JPH1177095A - Livestock excretion treatment system - Google Patents

Livestock excretion treatment system

Info

Publication number
JPH1177095A
JPH1177095A JP9252800A JP25280097A JPH1177095A JP H1177095 A JPH1177095 A JP H1177095A JP 9252800 A JP9252800 A JP 9252800A JP 25280097 A JP25280097 A JP 25280097A JP H1177095 A JPH1177095 A JP H1177095A
Authority
JP
Japan
Prior art keywords
treated water
livestock
discharged
tank
evaporator
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
JP9252800A
Other languages
Japanese (ja)
Inventor
Michiru Suzuki
美智留 鈴木
Masami Yamamoto
正巳 山本
Kazunori Wakiya
和紀 脇屋
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.)
CHIKUSAN KANKYO HOZEN GIJUTSU
CHIKUSAN KANKYO HOZEN GIJUTSU KENKYU KUMIAI
Original Assignee
CHIKUSAN KANKYO HOZEN GIJUTSU
CHIKUSAN KANKYO HOZEN GIJUTSU KENKYU KUMIAI
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 CHIKUSAN KANKYO HOZEN GIJUTSU, CHIKUSAN KANKYO HOZEN GIJUTSU KENKYU KUMIAI filed Critical CHIKUSAN KANKYO HOZEN GIJUTSU
Priority to JP9252800A priority Critical patent/JPH1177095A/en
Publication of JPH1177095A publication Critical patent/JPH1177095A/en
Pending legal-status Critical Current

Links

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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Abstract

PROBLEM TO BE SOLVED: To provide a novel livestock excretion treatment system preventing the discharge of urine sewage treated water of livestock and mixing sludge removed in a purifying treatment process with livestock excrements and a moisture control material to ferment and dry the resulting mixture and carbonizing the obtained compost to reutilize the same as a soil conditioning material. SOLUTION: A livestock excretion treatment system is equipped with a purifying device 10, an evaporator 20 and a combuster 30 and the treated water of urine sewage purified by the purifying device 10 comes into contact with the exhaust gas discharged from the combuster 30 in the evaporator 20 to receive evaporation action to be conc. and, thereafter, the conc. water is mixed with a compost obtained by fermenting and drying livestock excrements, a moisture control material and sludge and the resulting mixture is carbonized in the combuster 30 while exhaust gas comes into contact with treated water in the evaporator 20 to be discharged to the outside.

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】本発明は養豚場等の畜舎から
排出される家畜のふん尿処理システムに関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a system for treating manure discharged from livestock such as a pig farm.

【0002】[0002]

【発明の背景】従来より養豚場等では家畜のふん尿を浄
化処理あるいは醗酵、乾燥処理した後、河川に放流した
り堆肥として再利用する等の方法がとられてきた。しか
しながら近年、悪臭等の理由から畜舎の建設場所が山地
に移行してきており、畜舎からの処理水が河川源流近く
に放流されたり、また養豚経営の大規模化による排水量
の増大から、養豚場の既存浄化処理施設の浄化能力の範
囲を超え、最終処理水の水質が悪化し、周囲住民の養豚
農家に対する苦情から処理水の放流が不可能になる問題
も発生している。またこれに加えて家畜のふんと浄化処
理工程において除去された汚泥等を醗酵、乾燥させた堆
肥の需要量の減少から、堆肥の売却も困難となる問題も
生じてきている。
BACKGROUND OF THE INVENTION In pig farms and the like, a method of purifying or fermenting livestock excreta has been conventionally used, and then discharged to a river or reused as compost. However, in recent years, the construction sites for livestock pens have shifted to mountainous areas due to foul odors, etc., and the treated water from the livestock breaches is discharged near the headwaters of the rivers. The quality of the final treated water has deteriorated beyond the purification capacity of the existing purification treatment facility, and there has been a problem that it is impossible to discharge the treated water due to complaints from swine farmers around the residents. In addition to this, the demand for compost obtained by fermenting and drying sludge and the like removed in livestock manure and the purification treatment process has decreased, and there has been a problem that it is difficult to sell compost.

【0003】[0003]

【開発を試みた技術的課題】本発明はこのような背景を
認識してなされたものであり、家畜の尿汚水を処理した
後の処理水を無放流化するとともに堆肥を炭化処理し、
土壌改良材として再利用できる新規な家畜ふん尿処理シ
ステムの開発を試みたものである。
[Technical Problems Attempted to Be Developed] The present invention has been made in view of such a background. The present invention has been made to release treated water after treating urinary sewage of livestock and to carbonize compost,
This is an attempt to develop a new livestock manure treatment system that can be reused as a soil conditioner.

【0004】[0004]

【課題を解決するための手段】すなわち請求項1記載の
家畜ふん尿処理システムは、畜舎から排出される家畜の
尿汚水を浄化処理する浄化装置と、浄化処理後の処理水
を蒸発処理する蒸発装置と、家畜のふんと浄化処理の途
中において排出される固形物や汚泥等を醗酵、乾燥させ
た堆肥を炭化または焼却処理する燃焼装置とを具えて成
り、前記浄化装置により浄化された処理水は蒸発装置に
おいて蒸発作用を受けるとともに、濃縮され、その後前
記堆肥と混合され、燃焼装置において炭化または焼却処
理されることを特徴として成るものである。この発明に
よれば、従来浄化処理が施された後、河川に放流される
ことが多かった処理水の無放流化が可能となる。またそ
のため周囲の環境を悪化させることもない。
A livestock manure treatment system according to a first aspect of the present invention comprises a purifying apparatus for purifying livestock wastewater discharged from a barn and an evaporating apparatus for evaporating treated water after the purification processing. And a combustion device for fermenting solids and sludge discharged during the purification process of livestock and carbonizing or incineration of dried compost, and the treated water purified by the purification device is It is subjected to an evaporative action in an evaporator, concentrated, then mixed with the compost, and carbonized or incinerated in a combustion device. According to the present invention, it is possible to eliminate the treated water that has been often discharged into a river after the conventional purification treatment. Therefore, the surrounding environment is not deteriorated.

