JP5877007B2 - Method for producing solid fuel - Google Patents

Method for producing solid fuel Download PDF

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JP5877007B2
JP5877007B2 JP2011171834A JP2011171834A JP5877007B2 JP 5877007 B2 JP5877007 B2 JP 5877007B2 JP 2011171834 A JP2011171834 A JP 2011171834A JP 2011171834 A JP2011171834 A JP 2011171834A JP 5877007 B2 JP5877007 B2 JP 5877007B2
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solid fuel
garbage
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JP2013035919A (en
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洋一 渡邉
洋一 渡邉
康彦 金尾
康彦 金尾
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株式会社日本リサイクルマネジメント
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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

Description

本発明は、固形燃料の製造方法に係わり、詳しくは、一般家庭から廃棄された生ごみを含む所謂「都市ゴミ」を主原料に、従来から一般に用いられている所謂「化石燃料」より地球温暖化対策に有効なバイオマス燃料としての固形燃料を効率良く製造する技術に関する。   The present invention relates to a method for producing a solid fuel. More specifically, the present invention uses a so-called “city waste” containing garbage disposed of from a general household as a main raw material, and has a more TECHNICAL FIELD OF THE INVENTION The present invention relates to a technology for efficiently producing solid fuel as a biomass fuel that is effective as a countermeasure for composting.

都市ゴミを処理し、それをリサイクル再利用する技術に、該都市ゴミを破砕、乾燥、分別してから成形し、クレヨン状若しくは葉巻状の固形燃料(通称「RDF」ともいう)にする技術がある。その具体的な製造プラントの一例を図3に示すが、この固形燃料の製造は、市中より回収され、水分が40〜50質量%含有する都市ゴミ1を、トラック27で搬送してゴミ回収ピット2に装入することから始まる。該ゴミ収集ピット2では、一時的にゴミを貯留し、都市ゴミ中の水分が除かれる。その水分は、ゴミ収集ピット2に付設された汚水ピット3に集められる。そして、ゴミ収集ピット2で水分を減らした都市ゴミ1(以下、単に「ゴミ」ともいう)は、クレーン4を介してゴミ・ホッパ5に集められる。このゴミ・ホッパ5から切り出したゴミ1は、一次破砕選別手段17としての磁選機6を備えた破砕機7(例えば、二軸式特殊カッタ)を通過させて50〜100mm程度のサイズに破砕すると同時に、磁性を有する鉄スクラップ系やアルミニウム系の金属ゴミを除外する。この一次破砕されたゴミ1は、ロータリー・キルン方式の乾燥炉8に全量送られ、熱風炉23で灯油あるいは重油バーナー等を利用して発生させた熱風を用いて500〜600℃に加熱され、水分の除去が行われる。この乾燥炉8には、通常、乾燥温度調節用とするために前記汚水ピット3に溜まった汚水9も供給、処理される。なお、この乾燥段階でゴミの水分含有量は全体の10質量%以下までに減量される。   Technology for treating municipal waste and recycling and recycling it is a technology for crushing, drying and separating the municipal waste and then shaping it into a crayon-like or cigar-like solid fuel (also known as "RDF") . An example of a specific production plant is shown in FIG. 3. This solid fuel is produced from the city by collecting municipal waste 1 containing 40 to 50% by mass of moisture by a truck 27 and collecting the garbage. It begins with charging in pit 2. In the garbage collection pit 2, the garbage is temporarily stored, and the water in the city garbage is removed. The moisture is collected in a sewage pit 3 attached to the garbage collection pit 2. Then, city garbage 1 (hereinafter also simply referred to as “garbage”) whose moisture has been reduced in the garbage collection pit 2 is collected in the garbage / hopper 5 via the crane 4. When the waste 1 cut out from the waste hopper 5 is crushed to a size of about 50 to 100 mm through a crusher 7 (for example, a biaxial special cutter) equipped with a magnetic separator 6 as a primary crushing and sorting means 17. At the same time, magnetic scrap iron and aluminum metal dust is excluded. The primary crushed garbage 1 is sent to the rotary kiln type drying furnace 8 and heated to 500-600 ° C. using hot air generated in the hot air furnace 23 using kerosene or heavy oil burner, Moisture removal is performed. Normally, the sewage 9 collected in the sewage pit 3 is also supplied to and processed in the drying furnace 8 for adjusting the drying temperature. In this drying stage, the water content of the waste is reduced to 10% by mass or less.

