JP2011132469A - Recycled solid fuel derived from waste culture medium and apparatus for producing recycled solid fuel using waste culture medium - Google Patents

Recycled solid fuel derived from waste culture medium and apparatus for producing recycled solid fuel using waste culture medium Download PDF

Info

Publication number
JP2011132469A
JP2011132469A JP2009295130A JP2009295130A JP2011132469A JP 2011132469 A JP2011132469 A JP 2011132469A JP 2009295130 A JP2009295130 A JP 2009295130A JP 2009295130 A JP2009295130 A JP 2009295130A JP 2011132469 A JP2011132469 A JP 2011132469A
Authority
JP
Japan
Prior art keywords
waste
solid fuel
culture medium
recycled solid
medium
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2009295130A
Other languages
Japanese (ja)
Other versions
JP5451368B2 (en
Inventor
Masami Katsuyama
正美 勝山
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toyota Kosan KK
Original Assignee
Toyota Kosan KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toyota Kosan KK filed Critical Toyota Kosan KK
Priority to JP2009295130A priority Critical patent/JP5451368B2/en
Publication of JP2011132469A publication Critical patent/JP2011132469A/en
Application granted granted Critical
Publication of JP5451368B2 publication Critical patent/JP5451368B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • 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
    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

Abstract

<P>PROBLEM TO BE SOLVED: To provide a recycled solid fuel derived from waste culture medium having a structure produced at a low cost even with a waste culture medium left immediately after mushroom cultivation or a waste culture medium in which parts of mushrooms remain is used as a raw material and to provide an apparatus for producing recycled solid fuel using the medium. <P>SOLUTION: The recycled solid fuel derived from a waste culture medium is characterized by being formed by mixing under heating a waste culture medium in a state mixed with at least the stone veneers of mushrooms with a waste resin is provided. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

本発明は茸の廃培地を用いたリサイクル固形燃料と廃培地を用いたリサイクル固形燃料製造装置に関する。   The present invention relates to a recycled solid fuel using a waste medium of straw and a recycled solid fuel production apparatus using the waste medium.

茸の人工栽培には、おが屑やコーンコブ等の植物由来の培地が用いられていることが多い。このような植物由来の培地を用いて茸の人工栽培を行った後は、一部の廃培地については堆肥化されることにより再利用がなされているものの、ほとんどの廃培地は廃棄処分されている。   In the artificial cultivation of straw, mediums derived from plants such as sawdust and corn cob are often used. After artificial cultivation of straw using such plant-derived medium, some waste medium is reused by composting, but most waste medium is discarded. Yes.

近年では、廃培地の廃棄処分に対する制約が多くなったことに加え、廃培地の廃棄処分には多額の費用をかけなければならず、茸栽培業者の生産コストが増大し、茸栽培業者の経営環境を悪化させている。そこで、茸の人工栽培後に発生する廃培地を原材料にしたいわゆるバイオマス燃料の製造方法が提案されている(特許文献1)。このようにして得られたバイオマス燃料により廃培地の廃棄処分量の削減および茸の人工栽培時に必要な燃料費の軽減が可能になった。   In recent years, in addition to increasing restrictions on the disposal of waste culture medium, disposal of waste culture medium has to be costly, which increases the production cost of grape growers and The environment is getting worse. Therefore, a so-called biomass fuel production method using a waste medium generated after artificial cultivation of straw as a raw material has been proposed (Patent Document 1). The biomass fuel thus obtained has made it possible to reduce the amount of waste medium discarded and reduce the fuel cost required for artificial cultivation of straw.

特開2008−120890号公報JP 2008-120890 A

特許文献1においても開示されているように、茸の人工栽培を終えた後の廃培地の含水率は60%以上と高いことがほとんどである。したがって廃培地を乾燥させるために、ストックヤードに一定期間貯蔵する方法が採用されることが多い。この場合、リサイクル固形燃料の製造現場の近くに、ストックヤードの確保が必要になるといったスペース的な課題や管理コストに関する課題がある。
これに対して、廃培地をストックヤードで乾燥させる工程を省略し、栽培直後の廃培地を原材料に用いて燃料化を試みようとする際には、含水率の高い廃培地を乾燥処理しなければならならない。すなわち、リサイクル燃料を製造するために燃料が必要になるといった状況になってしまうといったリサイクル固形燃料を製造する上でのコストに関する課題がある。さらに、茸の種類によっては、栽培容器内に茸の一部である石突きや子実体の一部を培地内に残した状態で栽培されることがある。このように培地に茸の一部が残存することにより、廃培地の含水率はさらに高くなり、廃培地を用いたリサイクル固形燃料の製造コスト増大の問題は甚大になる。
As disclosed in Patent Document 1, the water content of the waste medium after finishing the artificial cultivation of straw is almost as high as 60% or more. Therefore, in order to dry the waste medium, a method of storing in a stock yard for a certain period is often employed. In this case, there are space issues such as the need to secure a stockyard near the manufacturing site for recycled solid fuel, and issues related to management costs.
On the other hand, when the step of drying the waste medium in the stock yard is omitted, and when trying to use the waste medium immediately after cultivation as a raw material for fuel, the waste medium with a high water content must be dried. I must. That is, there is a problem relating to the cost of manufacturing a recycled solid fuel, such as a situation where fuel is required to manufacture the recycled fuel. Furthermore, depending on the kind of cocoon, it may be cultivated in a state in which a part of the cocoon or part of the fruit body is left in the culture medium in the cultivation container. Thus, when a part of the soot remains in the culture medium, the water content of the waste culture medium is further increased, and the problem of an increase in the production cost of recycled solid fuel using the waste culture medium becomes serious.

