JP2005140484A - Method for circulation type drying and pulverizing fuel system of waste, and device therefor - Google Patents
Method for circulation type drying and pulverizing fuel system of waste, and device therefor Download PDFInfo
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- JP2005140484A JP2005140484A JP2003408140A JP2003408140A JP2005140484A JP 2005140484 A JP2005140484 A JP 2005140484A JP 2003408140 A JP2003408140 A JP 2003408140A JP 2003408140 A JP2003408140 A JP 2003408140A JP 2005140484 A JP2005140484 A JP 2005140484A
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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特開平11−309495 JP-A-11-309495
コーヒーカス・茶カス・下水汚泥等の乾燥、微粉砕後、粉炭バーナー用燃料製造から粉炭バーナーで熱風発生炉内を加熱し、該熱風を乾燥用熱源として再利用した旋回流熱風乾燥装置に至る循環式廃棄物の乾燥及び微粉化燃料システムの方法とその装置。 After drying and pulverizing coffee residue, tea residue, sewage sludge, etc., the production of fuel for the pulverized coal burner is used to heat the inside of the hot air generating furnace with the pulverized coal burner, and the hot air is reused as a heat source for drying. Method and apparatus for circulating waste drying and pulverizing fuel system.
含水率の高い廃棄物の処理を行う時、海洋投棄が禁止され、特にコーヒカス・茶カスについては全量が産業廃棄物事業者による廃棄処理、或は焼却処分されていた。湿度を65%まで乾燥させれば生ゴミ等は、加熱或は水分調整用のオガクズや籾殻等を加えて湿度65%になるよう調節して有機肥料化されている。しかしコンポストも肥料の質の問題があり、肥料法の適用を受けなければ販売することができない。 When processing waste with a high water content, ocean dumping was prohibited, and in particular, the entire amount of coffee and tea residue was either disposed of by industrial waste businesses or incinerated. If the humidity is dried to 65%, the raw garbage is adjusted to a humidity of 65% by adding sawdust or rice husk for heating or moisture adjustment, and is made into an organic fertilizer. However, compost also has a problem with fertilizer quality and cannot be sold without the application of the fertilizer law.
コンポストはバクテリアによって発酵分解し、生ゴミ等の蛋白質や澱粉、或は木質部のセミロースに至るまで時間をかけて分解し、有機土質に近いところまで分解して有機肥料にしている。生に近いものは古来よりバクテリアの好物で放線菌による分解が可能であったが、コーヒーを抽出した後のコーヒーカスは全くバクテリア処理ができない。 Compost is fermented and decomposed by bacteria and decomposes over time until it reaches protein such as garbage and starch, or semi-loose in the woody part, and decomposes to a place close to organic soil to make organic fertilizer. Nearly raw ones have been a favorite of bacteria since ancient times and could be decomposed by actinomycetes, but the coffee residue after extracting coffee cannot be treated with bacteria at all.
多孔質の木の実であり、バクテリアのアメニティ環境を維持してもコーヒーカスは全く発酵しない、理由はコーヒーの焙煎である煎る前は白い豆が煎ることによってコーヒー色を呈するこのコーヒー色は黒ではないが濃い茶色である、これは黒の炭になる一歩手前まで煎られているので、食欲旺盛なバクテリアも全く歯が立たず発酵することができない。 It is a porous fruit, and even if it maintains a bacterial amenity environment, the coffee residue does not ferment at all.The reason is that it is roasted coffee. Although it is not dark but dark brown, it is roasted one step before it becomes black charcoal, so even the appetizing bacteria can not ferment at all and cannot ferment.
コンポストの次は炭化処理して脱臭剤や、有害物質の吸収剤への利用が見込まれるが、85%以上という含水率が災いし、炭化炉に投入する前に必ず気流乾燥方法が採用されている、炭化しなければならないものは仕方ないが、燃料化が目的ならば炭化しない方が火力を保持できる。 After composting, carbonization treatment is expected to be used as a deodorant and harmful substance absorbent, but the water content of 85% or more is damaged, and the airflow drying method is always adopted before putting it into the carbonization furnace. Although there is no help for what must be carbonized, if it is intended to be fueled, it is better not to carbonize to maintain thermal power.
セメント焼成用回転炉は粉炭バーナーが使用されているが、通常熱風発生炉内を所定の温度に達するまで重油等で暖気運転を行い800℃〜1000℃内外まで炉内温度を上げ、粉炭を投入して一瞬に着火するレベルまで温度が上がった時、排熱風から熱交換した1000℃程度のフレッシュエアと共に送風燃焼し一定の炉内温度を維持する。 The cement-fired rotary furnace uses a pulverized coal burner. Normally, the inside of the hot-air generator is warmed up with heavy oil until the temperature reaches a specified temperature, and the furnace temperature is raised to between 800 ° C and 1000 ° C, and then the pulverized coal is charged. Then, when the temperature rises to a level where it can be ignited instantaneously, it blows and burns together with about 1000 ° C. fresh air heat-exchanged from the exhaust hot air to maintain a constant furnace temperature.
