JP3259775B2 - Sludge decomposition equipment - Google Patents

Sludge decomposition equipment

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Publication number
JP3259775B2
JP3259775B2 JP22599499A JP22599499A JP3259775B2 JP 3259775 B2 JP3259775 B2 JP 3259775B2 JP 22599499 A JP22599499 A JP 22599499A JP 22599499 A JP22599499 A JP 22599499A JP 3259775 B2 JP3259775 B2 JP 3259775B2
Authority
JP
Japan
Prior art keywords
sludge
tank
decomposition treatment
treatment apparatus
pipe
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.)
Expired - Fee Related
Application number
JP22599499A
Other languages
Japanese (ja)
Other versions
JP2001047094A (en
Inventor
一徳 木幡
Original Assignee
一徳 木幡
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Filing date
Publication date
Application filed by 一徳 木幡 filed Critical 一徳 木幡
Priority to JP22599499A priority Critical patent/JP3259775B2/en
Publication of JP2001047094A publication Critical patent/JP2001047094A/en
Application granted granted Critical
Publication of JP3259775B2 publication Critical patent/JP3259775B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/20Sludge processing
    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/78Recycling of wood or furniture waste

Landscapes

  • Treatment Of Sludge (AREA)
  • Processing Of Solid Wastes (AREA)

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】本発明は浄化槽などに沈殿し
た汚泥を分解消滅させる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 an apparatus for eliminating sludge settled in a septic tank or the like.

【0002】[0002]

【従来の技術】一般に、下水道施設が完備していない地
域にある集合住宅や学校、病院、店舗、工場などでは汚
水処理装置を単独で設置して、排出される生活廃水や工
場廃水などを処理してから河川などに放流している。こ
の汚水処理装置1は、例えば図4に示すように台所や風
呂、洗面所、トイレなどの廃水2を汚泥沈殿槽3に導い
て、ここで廃水2中に含まれる汚泥4を沈殿させた後、
廃水2を一次曝気槽5に導き、ブロアーにより曝気槽5
の底面側から空気6を供給して廃水2中に含まれる有機
物質を微生物により分解させる。
2. Description of the Related Art In general, sewage treatment devices are installed independently in apartment buildings, schools, hospitals, stores, factories, etc. in areas where sewerage facilities are not fully equipped, and the discharged wastewater and factory wastewater are treated. After that, they are released into rivers. The sewage treatment apparatus 1 guides waste water 2 from a kitchen, bath, lavatory, toilet, or the like to a sludge sedimentation tank 3 as shown in FIG. 4, for example, where the sludge 4 contained in the waste water 2 is precipitated. ,
The wastewater 2 is guided to the primary aeration tank 5 and is blown by the blower 5.
The air 6 is supplied from the bottom side of the wastewater to decompose organic substances contained in the wastewater 2 by microorganisms.

【0003】この後、二次曝気槽7に導き、同様に底面
側から空気6を供給して廃水2中に含まれる有機物質を
微生物により分解させる。次に沈殿薬液槽8に導いて浮
遊している汚泥4を沈殿させてから、上澄液を塩素など
の薬液9で消毒してから外部に放流していた。またこの
沈殿薬液槽8で沈殿した汚泥4には有機物を分解する微
生物が多量に含まれているので、これをポンプ10で汲
み上げて、二次曝気槽7に戻していた。
[0003] After that, the wastewater 2 is guided to a secondary aeration tank 7 and air 6 is similarly supplied from the bottom side to decompose organic substances contained in the wastewater 2 by microorganisms. Next, the suspended sludge 4 was led to the precipitating solution tank 8 to settle, and then the supernatant was disinfected with a chemical solution 9 such as chlorine and then discharged outside. Further, since the sludge 4 precipitated in the precipitating solution tank 8 contains a large amount of microorganisms that decompose organic substances, it is pumped up by the pump 10 and returned to the secondary aeration tank 7.

【0004】しかしながら、廃水2が最初に流入する汚
泥沈殿槽3には多量の汚泥4が含まれ、ここで大部分沈
殿するので、次第に汚泥4が槽内に堆積していく。通
常、汚泥沈殿槽3の大きさは廃水量により設計されてい
るが、汚泥4は堆積していくため定期的にこれを除去す
る必要がある。従来は廃棄物処理業者がバキュームカー
で汚泥沈殿槽3に堆積した汚泥4を汲み取り、これを処
分場まで運搬して、埋め立て処分や焼却処分していた。
However, the sludge sedimentation tank 3 into which the wastewater 2 first flows in contains a large amount of sludge 4, and most of the sludge is settled here, so that the sludge 4 gradually accumulates in the tank. Usually, the size of the sludge sedimentation tank 3 is designed according to the amount of wastewater. However, since the sludge 4 accumulates, it is necessary to periodically remove the sludge. Conventionally, a waste disposal company pumps up the sludge 4 deposited in the sludge sedimentation tank 3 using a vacuum car, transports it to a disposal site, and performs landfill disposal or incineration.

