JPH08290989A - Treatment of garbage - Google Patents
Treatment of garbageInfo
- Publication number
- JPH08290989A JPH08290989A JP9218195A JP9218195A JPH08290989A JP H08290989 A JPH08290989 A JP H08290989A JP 9218195 A JP9218195 A JP 9218195A JP 9218195 A JP9218195 A JP 9218195A JP H08290989 A JPH08290989 A JP H08290989A
- Authority
- JP
- Japan
- Prior art keywords
- treatment
- product
- waste liquid
- compost
- waste liquor
- 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
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
- 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
Landscapes
- Processing Of Solid Wastes (AREA)
- Fertilizers (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は生ごみを無公害処理する
方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating food waste without pollution.
【0002】[0002]
【従来の技術】現在、生ごみは固形状態のままで焼却や
コンポスト化等により処理している。近年、生ごみの搬
送の便のため、生ごみを破砕して水で搬送する技術が開
発され、海外で一部実用化されている。しかし、破砕処
理物をそのまま下水や環境に排出すれば、下水処理施設
や環境への負荷を強いることになるため、破砕処理物の
汚濁成分の除去が望まれる。その際、破砕処理物を処理
するため必要な要素技術、例えば、固液分離,廃水処
理,固形粒子成分のコンポスト化,汚泥処理,脱臭等の
各単位工程を単に付加しただけではトータルプロセスと
しての処理コストが上昇し、経済性の点で実用化が困難
である。2. Description of the Related Art At present, food waste is treated by incineration or composting in a solid state. In recent years, for the convenience of transporting food waste, a technique for crushing food waste and transporting it with water has been developed and partially put into practical use overseas. However, if the crushed product is discharged as it is to sewage or the environment, it will impose a load on the sewage treatment facility and the environment. Therefore, it is desired to remove the polluted components of the crushed product. At that time, the elemental technology necessary for treating the crushed product, for example, solid-liquid separation, wastewater treatment, composting of solid particle components, sludge treatment, deodorization, etc., can be achieved as a total process simply by adding unit processes. The processing cost increases and it is difficult to put it into practical use in terms of economy.
【0003】生ごみをディスポーザ等の手段で破砕処理
し、水で搬送して固液分離して固形成分と廃液とに分離
し、固形成分に廃液処理で副生する汚泥とを組み合せて
コンポスト化するプロセスはすでに知られている(特開
平6−15794号公報)。これまで廃水処理施設から発生す
る汚泥は引き抜いて別途処分されてきたが、上述のプロ
セスは汚泥を生ごみを破砕処理して得られる固形成分と
同時に処理できる点で経済的に有利である。[0003] Garbage is crushed by a means such as a disposer, conveyed with water and solid-liquid separated to separate a solid component and a waste liquid, and the solid component is combined with sludge produced as a by-product in the waste liquid treatment to form a compost. The process for doing so is already known (Japanese Patent Laid-Open No. 6-15794). Up to now, the sludge generated from the wastewater treatment facility has been extracted and separately disposed, but the above-mentioned process is economically advantageous in that it can be treated simultaneously with the solid component obtained by crushing the garbage.
【0004】しかし、コンポスト化に伴い臭気の強い排
気と、臭気が強くて酸性もしくはアルカリ性を呈するド
レンが副生する。両者の無公害処理が不可欠となる。こ
れらを独立に処理しようとすると処理機構も煩雑にな
り、かつ運転費も増大し、実用に供しうるプロセスには
なり難い。中でも後者のドレンは中性でないため、単独
では一般的な水浄化技術である好気的微生物処理が適用
しにくい。However, with the composting, exhaust gas having a strong odor and drain having a strong odor and exhibiting acidity or alkalinity are produced as by-products. Pollution-free treatment of both is essential. If they are to be processed independently, the processing mechanism becomes complicated, and the operating cost increases, making it difficult for the process to be put to practical use. Among them, the latter drain is not neutral, and thus it is difficult to apply the aerobic microbial treatment, which is a general water purification technique, alone.
