JP2002192115A - Garbage treatment method and fertilizer - Google Patents

Garbage treatment method and fertilizer

Info

Publication number
JP2002192115A
JP2002192115A JP2000395671A JP2000395671A JP2002192115A JP 2002192115 A JP2002192115 A JP 2002192115A JP 2000395671 A JP2000395671 A JP 2000395671A JP 2000395671 A JP2000395671 A JP 2000395671A JP 2002192115 A JP2002192115 A JP 2002192115A
Authority
JP
Japan
Prior art keywords
garbage
tank
promote
steam
temperature
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.)
Pending
Application number
JP2000395671A
Other languages
Japanese (ja)
Inventor
Kinichiro Sakuma
佐久間金一郎
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.)
SHINSEI ENGINEERING KK
Original Assignee
SHINSEI ENGINEERING 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 SHINSEI ENGINEERING KK filed Critical SHINSEI ENGINEERING KK
Priority to JP2000395671A priority Critical patent/JP2002192115A/en
Publication of JP2002192115A publication Critical patent/JP2002192115A/en
Pending legal-status Critical Current

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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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Accessories For Mixers (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)
  • Fertilizers (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a treatment method for garbage or the like and to provide a fertilizer by dissolving garbage or the like with a strong acid, neutralizing the garbage, decomposing the resulting garbage by microorganism, and finally carrying out steam evaporation by high temperature thermochemical reaction to obtain a pure white powder in a garbage treatment tank. SOLUTION: The treatment method for garbage or the like is carried out by storing garbage in a garbage treatment tank after pulverization of the garbage, adding a prescribed amount of hydrochloric acid, heating to a prescribed temperature, stirring the garbage to decompose organic substances by the strong acid, acceleratedly produce a fluidizing decomposed product, and promote steam evaporation, discharging the generated steam out of the treatment tank to promote volume decrease, and successively adding a strong alkali containing no chlorine to make the resulting garbage mixture neutral or weakly alkaline, and next adding and mixing a powder of quicklime to cause high temperature thermochemical reaction to completely separate and remove high heat steam and produce a fine powder with pure white color subjected to the thermal decomposition, complete disinfection, dewatering, and volume decrease in the garbage treatment tank and recovering the powder outside the tank.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本願発明は、生ごみ等を強酸
により溶解し、中和してから微生物分解させ、最後に高
温熱化学反応により水蒸気蒸発を行なわせて生ごみ処理
槽内に純白微粉末を得る、生ごみ等の処理方法及び肥料
に関する。
BACKGROUND OF THE INVENTION The present invention relates to a method for dissolving garbage and the like with a strong acid, neutralizing the garbage, decomposing the bacterium into microorganisms, and finally vaporizing the garbage by a high-temperature thermochemical reaction to form pure white fines in the garbage processing tank. The present invention relates to a method for obtaining garbage, a method for obtaining powder, and a fertilizer.

【0002】[0002]

【従来の技術】従来の生ごみ等の処理装置として、
(1)生ごみをEM菌等の有効微生物群により分解させ
て約五分の一に減容する残滓を堆肥とするリサイクル型
の第一の生ごみ等の処理装置と、(2)生ごみを高温高
圧蒸気で溶解しEM菌等の有効微生物群とEMセラミッ
クスを混ぜて分解して約十分の一に減容する残滓を肥料
とするリサイクル型の第二の生ごみ等の処理装置(特開
平08-192136)と、(3)生ごみを加熱し攪拌して乾燥
・脱水を促し約十分の一に減容する残滓を肥料とするリ
サイクル型の第三の生ごみ等の処理装置と、(4)生ご
みを酸化・殺菌・液化して浸出液と残滓に分別しさらに
残滓を浸出液と搾り滓に分けて、浸出液をガス化して燃
料にするとともに搾り滓を加熱殺菌して肥料とするリサ
イクル型の第四の生ごみ等の処理装置(特開平11-10460
4)と、(5)バイオチップ(微生物を繁殖させた木質
細片)と生ごみを混ぜて8時間乃至48時間で水と二酸
化炭素等に分解し残滓を残さない完全分解型の第五の生
ごみ等の処理装置と、(6)生ごみに生石灰を添加し攪
拌して熱分解させて1週間堆積しさらに有効バクテリア
を添加し攪拌して圧縮して肥料とする第六の生ごみ等の
処理装置(特願2000-044373)と、(7)生ごみを機械
的に10mm以下に破砕しスラリーにして、該スラリー状
に消石灰と、被膜処理した生石灰を添加して攪拌混合し
反応熱で水分を蒸散させ乾燥・減容化する第七の生ごみ
等の処理装置(特願平06-263573、特願平07-303874)
と、(8)生ごみを機械的に粒状に破砕し生石灰を添加
して攪拌混合し反応熱で水分を蒸散させ乾燥・減容化す
る第八の生ごみ等の処理装置(特願平06-263573、特願
平06-007763、特願平09-243262、:類似技術として特願
平09-001103)と、(9)生ごみに生石灰と貝粉と植物
粕を混ぜてなる処理剤を添加して攪拌混合し反応熱で水
分を蒸散させ乾燥・減容化する第九の生ごみ等の処理装
置(特願平09-103753)と、(10)家畜等の排気血液
に生石灰を添加して攪拌し反応熱で水分を蒸散させ乾燥
・減容化・細粒化する第十の家畜等の排気血液の処理装
置(特願平06-305870)と、(11)細菌アルカリヂエ
ネス・レイタスを生ごみを混ぜて27から32℃の好気
性条件下で2・3日間分解を必要としその間腐敗臭を発
生させず大幅な減量化を促進させ残るケーキ状の固形分
を焼却する生ごみ等の処理方法(特願2000−117233)、
等がある。
2. Description of the Related Art As a conventional garbage processing apparatus,
(1) Recycling-type first garbage processing equipment that turns residue into a compost by decomposing garbage by effective microorganisms such as EM bacteria and reducing the volume to about one-fifth, and (2) garbage A second recycling garbage processing device that dissolves germs with high-temperature and high-pressure steam, mixes the effective microorganisms such as EM bacteria with EM ceramics, decomposes them, and reduces the volume to about one-tenth. Kaihei 08-192136), and (3) a recycle-type third garbage disposal device that uses the residue that is heated and agitated to promote drying and dehydration and reduces the volume to about one-tenth as fertilizer, (4) Recycle garbage by oxidation, sterilization and liquefaction to separate it into leachate and residue, separate the residue into leachate and pomace, gasify the leachate to produce fuel, and heat sterilize pomace to recycle as fertilizer 4th garbage processing device (Japanese Patent Laid-Open No. 11-10460)
4), and (5) a biodegradable (woody shard that has propagated microorganisms) mixed with garbage and decomposed into water, carbon dioxide, etc. in 8 to 48 hours to leave no residue and the fifth (6) Add lime to garbage and stir to pyrolyze it for one week, add effective bacteria, stir and compress to make fertilizer, etc. (7) mechanically crushing garbage to 10 mm or less to form a slurry, adding slaked lime and film-treated quick lime to the slurry, stirring and mixing, 7th garbage processing equipment that evaporates water to dry and reduce the volume of water (Japanese Patent Application Nos. 06-263573 and 07-303874)
And (8) an eighth garbage processing apparatus for mechanically crushing garbage into granules, adding quicklime, stirring and mixing, evaporating water with heat of reaction to dry and reduce volume (Japanese Patent Application No. 06 -263573, Japanese Patent Application No. 06-007763, Japanese Patent Application No. 09-243262: Japanese Patent Application No. 09-001103) and (9) A treatment agent that mixes quicklime, shellfish flour, and plant meal in garbage. A ninth garbage processing device (Japanese Patent Application No. 09-103753) that adds, stirs and mixes, evaporates water with the heat of reaction to dry and reduce the volume, and (10) adds quicklime to exhausted blood of livestock and the like. And a device for treating the exhausted blood of livestock etc. (Japanese Patent Application No. 06-305870), which is dried, reduced in volume and granulated by evaporating the water with the heat of reaction and drying, and (11) bacterial alkali It is necessary to decompose the lettuce with garbage under aerobic conditions at 27 to 32 ° C for a few days, during which time it does not generate putrefactive odor and promotes significant weight reduction and remains. Method of processing garbage such as incinerating Jo of the solids (Japanese Patent Application No. 2000-117233),
Etc.

【0003】[0003]

【発明が解決しようとする課題】生ごみ等の処理は、多
くの場合、800℃で長時間燃やしている。氷河が後退し
海面がどんどん上昇し流氷も年々少なくなっていて、20
10年に地球の温度が2℃上昇すると関東地方の五分の一
の面積が海面下に水没するという地球環境の下で、生ご
みの焼却による炭酸ガスの発生は地球温暖化の一因にな
っているとともに、ヒータや高温高圧蒸気等による加熱
を行うことから地球資源を消費することになっていて地
球環境に優しいとは言えない。この観点から、第二及び
第三の生ごみ等の処理装置は好ましくない。
The processing of garbage and the like often involves burning at 800 ° C. for a long time. Glaciers have receded, the sea level has risen steadily, and drift ice has been decreasing year by year.
In a global environment where one-fifth of the Kanto region will be submerged below sea level when the temperature of the earth rises by 2 ° C in 10 years, the generation of carbon dioxide by incineration of garbage contributes to global warming. In addition, heating with a heater, high-temperature high-pressure steam, or the like consumes earth resources, and cannot be said to be environmentally friendly. From this viewpoint, the second and third garbage processing apparatuses are not preferable.

【0004】上記の第一の生ごみ等の処理装置は、EM
菌等の有効微生物群のランニングコストが高く付いてい
ること、残滓が綺麗ではなく、容器に汚く付着するこ
と、汚い分解液の処理が必要なこと、ゴミ投入時に臭い
匂いが出ることが欠点である。この欠点は上記の第二の
生ごみ等の処理装置にもある。上記の第三の生ごみ等の
処理装置は、残滓が綺麗ではないことも欠点である。
[0004] The above-mentioned first garbage processing apparatus is an EM.
Disadvantages are that the running cost of effective microorganisms such as bacteria is high, the residue is not clean, it adheres dirty to the container, it is necessary to treat the dirty decomposition solution, and the odor comes out when throwing garbage. is there. This disadvantage also exists in the above-mentioned second garbage processing apparatus. The above-mentioned third garbage processing apparatus also has a disadvantage that the residue is not clean.

【0005】上記の第四の生ごみ等の処理装置は、シス
テムが大型プラントになり設備費が極めて高く付き、装
置の設置空間を極めて大きくとること、処理に長時間か
かることが欠点である。
[0005] The above-mentioned fourth garbage processing apparatus has disadvantages in that the system becomes a large plant, the facility cost is extremely high, the installation space for the apparatus is extremely large, and the processing takes a long time.