【0005】このように汚水処理装置1を最適条件で運
転維持していくためには、必然的に堆積してくる汚泥4
を定期的に除去しなければならず、このための回収や運
搬、処理に多大のコストがかかり、設置者の維持管理費
や処分費の負担だけではなく、自治体にとっても処分場
の確保など問題がありその対策が望まれていた。
[0005] In order to maintain the operation of the sewage treatment apparatus 1 under the optimum conditions, the sludge 4 inevitably accumulates.
Must be removed on a regular basis, which requires enormous costs for collection, transportation, and disposal. Not only is the burden of maintenance and disposal costs for installers, but also local governments have issues such as securing disposal sites. There was a need for countermeasures.

【0006】また一般家庭や、ホテル、レストラン、病
院あるいは給食センターの厨房、食品工場などから出る
食品残渣(生ごみ)は、一般にゴミ回収車により回収さ
れて、ゴミ焼却場で焼却するか、あるいは廃棄物処理場
で埋め立て処分している。しかしながら野菜や肉、魚な
どの調理の際に出る廃棄物や食べ残しなどの生ごみは水
分含有率が高いため単独では焼却することができない。
また近年、埋め立て処分場も不足していることから、生
ごみを排出する施設では現場で処分することが望まれて
いる。
Food residues (garbage) from general households, hotels, restaurants, hospitals or catering centers, food factories, etc. are generally collected by garbage trucks and incinerated at garbage incineration plants, or Landfill at a waste disposal site. However, garbage such as wastes and leftovers produced during cooking of vegetables, meat, fish, etc. cannot be incinerated alone due to its high moisture content.
In recent years, there is also a shortage of landfill sites, and it is desired that facilities that discharge garbage dispose of it at the site.

【0007】このため大量に食品残渣が排出される施設
で使用できる処理装置が種々開発されており、例えば食
品残渣を発酵分解して堆肥を作る装置が開発されてい
る。この発酵分解方式は、好気性微生物を主成分として
食品残渣を発酵させて堆肥化するものであり、得られた
堆肥は土壤改良剤として有効利用される。しかしながら
堆肥化する方法では食品残渣の種類によっては発酵でき
ず、腐敗して悪臭が発生することがある。
[0007] For this reason, various treatment apparatuses have been developed that can be used in facilities that discharge a large amount of food residues. For example, an apparatus for producing compost by fermenting and decomposing food residues has been developed. In this fermentation decomposition method, a food residue is fermented with an aerobic microorganism as a main component and composted, and the obtained compost is effectively used as a soil conditioner. However, in the method of composting, depending on the type of food residue, fermentation is not possible, and it may rot and produce a bad smell.

【0008】また製造された堆肥は、処理槽から一旦、
排出しないと次の処理が行なえず、また生産された堆肥
を製品として販売するためには、梱包や保管、輸送など
煩雑な手間がかかり、学校や病院、ホテル、レストラン
などの施設ではこれを販売するルートの確立が難しいた
め、製造された堆肥の処分が問題となってきている。
[0008] The produced compost is temporarily removed from the treatment tank.
If it is not discharged, the next processing cannot be performed, and selling compost produced as a product requires complicated labor such as packing, storage, and transportation, and it is sold at facilities such as schools, hospitals, hotels, and restaurants. Since it is difficult to establish a route for composting, disposal of manufactured compost has become a problem.

【0009】[0009]

【発明が解決しようとする課題】本発明は上記問題点を
解決し、小型の装置により、汚水処理装置に沈殿した汚
泥を汲み取ることなく、また排出された食品残渣をその
まま現場で分解消滅させて、汚泥や食品残渣の回収や運
搬、処分の手間を省いて費用を削減した汚泥分解処理装
置を提供するものである。
SUMMARY OF THE INVENTION The present invention solves the above-mentioned problems, and uses a small-sized apparatus to eliminate sludge settled in a sewage treatment apparatus and to eliminate the discharged food residue as it is on site. Another object of the present invention is to provide a sludge decomposing / treating apparatus in which the labor for collecting, transporting, and disposing of sludge and food residues is reduced and the cost is reduced.

【0010】[0010]

【課題を解決するための手段】本発明の請求項1記載の
汚泥分解処理装置は、多孔金属板で側壁を形成した筒状
の分解処理槽の内部に、温水配管や電熱線などの加熱手
段を設けると共に、木質チップからなる床材を充填し、
前記分解処理槽の上部に汚泥を槽内にポンプで供給する
導入管を接続し、分解処理槽の底部に処理した排水を外
部に排出する排水管を取付けると共に、この排水管に止
水弁を取付て、前記床材に含浸保持させた汚泥を、大気
と接触状態で好気性微生物と嫌気性微生物とにより消化
分解することを特徴とするものである。
According to a first aspect of the present invention, there is provided a sludge decomposing apparatus according to the first aspect of the present invention, wherein a heating means such as a hot water pipe or a heating wire is provided inside a cylindrical decomposition processing tank having a side wall formed of a porous metal plate. And filling with flooring made of wood chips,
An inlet pipe for supplying sludge by a pump into the tank is connected to the upper part of the decomposition tank, and a drain pipe for discharging treated wastewater to the outside is attached to the bottom of the decomposition tank. The sludge attached and impregnated and held in the floor material is digested and decomposed by aerobic microorganisms and anaerobic microorganisms in contact with the atmosphere.

