JP2002205096A - Treatment method and equipment for organic waste - Google Patents
Treatment method and equipment for organic wasteInfo
- Publication number
- JP2002205096A JP2002205096A JP2001004091A JP2001004091A JP2002205096A JP 2002205096 A JP2002205096 A JP 2002205096A JP 2001004091 A JP2001004091 A JP 2001004091A JP 2001004091 A JP2001004091 A JP 2001004091A JP 2002205096 A JP2002205096 A JP 2002205096A
- Authority
- JP
- Japan
- Prior art keywords
- solid
- composting
- biological reaction
- liquid
- carbide
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
-
- 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
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
Abstract
Description
【０００１】[0001]
【発明の属する技術分野】本発明は、有機性廃棄物の処
理方法及び装置に係り、より詳しくは家畜糞尿等の有機
性廃棄物をコンポスト化処理する有機性廃棄物の処理方
法及び装置に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for treating organic waste, and more particularly, to a method and an apparatus for treating organic waste such as livestock manure as compost. It is.
【０００２】[0002]
【従来技術】家畜糞尿は、肥料成分（Ｎ，Ｐ，Ｋ）の含
有率が高く、土壌改良性にも優れており、農耕地等に施
用される有機質資材として極めて有用である。ところ
が、家畜糞尿は一般に、そのままでは悪臭が強く、搬送
や施用等の作業性の点から取扱い難いものである。従っ
て、家畜糞尿を衛生的に処理し、良質のコンポストとし
て有効利用する必要がある。2. Description of the Related Art Livestock manure has a high content of fertilizer components (N, P, K) and is excellent in soil improvement properties, and is extremely useful as an organic material applied to agricultural lands and the like. However, livestock manure generally has a strong odor as it is, and is difficult to handle in terms of workability such as transportation and application. Therefore, it is necessary to treat livestock manure hygienically and to effectively use it as high-quality compost.
【０００３】家畜糞尿は、日本国内で年間９０００万ト
ン排泄されるが、このうちの肉牛の糞尿や鶏糞等は比較
的水分が少ないため、そのままの状態でコンポストとし
て利用されている。[0003] Domestic manure is excreted in an amount of 90 million tons annually in Japan. Of these, beef manure and chicken manure are used as they are as compost because they have relatively low water content.
【０００４】一方、家畜糞尿のうちの乳牛糞尿や豚糞尿
は一般に水分が高いため固液分離され、固形物について
はコンポスト化され、液状物については活性汚泥処理や
メタン発酵等の生物処理された後、河川等に放流されて
いる。On the other hand, dairy cow manure and pig manure among livestock manure are generally solid and liquid separated due to high water content, solids are composted, and liquids are subjected to biological treatment such as activated sludge treatment and methane fermentation. Later, they are released into rivers.
【０００５】また、家畜糞尿の処理方法として、例えば
特開平１１−１９７６３６号公報に開示される方法があ
る。同公報によれば、家畜糞尿が固液分離され、固形物
については可溶化した後に嫌気性発酵処理され、液状物
については嫌気性発酵処理される。そして、嫌気性発酵
処理により得られる余剰汚泥が脱水された後、コンポス
ト化される。As a method for treating livestock manure, for example, there is a method disclosed in Japanese Patent Application Laid-Open No. H11-197636. According to the publication, livestock manure is subjected to solid-liquid separation, solid matter is solubilized and then subjected to anaerobic fermentation treatment, and liquid matter is subjected to anaerobic fermentation treatment. Then, the excess sludge obtained by the anaerobic fermentation treatment is dewatered and then composted.
【０００６】[0006]
【発明が解決しようとする課題】しかしながら、前述し
た乳牛糞尿や豚糞尿の固液分離により得られる固形物を
直接コンポスト化する家畜糞尿処理方法では、乳牛糞尿
では稲藁等の敷き材が、豚糞尿では飼料粕や豚毛等が、
コンポスト化した製品中に残存し、良質のコンポストが
得られないため、製品価値が落ちてしまう。However, in the above-mentioned livestock manure treatment method in which solid matter obtained by solid-liquid separation of cow manure and pig manure is directly composted, the litter such as rice straw is used in the cow manure. In manure, feed lees, pig hair, etc.