【0005】また請求項2記載の家畜ふん尿処理システ
ムは、前記請求項1記載の要件に加え、前記浄化処理後
の処理水は、蒸発装置において燃焼装置から排出される
排気ガスと接触し、その廃熱により蒸発作用を受けるこ
とを特徴として成るものである。この発明によれば、燃
焼装置から排出される排気ガスの廃熱を利用して処理水
の蒸発を行うため、システム全体の運転費用、維持費用
が低減できる。
According to a second aspect of the present invention, in addition to the requirement of the first aspect, the treated water after the purification treatment comes into contact with exhaust gas discharged from a combustion device in an evaporator, and the wastewater is treated with the same. It is characterized by being subjected to evaporation by waste heat. According to the present invention, since the treated water is evaporated by using the waste heat of the exhaust gas discharged from the combustion device, the operation cost and the maintenance cost of the entire system can be reduced.

【0006】更にまた請求項3記載の家畜ふん尿処理シ
ステムは、前記請求項1または2記載の要件に加え、前
記燃焼装置より排出される排気ガスは蒸発装置において
処理水と接触した後、外部に放出されることを特徴とし
て成るものである。この発明によれば、排気ガスは処理
水と接触することにより洗浄され、排気ガス中に含まれ
る大気汚染物質を可能な限り軽減させた状態で放出でき
る。
According to a third aspect of the present invention, in addition to the requirements of the first or second aspect, the exhaust gas discharged from the combustion device is contacted with treated water in an evaporator and then discharged to the outside. It is characterized by being released. According to the present invention, the exhaust gas is washed by coming into contact with the treated water, and can be released in a state where air pollutants contained in the exhaust gas are reduced as much as possible.

【0007】更にまた請求項4記載の家畜ふん尿処理シ
ステムは、前記請求項1、2または3記載の要件に加
え、前記燃焼装置において炭化物が生成されることを特
徴として成るものである。この発明によれば、家畜ふん
や汚泥等を醗酵、乾燥させた堆肥を完全燃焼させずに炭
化し、炭化物を生成することにより土壌改良材として利
用・販売でき、システム全体の運転費用、維持費用を低
減できる。
A livestock manure processing system according to a fourth aspect is characterized in that, in addition to the requirements according to the first, second or third aspect, a carbide is generated in the combustion device. According to the present invention, livestock manure and sludge are fermented, carbonized without completely burning the dried compost, and can be used and sold as a soil improvement material by generating carbides. Can be reduced.

【0008】[0008]

【発明の実施の形態】以下本発明を図示の実施の形態に
基づいて説明する。説明にあたっては本発明の家畜ふん
尿処理システムを実質的に構成する家畜ふん尿処理装置
1について説明し、次いでこの装置の作動態様を説明し
ながら併せて家畜ふん尿処理システムについて説明す
る。家畜ふん尿処理装置1は、図1の流れ図に示すよう
に畜舎Aより排出される尿汚水を浄化処理する浄化装置
10と、浄化処理後の処理水を蒸発処理する蒸発装置2
0と、堆肥を焼却または炭化処理する燃焼装置30とを
具えて成るものである。以下各装置の概略について説明
する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below with reference to the illustrated embodiments. In the description, the livestock manure processing apparatus 1 which substantially constitutes the livestock manure processing system of the present invention will be described, and then the livestock manure processing system will be described together with the operation mode of this apparatus. As shown in the flow chart of FIG. 1, the livestock manure treatment device 1 includes a purification device 10 for purifying urine sewage discharged from the barn A, and an evaporator 2 for evaporating treated water after the purification process.
0 and a combustion device 30 for incinerating or carbonizing compost. The outline of each device will be described below.

【0009】先ず浄化装置10について説明する。浄化
装置10は豚舎等の畜舎Aから排出される尿汚水を浄化
処理するものであり、図1に示すように一例として原水
槽11と、固液分離機12と、調整槽13と、嫌気槽1
4と、好気槽15と、沈澱槽16と、凝集沈澱装置17
と、汚泥貯留槽18と、脱水機19とを具えて成るもの
である。原水槽11は畜舎Aから排出される尿汚水を一
旦貯留するものであり、固液分離機12は原水槽11か
ら送られる尿汚水を固液分離するものである。この固液
分離機12は一例としてスクリーンやフィルタ等により
尿汚水を濾過し、固形物を除去するものである。このよ
うな固液分離機12で除去された固形物は醗酵堆肥舎C
に送られる。また畜舎Aから排出される家畜ふんも醗酵
堆肥舎Cに送られる。
First, the purifying device 10 will be described. The purifying apparatus 10 is for purifying urine sewage discharged from a livestock house A such as a piggery. As shown in FIG. 1, as an example, a raw water tank 11, a solid-liquid separator 12, a regulating tank 13, an anaerobic tank, 1
4, aerobic tank 15, sedimentation tank 16, and coagulation sedimentation device 17
And a sludge storage tank 18 and a dehydrator 19. The raw water tank 11 temporarily stores the urine sewage discharged from the barn A, and the solid-liquid separator 12 separates the urine sewage sent from the raw water tank 11 into solid and liquid. The solid-liquid separator 12 filters urine sewage by a screen, a filter, or the like to remove solids. The solid matter removed by the solid-liquid separator 12 is a fermentation compost C
Sent to Livestock dung discharged from the livestock house A is also sent to the fermentation compost house C.

