JP2002084908A - Pigpen - Google Patents

Pigpen

Info

Publication number
JP2002084908A
JP2002084908A JP2000271350A JP2000271350A JP2002084908A JP 2002084908 A JP2002084908 A JP 2002084908A JP 2000271350 A JP2000271350 A JP 2000271350A JP 2000271350 A JP2000271350 A JP 2000271350A JP 2002084908 A JP2002084908 A JP 2002084908A
Authority
JP
Japan
Prior art keywords
aeration
septic tank
pig
activated sludge
treated water
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
JP2000271350A
Other languages
Japanese (ja)
Inventor
Sakujiro Nakamura
作二郎 中村
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.)
ITOCHU RINGYO KK
MENDERU JAPAN KK
Original Assignee
ITOCHU RINGYO KK
MENDERU JAPAN KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by ITOCHU RINGYO KK, MENDERU JAPAN KK filed Critical ITOCHU RINGYO KK
Priority to JP2000271350A priority Critical patent/JP2002084908A/en
Publication of JP2002084908A publication Critical patent/JP2002084908A/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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Abstract

PROBLEM TO BE SOLVED: To provide a pigpen solving the problems that operations for dealing with pig excreta including dung removal and contaminated water cleanup at pigpens in the pig-raising farm are often associated with difficulties, and occurrence of pollution due to bad odor and the generation of sanitary insect pests such as flies, adverse effects on pig growth due to the daily difference of both the temperature and humidity and the generation of harmful and odorous gas and, unpleasant feeling for workers, difficulties of operating septic tanks under low water temperature in winter in cold districts and the shortage of sites for septic tanks exist. SOLUTION: This pigpen is so designed that the floor thereof is constructed of concrete drain-board with narrow slits or metal or synthetic resin with netty slits so as to allow discharged excreta and washings to fall down via the slits, being characterized by that septic tanks with activated sludge system of oxidation ditch type are installed for receiving such discharged excreta and washings fallen down.

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、養豚農場における
浄化槽と立体的に一体化した豚舎に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a pig house three-dimensionally integrated with a septic tank on a pig farm.

【0002】[0002]

【従来の技術】従来の養豚農場の豚舎では豚舎内で排泄
された糞尿と洗い水などは豚舎の外に排出された後に汚
水の浄化処理、固形物の堆肥化発酵処理などの処理が行
われており、豚舎の床を細い隙間(スリット)のあるコ
ンクリートスノコや網目状の隙間のある金属または合成
樹脂製としたもの(以下、これらを一括して「スノコな
ど」という)とし、その下にスクレーパーと呼ばれる糞
の掻き取り装置と尿排出管を設け、糞と尿を豚舎内で分
離して豚舎外に取出している豚舎や、床下に槽を設け糞
尿混合で受けて豚舎外に取出して処理している例が多
い。
2. Description of the Related Art In a conventional pig farm on a pig farm, excreta and washing water excreted in the pig barn are discharged out of the pig barn and then subjected to treatment such as purification of sewage and composting and fermentation of solids. The floor of the piggery is made of concrete floor with narrow gaps (slits) or metal or synthetic resin with mesh-shaped gaps (hereinafter collectively referred to as "snow floors"), and below it It is equipped with a scraper called a dung scraper and a urine discharge pipe, and the dung and urine are separated inside the pig house and taken out of the pig house. There are many examples.