Since it remains in the composted product and high quality compost cannot be obtained, the product value is reduced.
【０００７】また、前述した公報に記載の家畜糞尿処理
方法では、固形物については嫌気性発酵処理により分解
するため良質のコンポストが得られるものの、嫌気性発
酵処理により得られる余剰汚泥を脱水しても、脱水され
た余剰汚泥にはまだ比較的多くの水分が含まれているた
め、脱水された余剰汚泥の発酵がうまく行かず、コンポ
スト化が困難である。In the livestock manure treatment method described in the above-mentioned publication, solids are decomposed by anaerobic fermentation to obtain high-quality compost, but excess sludge obtained by anaerobic fermentation is dewatered. However, since the dewatered surplus sludge still contains a relatively large amount of water, fermentation of the dewatered surplus sludge does not work well, and composting is difficult.
【０００８】本発明は、上記事情に鑑みてなされたもの
であり、良質のコンポストを容易に得ることができる有
機性廃棄物の処理方法及び装置を提供することを目的と
する。[0008] The present invention has been made in view of the above circumstances, and an object of the present invention is to provide a method and an apparatus for treating organic waste, which can easily obtain high-quality compost.
【０００９】[0009]
【課題を解決するための手段】上記目的を達成するた
め、本発明は、有機性廃棄物を固形物と液状物とに固液
分離する固液分離工程と、液状物を生物反応槽内で生物
反応処理する生物反応工程と、生物反応槽から余剰汚泥
を排出する汚泥排出工程と、固形物を炭化して炭化物を
得る炭化工程と、炭化物と余剰汚泥とを混合して混合物
を得る混合工程と、混合物をコンポスト化するコンポス
ト化工程とを含むことを特徴とする有機性廃棄物の処理
方法である。In order to achieve the above object, the present invention provides a solid-liquid separation step of solid-liquid separation of an organic waste into a solid substance and a liquid substance, and a step of separating the liquid substance in a biological reaction tank. Biological reaction step for biological reaction treatment, sludge discharge step for discharging excess sludge from the biological reaction tank, carbonization step for carbonizing solid matter to obtain carbide, and mixing step for mixing carbide and excess sludge to obtain a mixture And a composting step of composting the mixture.
【００１０】この発明によれば、固液分離された液状物
は、生物反応槽内で生物反応処理により生物反応処理さ
れ、生物反応槽からは余剰汚泥が排出される。この余剰
汚泥は通常水分を多く含んでおり、そのままコンポスト
化しようとすると、混合物が効率よく発酵処理されず、
コンポスト化が困難となる場合がある。そこで、本発明
では、余剰汚泥に、炭化工程で得られた炭化物を混合す
るようにしている。これにより、余剰汚泥の水分調整を
行うことが可能となり、コンポスト化に適した水分を有
する混合物を、コンポスト化に先立って得ることが可能
となる。また、コンポスト化に際して、固形物は炭化物
となっているため、稲藁等の敷き材、飼料粕、豚毛等の
不用物がコンポストに含まれることもない。According to the present invention, the liquid material subjected to the solid-liquid separation is subjected to a biological reaction treatment in the biological reaction tank by a biological reaction treatment, and excess sludge is discharged from the biological reaction tank. This excess sludge usually contains a lot of water, and if you try to compost as it is, the mixture is not efficiently fermented,
Composting may be difficult. Therefore, in the present invention, the excess sludge is mixed with the carbide obtained in the carbonization step. Thereby, the water content of the excess sludge can be adjusted, and a mixture having water suitable for composting can be obtained prior to composting. Further, when composting, since the solid is carbonized, the compost does not include litter such as rice straw, waste meal, and pig wool.