【0011】本発明の請求項2記載の汚泥分解処理装置
は、木質チップからなる床材の粒径を0.2〜5mmとし
たことを特徴とするものである。また請求項3記載の汚
泥分解処理装置は、分解処理槽の側壁を多孔金属板で二
重に形成し、この間に加熱手段をらせん状に配置したこ
とを特徴とするものである。
A sludge decomposition treatment apparatus according to a second aspect of the present invention is characterized in that the particle size of the floor material made of wood chips is 0.2 to 5 mm. Further, the sludge decomposition treatment apparatus according to claim 3 is characterized in that the side wall of the decomposition treatment tank is double-formed with a porous metal plate, and the heating means is spirally arranged between the side walls.

【0012】本発明の請求項4記載の汚泥分解処理装置
は、分解処理槽の上部に設けられた導入管の先端に、多
数の通水孔を開孔した拡散パイプを、床材の内部に埋設
して取付けたことを特徴とするものである。更に請求項
5記載の汚泥分解処理装置は、木質チップからなる床材
に、好気性微生物と嫌気性微生物を保持させたことを特
徴とするものである。
In the sludge decomposition treatment apparatus according to a fourth aspect of the present invention, a diffusion pipe having a large number of water passage holes is provided at the end of an introduction pipe provided at an upper part of the decomposition treatment tank, inside the floor material. It is characterized by being buried and attached. Further, the sludge decomposition treatment apparatus according to claim 5 is characterized in that a floor material made of wood chips holds aerobic microorganisms and anaerobic microorganisms.

【0013】[0013]

【発明の実施の形態】以下本発明の実施の一形態を図1
ないし図3を参照して詳細に説明する。図において12
は汚泥分解処理装置で、これは図1に示すように汚水処
理装置1の近傍に設置されている。この汚泥分解処理装
置12は、汚水処理装置1の汚泥沈殿槽3の底部側まで
挿入された導入管13に接続され、その下端にポンプ1
4が設けられている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the present invention is shown in FIG.
This will be described in detail with reference to FIG. In the figure, 12
Is a sludge decomposition treatment device, which is installed near the sewage treatment device 1 as shown in FIG. This sludge decomposition treatment device 12 is connected to an introduction pipe 13 inserted to the bottom side of the sludge sedimentation tank 3 of the sewage treatment device 1 and has a pump 1 at its lower end.
4 are provided.

【0014】汚泥分解処理装置12の内部構造は図2に
示すように、分解処理槽15はステンレス板などで円筒
状に形成され、その外部側壁16は円筒状の多孔金属板
で形成され、この内側に間隔をおいて円筒状の多孔金属
板で形成された内部側壁17が設けられて二重管構造に
なっている。前記導入管13は分解処理槽15の蓋板1
8を貫通して槽内に導かれ、この先端に拡散パイプ19
が接続されている。この拡散パイプ19は下端と側壁が
多孔金属板で形成されている。
As shown in FIG. 2, the internal structure of the sludge decomposition treatment device 12 is such that the decomposition treatment tank 15 is formed of a stainless steel plate or the like in a cylindrical shape, and the outer side wall 16 is formed of a cylindrical porous metal plate. An inner side wall 17 formed of a cylindrical porous metal plate is provided at intervals on the inner side to form a double tube structure. The introduction pipe 13 is a cover plate 1 of a decomposition treatment tank 15.
8 and is guided into the tank.
Is connected. The lower end and side walls of the diffusion pipe 19 are formed of a porous metal plate.

【0015】また多孔金属板で形成された外部側壁16
と内部側壁17との間の円筒空間にはらせん状の温水パ
イプ20が設置され、その流入管と排水管は図示しない
外部の温水ボイラーに接続されている。また分解処理槽
15の中心側の拡散パイプ19の下方にはらせん状の電
熱ヒーター21が設けられ、これは槽外に引出されてス
イッチ22を介して電源23に接続されている。また槽
内には温度センサー24が設けられ、これは制御器26
に接続されている。
An outer side wall 16 formed of a perforated metal plate
A spiral hot water pipe 20 is provided in a cylindrical space between the inner side wall 17 and the inner pipe 17, and its inflow pipe and drain pipe are connected to an external hot water boiler (not shown). A helical electric heater 21 is provided below the diffusion pipe 19 on the center side of the decomposition tank 15, and is drawn out of the tank and connected to a power source 23 via a switch 22. Further, a temperature sensor 24 is provided in the tank, and is provided with a controller 26.
It is connected to the.