【0003】いずれの場合も、豚が糞尿を排泄した後所
定の処理がなされるまでに相当の時間が経過し且つこれ
らが開放的空間においてなされるため、腐敗による豚舎
内外での悪臭の発生やハエなど衛生害虫の発生による公
害苦情が多く、また豚舎内でのアンモニアなどガスの発
生は豚の生育の障害となっており養豚農場で従事してい
る作業者の労働環境としても好ましくない。また豚舎内
での糞尿分離型豚舎の場合、上記スクレーパーなど除糞
機が故障した場合の修理作業は大変苦痛を伴うものであ
り、またスクレーパーの存在は豚舎の床下と豚舎外での
糞尿取出し口とが繋がっているため豚舎の密閉性を保つ
ことが困難であり、それ故、豚舎内の温度、湿度の調整
が難しい。さらに、豚舎外での浄化槽に要する用地面積
も少なからず必要であり、寒冷地においては戸外の浄化
槽内の水温を適性に保つことが極めて困難であり浄化槽
機能の維持に苦労が伴う。
[0003] In any case, since a considerable time elapses after the pig excretes manure and the predetermined treatment is performed, and these are performed in an open space, the generation of bad smell inside and outside the pig house due to putrefaction and the like. There are many pollution complaints due to the occurrence of sanitary pests such as flies, and the generation of gas such as ammonia in the piggery is a hindrance to the growth of pigs, which is not favorable as a working environment for workers working on pig farms. In addition, in the case of a manure separation type pig house in a pig house, repair work in case of failure of the feces removal machine such as the above scraper is very painful, and the presence of the scraper is under the floor of the pig house and the manure outlet outside the pig house. And it is difficult to maintain the hermeticity of the pig house, and therefore it is difficult to adjust the temperature and humidity in the pig house. Furthermore, a lot of land area is required for the septic tank outside the pig house, and it is extremely difficult to keep the water temperature inside the outdoor septic tank at an appropriate level in a cold region, and it is difficult to maintain the function of the septic tank.

【0004】[0004]

【発明が解決しようとする課題】豚舎内外での悪性ガス
の発生やハエなど衛生害虫の発生及びこれから派生する
豚、人間にとっての環境悪化、公害問題は、排泄された
糞尿が浄化、堆肥発酵などの処理がなされるまでの間豚
舎内外で滞留しているために起きる現象である。
The problem of the generation of malignant gas inside and outside the pig house, the occurrence of sanitary pests such as flies, and the resulting deterioration of the environment for pigs and humans and pollution, include the purification of excreted manure and compost fermentation. This is a phenomenon that occurs due to staying inside and outside the pig barn until the treatment is performed.

【0005】豚舎内での室温や湿度の調整の難しさと除
糞機の修理作業は糞尿分離を豚舎内で行おうとするが故
に発生する問題である。
[0005] Difficulty adjusting the room temperature and humidity in the piggery and the repair work of the dung removal machine are problems that occur because the manure is to be separated in the piggery.

【0006】豚舎外に浄化設備を設けようとすると豚舎
と別の用地を必要とする。また戸外に独立して設けられ
た浄化槽は特に寒冷地において冬期での適性水温維持が
むつかしい。
[0006] If a purification facility is to be provided outside the pig house, a separate site from the pig house is required. In addition, septic tanks that are provided independently outdoors are difficult to maintain an appropriate water temperature in winter, especially in cold regions.

【0007】上記したような課題を解決することが強く
要望されており、本発明はこのような実情に鑑みてなさ
れたものであり、排泄された糞尿や洗い水が豚舎内外に
滞留したり、豚舎外に搬出しなくてすむように豚舎内に
活性汚泥法浄化槽を設置した豚舎を提供することを目的
としている。
[0007] There is a strong demand to solve the above problems, and the present invention has been made in view of such circumstances, and excreted manure and washing water stay in and out of a piggery. It is an object of the present invention to provide a pig house in which an activated sludge septic tank is installed in the pig house so that it is not necessary to carry it out of the pig house.

【0008】[0008]

【課題を解決するための手段】上記の課題は、排泄され
た糞尿が豚舎とは別の場所と施設において浄化処理や堆
肥発酵処理されるために、処理されるまでの間に豚舎の
内外に糞尿や洗い水が滞留し、また豚舎の床下に除糞機
などの排出装置を設けているゆえに発生する。
Means for Solving the Problems The above-mentioned problem is caused by the fact that excreted manure is subjected to purification treatment or compost fermentation treatment in a place and facility different from the pig house, so that the excreted manure can be put in and out of the pig house before being treated. Manure and washing water accumulate, and occur because a discharge device such as a dung removal machine is installed under the floor of the piggery.

【0009】よって、床がスノコなどの豚舎において、
排泄された糞尿や洗い水が隙間から落下し、直ちに活性
汚泥と混合、曝気、浄化されるように、酸化溝(オキシ
デーションディッチ)形式の活性汚泥法浄化槽を床下に
設置し、容易かつ安定的にBODの酸化(浄化)、アン
モニア態窒素の亜硝酸、硝酸への酸化と亜硝酸、硝酸の
窒素ガスへの還元を行い、活性汚泥が沈殿した後の処理
水をポンプなどの取出し装置で取出すように構成されて
いる。
Therefore, in a pig barn with a floor such as a snowboard,
Oxidation ditch type activated sludge septic tank is installed under the floor so that excreted manure and washing water fall from the gap and are immediately mixed with aerated sludge and purified. (Purification) of BOD, oxidation of ammonia nitrogen to nitrous acid and nitric acid, and reduction of nitrous acid and nitric acid to nitrogen gas. The treated water after the activated sludge is settled out is taken out by a removal device such as a pump. It is configured as follows.