【0006】上記の第五の生ごみ等の処理装置は、生ご
みを完全分解するので残滓の処理が必要ないから生ごみ
を捨てて地球を汚すことはないが、資源となるべき生ご
みをリサイクルできないこと及び多量の二酸化炭素を排
出することから地球環境に優しいとは言えない。又、高
価のバイオチップが必要でありランニングコストが高く
付いている。
[0006] The fifth garbage processing apparatus described above completely decomposes garbage, so that it is not necessary to dispose of the residue. Therefore, the garbage is not thrown away and the earth is not polluted. Because it cannot be recycled and emits a large amount of carbon dioxide, it cannot be said that it is environmentally friendly. In addition, an expensive biochip is required, and the running cost is high.

【0007】上記の第六の生ごみ等の処理装置は、高価
の有効バクテリアが必要であり、ランニングコストが高
く付いているとともに、残滓である圧縮肥料は綺麗では
なく、袋詰め包装を清潔に行えない。
[0007] The above-mentioned sixth garbage disposal apparatus requires expensive and effective bacteria, running costs are high, and the compressed fertilizer as the residue is not clean, and the bagged packaging is clean. I can't.

【0008】上記の第七、第八、第九、第十の生ごみ等
の処理装置は、残滓である肥料が綺麗ではなく、袋詰め
包装を清潔に行えない。
In the seventh, eighth, ninth, and tenth garbage processing apparatuses, the fertilizer that is the residue is not clean, and the bag packaging cannot be performed cleanly.

【0009】上記の第十一の生ごみ等の処理方法は、分
解にかなりの日数がかかり、残滓を焼却処分する必要が
あり、資源となるべき生ごみをリサイクルできないこと
から地球環境に優しいとは言えない。
The eleventh method for treating garbage and the like requires a considerable number of days for decomposition, necessitates incineration of the residue, and is not environmentally friendly because garbage, which should be a resource, cannot be recycled. I can't say.

【0010】本願発明は、生ごみ等について、化学薬品
等の消毒薬を使用することなく溶解・殺菌・水分蒸発・
約五分の一の減容化を生じさせることができ、生ごみを
溶解・消臭・殺菌・水分蒸発・減容化を生じさせること
ができ、しかも残滓を片栗粉のような安全清潔で取り扱
いが容易な純白微粉末とすることができて袋詰め包装が
清潔に行えて、しかも地力が低下している水田や畑地の
肥料として頗る有効に再利用でき、生ごみ等の処理方法
及び肥料を提供することを目的としている。
[0010] The present invention provides a method for dissolving, sterilizing, evaporating water, and removing garbage without using a disinfectant such as a chemical.
It can reduce the volume by about 1/5, dissolve garbage, deodorize, sterilize, evaporate water, reduce the volume, and handle the residue safely and clean like potato starch. It can be used as a pure white fine powder that can be easily bagged and packed cleanly, and it can be very effectively reused as fertilizer for paddy fields and upland fields with reduced soil strength. It is intended to provide.

【0011】[0011]

【課題を解決するための手段】上記課題は、下記の手段
によって解決される。 (1)生ごみ処理槽内に生ごみ等を細粒化して収容し所
要量の塩素を含まない強酸を加え所要温度に加熱して攪
拌し生ごみ等を強酸により有機物分解して流動性分解物
を生成・促進するとともに加熱により水蒸気蒸発を促進
し水蒸気を生ごみ処理槽外に排出して減容化を促進しか
つ消臭を行い、次いで、塩素を含まない強アルカリを混
合し中性ないし弱アルカリ性に戻し、次いで、生石灰の
粉末を混合し攪拌して高温熱化学反応を生じさせて高熱
水蒸気を完全に分離除去し、熱分解・完全殺菌・無水化
・減容化を生じさせた純白色の微粉末を生ごみ処理槽内
に生成し生ごみ処理槽外に回収することを特徴とする生
ごみ等の処理方法。 (2)生ごみ処理槽内に生ごみ等を細粒化して収容し所
要量の塩素を含まない強酸を加え所要温度に加熱して攪
拌し生ごみ等を強酸により有機物分解して流動性分解物
を生成・促進するとともに加熱により水蒸気蒸発を促進
し水蒸気を生ごみ処理槽外に排出して減容化を促進しか
つ消臭を行い、次いで、塩素を含まない強アルカリを混
合し中性ないし弱アルカリ性に戻し生ごみ処理槽内の流
動性分解物を細菌に好適な温度にして菌担持体を投入し
て細菌を繁殖させて微生物的有機物分解を促進させ、か
つこの間も加熱により水蒸気蒸発を促進し水蒸気を生ご
み処理槽外に排出して減容化を促進し、次いで、生石灰
の粉末を混合し攪拌して高温熱化学反応を生じさせて高
熱水蒸気を完全に分離除去し、熱分解・完全殺菌・無水
化・減容化を生じさせた純白色の微粉末を生ごみ処理槽
内に生成し生ごみ処理槽外に回収することを特徴とする
生ごみ等の処理方法。 (3)生ごみ処理槽内に生ごみ等を細粒化して収容し菌
担持体を投入し細菌に好適な温度に加熱して撹拌し細菌
を繁殖させて微生物的有機物分解を促進させ、次いで、
所要量の塩素を含まない強酸を加えて該強酸により有機
物分解して流動性分解物を生成・促進するとともに加熱
により水蒸気蒸発を促進し水蒸気を生ごみ処理槽外に排
出して減容化を促進しかつ消臭を行い、次いで、塩素を
含まない強アルカリを加えて撹拌混合し中性ないし弱ア
ルカリ性に戻し、次いで、生石灰の粉末を混合し攪拌し
て高温熱化学反応を生じさせて高熱水蒸気を完全に分離
除去し、熱分解・完全殺菌・無水化・減容化を生じさせ
た純白色の微粉末を生ごみ処理槽内に生成し生ごみ処理
槽外に回収することを特徴とする生ごみ等の処理方法。 (4)生ごみ処理槽内に生ごみ等を細粒化して収容し菌
担持体を投入し細菌に好適な温度に加熱して撹拌し細菌
を繁殖させて微生物的有機物分解を促進させ、次いで、
所要量の塩素を含まない強酸を加えて該強酸により有機
物分解して流動性分解物を生成・促進するとともに加熱
により水蒸気蒸発を促進し水蒸気を生ごみ処理槽外に排
出して減容化を促進しかつ消臭を行い、次いで、塩素を
含まない強アルカリを混合し中性ないし弱アルカリ性に
戻し生ごみ処理槽内の流動性分解物を細菌に好適な温度
にして菌担持体を投入して細菌を繁殖させて微生物的有
機物分解を促進させ、かつこの間も加熱により水蒸気蒸
発を促進し水蒸気を生ごみ処理槽外に排出して減容化を
促進し、次いで、生石灰の粉末を混合し攪拌して高温熱
化学反応を生じさせて高熱水蒸気を完全に分離除去し、
熱分解・完全殺菌・無水化・減容化を生じさせた純白色
の微粉末を生ごみ処理槽内に生成し生ごみ処理槽外に回
収することを特徴とする生ごみ等の処理方法。 (5)前記のいずれかの生ごみ等の処理方法によって製
造される白色微粉末よりなることを特徴とする肥料。
The above object is achieved by the following means. (1) Garbage and the like are finely divided and stored in a garbage processing tank, a required amount of strong acid containing no chlorine is added, heated to a required temperature and agitated, and the garbage and the like are decomposed with a strong acid to decompose organic matter and flowable. Generates and promotes products, promotes steam evaporation by heating, discharges steam out of the garbage disposal tank to promote volume reduction and deodorizes, and then mixes with a strong alkali containing no chlorine to neutralize Or weakly alkaline, and then mixed and stirred quicklime powder to cause a high-temperature thermochemical reaction to completely separate and remove high-temperature steam, causing thermal decomposition, complete sterilization, dehydration, and volume reduction. A method for treating garbage or the like, wherein pure white fine powder is generated in a garbage processing tank and collected outside the garbage processing tank. (2) Garbage and the like are finely divided and stored in a garbage processing tank, a required amount of a strong acid containing no chlorine is added, heated to a required temperature and stirred, and the garbage and the like are decomposed with a strong acid to decompose organic substances with a fluidity. Generates and promotes products, promotes steam evaporation by heating, discharges steam out of the garbage disposal tank to promote volume reduction and deodorizes, and then mixes with a strong alkali containing no chlorine to neutralize It is returned to a weak alkalinity and the temperature of the fluid decomposition product in the garbage disposal tank is adjusted to a temperature suitable for bacteria, and a bacterial carrier is introduced to propagate the bacteria and promote the decomposition of microbial organic substances. The steam is discharged out of the garbage disposal tank to promote volume reduction, and then the lime powder is mixed and agitated to cause a high-temperature thermochemical reaction to completely separate and remove the high-temperature steam. Decomposition, complete sterilization, dehydration and volume reduction A method for treating garbage or the like, characterized in that pure white fine powder produced is generated in a garbage processing tank and collected outside the garbage processing tank. (3) Garbage and the like are stored in the garbage disposal tank in the form of fine granules, and a bacterial carrier is put into the garbage, heated to a temperature suitable for the bacteria, stirred, and the bacteria are propagated to promote microbial organic matter decomposition. ,
Add a required amount of strong acid which does not contain chlorine and decompose organic matter by the strong acid to generate and promote flowable decomposed product, and also to promote steam evaporation by heating and discharge steam out of garbage disposal tank to reduce volume. Accelerate and deodorize, then add strong alkali not containing chlorine and stir and mix to return to neutral or weak alkalinity, then mix quicklime powder and stir to generate high-temperature thermochemical reaction, It completely separates and removes water vapor, generates pure white fine powder that has undergone thermal decomposition, complete sterilization, dehydration, and volume reduction in the garbage disposal tank, and collects it outside the garbage disposal tank. How to process garbage. (4) Garbage and the like are finely divided and stored in a garbage processing tank, and a bacterial carrier is put into the garbage and heated to a temperature suitable for bacteria and stirred to propagate the bacteria and promote the decomposition of microbial organic matter. ,
Add a required amount of strong acid which does not contain chlorine and decompose organic matter by the strong acid to generate and promote flowable decomposed product, and also to promote steam evaporation by heating and discharge steam out of garbage disposal tank to reduce volume. Accelerate and deodorize, then mix strong alkali not containing chlorine, return to neutral or weak alkalinity, put the fluid decomposed product in the garbage disposal tank at a temperature suitable for bacteria, and put the bacterial carrier To promote the decomposition of microbial organic matter, and during this time, to promote the evaporation of water vapor by heating, discharge the water vapor out of the garbage disposal tank to promote volume reduction, and then mix the powder of quick lime. Stirring causes a high-temperature thermochemical reaction to completely separate and remove high-temperature steam,
A method for treating garbage, wherein pure white fine powder that has undergone thermal decomposition, complete sterilization, dehydration, and volume reduction is generated in a garbage processing tank and collected outside the garbage processing tank. (5) A fertilizer comprising a white fine powder produced by any of the above-mentioned methods for treating garbage and the like.