【0010】調整槽13は固液分離機12で固形物が除
去された後の尿汚水を貯留するとともに、嫌気槽14に
一定の流量で尿汚水を送るためのものである。そして嫌
気槽14及び好気槽15は、それぞれ嫌気性微生物及び
好気性微生物により尿汚水中の有機物を分解処理するい
わゆる生物処理を行うものである。そのため好気槽15
では好気性微生物の浄化作用を活発にさせるため、空気
を吹き込んで酸素を溶け込ませる曝気ブロワ15aが付
設され、嫌気槽14では嫌気性微生物の分解作用を活発
にさせるための攪拌機14aが付設される。また沈澱槽
16はこのような生物処理に伴って発生する微生物等の
汚泥を重力沈降により沈澱させ、除去するものである。
The regulating tank 13 is for storing urine sewage from which solids have been removed by the solid-liquid separator 12 and for sending urine sewage to the anaerobic tank 14 at a constant flow rate. The anaerobic tank 14 and the aerobic tank 15 perform so-called biological treatment in which anaerobic microorganisms and aerobic microorganisms respectively decompose organic substances in urine wastewater. Aerobic tank 15
In order to activate the purifying action of aerobic microorganisms, an aeration blower 15a for blowing air to dissolve oxygen is provided, and in the anaerobic tank 14, a stirrer 14a for activating the decomposition action of anaerobic microorganisms is provided. . The sedimentation tank 16 sediments sludge such as microorganisms generated by the biological treatment by sedimentation by gravity sedimentation and removes the sludge.

【0011】凝集沈澱装置17は沈澱槽16により汚泥
等が除去された後の液体中に残存する微細粒子を凝集剤
により多数合一させ、沈澱物として除去するものであ
る。そのためこのような処理は化学処理とも呼ばれてい
る。また凝集沈澱装置17により汚泥等が除去された処
理水は蒸発装置20の中継槽21に送られることとな
る。なお凝集剤は一例としてアルミニウム塩や鉄塩等が
用いられる。汚泥貯留槽18は、沈澱槽16及び凝集沈
澱装置17により除去された汚泥等を貯留するものであ
り、脱水機19はこの汚泥貯留槽18から送られる汚泥
等を凝集剤を用いて脱水するものである。
The coagulating sedimentation device 17 is a device that combines a large number of fine particles remaining in the liquid after the sludge or the like is removed by the sedimentation tank 16 with a coagulant and removes them as a precipitate. Therefore, such treatment is also called chemical treatment. The treated water from which the sludge and the like have been removed by the coagulation and sedimentation device 17 is sent to the relay tank 21 of the evaporator 20. As the coagulant, an aluminum salt, an iron salt or the like is used as an example. The sludge storage tank 18 stores sludge and the like removed by the sedimentation tank 16 and the coagulation sedimentation device 17, and the dehydrator 19 dewaters the sludge and the like sent from the sludge storage tank 18 using a coagulant. It is.

【0012】次に蒸発装置20について説明する。蒸発
装置20は浄化処理後の処理水の一部を蒸発させて濃縮
するものであり、浄化装置10から送られてくる処理水
を一旦蓄える中継槽21と、二つの処理水槽22、23
と、充填塔24及び噴霧塔25とを具えて成るものであ
る。中継槽21は浄化装置10より供給された処理水を
一旦貯留した後、処理水槽22に送るためのものであ
る。充填塔24は内部に適宜の充填物が詰められてお
り、上部から処理水槽22より汲み上げられた処理水が
供給されると同時に下部から噴霧塔25を中継して、燃
焼装置30から排出された排気ガスが供給されている。
このため処理水は処理水槽22と充填塔24を循環する
間に排気ガスにより蒸発作用を受けることになる。また
充填物はこの蒸発作用を促進させるため処理水と排気ガ
スとの接触面積を増大させる作用を担っている。
Next, the evaporator 20 will be described. The evaporator 20 is for evaporating and concentrating a part of the treated water after the purification treatment. The evaporator 20 temporarily stores the treated water sent from the purifier 10 and the two treated water tanks 22, 23.
And a packed tower 24 and a spray tower 25. The relay tank 21 is for temporarily storing the treated water supplied from the purification device 10 and then sending the treated water to the treated water tank 22. The packed tower 24 is filled with an appropriate packing material, and the treated water pumped from the treated water tank 22 is supplied from the upper portion, and is simultaneously relayed from the lower portion to the spray tower 25 and discharged from the combustion device 30. Exhaust gas is being supplied.
For this reason, the treated water is subjected to an evaporating action by the exhaust gas while circulating through the treated water tank 22 and the packed tower 24. Further, the filler plays a role of increasing the contact area between the treated water and the exhaust gas in order to promote the evaporation action.