次いで、乾燥されたゴミ1は、二次破砕選別手段18として重力差を利用する風選機10を備えた破砕機7(例えば、高速回転式カッタ)に送られ、破砕と不適切物(非燃焼物質)の選別を行う。この段階で主原料として適切な状態にされたゴミ1は、20〜30mm程度のサイズになっている。引き続き、その適切なゴミ1には、必要に応じて、防腐、脱臭の役割を果たす消石灰11が添加された後、定量供給機25を介して秤量され、ダイスを通過させることで圧縮する方式の成形機12に定量供給されて、クレヨン状もしくは葉巻状に成形した後、冷却機26で冷却して最終製品である固形燃料13となる。その最終製品のサイズは、平均して直径が15mm程度、長さが50〜60mm程度である。ここで、使用する成形機12は特に限定しないが、低速で回転するローラと固定された円盤状のダイスの間に適切なゴミを挟み込み、最高200kg/cmの高圧力と摩擦による反応熱の作用で固化するものを利用するのが良い。 Next, the dried garbage 1 is sent to a crusher 7 (for example, a high-speed rotary cutter) equipped with a wind separator 10 that uses the difference in gravity as the secondary crushing and sorting means 18, and is crushed and inappropriate (non- Select combustion substances. At this stage, the trash 1 made suitable as a main raw material has a size of about 20 to 30 mm. Subsequently, slaked lime 11 that plays a role of preserving and deodorizing is added to the appropriate garbage 1 as necessary, and then weighed through a quantitative feeder 25 and compressed by passing through a die. After a fixed amount is supplied to the molding machine 12 and formed into a crayon shape or a cigar shape, it is cooled by a cooler 26 to become a solid fuel 13 as a final product. The average size of the final product is about 15 mm in diameter and about 50 to 60 mm in length. Here, the molding machine 12 to be used is not particularly limited, but suitable dust is sandwiched between a roller rotating at a low speed and a fixed disk-shaped die, and the reaction heat generated by the high pressure and friction of 200 kg / cm 2 at the maximum. It is good to use what solidifies by action.

なお、これら製造プラントの必要な位置には、脱臭装置14、集塵機15、熱交換器16が配置されている。また、このような固形燃料13の主な利用先(ユーザー)としては、バイオマス燃料が化石燃料の使用より地球温暖化対策となり、安価・安定供給が可能であるとの観点から、製紙会社やRDF発電所等である。   In addition, the deodorizing apparatus 14, the dust collector 15, and the heat exchanger 16 are arrange | positioned in the required position of these manufacturing plants. Moreover, as a main user (user) of such a solid fuel 13, from the viewpoint that biomass fuel becomes a countermeasure against global warming than the use of fossil fuel, and can be cheaply and stably supplied, a paper manufacturer or RDF Such as a power plant.

ところで、かかる技術で製造した固形燃料には、従来、多少の臭気が残るという問題があった。そこで、防臭対策として、主原材料の都市ゴミに脱臭・防腐材を添加したり、製造工程に脱臭装置を多数設置して、現在では臭気問題の解決がほぼなされている(例えば、特許文献1及び特許文献2参照)。   By the way, the solid fuel manufactured by this technique has a problem that some odor remains in the past. Therefore, as a countermeasure against deodorization, a deodorizing / preserving material is added to the main raw material municipal waste, or a large number of deodorizing apparatuses are installed in the manufacturing process, and currently, the odor problem is almost solved (for example, Patent Document 1 and Patent Document 2).

しかしながら、最近、当該固形燃料13をユーザーがボイラーの燃料として使用すると、「ボイラー管が腐食して、その寿命が短くなってしまう」という問題が多発している。その後の調査では、0.6〜1.0質量%もの塩素が製品としての固形燃料13に含まれており、その塩素がボイラー管素材の鉄鋼材料を腐食する要因であることが判明した。ユーザー側としては、この塩素分を0.3質量%以下に低減すれば、上記ボイラー管の寿命が大きく改善されるので、使用の上で一層好ましいと主張している。   However, recently, when a user uses the solid fuel 13 as a fuel for a boiler, there is a frequent problem that “the boiler tube is corroded and its life is shortened”. Subsequent investigation revealed that 0.6 to 1.0% by mass of chlorine was contained in the solid fuel 13 as a product, and that chlorine was a factor corroding the steel material of the boiler tube material. The user claims that if the chlorine content is reduced to 0.3% by mass or less, the life of the boiler tube is greatly improved, and therefore it is more preferable in use.