【0012】[0012]

【発明の実施の態様】本願第一ないし第四の発明の生ご
み等の処理方法を実施するための生ごみ等の処理装置の
好ましい一例を図面を参照して説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS A preferred example of an apparatus for treating garbage and the like for carrying out the method for treating garbage and the like according to the first to fourth aspects of the present invention will be described with reference to the drawings.

【0013】図1、図2に示すように、生ごみ処理槽1
は、処理槽本体1aに蓋板1bを載置しボルト締めしてな
る密閉構造である。処理槽本体1aは、円筒形容器であ
り、特に耐食性に優れた高級ステンレス鋼(SUS316
等)、チタン鋼等の耐酸性・耐熱性の材質からなる。蓋
板1bは、処理槽本体1aと同材質である。
As shown in FIGS. 1 and 2, a garbage disposal tank 1
Has a closed structure in which a lid plate 1b is placed on the processing tank main body 1a and tightened with bolts. The treatment tank main body 1a is a cylindrical container, and is particularly made of high-grade stainless steel (SUS316) having excellent corrosion resistance.
Etc.), made of an acid and heat resistant material such as titanium steel. The lid plate 1b is made of the same material as the processing tank body 1a.

【0014】図1に示すように、処理槽本体1aの底面
中央と蓋板1bの底面中央に両端支持された撹拌軸2に
平面的配置が該撹拌軸2の周囲に互いに120度相違する
放射方向に片持式の上段翼3aと中段翼3bと下段翼3c
からなる撹拌翼を備えている。下段翼3cは、処理槽本
体1aの底面近傍を旋回する。撹拌軸2と上段翼3aと中
段翼3bと下段翼3cも、特に耐食性に優れた高級ステン
レス鋼(SUS316等)、チタン鋼等の耐酸性・耐熱性の材
質からなる。
As shown in FIG. 1, the stirring shaft 2 supported at both ends at the center of the bottom surface of the processing tank main body 1a and the bottom surface of the lid plate 1b has a two-dimensional arrangement around the stirring shaft 2 with a radiation difference of 120 degrees. Upper wing 3a, middle wing 3b and lower wing 3c
With a stirring blade consisting of The lower blade 3c turns near the bottom surface of the processing tank body 1a. The stirring shaft 2, the upper blade 3a, the middle blade 3b, and the lower blade 3c are also made of an acid-resistant and heat-resistant material such as high-grade stainless steel (such as SUS316) and titanium steel having particularly excellent corrosion resistance.

【0015】図1に示すように、撹拌軸2は蓋板1b上
に設置されたモータ5により回転駆動される。撹拌軸2
の上端に固定されたスプロケット歯車4aと蓋板1b上に
設置されたモータ5の出力軸に固定したスプロケット歯
車4bとにエンドレスチェーン4cが巻き掛けされてい
る。モータ5は、生ごみ等の処理の開始から処理の完了
まで駆動される。撹拌軸2は5〜10r.p.m.の低速で回転
される。
As shown in FIG. 1, the stirring shaft 2 is driven to rotate by a motor 5 installed on the cover plate 1b. Stirring shaft 2
An endless chain 4c is wound around a sprocket gear 4a fixed to the upper end of the motor and a sprocket gear 4b fixed to the output shaft of the motor 5 installed on the cover plate 1b. The motor 5 is driven from the start of processing such as garbage to the completion of the processing. The stirring shaft 2 is rotated at a low speed of 5 to 10 rpm.

【0016】図1、図2に示すように、処理槽本体1a
の外側に温風入口6a’と温風出口6a”を有する熱風式
加熱室6bを画成する加熱室形成壁6aが溶接されてい
る。図示しない熱風発生装置(ブロアとヒータの組み合
わせ)により発生する例えば200℃の熱風が温風入口6
a’より熱風式加熱室6b内に流通し、処理槽本体1aを
熱交換電熱面として処理槽本体1a内に収容され攪拌さ
れる生ごみ等を30℃〜60℃に暖め、温風出口6a”より
排気するようになっている。熱風式加熱室6bへの熱風
の供給は、生ごみ等の処理の開始から生石灰の投入後、
2〜3分で終了する。
As shown in FIGS. 1 and 2, the processing tank main body 1a
A heating chamber forming wall 6a defining a hot-air heating chamber 6b having a hot-air inlet 6a 'and a hot-air outlet 6a "is welded to the outside. The hot-air generating device (combination of blower and heater) (not shown) generates the heat. Hot air at 200 ° C
a ′, the garbage, etc., which are circulated in the hot-air heating chamber 6b and are stirred and stored in the processing tank body 1a with the processing tank body 1a as a heat exchange heating surface, are heated to 30 ° C. to 60 ° C. The hot air is supplied to the hot-air heating chamber 6b from the start of the processing of garbage and the like, after the injection of quick lime,
It takes a few minutes.

【0017】図1、図2に示すように、蓋板1bには、
生ごみ投入口1cが開口され該生ごみ投入口1cの上にエ
アシリンダ装置7aにより開閉されるシャッタ7bが取り
付けられ該シャッタ7bの上に生ごみ破砕機7cが取り付
けられさらに生ごみ投入用ホッパ7dが設けられてい
る。生ごみ投入用ホッパ7dには雨の進入防止のための
蓋7eが設けられる。蓋7eは、一端より持ち上げて揺動
して開けるようになっている。該蓋7eを開けるとシャ
ッタ7bが開くようになっている。又、蓋板1bには、熱
風排気口1dが開口され該熱風排気口1dに臭気処理筒8
bが設けられ該臭気処理筒8b内には下から順に排気ファ
ン8cとヒーター8dと例えばプラチナ触媒である消臭エ
レメント8eが取り付けられている。プラチナ触媒であ
る消臭エレメント8eは、例えば悪臭を放つ強烈な酢酸
の場合、炭酸ガスと水蒸気に分解して消臭する反応を効
果的に促進する。消臭原理は酸化触媒脱臭方式である。
反応式は、CHCOOH+2O→2CO+2H
Oとなる。排気ファン8cが生ごみ処理槽1内より吸気
した気体をヒーター8dが加熱して消臭エレメント8eに
接触させて流通させることにより極めて強い臭気を完全
無臭にする。ヒーター8dの発熱量は排気ファン8cが生
ごみ処理槽1内より吸気した気体を350℃以上に加熱し
うるように決定する。シャッタ7bとシャッタ8aは、特
に耐食性に優れた高級ステンレス鋼(SUS316等)、チタ
ン鋼等の耐酸性・耐熱性の材質からなる。臭気処理筒8
bには点検蓋8b′が設けられ排気ファン8cと消臭エレ
メント8dの点検・修理・交換ができる。臭気処理筒8b
の上面に排気管8fが設けられている。
As shown in FIGS. 1 and 2, the lid plate 1b has
A garbage inlet 1c is opened, a shutter 7b which is opened and closed by an air cylinder device 7a is mounted on the garbage inlet 1c, and a garbage crusher 7c is mounted on the shutter 7b. 7d is provided. The garbage input hopper 7d is provided with a lid 7e for preventing rain from entering. The lid 7e is lifted from one end and swings open. When the lid 7e is opened, the shutter 7b is opened. A hot air exhaust port 1d is opened in the lid plate 1b, and the hot air exhaust port 1d is
An exhaust fan 8c, a heater 8d, and a deodorizing element 8e, which is, for example, a platinum catalyst, are mounted in the odor processing cylinder 8b in this order from the bottom. The deodorizing element 8e, which is a platinum catalyst, for example, in the case of intense acetic acid that gives off a foul odor, effectively promotes a reaction of decomposing into odorous carbon dioxide and water vapor. The deodorizing principle is an oxidation catalyst deodorizing method.
The reaction formula is CH 3 COOH + 2O 2 → 2CO 2 + 2H 2
It becomes O. The heater 8d heats the gas sucked in from the garbage processing tank 1 by the exhaust fan 8c and makes the gas come into contact with the deodorizing element 8e to circulate the extremely strong odor to make it completely odorless. The calorific value of the heater 8d is determined so that the exhaust fan 8c can heat the gas sucked from the garbage processing tank 1 to 350 ° C. or more. The shutter 7b and the shutter 8a are made of an acid-resistant and heat-resistant material such as high-grade stainless steel (SUS316 or the like), titanium steel or the like, which is particularly excellent in corrosion resistance. Odor treatment tube 8
An inspection lid 8b 'is provided at b, so that the exhaust fan 8c and the deodorizing element 8d can be inspected, repaired, and replaced. Odor treatment tube 8b
An exhaust pipe 8f is provided on the upper surface of the air conditioner.

【0018】図1、図3に示すように、さらに、蓋板1
bに設けられた溶解促進剤投入口1eにエアシリンダ装置
9aにより開閉されるシャッタ9bが設けられ該シャッタ
9bの上に溶解促進剤投入ホッパ9cが設けられ、該溶解
促進剤投入ホッパ9cに閉じた状態にロックできる蓋9d
が設けられ、蓋9dを開くときはエアシリンダ装置9aが
作動してシャッタ9bが開くようになっているとともに
蓋9dを閉じたときはエアシリンダ装置9aが作動してシ
ャッタ9bが閉じるようになっている。シャッタ9bと溶
解促進剤投入ホッパ9cと蓋9dは、特に耐食性に優れた
高級ステンレス鋼(SUS316等)、チタン鋼等の耐酸性・
耐熱性の材質からなる。溶解促進剤投入ホッパ9cから
は、菌担持体、強酸(酢酸、氷酢酸、硝酸、又は硫酸、
好ましくは酢酸)、アルカリ(水酸化ナトリウム或いは
水酸化カリウム)が投入される。菌担持体は極少量が投
入される。強酸はごみ処理量に応じた量が投入される。
アルカリは、中和ないし弱アルカリ性に戻すための量が
投入される。PH値を確認するために、処理層本体1aの
側面下部にサンプル採取用のコック18よりを設ける。
菌担持体は、クロストリジウム、ペプトコッカス、ペプ
トスプレプトコッカス、バクテロイデス、フゾバクテリ
ウム等の嫌気性細菌を繁殖したもの、或いは、キサント
モナス、アシネトバクター、フラボバクテリム、ニトロ
ソモナス、ニトロバクター等の嫌気状態でぶどう糖を分
解するグラム陰性桿菌を繁殖したものが好ましい。この
他に、ストレプトマイセス、ラクトバチルス、バチラス
サブチルス、シュウドモナス、クロストリジウム、サッ
カロマイセス、クラブシゲラ、ペニシリウムといった細
菌を繁殖したものでも良い。
As shown in FIG. 1 and FIG.
A shutter 9b, which is opened and closed by an air cylinder device 9a, is provided at a dissolution promoter input port 1e provided at b. A dissolution promoter input hopper 9c is provided above the shutter 9b, and the dissolution promoter input hopper 9c is closed. Lid 9d that can be locked in the open position
When the lid 9d is opened, the air cylinder device 9a operates to open the shutter 9b, and when the lid 9d is closed, the air cylinder device 9a operates to close the shutter 9b. ing. The shutter 9b, the dissolution promoter charging hopper 9c and the lid 9d are made of high-grade stainless steel (SUS316, etc.) and titanium
Made of heat resistant material. From the dissolution promoter input hopper 9c, a bacterial carrier, a strong acid (acetic acid, glacial acetic acid, nitric acid, or sulfuric acid,
Preferably, acetic acid) and alkali (sodium hydroxide or potassium hydroxide) are added. A very small amount of the bacterial carrier is charged. The amount of the strong acid is charged according to the amount of the waste.
As the alkali, an amount for neutralization or returning to weak alkalinity is added. In order to check the PH value, a cock 18 for sampling is provided at the lower side of the processing layer main body 1a.
Bacterial carriers are those that have grown anaerobic bacteria such as Clostridium, Peptococcus, Peptopreptococcus, Bacteroides, Fusobacterium, or anaerobic glucose such as Xanthomonas, Acinetobacter, Flavobacterium, Nitrosomonas, Nitrobacter, etc. A breeding gram-negative rod that degrades is preferred. In addition, bacteria that have bred bacteria such as Streptomyces, Lactobacillus, Bacillus subtilis, Pseudomonas, Clostridium, Saccharomyces, Crabshigera, and Penicillium may be used.