【００１１】また、本発明は、有機性廃棄物を固形物と
液状物とに固液分離する固液分離装置と、液状物を生物
反応処理すると共に余剰汚泥を排出する生物反応槽と、
固形物を炭化して炭化物を得る炭化装置と、炭化物と余
剰汚泥とを混合するための混合装置と、混合装置で得ら
れた混合物をコンポスト化するコンポスト化装置とを備
えることを特徴とする有機性廃棄物の処理装置である。The present invention also provides a solid-liquid separation device for solid-liquid separation of an organic waste into a solid substance and a liquid substance, a biological reaction tank for performing a biological reaction treatment on the liquid substance and discharging excess sludge,
An organic material comprising: a carbonization device for carbonizing a solid to obtain a carbide; a mixing device for mixing the carbide with the excess sludge; and a composting device for composting the mixture obtained by the mixing device. It is a treatment device for toxic waste.
【００１２】この発明によれば、上記方法の発明を有効
に実施することができる。According to the present invention, the invention of the above method can be effectively implemented.
【００１３】[0013]
【発明の実施の形態】以下、本発明の実施形態について
詳細に説明する。DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, embodiments of the present invention will be described in detail.
【００１４】図１は、本発明に係る有機性廃棄物の処理
装置の一実施形態である家畜糞尿の処理装置を示すフロ
ー図である。図１に示すように、家畜糞尿の処理装置１
においては、家畜糞尿がラインＬ１を経て固液分離装置
２に導入され、稲藁、飼料粕、豚毛等の低水分の固形物
と、これら粗大有機物を含まない純粋な糞尿（液状物）
とに固液分離されるようになっている。固液分離装置２
としては、例えばスクリュープレス、遠心脱水機、ベル
トプレス、フィルタープレス、多重円板式脱水機等が用
いられる。FIG. 1 is a flow chart showing a livestock manure processing apparatus which is one embodiment of the organic waste processing apparatus according to the present invention. As shown in FIG. 1, livestock manure processing apparatus 1
In the above, livestock manure is introduced into the solid-liquid separation device 2 via the line L1, and low-moisture solids such as rice straw, feed lees, pig hair, etc., and pure manure (liquid matter) not containing these coarse organic substances.
And solid-liquid separation. Solid-liquid separator 2
Examples thereof include a screw press, a centrifugal dehydrator, a belt press, a filter press, and a multiple disc dehydrator.
【００１５】固液分離装置２により分離された糞尿は、
ラインＬ２を経て貯留槽３に導入されて希釈調整される
ようになっている。このように糞尿を希釈するのは、後
述する生物反応槽４における負荷を低減するためであ
る。The manure separated by the solid-liquid separator 2 is
It is introduced into the storage tank 3 via the line L2, and the dilution is adjusted. The reason for diluting the manure is to reduce the load on the biological reaction tank 4 described later.
【００１６】希釈された糞尿は、ラインＬ４を経て生物
反応槽４に導入され、生物反応処理される。生物反応槽
４は、汚泥を用いて有機物の生物分解を行うことが可能
であるものであればよく、例えば、生物反応槽４とし
て、嫌気性発酵槽、活性汚泥処理槽等が用いられる。こ
れらのうち、空気の供給を必要とせず、ランニングコス
トを節約できる点から嫌気性発酵槽が好ましい。The diluted manure is introduced into the biological reaction tank 4 via the line L4, and is subjected to a biological reaction treatment. The biological reaction tank 4 is only required to be capable of biodegrading organic substances using sludge. For example, an anaerobic fermentation tank, an activated sludge treatment tank, or the like is used as the biological reaction tank 4. Of these, an anaerobic fermenter is preferred because it does not require air supply and can save running costs.