そこで本願発明は、茸の人工栽培直後における廃培地を原料にしたり、茸の一部が残存している廃培地を原料に採用したとしても、低コストで製造することができる構成の廃培地を用いたリサイクル固形燃料と、廃培地を用いたリサイクル固形燃料製造装置の提供を目的としている。   Therefore, the present invention provides a waste medium having a configuration that can be produced at low cost even if the waste medium immediately after artificial cultivation of straw is used as a raw material, or even if a waste medium in which a part of the straw remains is used as a raw material. It aims at providing the recycled solid fuel used and the recycling solid fuel manufacturing apparatus using a waste culture medium.

上記課題を解決するために本発明は、鋭意研究を行った結果、茸の人工栽培後における廃培地を用いたリサイクル固形燃料の製造において好適な構成に想到した。
すなわち、茸のうち少なくとも石突きが混合している状態の廃培地と、廃棄樹脂と、を加熱混合したことにより形成されていることを特徴とする廃培地を用いたリサイクル固形燃料である。
In order to solve the above-mentioned problems, the present invention has been intensively studied, and as a result, has come up with a suitable configuration in the production of recycled solid fuel using a waste medium after artificial cultivation of straw.
That is, it is a recycled solid fuel using a waste medium, which is formed by heating and mixing a waste medium in a state where at least stone bumps are mixed with a waste resin.

また、ホッパーと、該ホッパーに投入された廃培地および廃棄樹脂を加熱混合する加熱混合機と、該加熱混合機に連設され、前記加熱混合機により加熱混合して得たリサイクル固形燃料を排出する排出口が複数形成された排出口ブロックとを有していることを特徴とする廃培地を用いたリサイクル固形燃料製造装置としての発明もある。   Also, a hopper, a heating mixer that heats and mixes the waste culture medium and waste resin charged in the hopper, and a recycle solid fuel that is connected to the heating mixer and heated and mixed by the heating mixer are discharged. There is also an invention as a recycle solid fuel manufacturing apparatus using a waste culture medium characterized by having a discharge port block in which a plurality of discharge ports are formed.

本発明にかかる廃培地を用いたリサイクル固形燃料と廃培地を用いたリサイクル固形燃料製造装置によれば、廃棄樹脂が混合されている廃培地を加熱混合しているため、廃棄樹脂が溶融した際の発熱により廃培地の乾燥処理を行うことができ、茸の人工栽培直後における含水率が高い廃培地であっても、直ちにしかも低コストでリサイクル固形燃料を得ることが可能になる。
このように含水率が高い状態の廃培地であってもリサイクル固形燃料が得られるので、従来のようにスペース的な課題や製造コスト的な課題を解決することができる。また、化石燃料の代替品としての利用の拡大が期待でき、二酸化炭素排出量の削減や産業廃棄物処分場の長寿命化にも貢献することができる。
According to the recycled solid fuel using the waste culture medium and the recycled solid fuel production apparatus using the waste culture medium according to the present invention, the waste culture medium in which the waste resin is mixed is heated and mixed. Due to this heat generation, the waste medium can be dried, and even if it is a waste medium having a high water content immediately after artificial cultivation of straw, it is possible to obtain a recycled solid fuel immediately and at a low cost.
Thus, even if it is a waste culture medium with a high moisture content, since a recycled solid fuel is obtained, the space problem and the manufacturing cost problem can be solved as in the past. In addition, it can be expected to expand its use as a substitute for fossil fuels, and it can contribute to reducing carbon dioxide emissions and extending the life of industrial waste disposal sites.