【0019】図2に示すように、さらに、蓋板1bに設
けられた生石灰投入口1fに二段シャッタ式計量器10
が設けられ該二段シャッタ式計量器10の上に生石灰投
入ホッパ11aが設けられ、生石灰貯留ホッパ10bに投
入される生石灰が下部水平スクリューコンベア10cと
傾斜スクリューコンベア10dと水平スクリューコンベ
ア10eにより搬送されて該生石灰投入ホッパ11aに投
入されるようになっている。生石灰が湿気を吸わないよ
うに、生石灰貯留ホッパ10bには、閉じた状態にロッ
クできかつ密封用のパッキンが付いた蓋10fが設けら
れており、又、下部水平スクリューコンベア10cと傾
斜スクリューコンベア10dと水平スクリューコンベア
10eも密閉構造となっている。生石灰投入ホッパ11a
と生石灰貯留ホッパ10bは、ホッパ円錐壁面の一部が
ガラスでできていて生石灰の貯留レベルが視認できるよ
うになっていて、生石灰投入ホッパ11aの生石灰の貯
留量が少なくなったときは、図示しない生石灰供給スイ
ッチをオンすると、下部水平スクリューコンベア10c
と傾斜スクリューコンベア10dと水平スクリューコン
ベア10eが一定時間駆動されて生石灰貯留ホッパ10b
内の生石灰が生石灰投入ホッパ11aに給送される。も
って、常に生石灰投入ホッパ11aに生石灰が貯留され
ていると、二段シャッタ式計量器10に生石灰の供給が
行なわれる。なお、生石灰投入ホッパ11aと生石灰貯
留ホッパ10bには、生石灰の付着を落とす振動発生手
段が付設される。二段シャッタ式計量器10は、上下二
段にシャッタ10a,10bを備えていて、起動スイッチ
をオンすると、各シャッタはエアシリンダ装置10c,1
0dにより開閉駆動されるようになっていて、下段のシ
ャッタ10aを閉じて上段のシャッタ10bを開き生石灰
を下段のシャッタ10aまで流下させてシャッタ間空間
に充満させ上段のシャッタ10bを閉じて下段のシャッ
タ10aを開くと、シャッタ間空間に充満した生石灰が
生ごみ処理槽1内に落下するようになっている。二段シ
ャッタ式計量器10は、上下二段にシャッタ10a,10
bの開閉回数とシャッタ間空間の容積を掛け算した値で
通過量を計量できる。生石灰は、350℃以上の高温熱化
学反応が生じるように投入量が決定される。前述した消
臭のための排気ファン8cの作動及びヒーター8dへの通
電は、ごみ処理の開始時から行なわれ、生石灰投入のた
めに前記の二段シャッタ式計量器10の起動スイッチを
オンすると、閉じられるようになっている。
As shown in FIG. 2, furthermore, a two-stage shutter type measuring instrument 10 is inserted into a quicklime input port 1f provided in the cover plate 1b.
The quick lime charging hopper 11a is provided on the two-stage shutter type weighing device 10, and the quick lime charged into the quick lime storage hopper 10b is transported by the lower horizontal screw conveyor 10c, the inclined screw conveyor 10d, and the horizontal screw conveyor 10e. The lime is supplied to the quick lime charging hopper 11a. To prevent quicklime from absorbing moisture, the quicklime storage hopper 10b is provided with a lid 10f that can be locked in a closed state and has a packing for sealing, a lower horizontal screw conveyor 10c and an inclined screw conveyor 10d. The horizontal screw conveyor 10e also has a closed structure. Quicklime hopper 11a
The quicklime storage hopper 10b is not shown when a portion of the hopper conical wall is made of glass so that the storage level of quicklime can be visually recognized. When the quicklime supply switch is turned on, the lower horizontal screw conveyor 10c
The inclined screw conveyor 10d and the horizontal screw conveyor 10e are driven for a certain period of time, and the quick lime storage hopper 10b is driven.
The quicklime inside is supplied to the quicklime input hopper 11a. Thus, if quicklime is always stored in the quicklime input hopper 11a, quicklime is supplied to the two-stage shutter type measuring device 10. The quick lime input hopper 11a and the quick lime storage hopper 10b are provided with vibration generating means for reducing the adhesion of quick lime. The two-stage shutter type weighing device 10 includes shutters 10a and 10b in two stages, the upper and lower stages.
0d, the lower shutter 10a is closed, the upper shutter 10b is opened, quick lime flows down to the lower shutter 10a, the space between the shutters is filled, the upper shutter 10b is closed, and the lower shutter 10b is closed. When the shutter 10a is opened, quicklime filled in the inter-shutter space falls into the garbage processing tank 1. The two-stage shutter type weighing device 10 has shutters 10a and 10
The passing amount can be measured by a value obtained by multiplying the number of times of opening and closing b and the volume of the space between shutters. The amount of quicklime is determined so that a high-temperature thermochemical reaction of 350 ° C. or more occurs. The operation of the exhaust fan 8c for deodorization and the energization of the heater 8d are performed from the start of the refuse treatment, and when the start switch of the two-stage shutter weighing device 10 is turned on for quick lime injection, It is designed to be closed.

【0020】図1、図3に示すように、さらに又、蓋板
1bには、吸排気管12が立ち上がっている。該吸排気
管12の立ち上がり部分の上端はT字型に別れていて、
該T字型部より上方へ分岐する部分には電磁仕切り弁1
3が取付けられその先にエルボ管19が取付けられてお
り、又、前記T字型部より水平方向へ分岐する管部分は
エルボ形排気ガス回収管20が設けられ垂直に下がって
液溜め回収タンク14に連通していて、それよりも手前
部分に立下り管部分を被嵌固定される空冷フィン15が
設けられる。電磁仕切り弁13は、ごみ処理の開始時よ
り開いていて外気を生ごみ処理槽1内に取り込む通路を
確保し、生石灰投入のために前記の二段シャッタ式計量
器10の起動スイッチをオンすると、生石灰投入により
高温熱化学反応を生起し該高温熱化学反応で生起する高
熱水蒸気と発酵ガスを吸排気管12の立ち上がり部分の
T字型部分より水平管部分に導いて液溜め回収タンク1
4に導くようになっている。吸排気管12を通る高熱水
蒸気と反応・発酵ガスは、該吸排気管12の中途に被嵌
された空冷フィン15により冷却され液化して液溜め回
収タンク14に回収されるようになっている。液溜め回
収タンク14に回収される液は、殆どが水であるがメタ
ン・ブタン、炭酸ガス、アルコール、油分を多く含んで
いるので、石油製品と混ぜて可燃液体として処理でき、
熱エネルギーの回収につながる。排気ファン8cを駆動
すると生ごみ処理槽1内を陰圧になる。排気ファン8c
が駆動して吸排気管12から外気を取り込むことは、排
気ファン8cが生ごみ処理槽1内の悪臭を伴った水蒸気
を生ごみ処理槽1の外へ排気する気体の流通を保障し、
かつ消臭反応に必要な酸素の供給となり、さらに、蓋9
dを開いて溶解促進剤投入ホッパ9cより強酸や強アルカ
リを投入するときに、ここから悪臭が出ないようにでき
る。又、図示しない冷却スイッチをオンすると、排気フ
ァン8cが逆回転するとともに電磁仕切り弁13が開く
ようになっている。
As shown in FIGS. 1 and 3, an intake / exhaust pipe 12 stands up on the cover plate 1b. The upper end of the rising portion of the intake / exhaust pipe 12 is divided into a T-shape,
An electromagnetic gate valve 1 is provided at a portion branched above the T-shaped portion.
An elbow pipe 19 is mounted at the end of the pipe 3 and an elbow-shaped exhaust gas recovery pipe 20 is provided at a pipe part branched from the T-shaped section in the horizontal direction. An air-cooling fin 15 is provided at the front side of the air-cooling fin 15 and communicates with the air-cooling fin 15. The electromagnetic gate valve 13 is open from the start of the refuse treatment, secures a passage for taking in outside air into the garbage treatment tank 1, and turns on the start switch of the two-stage shutter weighing device 10 for charging quicklime. A high-temperature thermochemical reaction is caused by the injection of quick lime, and high-temperature steam and fermentation gas generated by the high-temperature thermochemical reaction are led to a horizontal pipe portion from a T-shaped portion at the rising portion of the intake / exhaust pipe 12 to collect a liquid in the liquid collecting tank 1.
4 The high-temperature steam and the reaction / fermentation gas passing through the intake / exhaust pipe 12 are cooled and liquefied by the air-cooled fins 15 fitted in the middle of the intake / exhaust pipe 12, and are collected in the liquid collecting tank 14. The liquid collected in the liquid collecting tank 14 is mostly water, but contains a large amount of methane / butane, carbon dioxide, alcohol, and oil, so that it can be mixed with petroleum products and treated as a flammable liquid.
This leads to recovery of heat energy. When the exhaust fan 8c is driven, the inside of the garbage disposal tank 1 becomes negative pressure. Exhaust fan 8c
Is driven to take in the outside air from the intake / exhaust pipe 12, and the exhaust fan 8 c ensures the flow of gas that exhausts the water vapor with the bad smell in the garbage disposal tank 1 to the outside of the garbage disposal tank 1,
In addition, the supply of oxygen necessary for the deodorization reaction is achieved,
When d is opened and a strong acid or strong alkali is charged from the dissolution promoter charging hopper 9c, a bad odor can be prevented from being emitted from this. When a cooling switch (not shown) is turned on, the exhaust fan 8c rotates in the reverse direction and the electromagnetic gate valve 13 opens.