【0016】また分解処理槽15の底板27は中心に向
かって傾斜し、この中心部に排水管28が接続されてい
る。この排水管28には止水弁となる電磁弁29が設け
られ、これと前記ポンプ14とは制御器26に接続さ
れ、タイマーによりポンプ14の運転に連動して電磁弁
29を制御し、排水管28を遮断するようになってい
る。また排水管28は図1に示すように汚水処理装置1
の二次曝気槽7に導かれて、処理した排水を戻すように
なっている。なお汚水処理装置1の構成は図4と同様で
ある。
The bottom plate 27 of the decomposition tank 15 is inclined toward the center, and a drain pipe 28 is connected to the center. The drain pipe 28 is provided with an electromagnetic valve 29 serving as a water stop valve. The electromagnetic valve 29 is connected to the controller 26, and the electromagnetic valve 29 is controlled by a timer in conjunction with the operation of the pump 14, and the drain valve 28 is drained. The tube 28 is shut off. The drain pipe 28 is connected to the sewage treatment apparatus 1 as shown in FIG.
Is returned to the secondary aeration tank 7 to return the treated wastewater. The configuration of the sewage treatment apparatus 1 is the same as that in FIG.

【0017】また分解処理槽15の内部には図2に示す
ように、細菌の住み家となる床材30が充填されてい
る。この床材30としては例えば、杉チップや桧チップ
などの多孔質の木質チップが好ましい。この床材30は
原木を粉砕して、粉末部分を除去したものでその粒径は
0.2〜5mmの範囲が望ましい。この場合、粒径が0.
2mm未満では、濾過材として目詰まりを生じ易く、また
床材30同志の隙間が狭くなって外気と接触しなくな
り、好気性細菌の活動が阻害されるからである。また粒
径が5mmを越えると、単位体積当りの表面積が小さくな
り、汚泥4の十分な保水能力と分解能力が得られなくな
るからである。なお特に粒径が0.5〜3mmの範囲が最
も望ましい。
As shown in FIG. 2, the inside of the decomposition treatment tank 15 is filled with a floor material 30 which becomes a house for bacteria. As the floor material 30, for example, a porous wood chip such as a cedar chip or a cypress chip is preferable. The floor material 30 is obtained by pulverizing raw wood to remove a powder portion, and its particle size is preferably in the range of 0.2 to 5 mm. In this case, the particle size is 0.
If it is less than 2 mm, clogging is likely to occur as a filtering material, and the gap between the flooring materials 30 is narrowed so that the flooring material 30 does not come into contact with the outside air, thereby inhibiting the activity of aerobic bacteria. On the other hand, if the particle size exceeds 5 mm, the surface area per unit volume becomes small, so that the sludge 4 cannot have a sufficient water retention ability and decomposition ability. Particularly, the particle size is most preferably in the range of 0.5 to 3 mm.

【0018】また前記外部側壁16と内部側壁17を構
成する多孔金属板としてはパンチングメタルや金網、ラ
ス材などでも良く、外部側壁16の通気孔は平均直径が
10〜15mm程度が好ましく、内部側壁17はこれより
やや小さい平均直径が5〜8mm程度が好ましい。
The perforated metal plate forming the outer side wall 16 and the inner side wall 17 may be a punched metal, a wire mesh, a lath material, or the like. The ventilation hole of the outer side wall 16 preferably has an average diameter of about 10 to 15 mm. 17 preferably has a slightly smaller average diameter of about 5 to 8 mm.

【0019】また前記導入管13の先端に接続された拡
散パイプ19は、充填した床材30の上面から数十cm深
く埋め込まれ、汚泥4を分解処理槽15内に注入する時
に、均一に分散させると共に、空気の巻き込みを防止す
るようになっている。また拡散パイプ19の側壁を構成
する多孔金属板の通水孔は平均直径が10〜16mm程度
が好ましい。
The diffusion pipe 19 connected to the tip of the introduction pipe 13 is buried several tens cm deep from the upper surface of the filled flooring 30, and is uniformly dispersed when the sludge 4 is injected into the decomposition tank 15. At the same time as preventing the entrainment of air. It is preferable that the water holes of the porous metal plate constituting the side wall of the diffusion pipe 19 have an average diameter of about 10 to 16 mm.

【0020】次に上記装置により汚水処理装置1の汚泥
4を分解消滅処理する方法について説明する。廃水2中
には3〜5%程度の汚泥4が含まれており、これが汚水
処理装置1の汚泥沈殿槽3に最初に流入し、ここで大部
分沈殿して、次第に汚泥4が槽内に堆積していく。汚泥
4が槽内に堆積したら例えば1〜4日に1回、ポンプ1
4を運転して汚泥4を汲み上げ、導入管13を通して分
解処理槽15内に導く。このとき制御器26により電磁
弁29は開いた状態にしておく。
Next, a method of treating the sludge 4 of the sewage treatment apparatus 1 by the above apparatus will be described. The wastewater 2 contains about 3 to 5% of sludge 4, which first flows into the sludge settling tank 3 of the sewage treatment apparatus 1, where most of the sludge is settled, and the sludge 4 gradually enters the tank. It accumulates. When the sludge 4 accumulates in the tank, for example, once every 1 to 4 days, the pump 1
4 is operated to pump up the sludge 4 and to lead it into the decomposition treatment tank 15 through the introduction pipe 13. At this time, the controller 26 keeps the solenoid valve 29 open.