第1実施形態における廃培地を用いたリサイクル固形燃料製造装置の概略正面図である。It is a schematic front view of the recycling solid fuel manufacturing apparatus using the waste culture medium in 1st Embodiment. 排出口ブロックの拡大透視正面図である。It is an expansion see-through | perspective front view of a discharge port block. 排出路の配設状態を説明するための拡大透視正面図である。It is an expansion see-through | perspective front view for demonstrating the arrangement | positioning state of a discharge path. 他の実施形態の一例を示す樹脂廃棄物処理装置の概略正面図である。It is a schematic front view of the resin waste processing apparatus which shows an example of other embodiment. 図4の排出口ブロック部分の拡大正面図である。It is an enlarged front view of the discharge port block part of FIG.

以下、本発明にかかる廃培地を用いたリサイクル固形燃料の製造装置の実施形態について、図面に基づいて説明する。本実施形態においては、廃棄樹脂の一例として、いわゆる農業用マルチと呼ばれる合成樹脂製シート体を例示しているが、本願発明における廃棄樹脂は農業用マルチに限定されるものではなく、いわゆるビニールハウスに用いられた後の廃ビニールシートや、使用済みの樹脂容器(廃棄樹脂容器)等を用いることができるのはもちろんである。
また、本実施形態における廃培地とは、エリンギ茸の人工栽培後に発生した廃培地のことを指し、廃培地中には、子実体の一部、石突き、菌床部分が混合した状態のものを想定している。
Hereinafter, an embodiment of a manufacturing apparatus of a recycle solid fuel using a waste culture medium concerning the present invention is described based on a drawing. In this embodiment, as an example of the waste resin, a synthetic resin sheet called a so-called agricultural mulch is illustrated, but the waste resin in the present invention is not limited to the agricultural mulch, so-called a greenhouse. Of course, it is possible to use a waste vinyl sheet after being used in the above, a used resin container (waste resin container), or the like.
In addition, the waste medium in the present embodiment refers to a waste medium generated after the artificial cultivation of eringi koji, and in the waste medium, a part of fruiting body, a stone bump, and a fungus bed part are mixed. Is assumed.

図1は、本実施形態における廃培地を用いたリサイクル固形燃料製造装置の概略正面図である。図2は、排出口ブロックの拡大透視正面図である。図3は、排出路の配設状態を説明するための拡大透視正面図である。本実施形態における廃培地を用いたリサイクル固形燃料製造装置50は、材料投入口であるホッパー10と、加熱混合機であるスクリューコンベア20と、排出口ブロック30とを有している。   FIG. 1 is a schematic front view of a recycled solid fuel production apparatus using a waste medium in the present embodiment. FIG. 2 is an enlarged perspective front view of the discharge port block. FIG. 3 is an enlarged perspective front view for explaining an arrangement state of the discharge path. The recycle solid fuel manufacturing apparatus 50 using a waste medium in the present embodiment includes a hopper 10 that is a material input port, a screw conveyor 20 that is a heating mixer, and a discharge port block 30.

ホッパー10には、エリンギ茸の人工栽培を終え、栽培容器から取り出された直後の廃培地と、使用後の農業用マルチの廃棄品が投入される。原材料の一部としてホッパー10に投入される原材料の一部である廃培地には、エリンギ茸の石突きや子実体の一部の他、エリンギ茸の菌床部分といった含水率が高い残存物が混合していることがあるが、これら高含水率の残存物を廃培地から分離する必要はない。また、廃培地と共に原材料としてホッパー10に投入される廃棄樹脂である農業用マルチの廃棄品は、予め破砕機等により所要長さに切断処理されたものを投入することが好ましい。含水率が60%程度である廃培地の投入質量に対して農業用マルチの廃棄物の投入質量は、質量比で90:10〜95:5程度であることが好ましい。
ホッパー10には投入口を覆う蓋(図示せず)を配設してもよい。ホッパー10に蓋を配設することにより、廃培地および農業用マルチの廃棄品からの臭いの発散を防止することができ好都合である。
In the hopper 10, the waste culture medium immediately after the artificial cultivation of the eringi rice cake is taken out from the cultivation container and the waste product of the agricultural mulch after use are input. In the waste medium that is a part of the raw material that is input to the hopper 10 as a part of the raw material, there is a residue having a high water content such as a swordbump of the eringi moth and a part of the fruiting body, and a fungal bed part of the eringi moth. Although they may be mixed, it is not necessary to separate these high water content residues from the waste medium. Moreover, it is preferable to introduce the agricultural mulch waste product, which is a waste resin to be put into the hopper 10 as a raw material together with the waste medium, that has been cut to a required length by a crusher or the like in advance. The input mass of the agricultural mulch waste is preferably about 90:10 to 95: 5 with respect to the input mass of the waste medium having a water content of about 60%.
The hopper 10 may be provided with a lid (not shown) that covers the charging port. By disposing the lid on the hopper 10, it is possible to prevent the odor from being emitted from the waste culture medium and the agricultural mulch waste.