また、都市ゴミからの水分除去に利用する乾燥炉では、熱風の発生に灯油、重油等の化石燃料を多量に使用するため、COの発生で地球環境に優しくないという問題もあり、製造プラントとしてはまだまだ改造の余地があった。 In addition, drying ovens used to remove moisture from municipal waste use a large amount of fossil fuels such as kerosene and heavy oil to generate hot air, and there is also a problem that CO 2 generation is not friendly to the global environment. There was still room for remodeling.

そこで、本出願人は、上記問題点である塩素の含有量を従来より低減するばかりでなく、地球温暖化にも貢献可能なように、製造方法を改良することを試み、その成果を、平成22年2月18日付けで特願2010−033797号として特許出願した。その改良した製造方法の内容は(図2参照)、
『(A)ゴミ収集ピット、一次破砕選別手段、乾燥炉、二次破砕選別手段を順次経て、乾燥、粉砕、選別された粉状の都市ゴミを成形機に供給し、圧縮して所定形状の固形燃料とするに際して、ゴミの回収を可燃ゴミとプラスチック・ゴミとで分別回収すると共に、以下の3つの手段から選ばれた1つ又は2つ以上の手段を施し、固形燃料の塩素含有量を0.3質量%以下に低減すること特徴とする固形燃料の製造方法。
Therefore, the present applicant tried to improve the production method so that not only the chlorine content, which is the above-mentioned problem, was reduced, but also contributed to global warming. A patent application was filed as Japanese Patent Application No. 2010-033797 on February 18, 2010. The details of the improved manufacturing method (see FIG. 2)
“(A) After passing through the garbage collection pit, primary crushing and sorting means, drying furnace, and secondary crushing and sorting means, the dried, pulverized and sorted powdery municipal waste is supplied to the molding machine and compressed into a predetermined shape. When making solid fuel, garbage is collected separately by combustible waste and plastic waste, and one or more means selected from the following three means are applied to reduce the chlorine content of the solid fuel. A method for producing a solid fuel, which is reduced to 0.3% by mass or less.

手段1:市中から分別回収したプラスチック・ゴミを前記ゴミ収集ピットへ投入する前に、該プラスチック・ゴミから塩化ビニールを除去する
手段2:前記ゴミ収集ピットに付属する汚水ピットに溜まった汚水を、乾燥炉に供給せずにオフ・ラインで別途加熱処理する
手段3:ゴミにバイオマス材料を混合する
(B)前記手段1の塩化ビニールの除去を、該塩化ビニールとそれ以外のゴミとを赤外線照射で識別し、識別された塩化ビニールだけを空気で吹き飛ばして分別する。
Mean 1: Before putting plastic / garbage separated and collected from the city into the garbage collection pit, vinyl chloride is removed from the plastic / garbage. Mean 2: Sewage collected in the sewage pit attached to the garbage collection pit The heat treatment is separately performed off-line without supplying to the drying furnace. Means 3: The biomass material is mixed with the garbage. It is identified by irradiation, and only the identified vinyl chloride is blown away with air for separation.

(C)前記手段3のゴミへのバイオマス材料の混合量を、質量で20〜50%とする。   (C) The mixing amount of the biomass material into the garbage of the means 3 is set to 20 to 50% by mass.

(D)前記バイオマス材料にヤシ殻を用い、その混合を前記二次破砕選別手段で行う。
』というものであった。なお、バイオマス材料のゴミへの混合は、ゴミ中の塩素含有量を希釈する役割を有する。
(D) A coconut shell is used for the biomass material, and the mixing is performed by the secondary crushing and sorting means.
It was something like that. In addition, mixing of the biomass material into the garbage has a role of diluting the chlorine content in the garbage.

ところが、この改良方法を実際に用い、ゴミに対する低塩素希釈対策のための混合物質として、下水汚泥、発泡ウレタン及びヤシ殻等を採用して固形燃料を試作したところ、全ゴミ量に対し10質量%までの添加で、製品である固形燃料の塩素含有量が0.60質量%から0.48質量%に低減したが、それ以上の量を添加すると製品が粉化してしまい、成形が困難になった。これでは、下水汚泥、発泡ウレタン及びヤシ殻等のバイオマス材料の消費量が少なく、塩素の希釈効果が不十分で技術的には不満足な結果であった。   However, when this improved method was actually used and a solid fuel was prototyped using sewage sludge, foamed urethane, coconut shell, etc., as a mixed material for low chlorine dilution measures against garbage, the mass was 10 mass relative to the total amount of garbage. %, The chlorine content of the product solid fuel has been reduced from 0.60% by mass to 0.48% by mass, but adding more than that would cause the product to be powdered and difficult to mold became. In this case, the consumption of biomass materials such as sewage sludge, urethane foam and coconut shells was small, and the chlorine dilution effect was insufficient, resulting in technically unsatisfactory results.