【0013】処理水槽23は以上のような蒸発作用を受
けた処理水を処理水槽22からオーバーフローさせるよ
うに構成されている。そして噴霧塔25も上部からこの
処理水槽23より汲み上げられた処理水が噴霧されると
同時に下部から燃焼装置30より排出される排気ガスが
供給される。このため処理水は処理水槽23と噴霧塔2
5を循環する間に排気ガスにより蒸発作用を受け、濃縮
水となって噴霧塔25の下部より処理水槽23へ排出さ
れる。一方、排気ガスは噴霧塔25及び充填塔24内で
処理水と接触することにより洗浄され、排気ガス内に含
まれた大気汚染物質が濃縮水中に溶け込み除去されるこ
とになる。そして充填塔24から排出された排気ガスは
その後、集塵機により塵が回収され、誘引ファンにより
外部に放出される。
The treated water tank 23 is configured to overflow the treated water subjected to the above-described evaporating action from the treated water tank 22. The spray tower 25 is also sprayed with the treated water pumped from the treated water tank 23 from the upper part, and at the same time, the exhaust gas discharged from the combustion device 30 is supplied from the lower part. Therefore, the treated water is supplied to the treated water tank 23 and the spray tower 2
While circulating through 5, the gas is subjected to an evaporating effect by the exhaust gas, and is discharged as concentrated water from the lower part of spray tower 25 to treated water tank 23. On the other hand, the exhaust gas is washed by coming into contact with the treated water in the spray tower 25 and the packed tower 24, and the air pollutants contained in the exhaust gas are dissolved into the concentrated water and removed. After that, the exhaust gas discharged from the packed tower 24 is collected by a dust collector, and is discharged to the outside by an induction fan.

【0014】次に燃焼装置30について説明する。燃焼
装置30は一例として特開平8−121734号「汚泥
等の炭化・焼却処理方法並びにその装置」に見られるよ
うな炭化処理または焼却処理が必要に応じて選択して行
えるものが適用されるが、炭化処理のみが行えるもので
あっても構わない。なお燃焼装置30の前段に醗酵堆肥
舎Cが設けられており、畜舎Aから排出された家畜ふん
や浄化装置10の固液分離機12により除去された固形
物及び脱水機19により除去された汚泥等をこの醗酵堆
肥舎Cにおいて水分調整材と混合して醗酵、乾燥し、堆
肥にしている。そして燃焼装置30は一例として燃焼炉
31と、燃焼ブロワ32と、燃焼バーナ33と、脱臭バ
ーナ34とを具えて成るものである。燃焼炉31は醗酵
堆肥舎Cより送られる堆肥及び処理水槽23より送られ
る処理水濃縮液等の被処理物を受け入れる供給ホッパ3
5と、この被処理物を燃焼炉31内で満遍なく掻き均す
攪拌部材36と、排気ガスを主に噴霧塔25に排出する
排気口37と、生成した炭化物等を排出する排出口38
とを具えて成るものである。
Next, the combustion device 30 will be described. As the combustion device 30, for example, a device capable of selectively performing carbonization treatment or incineration treatment as required in Japanese Unexamined Patent Publication No. Hei 8-121634, "Method and Apparatus for Carbonization and Incineration of Sludge" is applied. Alternatively, only the carbonization treatment may be performed. A fermentation compost C is provided in front of the combustion device 30. Livestock manure discharged from the barn A, solids removed by the solid-liquid separator 12 of the purification device 10, and sludge removed by the dehydrator 19 are provided. Are fermented in this fermentation compost house C, mixed with a water conditioner, fermented, dried and composted. The combustion apparatus 30 includes, for example, a combustion furnace 31, a combustion blower 32, a combustion burner 33, and a deodorization burner 34. The combustion furnace 31 is a feed hopper 3 for receiving the compost sent from the fermentation composting room C and the treated objects such as the treated water concentrate sent from the treated water tank 23.
5, a stirring member 36 for evenly stirring the object in the combustion furnace 31, an exhaust port 37 for discharging exhaust gas mainly to the spray tower 25, and an outlet port 38 for discharging generated carbides and the like.
It comprises.

【0015】燃焼ブロワ32は、燃焼炉31内に供給さ
れた被処理物に燃焼空気を送るものであり、被処理物の
表面または被処理物の層の中に必要に応じて切り替え可
能に送り込む形態をとるが、被処理物の表面のみに送り
込む形態をとってもよい。これは被処理物を炭化処理す
る場合にはまず被処理物の層において酸素の少ない状態
を作り出すためであり、被処理物を焼却処理する場合に
は被処理物を完全燃焼させるためである。従って炭化処
理のみを行う形態では被処理物の表面のみに燃焼空気を
送り込めればよいことになる。
The combustion blower 32 sends the combustion air to the object supplied into the combustion furnace 31, and switchesably sends the air to the surface of the object or a layer of the object as required. Although it takes a form, a form in which it is fed only to the surface of the object to be processed may be adopted. This is for the purpose of first creating a state of low oxygen in the layer of the object to be treated when carbonizing the object to be treated, and to completely burn the object to be treated when incinerating the object to be treated. Therefore, in a mode in which only the carbonization process is performed, the combustion air only needs to be sent to the surface of the workpiece.