【0005】[0005]
【発明が解決しようとする課題】本発明の目的は従来公
知のディスポーザによる破砕を中核とする生ごみ処理プ
ロセスの欠点を改善し、コンポスト化に際し副生する臭
気の強い排気や、臭気が強く酸性もしくはアルカリ性を
呈するドレンを経済的に無公害処理することにある。DISCLOSURE OF THE INVENTION The object of the present invention is to improve the drawbacks of the food waste treatment process, which is centered on the crushing by a conventionally known disposer, and to exhaust the strong odor produced as a by-product during composting and to generate a strong odor and acidity. Alternatively, it is an economical pollution-free treatment of alkaline drainage.
【0006】[0006]
【課題を解決するための手段】本発明の第1の特徴は、
生ごみを破砕し、水で搬送し、固液分離して固形成分と
廃液とに分離し、前記固形成分と、前記廃液とを好気的
に微生物処理する際に副生する汚泥とを合せてコンポス
ト化する方法に於いて、コンポスト化の際に副生する含
臭排気を前記廃液処理の給気に用いることである。The first feature of the present invention is to:
Crush raw garbage, transport with water, separate solid and liquid to separate solid component and waste liquid, combine the solid component and sludge by-produced when aerobically treating the waste liquid with microorganisms In the method for composting, the odorous exhaust gas produced as a by-product during composting is used as the air supply for the waste liquid treatment.
【0007】本発明の第2の特徴は、コンポスト化の含
臭排気の他にコンポスト化の際に副生する含臭ドレンを
前記液廃と合せて処理することである。The second feature of the present invention is that, in addition to the odorous exhaust gas for composting, the odorous drain by-produced during composting is treated together with the liquid waste.
【0008】生ごみの破砕方法は、ディスポーザ,回転
ハンマー,回転ロールを用いる等、ほぼ均一な粒子に破
砕できるものであれば特に限定しない。搬送には生ごみ
重量の2〜20倍量の水を供給し、傾斜した配管中を主
として重力で移送する方法が取られる。破砕と搬送の手
段は集合住宅の各戸に設け、それより下流の要素よりも
多くの系統を配置する。固形粒子成分と廃液との分離方
法も特に限定するものではなく、沈降分離,スクリーン
濾過,遠心分離等、従来公知の技術が適用できる。分離
した固形粒子成分は、後述する廃液の好気的微生物処理
の際に副生する汚泥と共に従来公知のコンポスト化技術
によりコンポストに転換する。コンポスト化の発酵条件
すなわち発酵温度,通気量,混合効率等も適宜選択でき
る。発酵温度は常温から70℃の範囲から適宜選択す
る。発酵排気には低級のアルコール,アルデヒド,ケト
ン,有機酸等の臭気成分を含む他、15〜20容積%の
酸素と、その発酵温度における90%以上の相対湿度を
含む。発酵排気の温度は発酵温度にほぼ等しい。The method of crushing food waste is not particularly limited as long as it can crush into substantially uniform particles such as using a disposer, a rotary hammer, a rotary roll. For transportation, a method is used in which water is supplied in an amount of 2 to 20 times the weight of raw garbage and is transferred mainly by gravity in an inclined pipe. The crushing and transportation means will be installed in each house of the housing complex, and more systems will be installed than the downstream elements. The method of separating the solid particle component and the waste liquid is not particularly limited, and conventionally known techniques such as sedimentation separation, screen filtration and centrifugation can be applied. The separated solid particle component is converted into compost by a conventionally known composting technique together with sludge produced as a by-product during aerobic microbial treatment of waste liquid described later. Fermentation conditions for composting, that is, fermentation temperature, aeration rate, mixing efficiency, etc. can be appropriately selected. The fermentation temperature is appropriately selected from the range of normal temperature to 70 ° C. The fermentation exhaust contains odorous components such as lower alcohols, aldehydes, ketones and organic acids, and also contains 15 to 20% by volume of oxygen and 90% or more relative humidity at the fermentation temperature. The temperature of the fermentation exhaust is approximately equal to the fermentation temperature.