特許第3545504号公報Japanese Patent No. 3545504 特許第2865541号公報Japanese Patent No. 2865541

本発明は、かかる事情に鑑み、上記特願2010−033797号の技術をさらに改良し、その問題点であるゴミの成形性を向上させると共に、塩素含有量を従来より低減し、地球温暖化にも貢献可能な固形燃料の製造方法を提供することを目的としている。   In view of such circumstances, the present invention further improves the technology of the above Japanese Patent Application No. 2010-033797, improves the moldability of dust, which is the problem, and reduces the chlorine content from the conventional level, resulting in global warming. It aims at providing the manufacturing method of the solid fuel which can contribute.

発明者は、上記目的を達成するため鋭意研究を重ね、その成果を本発明に具現化した。   The inventor has intensively studied to achieve the above object, and the results have been embodied in the present invention.

すなわち、本発明は、ゴミ収集ピット、一次破砕選別手段、乾燥炉、二次破砕選別手段を順次経て、乾燥、粉砕、選別された粉状の都市ゴミを成形機に供給し、圧縮して所定形状の固形燃料とするに際して、ゴミの回収を可燃物とプラスチック・ゴミとで分別回収すると共に、以下の3つの手段から選ばれた1つ又は2つ以上の手段を施し、固形燃料の塩素含有量を0.3質量%以下に低減する固形燃料の製造方法において、
前記ゴミに、バーク材を添加、混合すると共に、その添加量を、製品となる固形燃料の圧潰強度が25.5〜20kgになるように、質量で10〜50%に調整することを特徴とする固形燃料の製造方法である。
That is, the present invention sequentially supplies dust molding pits, primary crushing and sorting means, a drying furnace, and secondary crushing and sorting means to supply dried, pulverized and sorted powdery municipal waste to a molding machine, and compresses it to a predetermined value. When making solid fuel into a shape, the collection of garbage is separated and collected by combustibles and plastics and garbage, and one or more means selected from the following three means are applied, and the solid fuel contains chlorine In the method for producing a solid fuel in which the amount is reduced to 0.3% by mass or less,
The bark material is added to and mixed with the waste, and the amount added is adjusted to 10 to 50% by mass so that the crushing strength of the solid fuel as the product is 25.5 to 20 kg. This is a method for producing a solid fuel.

手段1:市中から分別回収したプラスチック・ゴミを前記ゴミ収集ピットへ投入する前に、該プラスチックス・ゴミから塩化ビニールを除去する
手段2:前記ゴミ収集ピットに付属する汚水ピットに溜まった汚水を、乾燥炉に供給せずにオフ・ラインで別途加熱処理する
手段3:ゴミにバイオマス材料を混合する
この場合、前記バーク材の添加、混合を、前記ゴミ収集ピットで行ったり、あるいは、前記バーク材に代え、リグニン接着剤を用いても良い。
Mean 1: Remove vinyl chloride from the plastics / trash before the plastic / garbage collected separately from the city is put into the garbage collection pit. Mean 2: Sewage collected in the sewage pit attached to the garbage collection pit. and means for separately heating at off-line without supplying the drying oven 3: If this mixing biomass material to dust, the addition of pre-Symbol bark material, mixed, and go in the garbage pit, or A lignin adhesive may be used in place of the bark material.

ゴミに、リグニンを含有し、樹木の皮であるバーク材を添加、混合するようにしたので、該バーク材が接着効果を発現し、製品である固形燃料の成形性が向上した。その結果、塩素含有量が0.3質量%以下の固形燃料が安定して低減できるようになり、製紙会社やRDF発電所ばかりでなく、固形燃料の使用先が従来より拡大するものと期待される。   Since the bark material that contains lignin and is the bark of the tree was added and mixed in the garbage, the bark material exhibited an adhesive effect, and the formability of the solid fuel that was the product was improved. As a result, solid fuel with a chlorine content of 0.3% by mass or less can be stably reduced, and it is expected that not only paper companies and RDF power plants but also the use of solid fuel will expand from the past. The

本発明の実施に利用した固形燃料の製造プラントを示すフロー図である。It is a flowchart which shows the manufacturing plant of the solid fuel utilized for implementation of this invention. 特願2010−033797号に記載した固形燃料の製造プラントを示すフロー図である。It is a flowchart which shows the solid fuel manufacturing plant described in Japanese Patent Application No. 2010-033797. 従来の固形燃料の製造プロセスを説明するフロー図である。It is a flowchart explaining the manufacturing process of the conventional solid fuel. 樹木におけるリグニンの接着機能を説明する模式図である。It is a schematic diagram explaining the adhesion | attachment function of the lignin in a tree.