【0016】また脱臭バーナ34は、排気口37の近傍
に設けられ、排気ガスの脱臭を行うとともに、炭化処理
する際、被処理物から揮発する熱分解ガスを燃焼炉31
の上部において燃焼させ、被処理物を炭化処理するに必
要な熱量を放射伝熱として利用するものである。燃焼バ
ーナ33は、被処理物を燃焼させるためのものである。
なお燃焼炉31より排出される排気ガスは主に噴霧塔2
5へ送られる。
A deodorizing burner 34 is provided in the vicinity of the exhaust port 37 to deodorize the exhaust gas and to remove pyrolysis gas volatilized from the processing object at the time of carbonization.
Is burned in the upper part of the refuse, and the amount of heat required to carbonize the object is used as radiant heat transfer. The combustion burner 33 is for burning an object to be processed.
The exhaust gas discharged from the combustion furnace 31 is mainly
Sent to 5.

【0017】次に以上のように構成された家畜ふん尿処
理装置1の作動態様を説明しながら併せて本発明の家畜
ふん尿処理システムについて説明する。 (1)浄化処理 まず豚舎等の畜舎Aより排出された尿汚水は、一旦原水
槽11に貯留された後、固液分離機12により固液分離
される。その後、除去された含水率約85%の固形物
は、醗酵堆肥舎Cに送られて家畜ふん及び水分調整材と
混合され、含水率約30%になるまで醗酵、乾燥され
る。一方、固液分離機12により固形物が除去された後
の尿汚水は調整槽13に送られ、ここで流量が制御され
ながら嫌気槽14に送られる。
Next, the livestock manure processing system of the present invention will be described together with the operation mode of the livestock manure processing apparatus 1 configured as described above. (1) Purification treatment First, urine sewage discharged from a livestock house A such as a piggery is once stored in a raw water tank 11, and then separated into a solid and a liquid by a solid-liquid separator 12. Thereafter, the removed solid matter having a water content of about 85% is sent to the fermentation compost C, mixed with livestock dung and a water conditioner, and fermented and dried until the water content becomes about 30%. On the other hand, the urine sewage from which solids have been removed by the solid-liquid separator 12 is sent to the adjusting tank 13 where it is sent to the anaerobic tank 14 while controlling the flow rate.

【0018】(2)浄化処理(生物処理) 調整槽13から送られた尿汚水は、まず嫌気槽14で嫌
気性微生物(嫌気性細菌)により、次いで好気槽15で
好気性微生物により尿汚水中の有機物の大部分が除去さ
れる。なお尿汚水は好気槽15から再び嫌気槽14へ戻
され、これらを循環する間に好気槽15で有機性窒素や
アンモニア性窒素は硝酸性あるいは亜硝酸性窒素に変換
され、更にこれらは嫌気槽14において窒素ガスに分解
され、尿汚水中の窒素が除去されることとなる。因みに
好気槽15では好気性微生物により尿汚水中の有機物の
うち約半分が微生物の細胞を構成する細胞物質に変換さ
れ、新たに微生物を増殖させ、残りの約半分が二酸化炭
素と水に分解され、尿汚水は浄化されることとなる。ま
た嫌気槽14では嫌気性微生物により尿汚水中の高分子
有機物が加水分解され低分子化し、最終的にはメタンガ
ス及び二酸化炭素に変換されるが、その割合は90%程
度であり、残りは新たな微生物(嫌気性細菌)を増殖さ
せる。以上述べたような生物処理が充分進むと尿汚水中
には微生物等が増えてくる。そしてこのような微生物の
中には非常に多数が集まってフロックといわれる大きな
塊を形成し、沈澱する場合もあり、生物処理が充分にな
された尿汚水は沈澱槽16に送られ、この沈澱物が除去
されることになる。因みにこの沈澱物が一般に汚泥と呼
ばれている。その後、沈澱物たる汚泥は汚泥貯留槽18
に送られ、汚泥が除去された後の液体は凝集沈澱装置1
7に送られる。
(2) Purification (biological treatment) The urine sewage sent from the regulating tank 13 is first subjected to anaerobic microorganisms (anaerobic bacteria) in an anaerobic tank 14 and then to aerobic microorganisms in an aerobic tank 15. Most of the organic matter inside is removed. The urine sewage is returned from the aerobic tank 15 to the anaerobic tank 14 again, and while circulating, the organic nitrogen and ammonia nitrogen are converted into nitric or nitrite nitrogen in the aerobic tank 15, and It is decomposed into nitrogen gas in the anaerobic tank 14, and nitrogen in urine sewage is removed. By the way, in the aerobic tank 15, about half of the organic matter in the urine sewage is converted by the aerobic microorganisms into cellular substances constituting the cells of the microorganism, and the microorganisms are newly grown, and the other half is decomposed into carbon dioxide and water. As a result, urine sewage is purified. In the anaerobic tank 14, high-molecular organic matter in urine sewage is hydrolyzed to lower molecular weight by anaerobic microorganisms, and is eventually converted into methane gas and carbon dioxide. The ratio is about 90%, and the rest is new. Propagation of various microorganisms (anaerobic bacteria). When the biological treatment described above is sufficiently advanced, microorganisms and the like increase in urine sewage. A very large number of such microorganisms may form large clumps called flocs and precipitate in some cases, and the urine sewage that has been sufficiently subjected to biological treatment is sent to the sedimentation tank 16 and the sediment is removed. Will be removed. Incidentally, this precipitate is generally called sludge. Thereafter, the sludge, which is the sediment, is removed from the sludge storage tank 18.
The liquid after the sludge is removed is transferred to the coagulation and sedimentation device 1
7