【００１７】ここで、嫌気性発酵槽としては、メタン発
酵槽、消化槽等が挙げられるが、このうちメタン発酵槽
が好ましい。この場合、図１に示すように、メタンガス
発酵槽で発生したメタンガスは、ラインＬ９を経てガス
貯留槽９に導入され、ガス貯留槽９からラインＬ１０を
経て、後述する炭化装置７へ供給され、メタンガスが炭
化装置７で固形物を炭化するときの燃料として供給され
るようになっている。これにより、家畜糞尿の処理装置
１におけるランニングコストの大幅な低減を図ることが
できる。なお、ラインＬ９、ガス貯留槽９、ラインＬ１
０により燃料供給手段が構成されている。Here, examples of the anaerobic fermenter include a methane fermenter and a digester, and among them, the methane fermenter is preferable. In this case, as shown in FIG. 1, the methane gas generated in the methane gas fermenter is introduced into the gas storage tank 9 via the line L9, and is supplied from the gas storage tank 9 to the carbonization device 7 described later via the line L10, Methane gas is supplied as fuel when carbonizing solids in the carbonization device 7. As a result, the running cost of the livestock manure processing device 1 can be significantly reduced. In addition, line L9, gas storage tank 9, line L1
0 constitutes a fuel supply means.
【００１８】生物反応槽４から排出される余剰汚泥は、
ラインＬ４を経て脱水機５に送られ、脱水される。脱水
機５としては、例えばスクリュープレス、遠心脱水機、
ベルトプレス、フィルタープレス、多重円板式脱水機等
が用いられる。脱水機５で脱水された余剰汚泥（以下、
「脱水汚泥」という）は、ラインＬ５を経て混合装置６
に導入される。The surplus sludge discharged from the biological reaction tank 4 is
It is sent to the dehydrator 5 via the line L4 and dehydrated. Examples of the dehydrator 5 include a screw press, a centrifugal dehydrator,
A belt press, a filter press, a multiple disc dehydrator, and the like are used. Excess sludge dehydrated by the dehydrator 5 (hereinafter, sludge)
"Dewatered sludge") passes through line L5 to the mixing device 6
Will be introduced.
【００１９】一方、固液分離装置２で分離された固形物
は、ラインＬ６を経て炭化装置７へ送られるようになっ
ている。炭化装置７は、固形物を炭化するものであり、
固形物を加熱することが可能な装置であればよく、加熱
形式は、内熱式、外熱式のいずれでもよい。On the other hand, the solid separated by the solid-liquid separation device 2 is sent to a carbonization device 7 via a line L6. The carbonizing device 7 is for carbonizing solid matter,
Any device can be used as long as it can heat a solid, and the heating method may be any of an internal heating type and an external heating type.
【００２０】炭化装置７で炭化された炭化物は、ライン
Ｌ７を経て混合装置６へ送られ、脱水汚泥と混合される
ようになっている。The carbide carbonized by the carbonizing device 7 is sent to the mixing device 6 via the line L7, and is mixed with the dewatered sludge.
【００２１】混合装置６は通常、混合槽の内部に攪拌装
置を備えており、脱水汚泥と炭化物とを均一に混合する
ことが可能である。ただし、攪拌装置は必ずしも必要な
ものではない。The mixing device 6 is usually provided with a stirring device inside the mixing tank, so that the dewatered sludge and the carbide can be uniformly mixed. However, a stirrer is not always necessary.
【００２２】混合装置６で得られる混合物は、ラインＬ
８を経てコンポスト化装置８へ送られ、コンポスト化装
置８でコンポスト化されるようになっている。コンポス
ト化装置８は通常、混合物を収容する容器と、混合物を
切返す切返し機と、混合物に給気を行う給気装置とで構
成される。The mixture obtained in the mixing device 6 is
After that, it is sent to the composting device 8 and composted by the composting device 8. The composting device 8 is generally composed of a container for containing the mixture, a turning machine for turning over the mixture, and an air supply device for supplying air to the mixture.
【００２３】次に、前述した家畜糞尿の処理装置１にお
ける家畜糞尿の処理方法について説明する。Next, a method of processing livestock manure in the above-described livestock manure processing apparatus 1 will be described.
【００２４】まず家畜糞尿をラインＬ１を経て固液分離
装置２に導入し、稲藁、飼料粕、豚毛等の低水分の固形
物と、これら粗大有機物を含まない純粋な糞尿（液状
物）とに固液分離する（固液分離工程）。First, livestock manure is introduced into the solid-liquid separation device 2 via the line L1, and low-moisture solids such as rice straw, feed lees, pig hair, etc., and pure manure (liquid matter) not containing these coarse organic substances. (Solid-liquid separation step).