本システムではセメント焼成炉のような時間当り10頓〜20頓の粉炭バーナーではなく、1/100程度の、時間当り100kg〜200kgという小型の熱発生炉であり、燃料も粉炭の6000Kcalという熱量ではなくコーヒーカスで4000Kcalである為、燃料の不足カロリーを補う必要がある。その対処方法は新規に作成した球形粉炭酸素混合バーナーを用いて酸素補給制御を行いながらの燃焼になる。石炭の微粉炭では圧力容器から粉炭を切出して粉炭バーナーへのパイプ移送中に揮発性物質による失火を避けるため、窒素ガスによる制御を行っているので、窒素富化装置を用いるか酸素富化装置を用いるかの違いである。酸素によるゴミ焼却方法はスイス・サーモセレクト社によって既に実用化されている。 This system is not a pulverized coal burner of 10 to 20 times per hour like a cement firing furnace, but a small heat generating furnace of about 1/100, 100 kg to 200 kg per hour, and the fuel is 6000 Kcal of calorie. Since it is 4000 Kcal for coffee residue, it is necessary to compensate for the shortage of fuel. The coping method is combustion while performing oxygen replenishment control using a newly created spherical powder carbon dioxide mixing burner. For coal pulverized coal, nitrogen gas is controlled to cut off pulverized coal from the pressure vessel and avoid misfire due to volatile substances during pipe transfer to the pulverized coal burner. Use a nitrogen enrichment device or an oxygen enrichment device. Is the difference between using. Oxygen waste incineration has already been put to practical use by Swiss Thermo Select.
微細粉炭を燃焼する為、燃焼した後に灰が舞うことになるセメント焼成炉ではセメント内に5%の前後の灰が混入されても問題にされないので、粉炭バーナー燃焼はセメント業界向といわれている。本システムは燃料製造のための乾燥で、乾燥後に燃焼用の燃料になる循環式リサイクル方法であるので、多少の灰混入は許容範囲内で、大気放出に際してはバッグフイルターやサイクロン回収等万全の策を講じる必要がある。 In a cement firing furnace where ash will fly after combustion because it burns fine pulverized coal, it is not a problem even if ash of around 5% is mixed in the cement, so pulverized coal burner combustion is said to be suitable for the cement industry . Since this system is a recycle recycling method that is used for fuel production and becomes a fuel for combustion after drying, some ash contamination is within the acceptable range. It is necessary to take.
下水汚泥では石炭粉の混入と乾燥で火力発電用或はセメント焼成用燃料として三菱マテリアル社から特開平11−309495で出願されており、コーヒーカスのカロリー向上には微粉炭の混合も一つの方法であるが、石炭の燃焼による大気汚染対策を視野に入れる必要がある。石炭を混合してカロリー不足を補えば酸素補給はしなくてもよくなるので2者択1でどちらをとるかは採用会社に任せることにしたい。 In sewage sludge, Mitsubishi Materials Corporation has filed an application in Japanese Patent Application Laid-Open No. 11-309495 as a fuel for thermal power generation or cement burning by mixing and drying coal powder. However, it is necessary to consider air pollution countermeasures caused by coal combustion. If you add coal and make up for the calorie shortage, you don't need to supply oxygen.
わが国の文化として定着しつつある自動販売機やコンビニエンスストアが増えるにつれて缶入コーヒーや缶入り茶等の需要が旺盛になり、その生産高が年毎に大きくなり、生産量に伴って排出されるコーヒー或はお茶葉の抽出後の処理が問題になりながらも、殆ど産業廃棄物処理業者依頼か、燃焼に任されていた。しかし本発明により厄介者扱い視されていた高含水廃棄物が乾燥により、有用な資源に蘇り、更に微粉砕と粉炭バーナーの開発により被乾燥物に甘んじていたコーヒーカス茶カスが乾燥後に燃料として生まれ変わる再利用の方法が発見されたのである。 As vending machines and convenience stores are becoming established as a culture of Japan, the demand for canned coffee and canned tea has increased, and the production volume has been increasing year by year, resulting in an increase in production volume. Although processing after the extraction of coffee or tea leaves became a problem, most of them were commissioned by industrial waste processing companies or burned. However, the highly water-containing waste that has been regarded as a troublesome person by the present invention is restored to a useful resource by drying. A reusable recycling method was discovered.
本発明の最大の糸口は、旋回流熱風乾燥装置本人特願(2000−404312)であり、乾燥後の微粉砕方法の採用から粉炭バーナーの開発に至る一連の発明の連続と、そのシステム化が産んだ効果で、コーヒー缶充填事業者を始めとする清涼飲料関連事業者の福音となる新規発明である。循環式廃棄物の乾燥及び微粉化燃料システムの方法とその装置。 The greatest clue of the present invention is the swirling flow hot air drying device (Japanese Patent Application No. 2000-404312), which is a series of inventions from the adoption of a fine pulverization method after drying to the development of a pulverized coal burner, and its systematization. It is a new invention that becomes the gospel of soft drink related businesses, including coffee can filling businesses, due to the effects produced. Method and apparatus for circulating waste drying and pulverizing fuel system.