【0019】(3)浄化処理(化学処理) 凝集沈澱装置17ではアルミニウム塩、鉄塩等の凝集剤
が加えられ、沈澱槽16より送られた液体中に含まれる
微細粒子はその負電荷が中和され、凝集し、沈澱除去さ
れる。またこのような化学処理により生物処理後の液体
中に含まれていたリンも除去され、清澄度の高い処理水
が得られる。なおここでも沈澱物たる汚泥は汚泥貯留槽
18に送られ、処理後の処理水は蒸発装置20の中継槽
21に送られる。そして沈澱槽16及び凝集沈澱装置1
7から送られた汚泥は一旦汚泥貯留槽18に貯留された
後、約98%の含水率で脱水機19に送られ、ここで凝
集剤が加えられて約85%の含水率になるまで脱水され
た後、醗酵堆肥舎Cに送られる。一方、脱水機19によ
り脱水された水分は調整槽13に戻され再度処理が施さ
れる。
(3) Purification Treatment (Chemical Treatment) In the coagulation / sedimentation apparatus 17, a coagulant such as aluminum salt or iron salt is added, and fine particles contained in the liquid sent from the precipitation tank 16 have a negative charge. Summed, aggregated and settled off. In addition, phosphorus contained in the liquid after the biological treatment is also removed by such chemical treatment, and treated water with high clarity is obtained. In this case as well, the sludge as the precipitate is sent to the sludge storage tank 18, and the treated water after the treatment is sent to the relay tank 21 of the evaporator 20. And the sedimentation tank 16 and the coagulation sedimentation device 1
The sludge sent from 7 is once stored in a sludge storage tank 18 and then sent to a dehydrator 19 with a water content of about 98%, where a coagulant is added and dewatered until a water content of about 85%. After that, it is sent to fermentation compost C. On the other hand, the water dehydrated by the dehydrator 19 is returned to the adjusting tank 13 and processed again.

【0020】(4)蒸発処理 蒸発装置20の中継槽21に供給された清浄な処理水は
処理水槽22に送られた後、処理水槽23にオーバーフ
ローして送られるが、その途中、処理水槽22から充填
塔24へ循環し、処理水槽23から噴霧塔25へ循環す
る。また燃焼装置30から排出された排気ガスが噴霧塔
25から充填塔24に送られており、処理水は充填塔2
4及び噴霧塔25において排気ガスとの接触による蒸発
作用を受けることになる。そして処理水は主に噴霧塔2
5で濃縮され、一例として約20倍程度の処理水濃縮液
となった状態で燃焼装置30に送られることとなる。な
お排気ガスは充填塔24から排出された後、集塵機を通
り、誘引ファンから外部に放出されるが、噴霧塔25及
び充填塔24において処理水と接触しているため、大気
汚染物質が除去された状態で外部に放出されることとな
る。
(4) Evaporation treatment The clean treated water supplied to the relay tank 21 of the evaporator 20 is sent to the treated water tank 22 and then overflowed to the treated water tank 23. From the treated water tank 23 to the spray tower 25. Further, exhaust gas discharged from the combustion device 30 is sent from the spray tower 25 to the packed tower 24, and the treated water is supplied to the packed tower 2
4 and the spray tower 25 are subjected to an evaporating effect due to contact with the exhaust gas. The treated water is mainly used in the spray tower 2
5 and is sent to the combustion device 30 in a state of a treated water concentrate of about 20 times as an example. After the exhaust gas is discharged from the packed tower 24, it passes through the dust collector and is discharged to the outside from the induction fan. However, since the exhaust gas is in contact with the treated water in the spray tower 25 and the packed tower 24, the air pollutants are removed. It will be released to the outside in the state where it was.

【0021】(5)燃焼処理 浄化装置10の固液分離機12及び脱水機19により除
去された固形物及び汚泥等は家畜ふん及び水分調整材と
共に醗酵堆肥舎Cで約30%の含水率の堆肥に醗酵、乾
燥された後、燃焼装置30の供給ホッパ35に供給され
る。この際、処理水槽23より排出される約97.8%
の含水率の処理水濃縮液を堆肥と混合し、これを被処理
物とし、燃焼炉31に投入する際には、被処理物の含水
率を約46%に設定している。燃焼炉31内では攪拌部
材36による攪拌作用が開始され、また燃焼バーナ33
への着火及び燃焼ブロワ32による燃焼空気の供給が開
始される。この際、燃焼空気は被処理物の表面に供給さ
れ、被処理物の層において酸素の少ない状態が作り出さ
れる。またこれと同時に被処理物から揮発する熱分解ガ
スを排気口37付近で脱臭バーナ34により燃焼させ、
炭化処理に必要な放射伝熱として利用する。その後、生
成された炭化物は排出口38より搬出される。なお燃焼
装置30において被処理物を焼却処理する際には、燃焼
ブロワ32による燃焼空気の供給は被処理物の層の中に
充分送り込まれ被処理物を完全燃焼させるものである。
(5) Combustion treatment The solids and sludge removed by the solid-liquid separator 12 and the dehydrator 19 of the purification device 10 together with livestock manure and a water conditioner have a water content of about 30% in the fermentation manure C. After being fermented into compost and dried, the compost is supplied to the supply hopper 35 of the combustion device 30. At this time, about 97.8% discharged from the treated water tank 23
When the treated water concentrate having a water content of 3 is mixed with compost to be treated and put into the combustion furnace 31, the moisture content of the treated material is set to about 46%. In the combustion furnace 31, the stirring operation by the stirring member 36 is started.
And the supply of combustion air by the combustion blower 32 is started. At this time, the combustion air is supplied to the surface of the object to be processed, and a low oxygen state is created in the layer of the object to be processed. At the same time, the pyrolysis gas volatilized from the object is burned by the deodorizing burner 34 near the exhaust port 37,
Used as radiant heat transfer required for carbonization. Thereafter, the generated carbide is carried out from the outlet 38. When the object to be treated is incinerated in the combustion device 30, the supply of the combustion air by the combustion blower 32 is sufficiently fed into the layer of the object to be treated to completely burn the object to be treated.