【0021】また汚泥4の供給量は、床材30の10容
積部に対して汚泥4が2〜5容積部となる範囲が好まし
い。導入管13を通して供給された汚泥4は先端に接続
した拡散パイプ19の側面と底面から充填した床材30
内に流出していく。拡散パイプ19は、床材30の上面
から数十cm深く埋め込まれているので、空気の巻き込み
を防止しながら全体に広がって床材30に浸透していき
ここに含浸、保水される。
The amount of the sludge 4 to be supplied is preferably in a range where the sludge 4 is 2 to 5 parts by volume with respect to 10 parts by volume of the floor material 30. The sludge 4 supplied through the introduction pipe 13 is filled with floor material 30 filled from the side and bottom of the diffusion pipe 19 connected to the tip.
Spill out into Since the diffusion pipe 19 is buried several tens of cm deep from the upper surface of the flooring material 30, it spreads throughout while permeating the flooring material 30 while preventing air from being entrained, and is impregnated and retained therein.

【0022】この場合、分解処理槽15は外部側壁16
と内部側壁17が多孔板で形成され、外気と連通してい
るが、床材30の全体の保水量より少ない量の汚泥4を
供給して含浸させているので、汚泥4は床材30に保持
されて外部に流失しない。
In this case, the decomposition tank 15 is provided on the outer side wall 16.
And the inner side wall 17 is formed of a perforated plate and communicates with the outside air. However, since the sludge 4 is supplied and impregnated in an amount smaller than the entire water holding capacity of the floor material 30, the sludge 4 It is retained and does not flow out.

【0023】所定量の汚泥4を注入したらポンプ14を
止めて、暫くしてから電磁弁29を閉じる。この後、ら
せん状の温水パイプ20に温水を供給すると共に、らせ
ん状の電熱ヒーター21に通電して、床材30に含浸保
持された汚泥4を加熱する。温水パイプ20と電熱ヒー
ター21の温度は40℃程度にして汚泥4を加熱する。
When a predetermined amount of sludge 4 has been injected, the pump 14 is stopped, and after a while, the solenoid valve 29 is closed. Thereafter, hot water is supplied to the spiral hot water pipe 20 and the spiral electric heater 21 is energized to heat the sludge 4 impregnated and held in the flooring 30. The temperature of the hot water pipe 20 and the electric heater 21 is set to about 40 ° C. to heat the sludge 4.

【0024】汚泥沈殿槽3内の汚泥4には好気性微生物
と嫌気性微生物が繁殖しており、これらの微生物を含む
汚泥4が多孔質の床材30に吸着すると、ここが住み家
となって、汚泥4に含まれる有機物を発酵分解して繁殖
していく。約4時間位で汚泥4の発酵が進んで40℃程
度に温度が上昇してきたら、これを温度センサー24で
検知して、温水の供給と通電を停止する。この後、更に
自家発酵が進行して温度が50〜70℃に上昇して急速
に分解が進行して炭酸ガスと水に分解される。
An aerobic microorganism and an anaerobic microorganism are breeding in the sludge 4 in the sludge sedimentation tank 3, and when the sludge 4 containing these microorganisms is adsorbed on the porous floor material 30, it becomes a dwelling house. Then, the organic matter contained in the sludge 4 is fermented and decomposed and propagated. When the fermentation of the sludge 4 proceeds in about 4 hours and the temperature rises to about 40 ° C., this is detected by the temperature sensor 24, and the supply of hot water and the supply of electricity are stopped. Thereafter, the self-fermentation further proceeds, the temperature rises to 50 to 70 ° C., and the decomposition proceeds rapidly to be decomposed into carbon dioxide and water.

【0025】本発明の装置では、汚泥4を含浸させると
床材30の隙間が汚泥4で満たされ、この状態では外気
と遮断されて嫌気性微生物の活動が活発になる。更に汚
泥4が流下し、その水分が次第に蒸発していくと粒状の
床材30の間に隙間が生じてくる。床材30は、多孔金
属板で外部側壁16と内部側壁17を形成した筒状の分
解処理槽15の内部に充填されているので、多孔金属板
を通して外気が流入し、更に粒状の床材30の隙間を通
って外気が流入して、床材30の表面は酸素と接触した
状態となって好気性微生物の活動が活発になる。
In the apparatus of the present invention, when the sludge 4 is impregnated, the gap between the flooring materials 30 is filled with the sludge 4, and in this state, it is shut off from the outside air and the activity of the anaerobic microorganisms becomes active. Furthermore, when the sludge 4 flows down and the water gradually evaporates, a gap is generated between the granular flooring materials 30. Since the floor material 30 is filled in the cylindrical decomposition treatment tank 15 having the outer side wall 16 and the inner side wall 17 formed of a perforated metal plate, outside air flows through the perforated metal plate, and the granular floor material 30 The outside air flows in through the gap, and the surface of the floor material 30 comes into contact with oxygen, and the activity of the aerobic microorganisms becomes active.