【0010】すなわち、本請求項1の発明は、床が細い
隙間(スリット)のあるコンクリートスノコまたは網目
状の隙間のある金属あるいは合成樹脂によって構成さ
れ、その隙間から排泄された糞尿や洗い水が落下する豚
舎において、該床下に床から落下した糞尿や洗い水を受
ける酸化溝(オキシデーションディッチ)形式の活性汚
泥法浄化槽を設置したことを特徴とする豚舎であり、請
求項2の発明は、前記浄化槽はBOD容積負荷0.1〜
0.3kg/m・日の容量である請求項1記載の豚舎
であり、請求項3の発明は、前記浄化槽は、付帯装置と
して、曝気の時間や強度を制御できる曝気・攪拌装置、
処理水の取出し装置、糞に含まれる未消化の餌かすなど
の粗い浮遊固形物の除去装置及び余剰活性汚泥の抜取装
置を備えている請求項1記載の豚舎であり、請求項4の
発明は、前記浄化槽の運転は、曝気・攪拌時間(好気
条件)、曝気停止・静置・活性汚泥沈澱時間(嫌気条
件)、処理水の上澄み取出し時間を区切って繰り返す
間欠曝気の回分式にて行われる請求項3記載の豚舎であ
り、請求項5の発明は、前記浄化槽の運転は、曝気・攪
拌を連続して行う請求項3記載の豚舎であり、請求項6
の発明は、処理水の取出し装置がポンプあるいは排水弁
であって、これを用いて曝気停止・静置・汚泥沈澱時間
後の上澄み処理水を取出す請求項4記載の豚舎であり、
請求項7の発明は、処理水の取出し装置が精密濾過膜で
あって、これを浄化槽の中または別に設けた槽に設置し
てある請求項5記載の豚舎であり、請求項8の発明は、
前記浄化槽に更に溶存酸素濃度計、酸化還元電位計及び
水素イオン濃度計を備えている請求項3記載の豚舎であ
る。
That is, according to the first aspect of the present invention, the floor is formed of a concrete saw with a narrow gap (slit) or a metal or synthetic resin having a mesh-shaped gap, and excrement and washing water excreted from the gap are formed. The pig house, wherein an activated sludge method septic tank of an oxidation ditch (oxidation ditch) type for receiving manure and washing water dropped from the floor under the floor is installed in the falling pig house. The septic tank has a BOD volume load of 0.1 to
A pigsty of claim 1, wherein the capacitance of 0.3 kg / m 3 · day, the invention of claim 3, wherein the septic tank, as supplementary devices, aeration and stirring apparatus that can control the time and intensity of aeration,
The pig house according to claim 1, further comprising a device for removing treated water, a device for removing coarse suspended solids such as undigested food waste contained in feces, and a device for removing excess activated sludge. The operation of the septic tank is performed in a batch mode of intermittent aeration which is repeated by dividing aeration / agitating time (aerobic condition), aeration stop / standing, activated sludge sedimentation time (anaerobic condition), and treatment water supernatant removal time. According to a third aspect of the present invention, there is provided the piggery according to the third aspect, wherein the operation of the septic tank is performed by continuously performing aeration and stirring.
The invention of claim 4 is a piggery according to claim 4, wherein the device for taking out treated water is a pump or a drain valve, and using this, takes out the supernatant treated water after aeration stoppage, standing, and sludge sedimentation time,
The invention according to claim 7 is the piggery according to claim 5, wherein the apparatus for removing treated water is a microfiltration membrane, which is installed in a septic tank or in a separate tank. ,
The pig house according to claim 3, wherein the septic tank is further provided with a dissolved oxygen concentration meter, a redox potential meter, and a hydrogen ion concentration meter.