【0021】図1、図3に示すように、生ごみ処理槽1
内には、熱電対16が蓋板1bより垂下される。該熱電
対16は、上段翼3aよりも高い位置になるように処理
槽本体1aの内周面近傍に設けられる。該熱電対16
は、生石灰投入により高温熱化学反応時の温度変化を検
出するために設けられる。生石灰の投入回数はごみ処理
量によって異なる。一回又は二回の生石灰の投入で1分
経過時に350℃以上の高温熱化学反応が生じないとき
は、三度目の生石灰投入を行なう。三度目の生石灰投入
でも350℃の高温にならないときは三度目の生石灰投入
を行なう。このために、該熱電対16の信号はモニタに
時間と温度の関係がグラフ表示され、これを見て生石灰
投入を適切に行えるようになっている。生ごみ処理槽1
で処理を完了すると、水分除去が完全に行なわれ、熱分
解・完全殺菌・減容化を生じた純白色の微粉末が生ごみ
処理槽1内に残る。
As shown in FIGS. 1 and 3, a garbage disposal tank 1
Inside, a thermocouple 16 is suspended from the lid plate 1b. The thermocouple 16 is provided near the inner peripheral surface of the processing tank body 1a so as to be higher than the upper blade 3a. The thermocouple 16
Is provided to detect a temperature change at the time of a high-temperature thermochemical reaction by the input of quick lime. The number of times of quick lime charging differs depending on the amount of waste. If the high-temperature thermochemical reaction of 350 ° C. or more does not occur after one minute of one or two quick lime injections, a third quick lime injection is performed. If the temperature does not rise to 350 ° C even after the third quick lime charging, perform the third quick lime charging. For this purpose, the relationship between time and temperature is graphically displayed on the monitor of the signal of the thermocouple 16, and the quick lime can be properly introduced by looking at the graph. Garbage disposal tank 1
When the processing is completed, the moisture is completely removed, and the pure white fine powder that has undergone thermal decomposition, complete sterilization, and volume reduction remains in the garbage processing tank 1.

【0022】図1、図3に示すように、生ごみ処理槽1
から純白色の微粉末を排出・回収するために、処理槽本
体1aの下面に排出管1fが設けられる仕切り弁17aが
取付けられさらにエルボ管17bが設けられている。
又、処理槽本体1aの側面部に点検扉兼用覗き窓21が
設けられている。点検扉兼用覗き窓21には耐熱ガラス
が取付けられている。点検扉兼用覗き窓21があること
により、粉体化しないプラスチック塊等を確認して除去
することができ、又、生ごみ処理槽1に水蒸気が無くな
って純白色の微粉末がサラサラと攪拌されていることを
外部から肉眼で確認できる。
As shown in FIGS. 1 and 3, the garbage processing tank 1
A gate valve 17a provided with a discharge pipe 1f is attached to the lower surface of the processing tank main body 1a, and an elbow pipe 17b is provided in order to discharge and recover the pure white fine powder from the tank.
In addition, an inspection window 21 is also provided on the side surface of the processing tank body 1a. A heat-resistant glass is attached to the inspection window 21. The presence of the inspection door and viewing window 21 enables the confirmation and removal of non-pulverized plastic lumps and the like. In addition, when the garbage disposal tank 1 is free of water vapor, the pure white fine powder is stirred smoothly. Can be visually confirmed from the outside.

【0023】続いて、本願第一の発明ないし第四の発明
に共通する生ごみ等の処理方法を上記構成の生ごみ等の
処理装置を参照して説明する。装置の起動スイッチをオ
ンすると、モータ5が駆動し攪拌翼3a、3b、3cが回
転する。又、図示しない熱風発生装置により加熱室形成
壁6aに熱風が送給され生ごみ処理槽1の槽壁面が過熱
される。蓋7eを開くとシャッタ7bも開くので、生ごみ
投入用ホッパ7dに生ごみ等を投入する。蓋7eを閉じる
とシャッタ7bも閉じる。生ごみ投入用ホッパ7dに投入
された生ごみは、生ごみ破砕機7cにより細粒化されて
から生ごみ処理槽1内に落下する。そして、攪拌翼3
a、3b、3cにより攪拌されかつ30℃〜60℃に暖めら
れ、生ごみに含まれる腐敗菌により有機物分解が短時間
に進行する。微生物的有機物分解を促進するために、生
ごみの投入とともに菌担持体を投入することが好まし
い。蓋9dを開くとシャッタ9bも開くので、溶解促進剤
投入ホッパ9cより菌担持体を投入する。この段階で投
入する菌担持体は、好気性細菌が好ましい。又、キサン
トモナス、アシネトバクター、フラボバクテリム、ニト
ロソモナス、ニトロバクター等の嫌気状態でぶどう糖を
分解するグラム陰性桿菌を繁殖した菌担持体の投入が好
ましい。この間、排気ファン8cが駆動しており、吸排
気管12から外気を取り込まれ、排気ファン8cが生ご
み処理槽1内の悪臭を伴った水蒸気を吸い込み、ヒータ
ー8dが 排気ファン8cが吸気した気体を350℃以上に
加熱して消臭エレメント8eに接触させて極めて強い臭
気を完全無臭にして生ごみ処理槽1の外へ排気する。続
いて、1時間前後経過したら、蓋9dを開き、溶解促進
剤投入ホッパ9cより酢酸を投入する。酢酸の投入量
は、生ごみの投入量に比例した量とする。酢酸は強酸で
あるので、投入量が多いときはそれまでの有機物分解に
関与した細菌類が死滅する。以後は、分解途中の生ごみ
の有機分解物には酢酸が加わり引き続き30℃〜60℃の温
度条件で攪拌され酢酸が有機物分解に関与して流動性分
解物を生成・促進するとともに加熱により水蒸気蒸発を
促進し水蒸気を生ごみ処理槽1の外に排出して減容化を
促進する。この時点で生ごみ処理槽1の外に排出される
水蒸気の量は生ごみに含まれていた水分の約三分の一乃
至四分の一である。30℃〜60℃の温度条件で攪拌される
酢酸による有機物分解は動物の胃袋での分解作用と同様
に極めて強力であり、短時間に分解が進む。酢酸による
有機物分解は一時間から一時間半で十分である。この
間、排気ファン8cが駆動しており、エルボ管19、吸
排気管12から外気を取り込まれ、排気ファン8cが生
ごみ処理槽1内の悪臭を伴った水蒸気を吸い込み、ヒー
ター8dが排気ファン8cが吸気した気体を350℃以上に
加熱して消臭エレメント8eに接触させて極めて強い臭
気を完全無臭にして生ごみ処理槽1の外へ排気する。悪
臭を放つ強烈な酢酸は、炭酸ガスと水蒸気に分解されて
消臭する。続いて、1時間前後経過したら、蓋9dを開
き、溶解促進剤投入ホッパ9cより塩素を含まない強ア
ルカリを投入し流動状分解有機物を中性ないし弱アルカ
リ性に戻す。このとき、強アルカリの投入量は、強アル
カリを少量ずつ投入する毎に一定攪拌時間が経過したら
サンプル採取用のコック18を極僅かに開いて流動状分
解有機物のサンプルを取り出してそのPH値を測定し、中
性ないし弱アルカリ性に戻ったことを確認する。続い
て、蓋9dを開き、溶解促進剤投入ホッパ9cより菌担持
体を投入して、微生物による流動状分解有機物のさらな
る分解を行う。流動状分解有機物は、PH値が中性ないし
弱アルカリ性に戻されており、微生物が直ちに分解にア
タックしやすい分解物になっていて、30℃〜60℃の温度
条件で攪拌されるので、30分以内の極めて短時間で急
速な分解が進行する。この段階では、流動状分解有機物
に対する微生物的分解を行うものであるので、投入する
菌担持体は、嫌気性発酵(エタノール発酵、メタン発
酵、ブタン発酵等の可燃流体を生成する発酵)を行う高
温細菌を繁殖したものが好ましい。酢酸による有機物分
解を二時間も行う場合には、固定物が微粉クラスの大き
さになるように分解が十分に進んでおり、微生物による
流動状分解有機物のさらなる分解は必要的ではない。し
かし、処理の最後にガスを液化して回収する液体を可燃
液体としてエネルギー回収ができるように考慮すると、
嫌気性発酵(エタノール発酵、メタン発酵、ブタン発酵
等の可燃流体を生成する発酵)の処理を行うことが好ま
しい。続いて、二段シャッタ式計量器10の起動スイッ
チをオンして、所要量の生石灰を生ごみ処理槽1内に投
入する。このとき、他のシャッタは全て閉じている。
又、電磁仕切り弁13が閉じている。生石灰の投入量は
流動状分解有機物の容量の六割前後とするのが目安とな
る。適正な量の生石灰が投入されると、流動状分解有機
物との間で急激な高温熱化学反応を生起し、一分経過時
で100℃を超え、数分以内に300℃を越え、猛烈な水蒸気
蒸発が生じると共に、嫌気性発酵によって生じた可燃ガ
ス、エタノール、炭酸ガスが水蒸気の全量とともに吸排
気管12を通って空冷フィン15で冷やされ、液溜め回
収タンク14に液化回収される。液溜め回収タンク14
に回収される液は、殆どが水であるがメタン・ブタン、
炭酸ガス、アルコール、油分を多く含んでいるので、石
油製品と混ぜて可燃液体として処理でき、熱エネルギー
の回収につながる。生石灰を投入してから十分位経過す
ると、水蒸気等の排出が殆ど無くなる。生ごみ処理槽1
内には、熱分解・完全殺菌・無水化・減容化を生じさせ
た純白色の微粉末が生成されて残る。この時点で、図示
しない冷却スイッチをオンして、電磁仕切り弁13を開
き、排気ファン8cを逆回転して外気を生ごみ処理槽1
内に流入させると、攪拌翼3a、3b、3cが回転してい
るので、純白色の微粉末の効果的な冷却が行なわれる。
生ごみ処理槽1内の気体は、吸排気管12を通り電磁仕
切り弁13を通って大気中に排気される。生ごみ処理槽
1内には水分を含んでおらずサラサラした純白色の微粉
末が残る。点検扉兼用覗き窓21は水蒸気の付着がなく
なり内部が良く見えるようになる。モニタを見ながら生
ごみ処理槽1内の気体温度が常温近くに温度降下した
ら、仕切り弁17aを開く。すると、純白色の微粉末
は、水分を含んでおらずサラサラしており、攪拌翼3
a、3b、3cが回転しているので、仕切り弁17aを通っ
て全量が良好に排出される。生ごみ処理槽1の内周面及
び撹拌軸2と攪拌翼3a、3b、3cには、有機物が付着
して残ることはない。
Next, a method of treating garbage and the like common to the first to fourth inventions of the present application will be described with reference to the apparatus for treating garbage and the like having the above configuration. When the start switch of the apparatus is turned on, the motor 5 is driven to rotate the stirring blades 3a, 3b, 3c. In addition, hot air is supplied to the heating chamber forming wall 6a by a hot air generating device (not shown), and the tank wall surface of the garbage processing tank 1 is overheated. When the lid 7e is opened, the shutter 7b is also opened, so that garbage is put into the garbage hopper 7d. When the lid 7e is closed, the shutter 7b is also closed. The garbage thrown into the garbage throwing hopper 7d is pulverized by the garbage crusher 7c and then falls into the garbage processing tank 1. And the stirring blade 3
The mixture is stirred by a, 3b, and 3c and heated to 30 ° C to 60 ° C, and decomposition of organic matter proceeds in a short time by spoilage bacteria contained in garbage. In order to promote microbial organic matter decomposition, it is preferable to add a bacterial carrier together with the input of garbage. When the lid 9d is opened, the shutter 9b is also opened, so that the bacterial carrier is introduced from the dissolution promoter introduction hopper 9c. An aerobic bacterium is preferably used as the bacterium carrier introduced at this stage. In addition, it is preferable to load a bacterial carrier, such as Xanthomonas, Acinetobacter, Flavobacterium, Nitrosomonas, or Nitrobacter, which has propagated Gram-negative rods that degrade glucose under anaerobic conditions. During this time, the exhaust fan 8c is driven, the outside air is taken in from the intake / exhaust pipe 12, the exhaust fan 8c sucks in the odorous steam in the garbage disposal tank 1, and the heater 8d removes the gas sucked in by the exhaust fan 8c. The garbage is heated to 350 ° C. or more and brought into contact with the deodorizing element 8 e to exhaust the extremely strong odor completely out of the garbage disposal tank 1. Subsequently, after about one hour has passed, the lid 9d is opened, and acetic acid is introduced from the dissolution promoter introduction hopper 9c. The input amount of acetic acid shall be proportional to the input amount of garbage. Since acetic acid is a strong acid, when the input amount is large, bacteria involved in organic matter decomposition up to that time are killed. Thereafter, acetic acid is added to the organic decomposition product of the garbage in the course of decomposition, and the mixture is continuously stirred at a temperature of 30 ° C to 60 ° C. It promotes evaporation and discharges water vapor out of the garbage disposal tank 1 to promote volume reduction. At this time, the amount of water vapor discharged out of the garbage processing tank 1 is about one third to one fourth of the water contained in the garbage. Decomposition of organic substances by acetic acid stirred at a temperature of 30 ° C to 60 ° C is extremely strong as in the case of decomposing stomachs of animals, and decomposition proceeds in a short time. One to one and a half hours is sufficient for the decomposition of organic substances by acetic acid. During this time, the exhaust fan 8c is driven, the outside air is taken in from the elbow pipe 19 and the intake / exhaust pipe 12, the exhaust fan 8c sucks in the odorous steam in the garbage processing tank 1, and the heater 8d is operated by the exhaust fan 8c. The inhaled gas is heated to 350 ° C. or more and brought into contact with the deodorizing element 8 e to exhaust the extremely strong odor completely out of the garbage disposal tank 1. Intense acetic acid, which gives off a foul odor, is decomposed into carbon dioxide and water vapor and deodorized. Subsequently, after about one hour, the lid 9d is opened, and a strong alkali containing no chlorine is supplied from the dissolution promoter charging hopper 9c to return the fluidized organic substances to neutral or weakly alkaline. At this time, the feeding amount of the strong alkali is determined as follows: every time the strong alkali is added little by little, after a fixed stirring time has elapsed, the cock 18 for sampling is opened slightly, a sample of the fluidized organic matter is taken out, and its PH value is measured. Measure and confirm that it has returned to neutral or weakly alkaline. Subsequently, the lid 9d is opened, and the microorganism carrier is introduced from the dissolution promoter introduction hopper 9c to further decompose the fluid decomposition organic matter by the microorganism. The fluidized decomposed organic substance has a PH value returned to neutral or weakly alkaline, and is a decomposed substance in which microorganisms are easily attacked for decomposition, and is stirred at a temperature of 30 ° C to 60 ° C. Rapid decomposition progresses in a very short time within minutes. At this stage, microbial decomposition of fluidized organic matter is carried out. Therefore, the microorganism carrier to be introduced is subjected to anaerobic fermentation (fermentation that produces a flammable fluid such as ethanol fermentation, methane fermentation, or butane fermentation). Those that have propagated bacteria are preferred. When the organic matter is decomposed with acetic acid for as long as two hours, the decomposition has sufficiently proceeded so that the fixed substance has a size of the fine powder class, and further decomposition of the fluidly decomposed organic matter by microorganisms is not necessary. However, considering that the liquid to be liquefied and recovered at the end of the process can be used as a flammable liquid for energy recovery,
It is preferable to perform anaerobic fermentation (fermentation that produces a flammable fluid such as ethanol fermentation, methane fermentation, or butane fermentation). Subsequently, the start switch of the two-stage shutter type weighing device 10 is turned on, and a required amount of quicklime is put into the garbage processing tank 1. At this time, all other shutters are closed.
Further, the electromagnetic gate valve 13 is closed. As a guide, the amount of quicklime to be added is about 60% of the volume of the fluidized decomposition organic matter. When the appropriate amount of quicklime is injected, a rapid high-temperature thermochemical reaction occurs with the fluidized decomposed organic matter, exceeding 100 ° C after one minute, exceeding 300 ° C within several minutes, At the same time as the steam evaporation occurs, the combustible gas, ethanol, and carbon dioxide gas generated by the anaerobic fermentation are cooled by the air-cooling fins 15 through the intake / exhaust pipe 12 together with the entire amount of the steam, and are liquefied and collected in the sump collection tank 14. Liquid collection tank 14
Is mostly water, but methane and butane,
Since it contains a lot of carbon dioxide, alcohol and oil, it can be mixed with petroleum products and treated as a flammable liquid, leading to the recovery of thermal energy. When a sufficient amount of time has passed since the introduction of quick lime, the discharge of water vapor and the like almost disappears. Garbage disposal tank 1
Inside, a pure white fine powder that has undergone thermal decomposition, complete sterilization, dehydration, and volume reduction is generated and remains. At this time, a cooling switch (not shown) is turned on, the electromagnetic gate valve 13 is opened, and the exhaust fan 8c is rotated in the reverse direction to generate outside air into the garbage treatment tank 1.
When flowing into the inside, the stirring blades 3a, 3b, 3c are rotating, so that the pure white fine powder is effectively cooled.
The gas in the garbage processing tank 1 passes through the intake / exhaust pipe 12, passes through the electromagnetic gate valve 13, and is exhausted to the atmosphere. In the garbage treatment tank 1, pure white fine powder which does not contain moisture and is smooth remains. The inspection door and viewing window 21 is free of water vapor and the inside can be clearly seen. When the gas temperature in the garbage disposal tank 1 drops to near normal temperature while watching the monitor, the gate valve 17a is opened. Then, the pure white fine powder is smooth without containing water, and the stirring blade 3
Since a, 3b and 3c are rotating, the entire amount is discharged well through the gate valve 17a. Organic substances do not adhere and remain on the inner peripheral surface of the garbage processing tank 1, the stirring shaft 2, and the stirring blades 3a, 3b, 3c.