ホッパー10に投入されたエリンギ茸の一部が混入した廃培地(以下、単に廃培地という)は、ホッパー10の底部に連設されたスクリューコンベア20により加熱処理と混合処理が並行して行われる。一般にスクリューコンベア20は、図1に示すように被搬送物が搬送されるにしたがって搬送経路22の断面積が減少する(搬送経路22の下流側の断面積が減少する)構成に形成されている。したがってスクリューコンベア20内を搬送される廃培地と農業用マルチの廃棄品からは圧縮熱が発生する。この圧縮熱によって廃培地および農業用マルチの廃棄品が加熱され、廃培地と農業用マルチの廃棄品との混合物の含水率を低下させることができる。このようにして含水率の低減処理がなされた廃培地と農業用マルチの廃棄品とを圧縮処理することによって固形燃料の成形が可能になっている。
スクリューコンベア20には、スクリューコンベア20内の搬送経路22の中を圧縮搬送された際に発生する水蒸気をスクリューコンベア20の外部に排出する蒸気排出部24が配設されていることが好ましい。また、搬送経路22の下流側には、搬送経路22を閉塞する配置で鉄製の排出口ブロック30が取り付けられている。
A waste culture medium (hereinafter simply referred to as a waste culture medium) in which a part of the eringi mash introduced into the hopper 10 is mixed is subjected to a heating process and a mixing process in parallel by the screw conveyor 20 connected to the bottom of the hopper 10. . In general, the screw conveyor 20 is formed in a configuration in which the cross-sectional area of the transport path 22 decreases (the cross-sectional area on the downstream side of the transport path 22 decreases) as the object to be transported is transported as shown in FIG. . Therefore, compression heat is generated from the waste culture medium and the agricultural multi-use waste conveyed in the screw conveyor 20. The waste culture medium and agricultural mulch waste are heated by the compression heat, and the water content of the mixture of the waste culture medium and agricultural mulch waste can be reduced. The solid fuel can be molded by compressing the waste medium that has been subjected to the moisture content reduction process and the agricultural mulch waste product.
The screw conveyor 20 is preferably provided with a steam discharge portion 24 that discharges water vapor generated when being compressed and conveyed through the conveyance path 22 in the screw conveyor 20 to the outside of the screw conveyor 20. In addition, an iron discharge block 30 is attached to the downstream side of the transport path 22 so as to close the transport path 22.

図2に示すように、排出口ブロック30には、スクリューコンベア20側から部材厚さ方向に排出口ブロック30を貫通する排出路32が複数箇所に形成されている。
また、図3に示すように、搬送方向に直交する方向の搬送経路22の断面内を、搬送経路22の中心軸AXから各排出路32,32,・・・の中間位置を通って搬送経路22の断面の外方に延びる線L1,L2,L3,L4により区切った場合、各区分A1,A2,A3,A4の面積がそれぞれ均等になる配置で排出口32が配設されている。また、各排出路32は、排出路32,32,・・・の中心軸ax,ax,・・・と搬送経路22の中心軸AXとが平行になるように形成されている。
As shown in FIG. 2, the discharge port block 30 is formed with a plurality of discharge passages 32 penetrating the discharge port block 30 in the member thickness direction from the screw conveyor 20 side.
Further, as shown in FIG. 3, in the cross section of the transport path 22 in the direction orthogonal to the transport direction, the transport path passes from the central axis AX of the transport path 22 through the intermediate positions of the discharge paths 32, 32,. When divided by lines L1, L2, L3, L4 extending outward from the cross section of 22, the discharge ports 32 are arranged in such an arrangement that the areas of the sections A1, A2, A3, A4 are equal. Further, each discharge path 32 is formed such that the central axes ax, ax,... Of the discharge paths 32, 32,.

先述のとおり、排出口ブロック30は鉄製であるから排出ブロック30の比熱は高い。これにより、スクリューコンベア20の搬送経路22の中で発生した圧縮熱を排出口ブロック30に蓄積することができる。また、スクリューコンベア20の搬出経路22の中で加熱混合(加熱圧縮)された廃培地と農業用マルチの廃棄品の混合物は、複数の排出路32,32,・・・に分岐されることになる。以上により、廃培地と農業用マルチの廃棄品の混合物のうち、スクリューコンベア20の搬送経路22において搬送経路22の内壁面に直接接触していなかった部分を、排出口ブロック30内の各排出路32,32,・・・の内壁面に接触させて加熱処理を十分に行うことが可能になる。   As described above, since the discharge port block 30 is made of iron, the specific heat of the discharge block 30 is high. Thereby, the compression heat generated in the conveying path 22 of the screw conveyor 20 can be accumulated in the discharge port block 30. In addition, the mixture of the waste culture medium and the agricultural mulch waste product that has been heated and mixed (heated and compressed) in the carry-out path 22 of the screw conveyor 20 is branched into a plurality of discharge paths 32, 32,. Become. By the above, among the mixture of waste culture media and agricultural mulch waste products, the portions that are not in direct contact with the inner wall surface of the conveyance path 22 in the conveyance path 22 of the screw conveyor 20 are each discharged in the discharge port block 30. It is possible to sufficiently perform the heat treatment by contacting the inner wall surfaces of 32, 32,.