【0011】[0011]

【発明の実施の形態】以下、本発明を図1〜4に基づい
て詳細に説明する。これらの図は、酸化溝(オキシデー
ションディッチ)形式の活性汚泥法浄化槽と一体化した
豚舎を説明するための概略構成図であり、図1は本発明
の豚舎の横断面図を、図2は浄化槽とスノコ床との構成
の一部を示す斜視図、図3は豚舎の床下に設置した浄化
槽の平面図を、図4は本発明の豚舎の縦断面形状および
付帯装置構成図をそれぞれ示す。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described in detail with reference to FIGS. These figures are schematic structural diagrams for explaining a pig house integrated with an activated sludge process septic tank of an oxidation ditch (oxidation ditch) type. FIG. 1 is a cross-sectional view of a pig house of the present invention, and FIG. FIG. 3 is a perspective view showing a part of the configuration of the septic tank and the floor of the mushroom, FIG. 3 is a plan view of the septic tank installed under the floor of the piggery, and FIG. 4 is a vertical sectional view of the piggery of the present invention and a configuration diagram of an auxiliary device.

【0012】豚舎1は、建屋2と豚房3、スノコなどの
隙間を通して糞尿が自然落下する床4と床下の酸化溝形
式の活性汚泥法浄化槽5を有している。
The pig house 1 has a building 2, a pig tub 3, a floor 4 on which manure falls naturally through gaps such as a snowboard, and an activated-sludge-type purification tank 5 in the form of an oxidation ditch below the floor.

【0013】酸化溝形式の活性汚泥法浄化槽(以下「O
D法」という)は歴史のある浄化法であり、水深1.5
〜2m程度の水深の浅い処理槽を図2に示したようにド
ーナッツ型長円形に構築し、水面に設置するケスナーブ
ラシなどにより活性汚泥液を空中にはねあげて空気と接
触させ酸素を取り込む(曝気)と共に、水平方向に水流
をおこさせ活性汚泥液と流入原水を攪拌・混和すること
が本方式の原形である。ひとつの処理槽で曝気、曝気停
止・汚泥沈澱、処理水取出しを行う回分式と、連続して
曝気し別に設けた沈殿槽で処理水を取出す連続式があ
る。
An activated sludge process septic tank of the oxidation ditch type (hereinafter referred to as “O
D method) is a purification method with a long history,
As shown in Fig. 2, a shallow treatment tank with a depth of about 2 m is constructed in a donut-shaped oval shape, and activated sludge liquid is splashed into the air by a Kessner brush or the like installed on the surface of the water to contact oxygen to take in oxygen (aeration) ) Together with a horizontal flow of water to stir and mix the activated sludge liquid and the inflowing raw water is the original form of this method. There are a batch type in which aeration, aeration stop, sludge sedimentation, and removal of treated water are performed in one treatment tank, and a continuous type in which treated water is removed in a separate sedimentation tank provided with continuous aeration.

【0014】OD法は必要曝気動力が比較的すくなくて
すみまた操作も簡便であるが、水深が浅いため大きい用
地面積を要しまた水の表面積が大きいため外気温の影響
を受けやすいという欠点がある。然るに、この浄化槽
(酸化溝)の上に豚舎をのせて一体化させることにより
浄化槽が外気温の影響を受けやすいという欠点をも同時
に解消する。
The OD method requires a relatively small amount of aeration power and is easy to operate. However, it has a disadvantage that it requires a large land area because of its shallow water depth, and is susceptible to the outside air temperature because of its large surface area. is there. However, by putting the pig house on the septic tank (oxidized ditch) and integrating it, the disadvantage that the septic tank is easily affected by the outside temperature is also eliminated.

【0015】建屋2と豚房3と床4は豚の飼養目的によ
り構造・平面積・床材質など必要な形式とする。
The building 2, the pig bunches 3, and the floor 4 are of a required type such as structure, flat area, floor material and the like according to the purpose of breeding pigs.