【0026】このように、多孔金属板で形成された分解
処理槽15の内部に木質チップからなる床材30を充填
して、ここに汚泥4を含浸保水させることにより側壁か
らの流失を防止しながら、好気性微生物と嫌気性微生物
に最も適した活動環境が形成されて、汚泥4に含まれる
有機物を効率よく炭酸ガスと水に分解して消滅させるこ
とができる。
As described above, the inside of the decomposition treatment tank 15 formed of a perforated metal plate is filled with the floor material 30 made of wood chips, and the sludge 4 is impregnated and held therein, thereby preventing runoff from the side wall. However, an activity environment most suitable for the aerobic microorganisms and the anaerobic microorganisms is formed, and the organic matter contained in the sludge 4 can be efficiently decomposed into carbon dioxide and water and eliminated.

【0027】このように床材30で保持させた状態で1
2〜24時間程度で汚泥4が炭酸ガスと水に分解して消
滅する。また汚泥沈殿槽3内に汚泥4が堆積してきた
ら、再びポンプ14を運転して汚泥4を汲み上げ、導入
管13を通して分解処理槽15内に導くと同時に電磁弁
29を開く。この結果、床材30に保持されていた水
は、排水管28を通って汚水処理装置1の二次曝気層7
に戻される。また床材30に保持されていた水の排水と
共に、今度は上方から汚泥4が送り込まれてくるので、
ポンプ14を所定時間運転してから、分解し終わった水
の排水が完了した時点で電磁弁29を閉じて、以下同様
の動作を繰り返して行なう。
In the state where the floor material 30 is held,
In about 2 to 24 hours, the sludge 4 decomposes into carbon dioxide and water and disappears. When the sludge 4 accumulates in the sludge settling tank 3, the pump 14 is again operated to pump up the sludge 4, guide the sludge 4 into the decomposition treatment tank 15 through the introduction pipe 13, and simultaneously open the electromagnetic valve 29. As a result, the water retained in the floor material 30 passes through the drain pipe 28 and passes through the secondary aeration layer 7 of the sewage treatment apparatus 1.
Is returned to. In addition, the sludge 4 is sent in from the upper side together with the drainage of the water held in the flooring 30.
After the pump 14 has been operated for a predetermined time, the solenoid valve 29 is closed when the decomposed water is completely drained, and the same operation is repeated.

【0028】なお分解処理槽15の側壁が多孔金属板で
形成された外部側壁16と内部側壁17とで二重構造を
なし、この間にらせん状の温水パイプ20を設けている
ので、この部分が断熱保温層となり、外気温が低い季節
でも汚泥4の温度低下を防止することができる。従って
外気温が高い場所に設置する場合には、外部側壁16だ
けの構造でも良い。
The side wall of the decomposition tank 15 has a double structure of an outer side wall 16 and an inner side wall 17 formed of a porous metal plate, and a helical hot water pipe 20 is provided therebetween. It becomes an adiabatic heat insulating layer, and can prevent the temperature of the sludge 4 from decreasing even in a season when the outside air temperature is low. Therefore, when installing in a place where the outside air temperature is high, a structure having only the outer side wall 16 may be used.

【0029】[0029]

【実施例】分解処理槽15の容量を150リットルと
し、この中に床材30として杉のチップを140リット
ル充填した。この杉のチップの粒度分布は、0.2〜1
mmのものが約30%、1〜2mmのものが約30%、2〜
4mmのものが約40%の割合のチップを充填した。この
汚泥分解処理装置12に事務所から排出されたし尿と生
活雑廃水を汚水処理装置1に送り、この汚泥沈殿槽3内
に沈殿したBOD257の汚泥4を40リットル、分解
処理槽15に供給した。この状態で温水パイプ20と電
熱ヒーター21で4時間加熱した後、加熱を停止して2
0時間処理した。この処理後の水のBODを測定したと
ころ9まで低下していた。
EXAMPLE The capacity of the decomposition tank 15 was set to 150 liters, and 140 liters of cedar chips as the floor material 30 were filled therein. The particle size distribution of this cedar chip is 0.2-1
mm is about 30%, 1-2mm is about 30%,
A 4 mm chip filled about 40% of the chips. The human waste and household wastewater discharged from the office into the sludge decomposition treatment device 12 were sent to the wastewater treatment device 1, and 40 liters of the BOD257 sludge 4 precipitated in the sludge sedimentation tank 3 were supplied to the decomposition treatment tank 15. . After heating in this state with the hot water pipe 20 and the electric heater 21 for 4 hours, the heating was stopped and
Treated for 0 hours. When the BOD of the water after this treatment was measured, it was reduced to 9.

【0030】また上記と同じ分解処理槽15を用い、養
豚場の畜糞尿を処理する汚水処理装置1の汚泥沈殿槽3
内に沈殿したBOD1650の汚泥4を40リットル、
分解処理槽15に供給して処理を行なった。この結果、
処理後の水のBODを測定したところ58まで低下して
いた。
The sludge sedimentation tank 3 of the sewage treatment apparatus 1 for treating livestock manure in a pig farm using the same decomposition treatment tank 15 as described above.
40 liters of BOD 1650 sludge 4 precipitated in the
It was supplied to the decomposition treatment tank 15 to perform the treatment. As a result,
When the BOD of the water after the treatment was measured, it was lowered to 58.