本実施形態においては、排出口ブロック30に複数の排出路32,32,・・・を設けているので、スクリューコンベア20の搬送経路22の断面積に対する排出路32の断面積の減少量を抑えることができる。これにより、排出口ブロック30内における廃培地と農業用マルチの廃棄品の混合物の搬送速度を可及的に低速にすることができ、排出口ブロック30内においても廃培地と農業用マルチの廃棄品の混合物に充分な加熱処理を行うことができる。このように本実施形態に係るリサイクル固形燃料製造装置50によれば、廃培地と農業用マルチの廃棄品の混合物の全体に対して満遍なくしかも十分に加熱処理することができ、均一な状態のリサイクル固形燃料を得ることができる。したがってきわめて高品質なリサイクル固形燃料を得ることができる。   In this embodiment, since the discharge port block 30 is provided with a plurality of discharge paths 32, 32,..., The amount of reduction in the cross-sectional area of the discharge path 32 relative to the cross-sectional area of the transport path 22 of the screw conveyor 20 is suppressed. be able to. Thereby, the conveyance speed of the mixture of the waste culture medium and the agricultural mulch waste product in the discharge port block 30 can be made as low as possible, and the waste medium and the agricultural mulch are also discarded in the discharge port block 30. Sufficient heat treatment can be performed on the product mixture. As described above, according to the recycled solid fuel manufacturing apparatus 50 according to the present embodiment, the entire mixture of the waste culture medium and the agricultural mulch waste product can be uniformly and sufficiently heat-treated, and can be recycled in a uniform state. A solid fuel can be obtained. Therefore, extremely high quality recycled solid fuel can be obtained.

(実施例)
エリンギ茸の子実体の一部(石突き)が残留した状態であり、含水率が60%である廃培地の投入質量100kgに対して農業用マルチの廃棄品の投入質量を7kgとした条件でリサイクル固形燃料を製造した事例について説明する。
ホッパー10に投入した廃培地と農業用マルチの廃棄品はスクリューコンベア20により加熱混合されながら搬送経路22の中を搬送される。搬送経路22を通過した後は排出口ブロック30に形成された複数の排出路32に分岐され、排出口ブロック30内で再び加熱処理がなされた後、排出路32の出口側(排出口)から排出される。このようにして製造されたリサイクル固形燃料の含水率を計測したところ7%程度であった。
(Example)
A part of the fruiting body of eringi persimmon remains (with stone bumps), under the condition that the input mass of the waste product of agricultural mulch is 7 kg with respect to the input mass of 100 kg of the waste medium whose water content is 60% An example of manufacturing recycled solid fuel will be described.
The waste culture medium thrown into the hopper 10 and the agricultural mulch waste are conveyed through the conveyance path 22 while being heated and mixed by the screw conveyor 20. After passing through the conveyance path 22, it is branched into a plurality of discharge paths 32 formed in the discharge port block 30, heated again in the discharge port block 30, and then from the outlet side (discharge port) of the discharge path 32. Discharged. The water content of the recycled solid fuel thus produced was measured and found to be about 7%.

また、本実施形態により製造したリサイクル固形燃料の単位質量あたりの発生熱量を分析したところ、石炭の単位質量あたりの発生熱量と同程度の発生熱量を有していることが判明した。これは、本実施形態に係るリサイクル固形燃料は、農業用マルチの廃棄品を混合させた状態で形成を行っているので、単に廃培地のみを用いて製造したリサイクル固形燃料の発生熱量に比較して、本実施形態におけるリサイクル固形燃料の発生熱量を大幅に増大させることができるためと考えられる。   Further, when the amount of heat generated per unit mass of the recycled solid fuel produced according to this embodiment was analyzed, it was found that the amount of heat generated was the same as the amount of heat generated per unit mass of coal. This is because the recycled solid fuel according to the present embodiment is formed in a state where the agricultural mulch waste products are mixed, and compared with the generated calorific value of the recycled solid fuel manufactured using only the waste medium. This is considered to be because the amount of heat generated by the recycled solid fuel in the present embodiment can be greatly increased.