【0016】浄化槽5は、有効容量がBOD容積負荷
0.1〜0.3kg/m・日)とすることが好まし
い。一般的に活性汚泥浄化槽の設計ではBOD容積負荷
が0.3kg/m・日未満の中〜低負荷設計や0.3
kg/m・日以上の中〜高負荷設計をとり得る。中〜
高負荷での設計においては必要槽容量は小さくてすむが
運転はむつかしく酸素不足・活性汚泥の沈澱不良・発泡
などのトラブルがおきやすい。これに対し、中〜低負荷
設計では運転はより容易であり同時に回分運転において
アンモニア態窒素の亜硝酸、硝酸への酸化と亜硝酸、硝
酸の窒素ガスへの還元を高度に行うことが出来る。
It is preferable that the septic tank 5 has an effective capacity of 0.1 to 0.3 kg / m 3 · day (BOD volume load). Generally, in the design of an activated sludge septic tank, the BOD volume load is less than 0.3 kg / m 3 · day.
A medium-to-high load design of kg / m 3 · day or more can be taken. During~
In a high-load design, the required tank capacity is small, but operation is difficult, and problems such as insufficient oxygen, poor sedimentation of activated sludge, and foaming are likely to occur. On the other hand, the operation is easier with a medium to low load design, and at the same time, the oxidation of ammonia nitrogen to nitrite and nitric acid and the reduction of nitrous acid and nitric acid to nitrogen gas can be performed in batch operation at a high level.

【0017】本発明の浄化槽と一体化した豚舎におい
て、豚が生活する訳であるから発泡などのトラブルはお
こしてはならず、またアンモニアガスなど悪性ガスの発
生を抑制することが目的の一つであるから脱窒も重要で
ある。これがOD法のBOD容積負荷を出来るだけ低負
荷に設計することが好ましい理由である。
One of the objects is to prevent troubles such as foaming from occurring because pigs live in a pig house integrated with the septic tank of the present invention, and to suppress the generation of malignant gas such as ammonia gas. Therefore, denitrification is also important. This is why it is preferable to design the BOD volume load of the OD method as low as possible.

【0018】槽の数、長さ、幅、深さについては飼養す
る豚の内容と豚舎の平面形状により決定し、槽の一部が
屋外にはみ出しても良い。
The number, length, width and depth of the tanks are determined according to the contents of the pigs to be bred and the planar shape of the pig house, and a part of the tanks may protrude outside.

【0019】浄化槽5は、曝気・攪拌装置6、処理水取
出し装置7、汚泥取出し装置8、粗い浮遊固形物の除去
装置9、溶存酸素濃度計(DO計)・酸化還元電位計
(ORP計)・水素イオン濃度計(pH計)等のセンサ
ー10、制御盤11を有している。
The septic tank 5 includes an aeration / stirring device 6, a treated water take-out device 7, a sludge take-out device 8, a device 9 for removing coarse suspended solids, a dissolved oxygen concentration meter (DO meter), and an oxidation-reduction potentiometer (ORP meter). A sensor 10 such as a hydrogen ion concentration meter (pH meter) and a control panel 11 are provided.

【0020】曝気・攪拌装置6は、浄化槽5に酸素を導
入する曝気と活性汚泥水を水平方向に流動させるための
装置である。曝気・攪拌装置は、必要とする導入酸素量
と流速に応じて、フローティング型・水中エジェクター
型・水中ミキサー型などを選択あるいは組合せて設置す
る。
The aeration / stirring device 6 is a device for introducing oxygen into the septic tank 5 and for horizontally flowing the activated sludge water. The aeration / stirring device is selected or combined with a floating type, an underwater ejector type, an underwater mixer type, etc., according to the required amount of introduced oxygen and flow rate.

【0021】浄化槽5の運転は、曝気・攪拌時間(好気
条件)と曝気停止・静置・汚泥沈澱時間(嫌気条件)、
処理水の上澄み取出し時間を区切って繰り返す間欠曝気
の回分式運転とすることが好ましいが、曝気・攪拌を連
続して行う連続式運転とすることも出来る。回分式運転
の1例として挙げると、豚が活動し糞尿を排泄する昼間
を曝気時間(好気条件)、夜間は曝気停止時間(嫌気条
件)としBODの酸化、アンモニア態窒素の酸化、還元
による脱窒素を行い曝気停止時間の終わり頃に活性汚泥
が沈殿した後の処理水をポンプなどの取出し装置で取出
すように構成されている。
The operation of the septic tank 5 includes aeration and stirring times (aerobic conditions), aeration stop, standing, and sludge settling times (anaerobic conditions).
It is preferable to use a batch-type operation of intermittent aeration which is repeated while separating the supernatant time of the treated water, but it is also possible to use a continuous operation in which aeration and stirring are continuously performed. As an example of batch-type operation, the daytime when pigs are active and excrete excreta are aerated during aerobic conditions (aerobic conditions), and the nighttime when aeration is stopped (anaerobic conditions), the oxidation of BOD and the oxidation and reduction of ammonia nitrogen are considered. It is configured to remove the treated water after the activated sludge has been settled at the end of the aeration stop time by denitrification and a removal device such as a pump.