【００２５】固液分離装置２により分離された糞尿は、
ラインＬ２を経て貯留槽３に導入し、希釈調整する。The manure separated by the solid-liquid separator 2 is
It is introduced into the storage tank 3 via the line L2, and the dilution is adjusted.
【００２６】希釈した糞尿は、ラインＬ３を経て生物反
応槽４に導入し、生物反応処理する（生物反応工程）。
これにより、糞尿中の悪臭の原因となる有機物が生物分
解される。次に、生物反応槽４から余剰汚泥を排出する
（汚泥排出工程）。この余剰汚泥を、ラインＬ４を経て
脱水機５に導入して脱水処理する。このとき、無機凝集
剤や高分子凝集剤等の脱水助剤を添加する。そして、脱
水汚泥をラインＬ５を経て混合装置６に導入する。The diluted manure is introduced into the biological reaction tank 4 via the line L3 and subjected to a biological reaction treatment (biological reaction step).
As a result, the organic matter causing the bad smell in the manure is biodegraded. Next, surplus sludge is discharged from the biological reaction tank 4 (sludge discharge step). The surplus sludge is introduced into the dehydrator 5 through the line L4 to be dehydrated. At this time, a dehydration aid such as an inorganic coagulant or a polymer coagulant is added. Then, the dewatered sludge is introduced into the mixing device 6 via the line L5.
【００２７】一方、固液分離装置２で分離された固形物
は、ラインＬ６を経て炭化装置７に導入する。炭化処理
は、コスト等を考慮して、通常は２００〜７００℃の温
度で行う。この炭化処理により、敷き材、飼料粕、豚毛
等の固形物が炭化される（炭化工程）。On the other hand, the solid separated by the solid-liquid separation device 2 is introduced into the carbonization device 7 via the line L6. The carbonization treatment is usually performed at a temperature of 200 to 700 ° C. in consideration of cost and the like. By this carbonization treatment, solids such as litter, feed lees, and pig hair are carbonized (carbonization step).
【００２８】炭化装置７で炭化した炭化物は、ラインＬ
７を経て混合装置６に送り、前述した脱水汚泥と混合す
る（混合工程）。[0028] The carbide carbonized by the carbonization device 7 is supplied to the line L
The mixture is sent to the mixing device 6 through 7 and mixed with the above-described dewatered sludge (mixing step).
【００２９】ここで、脱水汚泥は、通常多くの水分を含
んでおり、そのままコンポスト化すると、効率よく発酵
処理されず、コンポスト化が困難となる場合がある。そ
こで本発明では、上述したように、脱水汚泥に炭化物を
混合することにしている。これにより、脱水汚泥の水分
を調整することが可能となり、コンポスト化に適した水
分を有する混合物を、コンポスト化に先立って得ること
が可能となる。Here, the dewatered sludge usually contains a large amount of water, and if it is composted as it is, it is not efficiently fermented, and it may be difficult to compost it. Therefore, in the present invention, as described above, the carbide is mixed with the dewatered sludge. Thereby, the water content of the dewatered sludge can be adjusted, and a mixture having a water content suitable for composting can be obtained prior to composting.
【００３０】従って、この混合物を、ラインＬ８を経て
コンポスト化装置８へ導入し（コンポスト化工程）、通
気性を良くした上でコンポスト化を行うと、好気性微生
物の活動が活発化し、混合物を効率良く発酵処理するこ
とが可能となる。また、コンポスト化に先立ち、固液分
離された固形物が炭化物とされているため、得られるコ
ンポストには、稲藁等の敷き材、飼料粕、豚毛等の不用
物が含まれることもない。すなわち、本発明によれば、
良質のコンポストを容易に得ることができる。また、混
合物に含まれる炭化物は、アンモニア性窒素等の臭気成
分を吸着する能力を有するため、コンポスト化装置８か
ら発生する臭気を減少させることもできる。Therefore, when this mixture is introduced into the composting device 8 via the line L8 (composting step) and composting is performed after improving the air permeability, the activity of the aerobic microorganisms is activated and the mixture is removed. Fermentation can be performed efficiently. In addition, prior to composting, the solids that have been separated into solids and liquids are carbonized, so that the resulting compost does not include litter such as rice straw, feed lees, and waste such as pig hair. . That is, according to the present invention,
Good quality compost can be easily obtained. Further, since the carbide contained in the mixture has the ability to adsorb odor components such as ammoniacal nitrogen, the odor generated from the composting device 8 can be reduced.