本実施例に対して、廃培地に混合する農業用マルチの廃棄品の投入比率を高めることにより、排出路32の出口側から排出されるリサイクル固形燃料の側表面全体に、農業用マルチの廃棄品を溶融させて得た溶融樹脂を被覆させた状態にすることもできる。このようにリサイクル固形燃料の外表面に樹脂被覆を施すことで、リサイクル固形燃料への湿気の吸収を防止することができる。これにより長期間にわたり製造時におけるリサイクル固形燃料の含水率を維持することに加え、被覆部分の樹脂によりリサイクル固形燃料としての熱量をさらに増加させることもできる点においてきわめて好都合である。   Compared to the present embodiment, the agricultural mulch is disposed on the entire side surface of the recycled solid fuel discharged from the outlet side of the discharge path 32 by increasing the input ratio of the agricultural mulch waste mixed with the waste medium. The molten resin obtained by melting the product may be coated. Thus, by applying a resin coating to the outer surface of the recycled solid fuel, absorption of moisture into the recycled solid fuel can be prevented. Thereby, in addition to maintaining the water content of the recycled solid fuel during production over a long period of time, it is extremely advantageous in that the amount of heat as the recycled solid fuel can be further increased by the resin of the coated portion.

以上に、本願発明に係るリサイクル固形燃料とリサイクル固形燃料製造装置50について、実施形態に基づいて詳細に説明してきたが、本願発明は以上の実施形態に限定されるものではない。
例えば、本実施形態においては、排出口ブロック30にはスクリューコンベア20の搬送経路22の中心軸AXに対して排出路32の中心軸axが平行な配列になる配置で排出路32を形成しているが、排出路32の中心軸axを搬送経路22の中心軸AXの上流側又は下流側のいずれかの延長方向で交差する配列で形成しても良い。これにより、排出路32の延長を長くすることができ、排出口ブロック30における加熱処理時間を延ばすことができ、より確実に乾燥処理(加熱処理)されたリサイクル固形燃料を得ることができる。
As mentioned above, although the recycle solid fuel and the recycle solid fuel manufacturing apparatus 50 concerning this invention were demonstrated in detail based on embodiment, this invention is not limited to the above embodiment.
For example, in the present embodiment, the discharge port 32 is formed with an arrangement in which the central axis ax of the discharge path 32 is arranged parallel to the central axis AX of the conveyance path 22 of the screw conveyor 20 in the discharge port block 30. However, the central axis ax of the discharge path 32 may be formed in an array that intersects in either the upstream or downstream direction of the central axis AX of the transport path 22. Thereby, the extension of the discharge path 32 can be lengthened, the heat treatment time in the discharge port block 30 can be extended, and the recycled solid fuel that has been dried (heat treated) more reliably can be obtained.

搬送経路22と排出路32の中心軸線を混合物の搬送方向の延長上で交差させる形態を採用すれば、各々の排出路32から排出させるリサイクル固形燃料を一体化することができる。これとは逆に、搬送経路22と排出路32の中心軸線を混合物の搬送方向とは反対側(上流側)の延長上で交差させる形態を採用すれば、各々の排出路32から排出させるリサイクル固形燃料を確実に分離させることができる。
搬送経路22と排出路32の中心線を交差させる条件は、リサイクル固形燃料に要求される形態に応じて適宜選択すればよい。
By adopting a form in which the central axes of the transport path 22 and the discharge path 32 intersect each other on the extension of the transport direction of the mixture, the recycled solid fuel discharged from the respective discharge paths 32 can be integrated. On the contrary, if the form which crosses the center axis line of the conveyance path 22 and the discharge path 32 on the extension on the opposite side (upstream side) from the conveyance direction of the mixture is adopted, the recycle discharged from each discharge path 32 Solid fuel can be reliably separated.
The condition for intersecting the center line of the transport path 22 and the discharge path 32 may be appropriately selected according to the form required for the recycled solid fuel.

また、図4に示すように、リサイクル固形燃料製造装置50の排出側端部(排出口ブロック30の端部)に排出路32から排出されたリサイクル固形燃料を切断するための切断装置40を配設してもよい。この切断装置40は、図5に示すように、排出路32の開口部分で、排出経路22の軸線AXに平行な回転軸周りに回転する回転刃42と回転刃42の回転動力部44とを有している。図5には回転動力部44としてモータを採用している。回転動力部44の出力を調整可能に設定することで、回転刃42の回転速度を変更し、リサイクル固形燃料の長さ寸法(大きさ)を適宜変更することができる。また、回転刃42はブレード形の刃を図示しているが、鋼の線材等を保持部に張設して形成したいわゆる糸鋸方式の回転刃を採用すれば、回転刃42へのリサイクル固形燃料の付着による切れ味の劣化を防止することができる。   Further, as shown in FIG. 4, a cutting device 40 for cutting the recycled solid fuel discharged from the discharge passage 32 is arranged at the discharge side end portion (end portion of the discharge port block 30) of the recycled solid fuel production device 50. You may set up. As shown in FIG. 5, the cutting device 40 includes a rotary blade 42 that rotates around a rotation axis parallel to the axis AX of the discharge path 22 and a rotary power unit 44 of the rotary blade 42 at the opening portion of the discharge path 32. Have. In FIG. 5, a motor is employed as the rotational power unit 44. By setting the output of the rotary power unit 44 to be adjustable, the rotational speed of the rotary blade 42 can be changed, and the length dimension (size) of the recycled solid fuel can be changed as appropriate. The rotary blade 42 is illustrated as a blade-shaped blade, but if a so-called thread saw type rotary blade formed by stretching a steel wire or the like on a holding portion is employed, the recycled solid fuel to the rotary blade 42 is used. It is possible to prevent sharpness deterioration due to adhesion.