【0009】一方、廃液処理は好気的微生物処理であれ
ば特に限定するものではなく、活性汚泥法,微生物固定
床法,散水瀘床法等が用いられる。通気量は生ごみ処理
能力1kg/dに対して5〜100m3/d の範囲にあ
り、コンポスト化での通気量の数倍に相当する。廃液処
理は生ごみの破砕による廃液に加え、その他の生活廃水
も合流させ、同時に処理することもできる。副生汚泥は
いわゆる初沈汚泥,グリース,余剰汚泥,スクリーンか
す,浮上分離汚泥等,廃液処理に伴う固形成分を総称す
る。その分離濃縮方法も、沈降分離,浮上分離,凝集沈
澱,スクリーン圧搾濾過等、特に限定されないが、含水
率を生ごみ破砕の前記固形粒子成分の85%重量%以下
にできれば、コンポスト化での水分蒸発に要する熱供給
を節約できる。On the other hand, the waste liquid treatment is not particularly limited as long as it is an aerobic microbial treatment, and an activated sludge method, a microbial fixed bed method, a water sprinkling bed method or the like can be used. The air flow rate is in the range of 5 to 100 m 3 / d for 1 kg / d of garbage processing capacity, which corresponds to several times the air flow rate in composting. In the waste liquid treatment, in addition to the waste liquid obtained by crushing food waste, other domestic waste water can be combined and treated at the same time. By-product sludge is a general term for so-called initial settled sludge, grease, surplus sludge, screen sludge, floating separation sludge, and other solid components associated with waste liquid treatment. The separating and concentrating method is not particularly limited, such as sedimentation separation, flotation separation, coagulation sedimentation and screen compression filtration, but if the water content can be 85% by weight or less of the solid particle component of crushed food waste, the water content in composting can be reduced. The heat supply required for evaporation can be saved.
【0010】コンポスト化の際に発酵床に循環して通気
し、途中で除湿してドレンを除去して、酸素消費分だけ
新鮮空気を補充する発酵方法がとられる場合が多い。こ
の際に副生するドレンには有機酸を主体とする酸性成分
を含みpHが3〜5を呈するか、まれにはアンモニアを
含有するためpH8以上に達するものもある。発生量は
循環通気条件や発酵条件により異なるが、生ごみ処理能
力1kg/dで0.4 〜0.9kg/d の範囲にある。ドレ
ンは廃液と共に浄化される。In the case of composting, a fermentation method is often employed in which the fermentation bed is circulated and ventilated, dehumidified in the middle to remove drainage, and fresh air is replenished by oxygen consumption. At this time, the drain produced as a by-product contains an acidic component mainly composed of an organic acid and has a pH of 3 to 5, or rarely contains ammonia, so that the pH reaches 8 or more. The amount of generation varies depending on the circulation and aeration conditions and the fermentation conditions, but it is in the range of 0.4 to 0.9 kg / d with a garbage disposal capacity of 1 kg / d. The drain is purified together with the waste liquid.
【0011】[0011]
【作用】生ごみはディスポーザで破砕され、10mm以下
に破砕されて、水流により垂直及び傾斜配管中を移動し
て固液分離装置に至る。ここで、固形粒子成分と廃液と
に分離する。固形粒子成分は廃液の好気性生物処理で副
生する汚泥と合せてコンポスト化する。コンポスト化で
は、発酵床に通気した空気は除湿して循環使用して酸素
消費分だけ排気し、新鮮空気で置換される。除湿により
生成する含臭ドレンは廃液と共に廃液処理装置に導入
し、溶解有機成分及び臭気成分が分解され浄化される。
一方、コンポスト化装置から排出した含臭含湿排気は廃
液浄化用の含酸素給気として使用し、酸素の供源となる
だけでなく、排気中の臭気成分が分解し脱臭されると共
に湿度の一部が凝縮して浄化される。処理水及び脱臭排
気は系外に排出される。通常、発酵温度、引いては発酵
排気の温度及びドレンの温度は環境温度よりも高いた
め、廃液処理の温度も2〜10℃上昇し、その分だけ分
解速度を上昇し、処理効率が向上する。Function: Garbage is crushed by a disposer, crushed to 10 mm or less, and moved in vertical and inclined pipes by a water flow to reach a solid-liquid separation device. Here, the solid particle component and the waste liquid are separated. The solid particle component is composted together with the sludge produced as a by-product in the aerobic biological treatment of the waste liquid. In composting, the air vented to the fermentation bed is dehumidified and circulated for exhaustion of oxygen consumption and replaced with fresh air. Odor-containing drain generated by dehumidification is introduced into a waste liquid treatment device together with a waste liquid, and dissolved organic components and odorous components are decomposed and purified.