【００３１】なお、本発明は、前述した実施形態に限定
されるものではない。例えば、上述した実施形態では、
家畜糞尿の処理について説明したが、本発明は、家畜糞
尿に限らず、生ごみ、し尿、下水等の有機性廃棄物の処
理にも適用することができる。The present invention is not limited to the above embodiment. For example, in the embodiment described above,
Although the treatment of livestock manure has been described, the present invention is not limited to livestock manure but can be applied to the treatment of organic waste such as garbage, human waste, and sewage.
【００３２】また、上記実施形態では、生物反応槽４か
ら排出される余剰汚泥は、脱水機５により脱水されてい
るが、余剰汚泥を脱水機５で脱水せず、直接混合装置６
に導入してもよい。この場合でも、余剰汚泥に炭化物が
混合されるので、余剰汚泥の水分調整が可能である。In the above embodiment, the excess sludge discharged from the biological reaction tank 4 is dehydrated by the dehydrator 5, but the excess sludge is not dehydrated by the dehydrator 5, but is directly mixed by the mixing device 6.
May be introduced. Even in this case, since the carbide is mixed with the excess sludge, the water content of the excess sludge can be adjusted.
【００３３】[0033]
【発明の効果】以上説明したように本発明の有機性廃棄
物の処理方法及び装置によれば、生物反応処理で得られ
る余剰汚泥に、炭化処理により得られた炭化物を混合す
ることで、余剰汚泥の水分調整を行うことが可能とな
り、コンポスト化に適した水分を有する余剰汚泥をコン
ポスト化に先立って得ることができる。また、コンポス
ト化に際して、固形物が炭化物とされているため、得ら
れるコンポストには、稲藁等の敷き材、飼料粕、豚毛等
の不用物が含まれることもない。すなわち、本発明によ
れば、良質のコンポストを容易に得ることができる。As described above, according to the method and apparatus for treating organic waste according to the present invention, the excess sludge obtained by the biological reaction treatment is mixed with the carbide obtained by the carbonization treatment to thereby produce the excess waste. The water content of the sludge can be adjusted, and excess sludge having water suitable for composting can be obtained prior to composting. In addition, since the solid matter is converted into a carbide when composting, the resulting compost does not include waste materials such as rice straw, feed lees, and pig hair. That is, according to the present invention, high-quality compost can be easily obtained.
【図１】図１は、本発明の有機性廃棄物の処理装置の一
実施形態を示すフロー図である。FIG. 1 is a flowchart showing an embodiment of an organic waste treatment apparatus of the present invention.
１…家畜糞尿の処理装置（有機性廃棄物の処理装置）、
２…固液分離装置、４…生物反応槽、６…混合装置、７
…炭化装置、８…コンポスト化装置、９…ガス貯留槽
（燃料供給手段）、Ｌ９，Ｌ１０…ライン（燃料供給手
段）。1. ... livestock manure processing equipment (organic waste processing equipment),
2: Solid-liquid separation device, 4: Biological reaction tank, 6: Mixing device, 7
... Carburizing device, 8 ... Composting device, 9 ... Gas storage tank (fuel supply means), L9, L10 ... Line (fuel supply means).