また、図5には、切断装置40の回転動力部44としてモータを用いた形態を示しているが、回転動力部44の変形例として、スクリューコンベア20の動力を回転動力として用いる動力変換機構を採用することもできる。この動力変換機構としては減速機を用いることができる。ここで、減速比が調整可能な減速機を採用すれば、リサイクル固形燃料の長さ寸法(大きさ)を適宜変更することができるのはもちろんである。   5 shows a form in which a motor is used as the rotational power unit 44 of the cutting device 40. As a modification of the rotational power unit 44, a power conversion mechanism that uses the power of the screw conveyor 20 as rotational power is used. It can also be adopted. A reduction gear can be used as this power conversion mechanism. Here, of course, if a reduction gear with adjustable reduction ratio is employed, the length dimension (size) of the recycled solid fuel can be appropriately changed.

10 ホッパー
20 スクリューコンベア
22 搬送経路
24 蒸気排出部
30 排出口ブロック
32 排出路
40 切断装置
42 回転刃
44 回転動力部
50 リサイクル固形燃料製造装置
DESCRIPTION OF SYMBOLS 10 Hopper 20 Screw conveyor 22 Conveyance path 24 Steam discharge part 30 Discharge port block 32 Discharge path 40 Cutting apparatus 42 Rotary blade 44 Rotation power part 50 Recycled solid fuel manufacturing apparatus

Claims (5)

茸のうち少なくとも石突きが混合している状態の廃培地と、廃棄樹脂と、を加熱混合したことにより形成されていることを特徴とする廃培地を用いたリサイクル固形燃料。   A recycled solid fuel using a waste culture medium, characterized in that it is formed by heating and mixing a waste culture medium in which at least stone bumps are mixed with a waste resin. 前記加熱混合は、スクリューコンベアにより行われたものであることを特徴とする特徴とする請求項1記載の廃培地を用いたリサイクル固形燃料。   The recycle solid fuel using a waste medium according to claim 1, wherein the heating and mixing is performed by a screw conveyor. 前記茸は、エリンギ茸であることを特徴とする請求項1または2記載の廃培地を用いたリサイクル固形燃料。   The recycled solid fuel using a waste medium according to claim 1 or 2, wherein the soot is an eringi soot. ホッパーと、該ホッパーに投入された廃培地および廃棄樹脂を加熱混合する加熱混合機と、該加熱混合機に連設され、前記加熱混合機により加熱混合して得たリサイクル固形燃料を排出する排出口が複数形成された排出口ブロックとを有していることを特徴とする廃培地を用いたリサイクル固形燃料製造装置。   A hopper, a heating mixer that heats and mixes the waste medium and waste resin charged in the hopper, and a waste gas that is connected to the heating mixer and discharges recycled solid fuel obtained by heating and mixing with the heating mixer. An apparatus for producing a recycled solid fuel using a waste culture medium, comprising a discharge port block having a plurality of outlets. 前記排出口のリサイクル固形燃料の排出方向における中心軸は、前記加熱混合機内における前記廃培地および前記廃棄樹脂の搬送方向における中心軸と交差する配列に形成されていることを特徴とする請求項4記載のリサイクル固形燃料製造装置。   The central axis in the discharge direction of the recycled solid fuel at the discharge port is formed in an array intersecting with the central axis in the transport direction of the waste medium and the waste resin in the heating mixer. Recycled solid fuel manufacturing apparatus as described.
JP2009295130A 2009-12-25 2009-12-25 Recycled solid fuel production equipment using waste medium Active JP5451368B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2009295130A JP5451368B2 (en) 2009-12-25 2009-12-25 Recycled solid fuel production equipment using waste medium

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2009295130A JP5451368B2 (en) 2009-12-25 2009-12-25 Recycled solid fuel production equipment using waste medium

Publications (2)

Publication Number Publication Date
JP2011132469A true JP2011132469A (en) 2011-07-07
JP5451368B2 JP5451368B2 (en) 2014-03-26

Family

ID=44345549

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2009295130A Active JP5451368B2 (en) 2009-12-25 2009-12-25 Recycled solid fuel production equipment using waste medium