以下、図面を参照して本発明の実施の形態を説明する。   Embodiments of the present invention will be described below with reference to the drawings.

まず、発明者は、従来の固形燃料の製造プラントを用い、ゴミに対する低塩素希釈のための添加するバイオマス材料として、下水汚泥、発泡ウレタン及びヤシ殻等を採用して固形燃料を試作した。その結果、製造プラントに投入する全ゴミ量に対しそれぞれ10質量%程度までの添加で、製品である固形燃料の塩素含有量が0.60質量%から0.48質量%に低減したが、それ以上の量のバイオマス材料量を添加すると製品が粉化してしまい、成形が難しくなることがわかった。これでは、下水汚泥、発泡ウレタン及びヤシ殻等のバイオマス材料の消費量が少なく、塩素の希釈効果が不十分である。つまり、ユーザの希望する塩素含有量0.3質量%以下の固形燃料を安定して製造するには、ゴミの成形性をもっと改良する必要があると判断した。そこで、発明者は、ゴミの成形性の向上について鋭意検討し、ゴミ等の構成物質を鑑みると接着機能を有する物質を添加すれば、ゴミ同士を接着する効果が発現され、成形性が改善されると考えた。そして、具体的に接着機能を有する物質を模索したところ、建材ボードの製造にリグニン系接着剤が利用されていることから、ゴミの成形には、リグニンを含む物質(通常植物中に20〜25質量%は含有されている)として、製紙工場等で樹木の皮むき作業で発生するバーク材の利用が適切ではないかと結論した。その根拠は、樹木は、図4に示すように、セルロース繊維37をリグニン38が結合材としての効果を発揮し、樹木繊維を形成しているからである。なお、その際、樹木に別途含有されているヘミセルロース39は、セルロース繊維37とリグニン38との親和性を向上させる相溶化剤として機能している。   First, the inventor made a prototype of a solid fuel by using a conventional solid fuel production plant and adopting sewage sludge, urethane foam, coconut shell and the like as biomass materials to be added for low chlorine dilution with respect to garbage. As a result, the chlorine content of the solid fuel as a product was reduced from 0.60% by mass to 0.48% by mass, with the addition of up to about 10% by mass with respect to the total amount of garbage put into the production plant. It was found that when the above amount of biomass material was added, the product was pulverized and molding was difficult. This consumes less biomass material such as sewage sludge, foamed urethane, and coconut shells, and the effect of diluting chlorine is insufficient. That is, in order to stably produce a solid fuel having a chlorine content of 0.3% by mass or less desired by the user, it has been determined that it is necessary to further improve the formability of dust. Therefore, the inventor diligently studied to improve the formability of dust, and in view of constituent materials such as dust, if a substance having an adhesive function is added, the effect of adhering the dust is expressed, and the moldability is improved. I thought. And when a substance having an adhesion function was specifically sought, a lignin-based adhesive was used for the production of building material boards. Therefore, a substance containing lignin (usually 20-25 in plants) was used for molding of garbage. As a result, it was concluded that the use of bark material generated by the peeling of trees at a paper mill or the like is appropriate. The reason for this is that, as shown in FIG. 4, the lignin 38 of the tree exhibits the effect of the cellulose fiber 37 as a binder, and the tree fiber is formed. At this time, the hemicellulose 39 separately contained in the tree functions as a compatibilizing agent that improves the affinity between the cellulose fibers 37 and the lignin 38.

このことを立証するため、発明者は、実際に図2に示したプロセスを用い、手段3(バイオマス材料の混合)に代え、ゴミにバーク材を添加、混合し、固形燃料を製造することを試行した。その結果を表1に示すが、バーク材の添加、混合で成形体の強度が十分に維持できるばかりか、塩素の希釈効果のあることが確認できた。なお、表1の強度とは、圧縮強度であり、破砕までに負荷する荷重の値で評価している。   In order to prove this, the inventor actually uses the process shown in FIG. 2 to add bark to trash and mix to replace the means 3 (mixing of biomass material) to produce a solid fuel. Tried. The results are shown in Table 1, and it was confirmed that not only the strength of the molded body could be sufficiently maintained by adding and mixing the bark material, but also the effect of diluting chlorine. In addition, the intensity | strength of Table 1 is a compressive strength, and is evaluated by the value of the load loaded before crushing.