図面は本発明に係る循環式廃棄物の乾燥及び微粉化燃料システム方法とその装置の実施例を示し、図面は一連のシステムフロー図である。 The drawings show an embodiment of the circulating waste drying and pulverizing fuel system method and apparatus according to the present invention, and the drawings are a series of system flow diagrams.
図中、1は被乾燥物投入ホッパーで、旋回流乾燥炉2へは、図示されないがロータリーバルブ等の公知の技術で投入し、炉内の切替羽根の掻き揚げと旋回流熱風によって急速に乾燥される。詳しくは本人特願(2000−404312)を参照されたい。乾燥中の水分は蒸気となって煙突3から大気放出される。特に臭気が強い場合は煙突3の後に脱臭装置等の付帯設備が必要となる。 In the figure, reference numeral 1 denotes a material input hopper, which is input to the swirling
乾燥が完了した乾燥物は、乾燥物貯留ホッパー4に貯留され、微粉砕機5で粉砕される。微粉砕された乾燥物は微粉貯留ホッパー6で貯留される。貯留された微粉はカロリーが低い場合は、酸素富化装置7で酸素を発生させ微粉ノズル8内で酸素を混合しながら粉炭熱風炉9内に噴霧状態で微粉が投入され、予め800℃以上に温められていた粉炭熱風炉9内で一瞬にして燃焼される。微粉カロリーを上げる場合は石炭微粉を混入して燃焼を行う。 The dried product after drying is stored in the dried
本発明は缶入コーヒー等飲料水の充填業者等から排出するコーヒーカス・茶カス或は下水処理場から排出する下水汚泥等の水分は85%以上の高含水率のため、その殆どが減容されることもなく、高額の引取り価格で産業廃棄物処理業者に処理を依頼して推移してきたが、人口の上昇が止まり、天候不順等の影響から右肩上がりの業績に陰りが見え、或は廃掃法が施工される等、減容又はリサイクル方法の模索が行え初める気運が出始めた。 The present invention has a high water content of 85% or more, such as coffee scum, tea scum or sewage sludge discharged from a drinking water filling company such as canned coffee. However, it has been shifting to an industrial waste disposal contractor at a high collection price, but the rise in the population has stopped, and due to the effects of bad weather etc. Or, the beginning of the momentum to begin exploring volume reduction or recycling methods, such as the construction of a scrapping method.
上記の気運を殺ぐ最大の難関はイニシャルコストとランニングコストの安価な廃業物処理用の乾燥装置が世界的に解決されていなかったことに基因する。しかし本人特願(2000−404312)旋回流熱風乾燥装置を完成させたことで一気に弾みがつき、微粉砕から粉炭バーナーの新技術開発まで、夫々過去に捕われない方法を編みだし、他人の特許を使用することなく、抵触することのない全くの新規技術を提供するシステムと方法とその装置を提供する。 The biggest obstacle to killing the above-mentioned momentum is based on the fact that a drying apparatus for waste disposal that has low initial cost and running cost has not been solved globally. However, the completion of the swirl flow hot-air drying device (2000-404312) was a momentum, and from the fine grinding to the development of new technology for pulverized coal burners, we have devised methods that have not been caught in the past. A system and method and apparatus are provided that provide a completely new technology that is not used and without conflict.
1.被乾燥物投入ホッパー
2.旋回流熱風乾燥炉
3.煙突
4.乾燥物貯留ホッパー
5.微粉砕機
6.微粉貯留ホッパー
7.酸素富化装置
8.微粉ノズル
9.粉炭熱風炉
10.灰回収器1. 1. To-be-dried
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009104311A1 (en) * | 2008-02-18 | 2009-08-27 | 高橋 秀久 | Solid fuel and method of producing solid fuel |
JP2009297686A (en) * | 2008-06-17 | 2009-12-24 | Aura:Kk | Brewed tea-leaves reprocessing method and product made by the method |
CN103375974A (en) * | 2013-04-18 | 2013-10-30 | 安徽省昊晟能源科技有限公司 | Novel hot air drying system for preparing power |
CN111747628A (en) * | 2020-07-16 | 2020-10-09 | 南京中电环保固废资源有限公司 | Sludge drying system and process with water content of 80% |
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2003
- 2003-11-04 JP JP2003408140A patent/JP2005140484A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009104311A1 (en) * | 2008-02-18 | 2009-08-27 | 高橋 秀久 | Solid fuel and method of producing solid fuel |
JP4465411B2 (en) * | 2008-02-18 | 2010-05-19 | 真輔 栗山 | Solid fuel production apparatus and production method |
JPWO2009104311A1 (en) * | 2008-02-18 | 2011-06-16 | 真輔 栗山 | Solid fuel production apparatus and production method |
JP2009297686A (en) * | 2008-06-17 | 2009-12-24 | Aura:Kk | Brewed tea-leaves reprocessing method and product made by the method |
CN103375974A (en) * | 2013-04-18 | 2013-10-30 | 安徽省昊晟能源科技有限公司 | Novel hot air drying system for preparing power |
CN111747628A (en) * | 2020-07-16 | 2020-10-09 | 南京中电环保固废资源有限公司 | Sludge drying system and process with water content of 80% |
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