───────────────────────────────────────────────────── 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 7/00 ３０１ Ｃ０５Ｆ 7/00 ３０１Ｄ Ｃ１０Ｂ 53/00 ＺＡＢ Ｃ１０Ｂ 53/00 ＺＡＢＡ Ｃ１０Ｌ 3/06 ＺＡＢ Ｃ１０Ｌ 3/00 ＺＡＢＡ Ｆターム(参考） 4D040 AA01 AA13 AA24 AA25 AA27 4D059 AA01 AA05 BA03 BA27 BA44 BB05 BE08 BE16 BE19 CA07 CC01 4H012 HA01 HA06 4H061 AA02 AA03 CC36 CC47 EE66 GG14 GG48 GG70 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) C05F 7/00 301 C05F 7/00 301D C10B 53/00 ZAB C10B 53/00 ZABA C10L 3/06 ZAB C10L 3 / 00 ZABA F term (reference) 4D040 AA01 AA13 AA24 AA25 AA27 4D059 AA01 AA05 BA03 BA27 BA44 BB05 BE08 BE16 BE19 CA07 CC01 4H012 HA01 HA06 4H061 AA02 AA03 CC36 CC47 EE66 GG14 GG48 GG70
Claims (3)
分離する固液分離工程と、 前記液状物を生物反応槽内で生物反応処理する生物反応
工程と、 前記生物反応槽から余剰汚泥を排出する汚泥排出工程
と、 前記固形物を炭化して炭化物を得る炭化工程と、 前記炭化物と前記余剰汚泥とを混合して混合物を得る混
合工程と、 前記混合物をコンポスト化するコンポスト化工程と、を
含むことを特徴とする有機性廃棄物の処理方法。A solid-liquid separation step of solid-liquid separation of the organic waste into a solid substance and a liquid substance; a biological reaction step of subjecting the liquid substance to a biological reaction in a biological reaction tank; A sludge discharge step of discharging excess sludge, a carbonization step of carbonizing the solid to obtain a carbide, a mixing step of mixing the carbide and the excess sludge to obtain a mixture, and composting the mixture. And a method for treating organic waste.
分離する固液分離装置と、 前記液状物を生物反応処理すると共に余剰汚泥を排出す
る生物反応槽と、 前記固形物を炭化して炭化物を得る炭化装置と、 前記炭化物と前記余剰汚泥とを混合するための混合装置
と、 前記混合装置で得られた混合物をコンポスト化するコン
ポスト化装置と、を備えることを特徴とする有機性廃棄
物の処理装置。2. A solid-liquid separator for solid-liquid separating organic waste into a solid and a liquid, a biological reaction tank for subjecting the liquid to a biological reaction, and discharging excess sludge; A carbonization device for carbonizing to obtain a carbide; a mixing device for mixing the carbide and the excess sludge; and a composting device for composting the mixture obtained by the mixing device. Organic waste treatment equipment.
前記メタン発酵槽で発生したメタンガスを前記炭化装置
の燃料として供給する燃料供給手段を備えることを特徴
とする請求項２に記載の有機性廃棄物の処理装置。3. The bioreactor is a methane fermenter,
The organic waste treatment apparatus according to claim 2, further comprising a fuel supply unit configured to supply methane gas generated in the methane fermentation tank as fuel for the carbonization device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001004091A JP3593501B2 (en) | 2001-01-11 | 2001-01-11 | Organic waste treatment method and apparatus |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001004091A JP3593501B2 (en) | 2001-01-11 | 2001-01-11 | Organic waste treatment method and apparatus |
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| Publication Number | Publication Date |
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| JP3593501B2 JP3593501B2 (en) | 2004-11-24 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007260538A (en) * | 2006-03-28 | 2007-10-11 | Toshiba Corp | Organic waste treatment system |
| CN104446775A (en) * | 2014-11-21 | 2015-03-25 | 中国农业科学院农业资源与农业区划研究所 | Granular organic composite straw fertilizer |
-
2001
- 2001-01-11 JP JP2001004091A patent/JP3593501B2/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007260538A (en) * | 2006-03-28 | 2007-10-11 | Toshiba Corp | Organic waste treatment system |
| CN104446775A (en) * | 2014-11-21 | 2015-03-25 | 中国农业科学院农业资源与农业区划研究所 | Granular organic composite straw fertilizer |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3593501B2 (en) | 2004-11-24 |
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