Country Status (1)

Country Link
JP (1) JP5451368B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101567804B1 (en) 2013-10-28 2015-11-11 (주)컴퓨트론 Drying system for manufacturing agricultural byproducts into fuel pellets
CN110822410A (en) * 2019-10-09 2020-02-21 苏州德君环卫服务有限公司 High-efficient combustion apparatus of living beings solid fuel
JP2021137673A (en) * 2020-03-02 2021-09-16 プロスペックAz株式会社 Pretreatment method of mushroom abandoning/culturing medium

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59217796A (en) * 1983-05-24 1984-12-07 Katsumi Takao Solid fuel using waste material
JPH0987646A (en) * 1995-09-27 1997-03-31 Maitei 21:Kk Production of solid fuel using organic waste
JP2001172641A (en) * 2000-09-27 2001-06-26 Kuramoto Sangyo Kk Device for converting organic waste into resource and method for converting organic waste into resource
JP2008120890A (en) * 2006-11-10 2008-05-29 Itou Seibaku:Kk Method for producing biomass fuel, biomass fuel and method for utilizing used medium
JP2008239943A (en) * 2006-06-05 2008-10-09 Nakata:Kk Solid fuel and method for producing the same
JP2010077201A (en) * 2008-09-24 2010-04-08 Takumi Shikagawa Apparatus for producing biomass fuel

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59217796A (en) * 1983-05-24 1984-12-07 Katsumi Takao Solid fuel using waste material
JPH0987646A (en) * 1995-09-27 1997-03-31 Maitei 21:Kk Production of solid fuel using organic waste
JP2001172641A (en) * 2000-09-27 2001-06-26 Kuramoto Sangyo Kk Device for converting organic waste into resource and method for converting organic waste into resource
JP2008239943A (en) * 2006-06-05 2008-10-09 Nakata:Kk Solid fuel and method for producing the same
JP2008120890A (en) * 2006-11-10 2008-05-29 Itou Seibaku:Kk Method for producing biomass fuel, biomass fuel and method for utilizing used medium
JP2010077201A (en) * 2008-09-24 2010-04-08 Takumi Shikagawa Apparatus for producing biomass fuel

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101567804B1 (en) 2013-10-28 2015-11-11 (주)컴퓨트론 Drying system for manufacturing agricultural byproducts into fuel pellets
CN110822410A (en) * 2019-10-09 2020-02-21 苏州德君环卫服务有限公司 High-efficient combustion apparatus of living beings solid fuel
JP2021137673A (en) * 2020-03-02 2021-09-16 プロスペックAz株式会社 Pretreatment method of mushroom abandoning/culturing medium

Also Published As

Publication number Publication date
JP5451368B2 (en) 2014-03-26

Similar Documents

Publication Publication Date Title
Whittaker et al. Factors affecting wood, energy grass and straw pellet durability–A review
CN102666880B (en) Method for using biomass in blast furnace
EP2669261A2 (en) Method for producing granulated organomineral fertilizers from organic waste materials and device for implementing same
FI3919591T3 (en) Methods for renewable fuel
CN1756592A (en) Mixing and pulverizing device, melting method for mixing, and method of molding cellulose material impregnated with binder
JP2016532544A (en) Biomass processing apparatus and biomass processing method
KR20110115610A (en) Methods for producing biomass-based fuel with pulp processing equipment
JP2009102468A (en) Fuel pellet
JP5451368B2 (en) Recycled solid fuel production equipment using waste medium
FI126607B (en) Process for the production of biofuel and the use of biofuel
JP5155080B2 (en) Water separation and drying treatment system for livestock manure
CN1638928A (en) MDF mfg. technology
JP7240006B2 (en) Method and apparatus for producing cellulosic fuel pellets
JP5531289B2 (en) Method for producing bamboo pellet fuel
JP5742316B2 (en) Method for producing bamboo pellet fuel
CN110106005A (en) A kind of preparation method of biomass fuel
JP2008303305A (en) Woody pellet fuel, and production method and production system for woody pellet fuel
KR20160112129A (en) Preparation method of composite pellets for fuel using wooden by-products
CN106753661A (en) A kind of preparation technology of biomass granule fuel
CN105623772B (en) The preparation method and its special equipment of a kind of biomass fuel
EP3577210B1 (en) System for treating biomass with a gas
KR101574653B1 (en) Method for Menufacturing Plate type of Wood-Pellet containing Perfume
US20130042521A1 (en) Clean burning wood fiber fuel pellets and its method of manufacture
CN1609077A (en) Production process of slowly/controlled releasing fertilizer for summer corn
EP2948533B1 (en) Method of producing clean burning wood biomass fuel

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20111026

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20130813

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20131004

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20131029

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20131226

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

Ref document number: 5451368

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250