【0022】処理水取出し装置7は、回分式運転の場合
水面近くに設置する水中ポンプや排水弁によって曝気停
止・静置・活性汚泥沈澱の後作動させ処理水(上澄み
水)を取出し、あるいは回分式運転あるいは連続式運転
においてより高度の処理水質が求められる場合には精密
濾過膜を選択する。酸化溝の中または別に設けた槽に精
密濾過膜を設置し処理水取出し装置とすることは、沈殿
槽を別に設置せずに連続式運転とする場合やより高度の
処理水質が求められる場合において好ましい。
In the case of batch-type operation, the treated water take-out device 7 is operated after stopping aeration, standing still, and activated sludge sedimentation by a submersible pump or a drain valve installed near the water surface to take out treated water (supernatant water) or batch treatment. When a higher quality of treated water is required in a batch operation or a continuous operation, a microfiltration membrane is selected. Installing a microfiltration membrane in an oxidizing groove or in a separately provided tank and using it as a treated water take-out device is a continuous operation without separately installing a sedimentation tank, or when a higher treatment water quality is required preferable.

【0023】精密濾過膜は、バクテリアのサイズの粒子
と水をこし分けることの出来る微細な隙間をもつフィル
ターであり、活性汚泥と処理水を分離する方法として近
年普及してきたが、沈澱分離法と比べて活性汚泥の処理
水への混入はほとんどないので高度の処理水質を得るこ
とができる。
The microfiltration membrane is a filter having fine gaps capable of separating bacteria-sized particles and water, and has recently become popular as a method for separating activated sludge from treated water. In comparison, activated sludge is hardly mixed into the treated water, so that a high treated water quality can be obtained.

【0024】汚泥取出し装置8は、槽の底に設置する水
中ポンプまたは排水弁を選択する。
The sludge removal device 8 selects a submersible pump or a drain valve installed at the bottom of the tank.

【0025】粗い浮遊固形物の除去装置9は水中ポンプ
とスクリーンにより構成され槽内の活性汚泥水をスクリ
ーンに巡回させ糞に含まれる粗ゴミを除去する。
The coarse suspended solids removing device 9 is composed of a submersible pump and a screen, and the activated sludge in the tank is circulated through the screen to remove coarse dust contained in feces.

【0026】DO計・ORP計・pH計等のセンサー1
0は槽内の活性汚泥液12中に設置し、制御盤に併設す
る記録計及びメーターに表示され、これらのデータを参
考にして曝気強度、曝気時間などをコントロールする。
Sensor 1 such as DO meter, ORP meter, pH meter, etc.
0 is set in the activated sludge liquid 12 in the tank, and is displayed on a recorder and a meter attached to the control panel, and the aeration intensity and the aeration time are controlled by referring to these data.

【0027】活性汚泥による養豚廃水浄化の維持管理
は、流入負荷・活性汚泥量・曝気の強度とタイミング・
窒素分の挙動の4要素のバランスをコントロールしてい
くということであるといえるが、目視など人の感覚にの
み依存して判断することは難しい。このために上記セン
サーによって感知される溶存酸素(DO)、酸化還元電
位(ORP)、水素イオン濃度(pH)の数値及び波形
を読み取ることによって科学的管理をおこなうことが出
来る。
The maintenance and management of swine wastewater purification by activated sludge is based on inflow load, activated sludge amount, aeration intensity and timing,
It can be said that the balance of the four factors of the nitrogen content is controlled, but it is difficult to make a judgment depending only on human sensation such as visual observation. For this purpose, scientific management can be performed by reading numerical values and waveforms of dissolved oxygen (DO), redox potential (ORP), and hydrogen ion concentration (pH) sensed by the sensor.

【0028】DOの値は活性汚泥液中に送り込まれた酸
素の消費具合を示し、回分式運転における波形からはB
ODやアンモニアの酸化の進行程度を推定できると同時
に投入酸素量の適否を判定できる。
The value of DO indicates the degree of consumption of oxygen fed into the activated sludge, and B is obtained from the waveform in batch operation.
The progress of the oxidation of OD and ammonia can be estimated, and at the same time, the appropriateness of the input oxygen amount can be determined.