On the other hand, the odorous and moisturized exhaust gas discharged from the composting device is used as an oxygen-containing air supply for purifying the waste liquid, and not only serves as a source of oxygen, but also the odorous components in the exhaust gas are decomposed and deodorized and A part is condensed and purified. Treated water and deodorized exhaust are discharged outside the system. Usually, the fermentation temperature, and hence the temperature of the fermentation exhaust gas and the temperature of the drain are higher than the ambient temperature, so the temperature of the waste liquid treatment also rises by 2 to 10 ° C., and the decomposition rate increases correspondingly, and the treatment efficiency improves. .
【0012】[0012]
(実施例1)集合住宅の各戸で生ごみ1をディスポーザ
で破砕14し、複数戸分を合せて処理するブロック図を
図1に示す。(Example 1) Fig. 1 shows a block diagram in which raw garbage 1 is crushed 14 by a disposer at each house of an apartment house and a plurality of units are combined and processed.
【0013】各戸の厨房に於いて、生ごみ1を水2の供
給下でディスポーザを用いて破砕14し、配管中を水搬
送15し、固液分離16−1して固形粒子成分3と廃液
5を生成する。固形粒子成分3を空気6供給下でコンポ
スト化17して、コンポスト10に転換する。コンポス
ト化17で副生するドレン8は空気6の供給下で廃液5
と共に好気的微生物処理18した後、固液分離16−2
して処理水12と汚泥11に分離する。汚泥11はコン
ポスト化17に返送して固形粒子成分3と共にコンポス
ト化する。一方、コンポスト化17で発生する含臭排気
7は好気的微生物処理18の給気の一部として使用し、
脱臭排気9を得る。In the kitchen of each house, garbage 1 is crushed 14 using a disposer under the supply of water 2, water is conveyed 15 in the pipe, and solid-liquid separation 16-1 is carried out to obtain solid particle component 3 and waste liquid. 5 is generated. The solid particle component 3 is composted 17 under the supply of air 6 and converted into compost 10. The drain 8 produced as a by-product in composting 17 is a waste liquid 5 under the supply of air 6.
After the aerobic microbial treatment 18 together with the solid-liquid separation 16-2
Then, the treated water 12 and the sludge 11 are separated. The sludge 11 is returned to the composting 17 and composted together with the solid particle component 3. On the other hand, the odorous exhaust gas 7 generated by composting 17 is used as a part of the air supply of the aerobic microbial treatment 18,
Deodorizing exhaust 9 is obtained.
【0014】(実施例2)実施例1の生ごみ処理に際
し、生ごみ処理起源の廃液5以外に生活廃水13をも好
気的微生物処理4するブロック図を図2に示す。(Embodiment 2) FIG. 2 is a block diagram showing the aerobic microbial treatment 4 of domestic wastewater 13 in addition to the waste liquid 5 originating from the raw garbage treatment in the raw garbage treatment of the first embodiment.
【0015】生ごみ1の処理に際して、厨房以外から発
生する生活廃水13を固形成分を含むままで水搬送15
により集合し、生ごみ起源の廃液5と共に好気的微生物
処理18して、処理水12と汚泥11を得る。本実施例
の汚泥11には生ごみ起源の他に生活廃水起源の固形粒
子成分を含む。During the processing of food waste 1, domestic wastewater 13 generated from other than the kitchen is transported by water 15 while containing solid components.
And the waste liquid 5 originating from food waste is subjected to aerobic microbial treatment 18 to obtain treated water 12 and sludge 11. The sludge 11 of this embodiment contains solid particle components derived from domestic wastewater in addition to raw garbage.
【0016】(実施例3)実施例2が固形粒子成分を含
むままの生活廃水3を好気的微生物処理4するのに対
し、本実施例は、図3に示すように生ごみを破砕処理1
4した後、生活廃水13と合せて水搬送15し、両者中
の固形粒子成分3と廃液5に分離して各々を処理する。(Example 3) In Example 2, domestic wastewater 3 containing solid particle components is treated aerobically with microorganisms 4, whereas in this Example, garbage is crushed as shown in FIG. 1
After 4, the water is conveyed 15 together with the domestic wastewater 13, and the solid particle component 3 and the waste liquid 5 in both are separated and treated.