【0024】上記のように製造される純白色の微粉末
は、分器物分解と水蒸気蒸発により十分の一に減容され
た有機物の微粉末と、消石灰との混合物であり、混合割
合は1対0.4〜0.6位となり、完全殺菌されているので、
有機肥料として頗る有効である。
The pure white fine powder produced as described above is a mixture of organic fine powder whose volume has been reduced to one-tenth by decomposition of the sediment and steam evaporation, and slaked lime, and the mixing ratio is 1: 1. As it is 0.4-0.6 and completely sterilized,
Very effective as an organic fertilizer.

【0025】なお、生ごみ処理槽内に生ごみ等を細粒化
して収容し塩素を含まない強酸を加え所要温度に加熱し
て攪拌して有機物分解しかつ蒸発水蒸気を生ごみ処理槽
外に排出し、次いで、塩素を含まない強アルカリを混合
し中性ないし弱アルカリ性に戻すまでを行い、続いて、
流動状分解有機物をポンプにより別の処理槽に移送し
て、菌担持体を投入して微生物的有機物分解を促進さ
せ、次いで、生石灰の粉末を混合し攪拌して高温熱化学
反応を生じさせて高熱水蒸気を完全に分離除去し、熱分
解・完全殺菌・無水化・減容化を生じさせた純白色の微
粉末を生ごみ処理槽内に生成し生ごみ処理槽外に回収す
るようにする、二槽式に構成する場合も本願発明に含ま
れる。
It should be noted that garbage and the like are stored in the garbage disposal tank in the form of fine granules, a strong acid containing no chlorine is added, the mixture is heated to a required temperature and stirred to decompose organic substances, and evaporated steam is discharged outside the garbage disposal tank. Discharging, then mixing with strong alkali containing no chlorine and returning to neutral to weak alkali, then
The fluid decomposition organic matter is transferred to another treatment tank by a pump, and a microorganism carrier is charged to promote microbial organic matter decomposition, and then the powder of lime is mixed and stirred to cause a high-temperature thermochemical reaction. High-temperature steam is completely separated and removed, and pure white fine powder that has undergone thermal decomposition, complete sterilization, dehydration, and volume reduction is generated in the garbage processing tank and collected outside the garbage processing tank. The present invention also includes a case of a two-tank type.

【0026】[0026]

【発明の効果】以上説明してきたように、本願第一乃至
第四の発明の生ごみ等の処理方法によれば、生ごみ等を
短時間に純白微粉末とすることができ、悪臭を大気中に
撒き散らすことが無い。純白微粉末は、片栗粉のような
安全清潔で取り扱いが容易であり衛生的で袋詰めする等
により取り扱い容易である。生ごみ処理槽内に汚物が沢
山付着して残ることがなく、綺麗に全量を排出すること
ができ、衛生的で袋詰めする等により取り扱い容易であ
り、装置が汚らしくならない。塩素を含まない生ごみ処
理であるので、熱化学反応時にダイオキシンを含むガス
の発生を回避できる。処理剤である塩素を含まない強ア
ルカリと生石灰はは不揮発性であり、毒性がないので、
従来の技術の一つである消毒薬を使用して生ごみの殺菌
を行う処理工程を含む生ごみ等の処理方法に比べて安全
であり、分器物分解と水蒸気蒸発により十分の一に減容
された有機物の微粉末と、消石灰との混合物であり、生
ごみを有効できる。本願第五の発明の肥料は、生ごみの
分解物と消石灰の混合物であってサラサラとした完全殺
菌された中性領域の純白色の乾燥微粉末であり、土壌に
必要な窒素、燐酸、カリ等を多くを含んでいるので、土
壌に頗る有効であり、地球資源のリサイクル利用ができ
て地球環境に優しい。
As described above, according to the method for treating garbage and the like according to the first to fourth inventions of the present application, garbage and the like can be converted into pure white fine powder in a short time, and the odor is reduced to the atmosphere. There is no sprinkling inside. Pure white fine powder is safe, clean and easy to handle like potato starch, sanitary, and easy to handle by bagging. The waste does not adhere to the garbage disposal tank, so that the entire amount can be discharged cleanly, the sanitary treatment can be easily performed by bagging, etc., and the apparatus does not become dirty. Since the garbage treatment does not contain chlorine, generation of gas containing dioxin during the thermochemical reaction can be avoided. Since strong alkali and quicklime which do not contain chlorine which is a treating agent are non-volatile and have no toxicity,
It is safer than garbage and other treatment methods that include a sterilization process for garbage using a disinfectant, which is one of the conventional technologies. It is a mixture of the fine powder of organic matter and slaked lime, and can effectively use garbage. The fertilizer according to the fifth invention of the present application is a mixture of a decomposition product of kitchen garbage and slaked lime, and is a dry white powder of a neutral white region which is completely sterilized, and contains nitrogen, phosphoric acid and potassium required for soil. It is very effective for the soil because it contains a large amount of water, etc., and is recyclable for earth resources and is environmentally friendly.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本願第一ないし第四の発明の生ごみ等の処理方
法を実施するための生ごみ等の処理装置の好ましい一例
を示す全体正面図。
FIG. 1 is an overall front view showing a preferred example of an apparatus for treating garbage and the like for carrying out the method for treating garbage and the like according to the first to fourth inventions of the present application.