Figure 0005877007
Figure 0005877007

そこで、発明者は、このバーク材をゴミへ添加、混合すればゴミの成形性が改善すると考え、前記手段1〜手段3も併用することを条件に第1の本発明として完成させたのである。この場合、バーク材36の添加量は、種々の試行の結果として、質量で10〜50%とするのが良く、そのことを第2の本発明とした。10%未満では、成形性の改善の効果が十分でなく、50%超えでは効果が飽和し、それ以上の添加は無意味になるからである。   Therefore, the inventor considered that the formability of the dust would be improved if this bark material was added to and mixed with the garbage, and was completed as the first invention on condition that the means 1 to means 3 were also used. . In this case, the addition amount of the bark material 36 is preferably 10 to 50% by mass as a result of various trials, and this is the second aspect of the present invention. If it is less than 10%, the effect of improving the moldability is not sufficient, and if it exceeds 50%, the effect is saturated, and addition beyond that is meaningless.

また、添加する位置は、図2に記号30で示した従来のバイオマス材料を添加する位置として試行したが、添加したバーク材36とゴミとの混合状態を良くするには、もっと上流側のゴミ収集ピット2の方が良いことが分かった。そのため、図1に示すように、ゴミ収集ピット2にバーク材36の添加手段(ホッパー等)を新設し、それを利用することを第3の本発明とした。   In addition, the addition position was tried as a position where the conventional biomass material indicated by symbol 30 in FIG. 2 is added. However, in order to improve the mixing state of the added bark material 36 and the garbage, the garbage on the upstream side is further improved. It turns out that the collection pit 2 is better. Therefore, as shown in FIG. 1, it is a third aspect of the present invention that a means for adding a bark material 36 (such as a hopper) is newly installed in the garbage collection pit 2 and used.

次に、発明者は、リグニンを含有するバーク材が成形性に有効ならば、市販のリグニン系接着剤をゴミに混合しても同様の効果が得られると考え、バーク材に代えてリグニン接着剤の添加することを第4の発明とした。その際、ゴミへのリグニン系接着剤の添加方法は特に定めないことにする。リグニン系接着剤が液体状であれば、ゴミへスプレー散布すれば良いし、固体状であれば、粉砕して紛体としたものをゴミに混合すれば良いからである。勿論、その添加量はバーク材よりも少量となるが、ゴミの塩素希釈物質としての役割を下水汚泥等のバイオマス材料に行わせれば良い。   Next, the inventor believes that if a bark material containing lignin is effective for moldability, a similar effect can be obtained by mixing a commercially available lignin-based adhesive into the trash, and the lignin adhesive is used instead of the bark material. The addition of an agent is the fourth invention. At that time, a method for adding the lignin-based adhesive to the waste is not particularly defined. This is because if the lignin-based adhesive is in a liquid state, it may be sprayed onto the dust, and if it is in a solid state, it may be pulverized into a powder and mixed with the dust. Of course, the amount added is smaller than that of the bark material, but the biomass material such as sewage sludge may serve as a chlorine-diluting substance for waste.

なお、ここで、前記手段1とは、従来のゴミ収集ピット2、一次破砕選別手段17、乾燥炉8、二次破砕選別手段18及び成形機12等からなる製造工程に入れる前に、ゴミの回収を可燃ゴミとプラスチック・ゴミとで分別回収して取り入れることである。具体的には、図1より明らかなように、市中から可燃ゴミ(生ゴミ、紙ゴミ等)31とプラスチック・ゴミ32とを分別回収し、可燃ゴミ31はゴミ収集ピット2へ直接投入するが、プラスチック・ゴミ32は別の受け入れホッパ33に投入するようにした。そして、当該プラスチック・ゴミ32は磁選機6を備えた予備破砕機34を経由させて金属等の不適切物を除いてから新たに設けた塩化プラスチック選別装置35を介して塩化ビニール21を除去した後、ゴミ収集ピット2へ搬入するようにしたのである。   Here, the means 1 means that before entering the manufacturing process comprising the conventional dust collection pit 2, the primary crushing and sorting means 17, the drying furnace 8, the secondary crushing and sorting means 18 and the molding machine 12, etc. It is to collect the collected waste separately from combustible waste and plastic waste. Specifically, as is clear from FIG. 1, combustible garbage (raw garbage, paper garbage, etc.) 31 and plastic garbage 32 are separately collected from the city, and the combustible garbage 31 is directly thrown into the garbage collection pit 2. However, the plastic trash 32 is put into another receiving hopper 33. Then, the plastic waste 32 is removed through an auxiliary crusher 34 equipped with a magnetic separator 6 to remove inappropriate materials such as metal, and then the vinyl chloride 21 is removed through a newly provided chlorinated plastic sorting device 35. Later, it was carried into the garbage collection pit 2.