【0022】[0022]

【発明の効果】請求項1記載の家畜ふん尿処理システム
によれば、浄化装置10により浄化処理された処理水は
蒸発装置20により蒸発濃縮され、その後、燃焼装置3
0において浄化処理工程中に除去された汚泥等と混合さ
れ、炭化処理されるため尿汚水処理水の無放流化が可能
となる。また周囲の環境を悪化させることもない。
According to the livestock manure treatment system of the present invention, the treated water purified by the purification device 10 is evaporated and concentrated by the evaporator 20 and then the combustion device 3
At 0, it is mixed with sludge or the like removed during the purification treatment step and carbonized, so that no urine wastewater can be discharged. Also, the surrounding environment is not deteriorated.

【0023】また請求項2記載の家畜ふん尿処理システ
ムによれば、浄化装置10により浄化処理された処理水
は燃焼装置30から排出される排気ガスと接触すること
により蒸発作用を受けるため、燃焼装置30の熱量を可
能な限り利用でき、システム全体の運転費用、維持費用
が低減できる。
According to the livestock manure treatment system of the second aspect, the treated water purified by the purification device 10 is subjected to an evaporative action by coming into contact with the exhaust gas discharged from the combustion device 30. As much as 30 heat can be used as much as possible, and the operating and maintenance costs of the entire system can be reduced.

【0024】更にまた請求項3記載の家畜ふん尿処理シ
ステムによれば、排気ガスは噴霧塔25、充填塔24に
おいて処理水と接触することにより処理水を蒸発させる
一方で排気ガスは洗浄されることになり、大気汚染物質
が可能な限り軽減される。
Further, according to the livestock manure treatment system of the third aspect, the exhaust gas is contacted with the treated water in the spray tower 25 and the packed tower 24 to evaporate the treated water while the exhaust gas is washed. And air pollutants are reduced as much as possible.

【0025】更にまた請求項4記載の家畜ふん尿処理シ
ステムによれば、家畜ふんや汚泥等を醗酵、乾燥させた
堆肥を完全燃焼させずに炭化処理し、その結果得られる
炭化物を土壌改良材としてリサイクルできる。
Further, according to the livestock manure treatment system of the fourth aspect, livestock manure and sludge are fermented and carbonized without drying the compost completely dried, and the resulting carbonized material is used as a soil improving material. Can be recycled.

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

【図1】本発明の家畜ふん尿処理システムを骨格的に示
す流れ図である。
FIG. 1 is a flow chart schematically showing a livestock manure treatment system of the present invention.

【符号の説明】[Explanation of symbols]

1 家畜ふん尿処理装置 10 浄化装置 11 原水槽 12 固液分離機 13 調整槽 14 嫌気槽 14a 攪拌機 15 好気槽 15a 曝気ブロワ 16 沈澱槽 17 凝集沈澱装置 18 汚泥貯留槽 19 脱水機 20 蒸発装置 21 中継槽 22 処理水槽 23 処理水槽 24 充填塔 25 噴霧塔 30 燃焼装置 31 燃焼炉 32 燃焼ブロワ 33 燃焼バーナ 34 脱臭バーナ 35 供給ホッパ 36 攪拌部材 37 排気口 38 排出口 A 畜舎 C 醗酵堆肥舎 DESCRIPTION OF SYMBOLS 1 Livestock excrement processing apparatus 10 Purification apparatus 11 Raw water tank 12 Solid-liquid separator 13 Adjustment tank 14 Anaerobic tank 14a Stirrer 15 Aerobic tank 15a Aeration blower 16 Sedimentation tank 17 Aggregation sedimentation apparatus 18 Sludge storage tank 19 Dehydrator 20 Evaporation apparatus 21 Relay Tank 22 Treated water tank 23 Treated water tank 24 Filling tower 25 Spray tower 30 Combustion device 31 Combustion furnace 32 Combustion blower 33 Combustion burner 34 Deodorizing burner 35 Supply hopper 36 Stirrer 37 Exhaust port 38 Discharge port A Livestock house C Fermentation compost building

フロントページの続き (51)Int.Cl.6 識別記号 FI F23G 7/04 ZAB F23G 7/04 603J 603 B09B 3/00 302G Continued on the front page (51) Int.Cl. 6 Identification code FI F23G 7/04 ZAB F23G 7/04 603J 603 B09B 3/00 302G