【図2】図1に示す装置の要部正面図。FIG. 2 is a front view of a main part of the apparatus shown in FIG.

【図3】図1に示す装置の要部縦断側面図。FIG. 3 is a vertical sectional side view of a main part of the apparatus shown in FIG. 1;

【符号の説明】[Explanation of symbols]

1・・・生ごみ処理槽、1a・・・処理槽本体、1b・・
・蓋板、1c・・・生ごみ投入口、1d・・・熱風排気
口、1e・・・溶解促進剤投入口、1f・・・排出管、2
・・・撹拌軸、3a・・・上段翼、3b・・・中段翼、3
c・・・下段翼、4a,4b・・・スプロケット歯車、4c
・・・エンドレスチェーン、5・・・モータ、6a・・
・加熱室形成室、6a’・・・温風入口、6a”・・・温
風出口、6b・・・熱風式加熱壁、7a・・・エアシリン
ダ装置、7b・・・シャッタ、7c・・・生ごみ破砕機、
7d・・・生ごみ投入用ホッパ、7e・・・蓋、8a・・
・シャッタ、8b・・・臭気処理筒、8c・・・排気ファ
ン、8d・・・ヒーター、8e・・・消臭エレメント、9
a・・・エアシリンダ装置、9b・・・シャッタ、9c・
・・溶解促進剤投入ホッパ、9d・・・蓋、10・・・
二段シャッタ式計量器、10a・・・シャッタ、10b・
・・シャッタ、10c・・・エアシリンダ装置、10d・
・・エアシリンダ装置、11a・・・生石灰投入ホッ
パ、11b・・・生石灰貯留ホッパ、11c・・・下部水
平スクリューコンベア、11d・・・傾斜スクリューコ
ンベア、11e・・・上部水平スクリューコンベア、1
1f・・・蓋、12・・・吸排気管、13・・・電磁仕
切り弁、14・・・液溜め回収タンク、15・・・空冷
フィン、16・・・熱電対、16a・・・排出管、17a
・・・仕切り弁、17b・・・エルボ管、18・・・サ
ンプル採取用のコック、19・・・エルボ管、20・・
・エルボ形排気ガス回収管、21・・・点検扉兼用覗き
窓、
1 ... garbage disposal tank, 1a ... treatment tank body, 1b ...
・ Cover plate, 1c ・ ・ ・ Garbage input port, 1d ・ ・ ・ Hot air exhaust port, 1e ・ ・ ・ Dissolution promoter input port, 1f ・ ・ ・ Discharge pipe, 2
... Agitating shaft, 3a ... Upper stage blade, 3b ... Middle stage blade, 3
c: Lower wing, 4a, 4b: Sprocket gear, 4c
... Endless chain, 5 ... Motor, 6a ...
· Heating chamber forming chamber, 6a '· · · hot air inlet, 6a' · · · hot air outlet, 6b · · · hot air heating wall, 7a · · · air cylinder device, 7b · · · shutter, 7c · · · ·・ Garbage crusher,
7d: hopper for putting garbage, 7e: lid, 8a
-Shutter, 8b-Odor treatment cylinder, 8c-Exhaust fan, 8d-Heater, 8e-Deodorant element, 9
a ・ ・ ・ Air cylinder device, 9b ・ ・ ・ Shutter, 9c ・
..Dissolution promoter charging hopper, 9d ... lid, 10 ...
Two-stage shutter type measuring device, 10a ... shutter, 10b
..Shutter, 10c ... air cylinder device, 10d
..Air cylinder device, 11a: quick lime input hopper, 11b: quick lime storage hopper, 11c: lower horizontal screw conveyor, 11d: inclined screw conveyor, 11e: upper horizontal screw conveyor, 1
1f: lid, 12: intake / exhaust pipe, 13: electromagnetic gate valve, 14: liquid collecting tank, 15: air-cooled fin, 16: thermocouple, 16a: discharge pipe , 17a
... gate valve, 17b ... elbow tube, 18 ... cock for sampling, 19 ... elbow tube, 20 ...
・ Elbow type exhaust gas recovery pipe, 21 ・ ・ ・ Inspection window also used as inspection door,

【手続補正書】[Procedure amendment]

【提出日】平成12年12月26日(2000.12.
26)
[Submission date] December 26, 2000 (200.12.
26)

【手続補正1】[Procedure amendment 1]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】図面の簡単な説明[Correction target item name] Brief description of drawings

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【図面の簡単な説明】[Brief description of the drawings]

【図1】本願第一ないし第四の発明の生ごみ等の処理方
法を実施するための生ごみ等の処理装置の好ましい一例
を示す要部正面図。
FIG. 1 is a main part front view showing a preferred example of an apparatus for treating garbage and the like for carrying out the method for treating garbage and the like according to the first to fourth inventions of the present application.

【図2】図1に示す装置の要部縦断側面図。FIG. 2 is a vertical sectional side view of a main part of the apparatus shown in FIG.

【図3】図1に示す装置の生ごみ等の処理装置の好まし
い一例を示す全体正面図。
FIG. 3 is an overall front view showing a preferred example of a processing apparatus for processing garbage and the like in the apparatus shown in FIG. 1;

【符号の説明】 1・・・生ごみ処理槽、1a・・・処理槽本体、1b・・
・蓋板、1c・・・生ごみ投入口、1d・・・熱風排気
口、1e・・・溶解促進剤投入口、1f・・・排出管、2
・・・撹拌軸、3a・・・上段翼、3b・・・中段翼、3
c・・・下段翼、4a,4b・・・スプロケット歯車、4c
・・・エンドレスチェーン、5・・・モータ、6a・・
・加熱室形成室、6a’・・・温風入口、6a”・・・温
風出口、6b・・・熱風式加熱壁、7a・・・エアシリン
ダ装置、7b・・・シャッタ、7c・・・生ごみ破砕機、
7d・・・生ごみ投入用ホッパ、7e・・・蓋、8a・・
・シャッタ、8b・・・臭気処理筒、8c・・・排気ファ
ン、8d・・・ヒーター、8e・・・消臭エレメント、9
a・・・エアシリンダ装置、9b・・・シャッタ、9c・
・・溶解促進剤投入ホッパ、9d・・・蓋、10・・・
二段シャッタ式計量器、10a・・・シャッタ、10b・
・・シャッタ、10c・・・エアシリンダ装置、10d・
・・エアシリンダ装置、11a・・・生石灰投入ホッ
パ、11b・・・生石灰貯留ホッパ、11c・・・下部水
平スクリューコンベア、11d・・・傾斜スクリューコ
ンベア、11e・・・上部水平スクリューコンベア、1
1f・・・蓋、12・・・吸排気管、13・・・電磁仕
切り弁、14・・・液溜め回収タンク、15・・・空冷
フィン、16・・・熱電対、16a・・・排出管、17a
・・・仕切り弁、17b・・・エルボ管、18・・・サ
ンプル採取用のコック、19・・・エルボ管、20・・
・エルボ形排気ガス回収管、21・・・点検扉兼用覗き
窓、
[Description of Signs] 1 ... Garbage treatment tank, 1a ... Treatment tank body, 1b ...
・ Cover plate, 1c ・ ・ ・ Garbage input port, 1d ・ ・ ・ Hot air exhaust port, 1e ・ ・ ・ Dissolution promoter input port, 1f ・ ・ ・ Discharge pipe, 2
... Agitating shaft, 3a ... Upper stage blade, 3b ... Middle stage blade, 3
c: Lower wing, 4a, 4b: Sprocket gear, 4c
... Endless chain, 5 ... Motor, 6a ...
· Heating chamber forming chamber, 6a '· · · hot air inlet, 6a' · · · hot air outlet, 6b · · · hot air heating wall, 7a · · · air cylinder device, 7b · · · shutter, 7c · · · ·・ Garbage crusher,
7d: hopper for putting garbage, 7e: lid, 8a
-Shutter, 8b-Odor treatment cylinder, 8c-Exhaust fan, 8d-Heater, 8e-Deodorant element, 9
a ・ ・ ・ Air cylinder device, 9b ・ ・ ・ Shutter, 9c ・
..Dissolution promoter charging hopper, 9d ... lid, 10 ...
Two-stage shutter type measuring device, 10a ... shutter, 10b
..Shutter, 10c ... air cylinder device, 10d
..Air cylinder device, 11a: quick lime input hopper, 11b: quick lime storage hopper, 11c: lower horizontal screw conveyor, 11d: inclined screw conveyor, 11e: upper horizontal screw conveyor, 1
1f: lid, 12: intake / exhaust pipe, 13: electromagnetic gate valve, 14: liquid collecting tank, 15: air-cooled fin, 16: thermocouple, 16a: discharge pipe , 17a
... gate valve, 17b ... elbow tube, 18 ... cock for sampling, 19 ... elbow tube, 20 ...
・ Elbow type exhaust gas recovery pipe, 21 ・ ・ ・ Inspection window also used as inspection door,

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C05F 9/00 B09B 3/00 ZABD Fターム(参考) 4D004 AA03 BA03 BA04 CA04 CA15 CA19 CA24 CA32 CA42 CA46 CA48 CB04 CB06 CB13 CB27 CB36 CC12 DA01 DA06 4G037 CA04 EA04 4G078 AB20 BA05 DA01 EA03 4H061 AA01 AA02 CC47 CC55 EE12 EE66 FF07 GG18 GG30 GG43 GG48 GG70 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) C05F 9/00 B09B 3/00 ZABD F-term (Reference) 4D004 AA03 BA03 BA04 CA04 CA15 CA19 CA24 CA32 CA42 CA46 CA48 CB04 CB06 CB13 CB27 CB36 CC12 DA01 DA06 4G037 CA04 EA04 4G078 AB20 BA05 DA01 EA03 4H061 AA01 AA02 CC47 CC55 EE12 EE66 FF07 GG18 GG30 GG43 GG48 GG70