次に、手段2とは、図3の汚水ピット3に溜まった汚水9を乾燥炉8に供給せずに、図1及び図2に示すように、汚水9をトラック27でオフ・ラインに搬送し、別途加熱処理することである。これにより、製品の塩素量を低減できるからである。なお、その加熱処理の方法については、本発明では特に限定しない。   Next, the means 2 means that the sewage 9 collected in the sewage pit 3 in FIG. 3 is not supplied to the drying furnace 8 and the sewage 9 is conveyed off-line by the truck 27 as shown in FIGS. And heat treatment separately. This is because the amount of chlorine in the product can be reduced. Note that the heat treatment method is not particularly limited in the present invention.

また、手段3とは、乾燥処理を経た都市ゴミ1に塩素分を含まないバイオマス材料30
を加えることである。これにて製品の塩素分を希釈できるからである(図1及び図2参照)。なお、バイオマス材料30としては、ヤシ殻、下水汚泥、木クズ等、種々のものが存在するが、本発明ではヤシの実からパーム油を採取した後に残るヤシ殻を使用することを推薦する。
The means 3 is a biomass material 30 that does not contain chlorine in the municipal waste 1 that has undergone the drying treatment.
Is to add. This is because the chlorine content of the product can be diluted (see FIGS. 1 and 2). In addition, although various things, such as a coconut shell, a sewage sludge, and wood scrap, exist as biomass material 30, in this invention, it is recommended to use the coconut shell which remains after extract | collecting palm oil from a coconut.

市中から分別回収した都市ゴミ1を処理し、固形燃料13を製造した。その際に利用した製造工程は、本発明に係る図1に示したフローによるものである。なお、図1に示した乾燥炉8の内部雰囲気温度は500〜600℃、成形機12の加圧条件は最高加圧力で200kg/cm、都市ゴミ1の一次破砕選別17後のサイズは50〜100mm、二次破砕選別18後のサイズは20〜30mmとした。その他の主な製造条件及び製造結果を表2に一括して示す。なお、表2において、都市ゴミ量(質量%)とは、1回の操業に投入する都市ゴミの量であり、都市ゴミへの添加材量(また、バイオマス材料の添加量)は、(添加材量/(都市ゴミ量+添加材量)×100)で表している。また、本実施例では、従来例として図3の製造プロセスを用いた場合の他、バーク材に代えて都市ゴミにリグニン接着剤を添加する発明を実施し、その結果を表3に示した。 Municipal waste 1 separated and collected from the city was processed to produce solid fuel 13. The manufacturing process used at that time is based on the flow shown in FIG. 1 according to the present invention. The internal atmospheric temperature of the drying furnace 8 shown in FIG. 1 is 500 to 600 ° C., the pressurizing condition of the molding machine 12 is 200 kg / cm 2 at the maximum applied pressure, and the size after the primary crushing and sorting 17 of the municipal waste 1 is 50. The size after ˜100 mm and secondary crushing and sorting 18 was 20-30 mm. Table 2 collectively shows other main manufacturing conditions and manufacturing results. In Table 2, the amount of municipal waste (% by mass) is the amount of municipal waste input to one operation, and the amount of additive to municipal waste (and the amount of biomass material added) is Material amount / (amount of municipal waste + amount of additive material) × 100). Further, in this example, in addition to the case where the manufacturing process of FIG. 3 was used as a conventional example, an invention in which lignin adhesive was added to municipal waste instead of bark material was carried out, and the results are shown in Table 3.

Figure 0005877007
Figure 0005877007

Figure 0005877007
Figure 0005877007

表2及び表3より、本発明に係る固形燃料13の製造方法を適用すると、ゴミの成形性が改善され外見の優れた最終製品としての固形燃料13が得られるばかりでなく、そこに含まれる塩素含有量が低減し、ユーザーの希望値0.3質量%以下の固形燃料が安定して供給できることが明らかである。   From Table 2 and Table 3, when the production method of the solid fuel 13 according to the present invention is applied, not only the solid fuel 13 as an end product with improved dust moldability and excellent appearance is obtained, but also included therein. It is clear that the solid content of the chlorine content is reduced and the user's desired value of 0.3% by mass or less can be stably supplied.