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 畜舎から排出される家畜の尿汚水を浄化
処理する浄化装置と、浄化処理後の処理水を蒸発処理す
る蒸発装置と、家畜のふんと浄化処理の途中において排
出される固形物や汚泥等を醗酵、乾燥させた堆肥を炭化
または焼却処理する燃焼装置とを具えて成り、前記浄化
装置により浄化された処理水は蒸発装置において蒸発作
用を受けるとともに、濃縮され、その後前記堆肥と混合
され、燃焼装置において炭化または焼却処理されること
を特徴とする家畜ふん尿処理システム。
1. A purifying apparatus for purifying livestock urine sewage discharged from a livestock barn, an evaporating apparatus for evaporating treated water after the purifying processing, a dung for livestock and solid matter discharged during the purifying processing. Fermentation, sludge, etc., and a combustion device for carbonizing or incinerating the dried compost, and the treated water purified by the purification device is subjected to an evaporating action in the evaporator, concentrated, and then concentrated with the compost. A livestock manure processing system, which is mixed and carbonized or incinerated in a combustion device.
【請求項2】 前記浄化処理後の処理水は、蒸発装置に
おいて燃焼装置から排出される排気ガスと接触し、その
廃熱により蒸発作用を受けることを特徴とする請求項1
記載の家畜ふん尿処理システム。
2. The treated water after the purification treatment is brought into contact with exhaust gas discharged from a combustion device in an evaporator, and is subjected to an evaporative action by waste heat thereof.
A livestock manure processing system as described.
【請求項3】 前記燃焼装置より排出される排気ガスは
蒸発装置において処理水と接触した後、外部に放出され
ることを特徴とする請求項1または2記載の家畜ふん尿
処理システム。
3. The livestock manure treatment system according to claim 1, wherein the exhaust gas discharged from the combustion device is discharged to the outside after coming into contact with the treated water in the evaporator.
【請求項4】 前記燃焼装置において炭化物が生成され
ることを特徴とする請求項1、2または3記載の家畜ふ
ん尿処理システム。
4. The livestock manure treatment system according to claim 1, wherein the combustion device generates carbide.
JP9252800A 1997-09-01 1997-09-01 Livestock excretion treatment system Pending JPH1177095A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9252800A JPH1177095A (en) 1997-09-01 1997-09-01 Livestock excretion treatment system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9252800A JPH1177095A (en) 1997-09-01 1997-09-01 Livestock excretion treatment system

Publications (1)

Publication Number Publication Date
JPH1177095A true JPH1177095A (en) 1999-03-23

Family

ID=17242417

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9252800A Pending JPH1177095A (en) 1997-09-01 1997-09-01 Livestock excretion treatment system

Country Status (1)

Country Link
JP (1) JPH1177095A (en)

Cited By (10)

* Cited by examiner, † Cited by third party
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JPH11333416A (en) * 1998-05-27 1999-12-07 Kubota Corp Method for recycling resource from organic waste
WO2002004367A1 (en) * 2000-07-11 2002-01-17 Snf Sa Method and installation for treating industrial, agricultural and urban or agricultural waste, in particular pig slurry
JP2002180059A (en) * 2000-12-14 2002-06-26 Maywa Co Ltd Carbonization treatment of organic waste material of high moisture content
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JP2010508494A (en) * 2006-11-02 2010-03-18 レーダル ホールディング ベー. ヴィ. Method and system for drying water-containing materials
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CN110842008A (en) * 2019-11-19 2020-02-28 中车环境科技有限公司 Method and system for classifying and processing dispersed garbage in small and medium-sized villages and towns
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Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11333416A (en) * 1998-05-27 1999-12-07 Kubota Corp Method for recycling resource from organic waste
WO2002004367A1 (en) * 2000-07-11 2002-01-17 Snf Sa Method and installation for treating industrial, agricultural and urban or agricultural waste, in particular pig slurry
FR2811659A1 (en) * 2000-07-11 2002-01-18 Snf Sa PROCESS AND PLANT FOR THE TREATMENT OF INDUSTRIAL, AGRICULTURAL AND URBAN OR HOUSEHOLD LIQUID WASTE, ESPECIALLY PORK SLURRY
JP2002180059A (en) * 2000-12-14 2002-06-26 Maywa Co Ltd Carbonization treatment of organic waste material of high moisture content
BE1014437A3 (en) * 2001-10-24 2003-10-07 Meyer Andru De Drying and burning method for e.g. pig manure, carried out without separating wet material into thick and thin fractions
JP2010508494A (en) * 2006-11-02 2010-03-18 レーダル ホールディング ベー. ヴィ. Method and system for drying water-containing materials
JP2010005601A (en) * 2008-06-30 2010-01-14 Togami Electric Mfg Co Ltd Circulation type treatment method and system for waste in environment area including cowhouse
KR101373539B1 (en) * 2013-11-27 2014-03-13 천안시 Livestock wastewater treatment system
CN104791805A (en) * 2015-03-26 2015-07-22 奚振华 Integrated household refuse incineration treatment method and device
CN104791805B (en) * 2015-03-26 2017-06-23 奚振华 The incineration treatment method and equipment of integrated form house refuse
CN110842008A (en) * 2019-11-19 2020-02-28 中车环境科技有限公司 Method and system for classifying and processing dispersed garbage in small and medium-sized villages and towns
CN112239270A (en) * 2020-09-28 2021-01-19 南京师范大学 Novel material capable of being used as plant planting matrix, preparation method and application thereof

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