as the receiving hopper 12 and the screw feeder 13 shown in FIG.

さらに、木屑と籾殻の混合は、以下に示すような方法でも行うことができる。まず、木屑と籾殻とをそれぞれ図示しないシャベルカー等を使用することにより交互に積み上げて層状とする。この場合、例えば木屑と籾殻の層の厚みは20から50セントメートル程度である。また、層の数は、木屑と籾殻を1層とすると1〜5層である。こうして形成された層状物は、端部からシャベルカー等によって断面的に切り崩され、トラック(図示せず)に積み込まれる。そして、木屑と籾殻は、切り崩し、積み込まれる際に混合される。これにより、簡便な方法で木屑と籾殻を混合することができる。最後に、混合された木屑と籾殻は、トラックから図1に示す受入ホッパ12に投入される。   Further, the mixing of wood chips and rice husks can also be carried out by the following method. First, wood chips and rice husks are alternately stacked by using a shovel car or the like (not shown) to form a layer. In this case, for example, the thickness of the wood chip and rice husk layer is about 20 to 50 centimeters. In addition, the number of layers is 1 to 5 when wood chips and rice husks are one layer. The layered material thus formed is cut in a cross section from the end by a shovel car or the like and loaded on a track (not shown). The wood chips and rice husks are cut and mixed when loaded. Thereby, wood chips and rice husk can be mixed by a simple method. Finally, the mixed wood chips and rice husks are fed from the truck into the receiving hopper 12 shown in FIG.

以上述べたように、本実施形態に係る固体燃料およびその製造方法によれば、固体燃料の製造時における竪型ローラミル30での粉砕効率を向上させることができる。また、十分に細かく粉砕されて従来の固体燃料と性能差が少なく良好に燃焼される固体燃料を容易に製造することができる。   As described above, according to the solid fuel and the manufacturing method thereof according to the present embodiment, the pulverization efficiency in the vertical roller mill 30 at the time of manufacturing the solid fuel can be improved. In addition, a solid fuel that is sufficiently finely pulverized and burns well with little difference in performance from the conventional solid fuel can be easily manufactured.

本発明の一実施形態に係る固体燃料の製造燃焼設備の全体構成の一例を説明するための説明図である。It is explanatory drawing for demonstrating an example of the whole structure of the manufacture combustion equipment of the solid fuel which concerns on one Embodiment of this invention. 同製造燃焼設備における竪型ローラミルの運転時の各種運用データを示す図である。It is a figure which shows the various operation data at the time of the driving | operation of the vertical roller mill in the manufacturing combustion equipment. 同製造燃焼設備における籾殻と木屑との混合方法を説明するための図である。It is a figure for demonstrating the mixing method of the chaff and the wood chip in the manufacturing combustion equipment.

符号の説明Explanation of symbols

11…トラック、12…受入ホッパ、13…スクリューフィーダ、14…ディスクスクリーン、15…選磁機、16…ベルトコンベア、17…スクリューフィーダ、18…供給ホッパ、19…供給フィーダ、20…ベルトコンベア、21…ダブルフラップゲート、22…サイクロン、23…搬送ブロア、24…分配器、25…燃焼ボイラ、26…燃焼熱ガスサイクロン、27…加圧ファン、28…ミルファン、29…バグフィルタ、30…竪型ローラミル、31…回転分級機。   DESCRIPTION OF SYMBOLS 11 ... Truck, 12 ... Receiving hopper, 13 ... Screw feeder, 14 ... Disc screen, 15 ... Magnetic separator, 16 ... Belt conveyor, 17 ... Screw feeder, 18 ... Feeding hopper, 19 ... Feeding feeder, 20 ... Belt conveyor, DESCRIPTION OF SYMBOLS 21 ... Double flap gate, 22 ... Cyclone, 23 ... Conveyance blower, 24 ... Distributor, 25 ... Combustion boiler, 26 ... Combustion hot gas cyclone, 27 ... Pressurization fan, 28 ... Mill fan, 29 ... Bag filter, 30 ... Vertical roller mill, 31 ... Rotary classifier.

Claims (6)

籾殻と該籾殻以外のバイオマスとを混合し粉砕してなることを特徴とする固体燃料。   A solid fuel comprising a rice husk and a biomass other than the rice husk mixed and pulverized. 籾殻と該籾殻以外のバイオマス100重量%に対して、5〜15重量%の前記籾殻を混合し粉砕してなることを特徴とする請求項1記載の固体燃料。   2. The solid fuel according to claim 1, wherein 5-15% by weight of the rice husk is mixed and pulverized with respect to 100% by weight of rice husk and biomass other than the rice husk. 前記バイオマスは、建築廃材、伐採木等からなる木質バイオマスであることを特徴とする請求項1または2記載の固体燃料。   3. The solid fuel according to claim 1, wherein the biomass is a woody biomass composed of building waste, felled trees, or the like. 籾殻と該籾殻以外のバイオマスを混合して混合物を生成し、該混合物を竪型ローラミルにて粉砕することを特徴とする固体燃料の製造方法。   A method for producing a solid fuel, characterized in that rice husk and biomass other than the rice husk are mixed to form a mixture, and the mixture is pulverized by a vertical roller mill. 前記竪型ローラミルに熱風を供給しながら前記混合物を粉砕することを特徴とする請求項4記載の固体燃料の製造方法。   The method for producing a solid fuel according to claim 4, wherein the mixture is pulverized while supplying hot air to the vertical roller mill. 前記バイオマスは、建築廃材、伐採木等からなる木質バイオマスであることを特徴とする請求項4または5記載の固体燃料の製造方法。   6. The method for producing a solid fuel according to claim 4, wherein the biomass is a woody biomass composed of building waste, felled trees, and the like.
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JP2010060265A (en) * 2008-08-02 2010-03-18 Narita:Kk Heater
CN102072500A (en) * 2011-01-30 2011-05-25 孙小力 Pulverized coal preparation device based on pulverized coal combustion furnace, rotary dryer and mill
JP2018080295A (en) * 2016-11-18 2018-05-24 株式会社トーセン Manufacturing device with hopper for wood chip for fuel
CN109456813A (en) * 2018-12-18 2019-03-12 南京林业大学 A kind of sanding powder mixing rice husk prepares the process units and manufacturing method of granular fuel
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JP2010060265A (en) * 2008-08-02 2010-03-18 Narita:Kk Heater
CN102072500A (en) * 2011-01-30 2011-05-25 孙小力 Pulverized coal preparation device based on pulverized coal combustion furnace, rotary dryer and mill
JP2018080295A (en) * 2016-11-18 2018-05-24 株式会社トーセン Manufacturing device with hopper for wood chip for fuel
KR20190050291A (en) 2017-11-02 2019-05-10 미츠비시 히타치 파워 시스템즈 가부시키가이샤 Solid fuel supply device and combustion equipment and method of operating the solid fuel supply device
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JP2021152429A (en) * 2020-03-24 2021-09-30 株式会社タクマ Biomass fuel supply system and biomass power generation facility including biomass fuel supply system

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