1 都市ゴミ
2 ゴミ収集ピット
3 汚水ピット
4 クレーン
5 ゴミ・ホッパ
6 磁選機
7 破砕機
8 乾燥炉
9 汚水
10 風選機
11 消石灰
12 成形機
13 固形燃料
14 脱臭装置
15 集塵機
16 熱交換器
17 一次破砕選別手段
18 二次破砕選別手段
19 ベルト・コンベア
20 センサ
21 塩化ビニール
22 空気噴出しノズル
23 熱風炉
24 スクリーン
25 定量供給機
26 冷却機
27 トラック
28 信号
29 空気
30 バイオマス燃料
31 可燃ゴミ
32 プラスチック・ゴミ
33 別の受け入れホッパ
34 予備破砕機
35 塩化プラスチック選別装置
36 バーク材
37 セルロース繊維
38 リグニン
39 ヘミセルロース
DESCRIPTION OF SYMBOLS 1 Municipal waste 2 Waste collection pit 3 Wastewater pit 4 Crane 5 Waste / hopper 6 Magnetic separator 7 Crusher 8 Drying furnace 9 Wastewater 10 Wind separator 11 Slaked lime 12 Molding machine 13 Solid fuel 14 Deodorizer 15 Dust collector 16 Heat exchanger 17 Primary Crushing and sorting means 18 Secondary crushing and sorting means 19 Belt conveyor 20 Sensor 21 Vinyl chloride 22 Air outlet nozzle 23 Hot air furnace 24 Screen 25 Constant supply machine 26 Cooling machine 27 Truck 28 Signal 29 Air 30 Biomass fuel 31 Combustible waste 32 Plastic Garbage 33 Separate receiving hopper 34 Preliminary crusher 35 Chlorinated plastic sorting device 36 Bark material 37 Cellulose fiber 38 Lignin 39 Hemicellulose

Claims (3)

ゴミ収集ピット、一次破砕選別手段、乾燥炉、二次破砕選別手段を順次経て、乾燥、粉砕、選別された粉状の都市ゴミを成形機に供給し、圧縮して所定形状の固形燃料とするに際して、ゴミの回収を可燃物とプラスチック・ゴミとで分別回収すると共に、以下の3つの手段から選ばれた1つ又は2つ以上の手段を施し、固形燃料の塩素含有量を0.3質量%以下に低減する固形燃料の製造方法において、
前記ゴミに、バーク材を添加、混合すると共に、その添加量を、製品となる固形燃料の圧潰強度が25.5〜20kgになるように、質量で10〜50%に調整することを特徴とする固形燃料の製造方法。
手段1:市中から分別回収したプラスチック・ゴミを前記ゴミ収集ピットへ投入する前に、該プラスチックス・ゴミから塩化ビニールを除去する
手段2:前記ゴミ収集ピットに付属する汚水ピットに溜まった汚水を、乾燥炉に供給せずにオフ・ラインで別途加熱処理する
手段3:ゴミにバイオマス材料を混合する
After passing through the garbage collection pit, primary crushing and sorting means, drying furnace, and secondary crushing and sorting means, the dried, pulverized and sorted powdery municipal waste is supplied to the molding machine and compressed into a solid fuel of a predetermined shape. At that time, the collection of garbage is separated and collected by combustibles and plastics and garbage, and one or more means selected from the following three means are applied, and the solid fuel has a chlorine content of 0.3 mass. In the method for producing a solid fuel that is reduced to less than
The bark material is added to and mixed with the waste, and the amount added is adjusted to 10 to 50% by mass so that the crushing strength of the solid fuel as the product is 25.5 to 20 kg. A method for producing a solid fuel.
Mean 1: Remove vinyl chloride from the plastics / trash before the plastic / garbage collected separately from the city is put into the garbage collection pit. Mean 2: Sewage collected in the sewage pit attached to the garbage collection pit. Is separately heated off-line without supplying it to the drying furnace.
前記バーク材の添加、混合を、前記ゴミ収集ピットで行うことを特徴とする請求項1記載の固形燃料の製造方法。   2. The method for producing a solid fuel according to claim 1, wherein the bark material is added and mixed in the dust collection pit. 前記バーク材に代え、リグニン接着剤を用いることを特徴とする請求項1又は2記載の固形燃料の製造方法。   3. The method for producing a solid fuel according to claim 1, wherein a lignin adhesive is used instead of the bark material.
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