【0017】[0017]
【発明の効果】本発明によれば、生ごみの破砕に際し生
成する固形粒子成分及び廃液の好気微生物処理で副生す
る汚泥のコンポスト化に際して発生する含湿発酵排気を
効果的に脱臭し、かつ廃液と副生する含臭ドレンとを同
時にかつ高速で浄化できる。EFFECT OF THE INVENTION According to the present invention, the dehumidification of the humid fermented exhaust gas generated during composting of the sludge by-produced by the aerobic microbial treatment of the solid particle component and the waste liquid produced during the crushing of the garbage is effectively deodorized, Moreover, the waste liquid and the odorous drain produced as a by-product can be purified simultaneously and at high speed.
【図1】本発明の一実施例のプロセスのブロック図。FIG. 1 is a block diagram of the process of one embodiment of the present invention.
【図2】本発明の第二実施例のプロセスのブロック図。FIG. 2 is a block diagram of the process of the second embodiment of the present invention.
【図3】本発明の第三実施例のプロセスのブロック図。FIG. 3 is a block diagram of the process of the third embodiment of the present invention.
1…生ごみ、2…水、3…固形粒子成分、4…好気的微
生物処理、5…廃液、6…空気、7…含臭排気、8…ド
レン、9…脱臭排気、10…コンポスト、11…汚泥、
12…処理水、13…生活廃水、14…破砕、15…水
搬送、16−1,16−2…固液分離。1 ... Garbage, 2 ... Water, 3 ... Solid particle component, 4 ... Aerobic microbial treatment, 5 ... Waste liquid, 6 ... Air, 7 ... Odor containing exhaust, 8 ... Drain, 9 ... Deodorizing exhaust, 10 ... Compost, 11 ... sludge,
12 ... Treated water, 13 ... Domestic wastewater, 14 ... Crushing, 15 ... Water conveyance, 16-1, 16-2 ... Solid-liquid separation.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C05F 17/02 9356−4H C05F 17/02 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification number Office reference number FI technical display location C05F 17/02 9356-4H C05F 17/02
Claims (3)
て固形成分と廃液とに分離し、前記固形成分と、前記廃
液とを好気的に微生物処理する際に副生する汚泥とを合
せてコンポスト化する方法に於いて、コンポスト化の際
に副生する含臭排気を該廃液処理の給気に用いることを
特徴とする生ごみ処理方法。1. A by-product when crushing food waste, transporting it with water, performing solid-liquid separation to separate a solid component and a waste liquid, and subjecting the solid component and the waste liquid to aerobic microbial treatment. In the method of composting together with the sludge, the odor-containing exhaust gas produced as a by-product during composting is used as an air supply for the waste liquid treatment.
気の他にコンポスト化の際に副生する含臭ドレンを前記
廃液と合せて処理する生ごみ処理方法。2. The method for treating food waste according to claim 1, wherein, in addition to the odorous exhaust gas for composting, odorous drain produced as a by-product during composting is treated together with the waste liquid.
搬送するまでプロセスの系統数がそれ以降のプロセスの
系統数より小さい生ごみ処理方法。3. The method for treating food waste according to claim 1, wherein the number of process lines is smaller than the number of process lines after crushing the garbage and transporting it with water.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9218195A JPH08290989A (en) | 1995-04-18 | 1995-04-18 | Treatment of garbage |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9218195A JPH08290989A (en) | 1995-04-18 | 1995-04-18 | Treatment of garbage |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH08290989A true JPH08290989A (en) | 1996-11-05 |
Family
ID=14047274
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9218195A Pending JPH08290989A (en) | 1995-04-18 | 1995-04-18 | Treatment of garbage |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH08290989A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008246373A (en) * | 2007-03-30 | 2008-10-16 | Nishihara Engineering Co Ltd | Garbage disposal system |
CN113680796A (en) * | 2021-08-23 | 2021-11-23 | 江苏省农业科学院 | Efficient pretreatment method for resource utilization of kitchen waste |
-
1995
- 1995-04-18 JP JP9218195A patent/JPH08290989A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008246373A (en) * | 2007-03-30 | 2008-10-16 | Nishihara Engineering Co Ltd | Garbage disposal system |
CN113680796A (en) * | 2021-08-23 | 2021-11-23 | 江苏省农业科学院 | Efficient pretreatment method for resource utilization of kitchen waste |
CN113680796B (en) * | 2021-08-23 | 2023-06-09 | 江苏省农业科学院 | Efficient pretreatment method for recycling kitchen waste |
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