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 生ごみ処理槽内に生ごみ等を細粒化して
収容し所要量の塩素を含まない強酸を加え所要温度に加
熱して攪拌し生ごみ等を強酸により有機物分解して流動
性分解物を生成・促進するとともに加熱により水蒸気蒸
発を促進し水蒸気を生ごみ処理槽外に排出して減容化を
促進しかつ消臭を行い、次いで、塩素を含まない強アル
カリを混合し中性ないし弱アルカリ性に戻し、次いで、
生石灰の粉末を混合し攪拌して高温熱化学反応を生じさ
せて高熱水蒸気を完全に分離除去し、熱分解・完全殺菌
・無水化・減容化を生じさせた純白色の微粉末を生ごみ
処理槽内に生成し生ごみ処理槽外に回収することを特徴
とする生ごみ等の処理方法。
1. Garbage and the like are finely divided and stored in a garbage processing tank, a required amount of a strong acid containing no chlorine is added, the mixture is heated to a required temperature and stirred, and the garbage and the like are decomposed into organic substances by the strong acid and flow. In addition to generating and promoting decomposed products, it promotes steam evaporation by heating and discharges steam out of the garbage disposal tank to promote volume reduction and deodorization, and then mix strong alkali containing no chlorine. Return to neutral or slightly alkaline, then
The quicklime powder is mixed and stirred to cause a high-temperature thermochemical reaction to completely separate and remove the high-temperature steam, giving a pure white fine powder that undergoes thermal decomposition, complete sterilization, dehydration, and volume reduction. A method for treating garbage and the like, wherein the method is generated in a treatment tank and collected outside the garbage treatment tank.
【請求項2】 生ごみ処理槽内に生ごみ等を細粒化して
収容し所要量の塩素を含まない強酸を加え所要温度に加
熱して攪拌し生ごみ等を強酸により有機物分解して流動
性分解物を生成・促進するとともに加熱により水蒸気蒸
発を促進し水蒸気を生ごみ処理槽外に排出して減容化を
促進しかつ消臭を行い、次いで、塩素を含まない強アル
カリを混合し中性ないし弱アルカリ性に戻し生ごみ処理
槽内の流動性分解物を細菌に好適な温度にして菌担持体
を投入して細菌を繁殖させて微生物的有機物分解を促進
させ、かつこの間も加熱により水蒸気蒸発を促進し水蒸
気を生ごみ処理槽外に排出して減容化を促進し、次い
で、生石灰の粉末を混合し攪拌して高温熱化学反応を生
じさせて高熱水蒸気を完全に分離除去し、熱分解・完全
殺菌・無水化・減容化を生じさせた純白色の微粉末を生
ごみ処理槽内に生成し生ごみ処理槽外に回収することを
特徴とする生ごみ等の処理方法。
2. Garbage and the like are finely divided and stored in a garbage disposal tank, a required amount of a strong acid containing no chlorine is added, heated to a required temperature and stirred, and the garbage and the like are decomposed into organic substances by the strong acid and flow. In addition to generating and promoting decomposed products, it promotes steam evaporation by heating and discharges steam out of the garbage disposal tank to promote volume reduction and deodorization, and then mix strong alkali containing no chlorine. Neutral or weakly alkaline, the flowable decomposed product in the garbage disposal tank is brought to a temperature suitable for bacteria, a bacterial carrier is thrown in, bacteria are propagated, microbial organic matter decomposition is promoted, and during this time heating is performed. It promotes steam evaporation and discharges steam out of the kitchen garbage disposal tank to promote volume reduction, and then mixes and agitates quicklime powder to cause a high-temperature thermochemical reaction to completely separate and remove the hot steam. , Pyrolysis, complete sterilization, dehydration, volume reduction A method for treating garbage or the like, characterized in that the pure white fine powder that caused the garbage is generated in a garbage processing tank and collected outside the garbage processing tank.
【請求項3】 生ごみ処理槽内に生ごみ等を細粒化して
収容し菌担持体を投入し細菌に好適な温度に加熱して撹
拌し細菌を繁殖させて微生物的有機物分解を促進させ、
次いで、所要量の塩素を含まない強酸を加えて該強酸に
より有機物分解して流動性分解物を生成・促進するとと
もに加熱により水蒸気蒸発を促進し水蒸気を生ごみ処理
槽外に排出して減容化を促進しかつ消臭を行い、次い
で、塩素を含まない強アルカリを加えて撹拌混合し中性
ないし弱アルカリ性に戻し、次いで、生石灰の粉末を混
合し攪拌して高温熱化学反応を生じさせて高熱水蒸気を
完全に分離除去し、熱分解・完全殺菌・無水化・減容化
を生じさせた純白色の微粉末を生ごみ処理槽内に生成し
生ごみ処理槽外に回収することを特徴とする生ごみ等の
処理方法。
3. A garbage disposal tank containing finely divided garbage and the like, containing the garbage and the like, charging a bacterial carrier, heating the bacterium to a temperature suitable for the bacterium, stirring the garbage to propagate the bacterium, and promoting the decomposition of microbial organic matter. ,
Next, a required amount of a chlorine-free strong acid is added to decompose organic matter by the strong acid to generate and promote a flowable decomposed product, and to promote steam evaporation by heating and discharge the steam out of the garbage treatment tank to reduce the volume. To promote neutralization and deodorization, then add a strong alkali containing no chlorine and stir and mix to return to neutral to weakly alkaline, then mix and mix quicklime powder to cause a high-temperature thermochemical reaction. To completely separate and remove high-temperature steam, and to generate pure white fine powder that has undergone thermal decomposition, complete sterilization, dehydration, and volume reduction in the garbage disposal tank and collect it outside the garbage disposal tank. Characteristic garbage disposal method.
【請求項4】 生ごみ処理槽内に生ごみ等を細粒化して
収容し菌担持体を投入し細菌に好適な温度に加熱して撹
拌し細菌を繁殖させて微生物的有機物分解を促進させ、
次いで、所要量の塩素を含まない強酸を加えて該強酸に
より有機物分解して流動性分解物を生成・促進するとと
もに加熱により水蒸気蒸発を促進し水蒸気を生ごみ処理
槽外に排出して減容化を促進しかつ消臭を行い、次い
で、塩素を含まない強アルカリを混合し中性ないし弱ア
ルカリ性に戻し生ごみ処理槽内の流動性分解物を細菌に
好適な温度にして菌担持体を投入して細菌を繁殖させて
微生物的有機物分解を促進させ、かつこの間も加熱によ
り水蒸気蒸発を促進し水蒸気を生ごみ処理槽外に排出し
て減容化を促進し、次いで、生石灰の粉末を混合し攪拌
して高温熱化学反応を生じさせて高熱水蒸気を完全に分
離除去し、熱分解・完全殺菌・無水化・減容化を生じさ
せた純白色の微粉末を生ごみ処理槽内に生成し生ごみ処
理槽外に回収することを特徴とする生ごみ等の処理方
法。
4. A garbage disposal tank containing finely divided garbage and the like, containing the garbage, charging the bacteria carrier, heating the mixture to a temperature suitable for the bacteria, and agitating the bacteria to propagate the bacteria and promote the decomposition of microbial organic substances. ,
Next, a required amount of a chlorine-free strong acid is added to decompose organic matter by the strong acid to generate and promote a flowable decomposed product, and to promote steam evaporation by heating and discharge the steam out of the garbage treatment tank to reduce the volume. To promote neutralization and deodorization, and then mix strong alkalis containing no chlorine to return to neutral or weak alkalinity, and set the fluid decomposition product in the garbage disposal tank to a temperature suitable for bacteria to bring the bacterial carrier up. The bacteria are propagated to promote microbial organic matter decomposition, and during this time, heating promotes steam evaporation and discharges steam out of the garbage disposal tank to promote volume reduction. Mix and stir to create a high-temperature thermochemical reaction to completely separate and remove the high-temperature steam, and place pure white fine powder that has undergone thermal decomposition, complete sterilization, dehydration, and volume reduction into the garbage disposal tank. Generated and collected outside the garbage disposal tank Processing method of garbage, such as characterized by.
【請求項5】 [請求項1]ないし[請求項4]のいず
れか一項に記載の生ごみ等の処理方法によって製造され
る白色微粉末よりなることを特徴とする肥料。
5. A fertilizer comprising a white fine powder produced by the method for treating garbage or the like according to any one of [1] to [4].
JP2000395671A 2000-12-26 2000-12-26 Garbage treatment method and fertilizer Pending JP2002192115A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000395671A JP2002192115A (en) 2000-12-26 2000-12-26 Garbage treatment method and fertilizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000395671A JP2002192115A (en) 2000-12-26 2000-12-26 Garbage treatment method and fertilizer

Publications (1)

Publication Number Publication Date
JP2002192115A true JP2002192115A (en) 2002-07-10

Family

ID=18861095

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000395671A Pending JP2002192115A (en) 2000-12-26 2000-12-26 Garbage treatment method and fertilizer

Country Status (1)

Country Link
JP (1) JP2002192115A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005154257A (en) * 2003-10-29 2005-06-16 Okamura:Kk Manufacturing device and manufacturing plant of mixed sludge fertilizer
WO2006064616A1 (en) * 2004-12-16 2006-06-22 Matsushita Electric Industrial Co., Ltd. Raw garbage disposer
CN104758967A (en) * 2015-04-08 2015-07-08 芜湖锐进医疗设备有限公司 Medical electric sawing and drilling workshop disinfection vehicle
CN104841683A (en) * 2015-05-08 2015-08-19 张才友 Bio-robot for treating kitchen garbage and garbage treatment method of bio-robot
CN109331696A (en) * 2018-11-12 2019-02-15 安徽家思特涂料有限责任公司 A kind of building coating production graining paste reconciliation equipment
CN110508177A (en) * 2019-06-15 2019-11-29 盐城恒益绿化有限公司 A kind of liquid fertilizer process units

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005154257A (en) * 2003-10-29 2005-06-16 Okamura:Kk Manufacturing device and manufacturing plant of mixed sludge fertilizer
JP4502196B2 (en) * 2003-10-29 2010-07-14 有限会社オカムラ Mixed sludge fertilizer production equipment and production plant
WO2006064616A1 (en) * 2004-12-16 2006-06-22 Matsushita Electric Industrial Co., Ltd. Raw garbage disposer
CN104758967A (en) * 2015-04-08 2015-07-08 芜湖锐进医疗设备有限公司 Medical electric sawing and drilling workshop disinfection vehicle
CN104841683A (en) * 2015-05-08 2015-08-19 张才友 Bio-robot for treating kitchen garbage and garbage treatment method of bio-robot
CN109331696A (en) * 2018-11-12 2019-02-15 安徽家思特涂料有限责任公司 A kind of building coating production graining paste reconciliation equipment
CN110508177A (en) * 2019-06-15 2019-11-29 盐城恒益绿化有限公司 A kind of liquid fertilizer process units

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