【0031】図3は本発明の他の実施の形態を示すもの
で、調理場に設置されているシンク31の廃水管32に
ディスポーザー33を取付け、これを汚泥沈殿槽3に接
続する。この汚泥沈殿槽3内には導入管13が挿着さ
れ、これはポンプ14を介して汚泥分解処理装置12に
接続されている。なお汚泥分解処理装置12の構成は図
2に示すものと同様であが、分解処理槽15に充填した
床材30には予め好気性微生物と嫌気性微生物を添加し
ておく。
FIG. 3 shows another embodiment of the present invention. A disposer 33 is attached to a waste water pipe 32 of a sink 31 installed in a cooking place, and this is connected to a sludge settling tank 3. An introduction pipe 13 is inserted into the sludge settling tank 3, and is connected to a sludge decomposition treatment device 12 via a pump 14. The configuration of the sludge decomposition treatment device 12 is the same as that shown in FIG. 2, but aerobic microorganisms and anaerobic microorganisms are added to the floor material 30 filled in the decomposition treatment tank 15 in advance.

【0032】この装置では調理の際にでる生ゴミをディ
スポーザー33によりスラリー状に粉砕して汚泥沈殿槽
3に送り、ここでポンプ14により汚泥4を導入管13
で汲み上げて汚泥分解処理装置12に供給し、ここで微
生物により炭酸ガスと水に分解して消滅させることがで
きる。
In this apparatus, raw garbage generated during cooking is pulverized into a slurry by a disposer 33 and sent to a sludge settling tank 3, where the sludge 4 is introduced by a pump 14 into an inlet pipe 13.
And supplied to the sludge decomposition treatment device 12, where the microorganisms can be decomposed into carbon dioxide and water and eliminated.

【発明の効果】【The invention's effect】

【0033】以上説明した如く本発明の請求項1記載の
汚泥分解処理装置によれば、小型の装置により、汚水処
理装置に沈殿した汚泥を汲み取ることなく、また排出さ
れた食品残渣をそのまま現場で分解消滅できるので、汚
泥の回収や運搬、処分の手間を省いて処分費用を削減す
ることができる。
As described above, according to the sludge decomposition treatment apparatus of the first aspect of the present invention, the small-sized apparatus does not pump up the sludge settled in the sewage treatment apparatus, and the discharged food residue is directly used on site. Since the sludge can be eliminated, it is possible to reduce the disposal cost by eliminating the trouble of collecting, transporting and disposing of sludge.

【0034】また請求項2記載の汚泥分解処理装置は、
木質チップからなる床材の粒径を0.2〜5mmとしたの
で、汚泥による目詰まりを防止すると共に、微生物の住
み家として必要な体積と、酸素と接触する十分な表面積
を確保することができる。
The sludge decomposition treatment apparatus according to claim 2 is
Since the particle size of the flooring made of wood chips is 0.2 to 5 mm, it is possible to prevent clogging with sludge, and to secure a volume necessary for a microorganism and a sufficient surface area for contact with oxygen. it can.

【0035】また請求項3記載の汚泥分解処理装置は、
分解処理槽の側壁を多孔金属板で二重に形成し、この間
に加熱手段をらせん状に配置したので、外気温が低くな
る場所でも断熱保温作用があるので発酵を促進させるこ
とができる。
The sludge decomposition treatment apparatus according to claim 3 is
Since the side wall of the decomposition treatment tank is double-formed with a perforated metal plate and the heating means is helically arranged between the side walls, the fermentation can be promoted since it has an adiabatic heat retention function even in a place where the outside air temperature is low.

【0036】また請求項4記載の汚泥分解処理装置は、
分解処理槽の上部に設けられた導入管の先端に、多数の
通水孔を開孔した拡散パイプを、床材の内部に埋設して
取付けたので、空気の巻き込みを防止しながら汚泥を全
体に広げて床材に均一に浸透させて含浸、保水させるこ
とができる。
The sludge decomposition treatment apparatus according to claim 4 is
At the end of the introduction pipe provided at the top of the decomposition tank, a diffusion pipe with a large number of water holes was embedded and installed inside the floor material, so that the entire sludge was prevented while preventing air entrapment. It can be spread and spread uniformly on the floor material to impregnate and retain water.

【0037】更に請求項5記載の汚泥分解処理装置は、
木質チップからなる床材に、好気性微生物と嫌気性微生
物を保持させているので、特には調理の際にでる生ゴミ
をディスポーザーによりスラリー状に粉砕した汚泥を効
率よく分解することができる。
Further, the sludge decomposition treatment apparatus according to claim 5 is characterized in that:
Since aerobic microorganisms and anaerobic microorganisms are held on the flooring made of wood chips, sludge obtained by disintegrating garbage produced during cooking into a slurry with a disposer can be efficiently decomposed.

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

【図1】本発明の実施の一形態による汚水処理装置の汚
泥を汚泥分解処理装置で分解処理するシステムを示す説
明図である。
FIG. 1 is an explanatory diagram showing a system for decomposing sludge of a sewage treatment apparatus according to an embodiment of the present invention with a sludge decomposition processing apparatus.

【図2】図1の汚泥分解処理装置を拡大して示す断面図
である。
FIG. 2 is an enlarged sectional view showing the sludge decomposition treatment apparatus of FIG.

【図3】本発明の他の実施の形態によるディスポーザー
により粉砕した生ゴミの汚泥を汚泥分解処理装置で処理
するシステムを示す説明図である。
FIG. 3 is an explanatory diagram showing a system for processing sludge of garbage crushed by a disposer in a sludge decomposition treatment apparatus according to another embodiment of the present invention.

【図4】従来の汚水処理装置を示す断面図である。FIG. 4 is a sectional view showing a conventional sewage treatment apparatus.

【符号の説明】[Explanation of symbols]

1 汚水処理装置 2 廃水 3 汚泥沈殿槽 4 汚泥 5 一次曝気槽 6 空気 7 二次曝気槽 8 沈殿薬液槽 12 汚泥分解処理装置 13 導入管 14 ポンプ 15 分解処理槽 16 外部側壁 17 内部側壁 18 拡散パイプ 20 温水パイプ 21 電熱ヒーター 24 温度センサー 26 制御器 28 排水管 29 電磁弁 30 床材 31 シンク 33 ディスポーザー DESCRIPTION OF SYMBOLS 1 Sewage treatment apparatus 2 Wastewater 3 Sludge settling tank 4 Sludge 5 Primary aeration tank 6 Air 7 Secondary aeration tank 8 Precipitating chemical liquid tank 12 Sludge decomposition processing apparatus 13 Introducing pipe 14 Pump 15 Decomposition processing tank 16 External side wall 17 Internal side wall 18 Diffusion pipe Reference Signs List 20 hot water pipe 21 electric heater 24 temperature sensor 26 controller 28 drain pipe 29 solenoid valve 30 flooring material 31 sink 33 disposer

フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C02F 11/02 B09B 3/00,5/00 Continuation of front page (58) Field surveyed (Int. Cl. 7 , DB name) C02F 11/02 B09B 3/00, 5/00

Claims (5)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 多孔金属板で側壁を形成した筒状の分解
処理槽の内部に、温水配管や電熱線などの加熱手段を設
けると共に、木質チップからなる床材を充填し、前記分
解処理槽の上部に汚泥を槽内にポンプで供給する導入管
を接続し、分解処理槽の底部に処理した排水を外部に排
出する排水管を取付けると共に、この排水管に止水弁を
取付て、前記床材に含浸保持させた汚泥を、大気と接触
状態で好気性微生物と嫌気性微生物とにより消化分解す
ることを特徴とする汚泥分解処理装置。
1. A tubular decomposition processing tank having a side wall formed of a porous metal plate, a heating means such as a hot water pipe or a heating wire is provided, and a floor material made of wood chips is filled therein. An inlet pipe for supplying sludge into the tank by a pump is connected to an upper part of the tank, and a drain pipe for discharging the treated wastewater to the outside is attached to the bottom of the decomposition tank, and a water stop valve is attached to the drain pipe. A sludge decomposition treatment apparatus characterized in that sludge impregnated and held in floor material is digested and decomposed by aerobic microorganisms and anaerobic microorganisms in contact with the atmosphere.
【請求項2】 木質チップからなる床材の粒径を0.2
〜5mmとしたことを特徴とする請求項1記載の汚泥分解
処理装置。
2. The floor material made of wood chips has a particle size of 0.2.
The sludge decomposition treatment apparatus according to claim 1, wherein the sludge decomposition treatment apparatus has a thickness of 5 mm or less.
【請求項3】 分解処理槽の側壁を多孔金属板で二重に
形成し、この間に加熱手段をらせん状に配置したことを
特徴とする請求項1記載の汚泥分解処理装置。
3. The sludge decomposition treatment apparatus according to claim 1, wherein the side walls of the decomposition treatment tank are formed of a double-walled porous metal plate, and the heating means is spirally arranged between the side walls.
【請求項4】 分解処理槽の上部に設けられた導入管の
先端に、多数の通水孔を開孔した拡散パイプを、床材の
内部に埋設して取付けたことを特徴とする請求項1記載
の汚泥分解処理装置。
4. A diffusion pipe having a large number of water holes buried inside a floor material and attached to a tip of an introduction pipe provided at an upper part of the decomposition treatment tank. The sludge decomposition treatment apparatus according to claim 1.
【請求項5】 木質チップからなる床材に、好気性微生
物と嫌気性微生物を保持させたことを特徴とする請求項
1または2記載の汚泥分解処理装置。
5. The sludge decomposition treatment apparatus according to claim 1, wherein an aerobic microorganism and an anaerobic microorganism are held on a flooring made of wood chips.
JP22599499A 1999-08-10 1999-08-10 Sludge decomposition equipment Expired - Fee Related JP3259775B2 (en)

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