【0029】ORPの値はゼロを境にプラス電位(酸
化)とマイナス電位(還元)があるが、曝気中にはプラ
ス方向に推移しBODやアンモニアの酸化の進行状況を
推定でき、曝気停止中はマイナス方向に推移しアンモニ
アが酸化されて生成する硝酸や亜硝酸が還元され窒素ガ
スとなる脱窒の状況を推定できる。
The value of ORP has a positive potential (oxidation) and a negative potential (reduction) at the boundary of zero. During the aeration, the value changes in the positive direction, and the progress of oxidation of BOD and ammonia can be estimated. Can be estimated in a minus direction, and the state of denitrification in which nitric acid and nitrous acid generated by the oxidation of ammonia are reduced to nitrogen gas can be estimated.

【0030】pHの値は7(中性)を中心に大きくなれ
ばアルカリ性、小さくなれば酸性を示す。
As the pH value increases around 7 (neutral), the pH value is alkaline, and when the pH value is low, it is acidic.

【0031】汚水に含まれるアンモニアや有機酸の酸化
及び還元によって活性汚泥液のpHは変動する。
The pH of the activated sludge fluctuates due to the oxidation and reduction of ammonia and organic acids contained in the wastewater.

【0032】活性汚泥はバクテリァの集合体であるが、
pH7に近い環境において正常に機能するのでpHの値
を監視することにより活性汚泥のいわば健康度を推定す
ることができる。
Activated sludge is an aggregate of bacteria,
Since it functions normally in an environment close to pH 7, it is possible to estimate the so-called health of activated sludge by monitoring the pH value.

【0033】上記装置のモーター類は制御盤11により
運転制御される。
The operation of the motors of the above device is controlled by a control panel 11.

【0034】[0034]

【発明の効果】浄化槽と一体化した本発明の豚舎によれ
ば、豚が排泄した糞尿や洗い水がただちに活性汚泥と混
合・曝気・浄化され、腐敗につながる状態で豚舎内外に
滞留しないため悪性ガスは発生せず、ハエなど衛生害虫
も生育しない。スクレーパーなど除糞施設が不要なため
これらの設置費及び維持管理作業が不要である。浄化槽
内の水の熱容量が大きいため外気の変動に対し緩衝能力
を持ち同時に水面からの水の蒸散があり豚舎内の温度と
湿度を平準化する。浄化槽としては建屋で覆われている
ことから、寒冷地での低温外気の影響を直接受けない。
浄化槽と豚舎が立体として構成されるので汚水処理設備
のための用地を節約できる。このように従来の豚舎と比
較して格段に豚の生育環境が改善され、農場で働く従業
者の労働環境もいちじるしく改善される。
According to the pig bar of the present invention integrated with the septic tank, the excrement and washing water excreted by the pig are immediately mixed with the activated sludge, aerated and purified, and do not stay inside or outside the pig bar in a state that leads to putrefaction. No gas is generated, and no sanitary pests such as flies grow. Since no dung removal facility such as a scraper is required, these installation costs and maintenance work are unnecessary. Since the heat capacity of the water in the septic tank is large, it has a buffering capacity against fluctuations in the outside air, and at the same time, water evaporates from the surface of the water, leveling the temperature and humidity in the piggery. Since the septic tank is covered by a building, it is not directly affected by low-temperature outside air in cold regions.
Since the septic tank and the piggery are configured as three-dimensional, the land for sewage treatment facilities can be saved. As described above, the growing environment of pigs is remarkably improved as compared with the conventional pig barn, and the working environment of employees working on the farm is also significantly improved.

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

【図1】 本発明の豚舎の横断面図。FIG. 1 is a cross-sectional view of a pigger of the present invention.

【図2】 浄化槽とスノコ床との構成の一部を示す斜視
図。
FIG. 2 is a perspective view showing a part of a configuration of a septic tank and a mushroom floor.

【図3】 豚舎の床下に設置した浄化槽の平面図。FIG. 3 is a plan view of a septic tank installed under the floor of a piggery.

【図4】 本発明の豚舎の縦断面形状および付帯装置構
成図。
FIG. 4 is a vertical cross-sectional view of a pig house of the present invention and a configuration diagram of an auxiliary device.

【符号の説明】[Explanation of symbols]

1…豚舎 2…建屋 3…豚房 4…スノコなど糞尿や洗い水が自然落下する床 5…床下の酸化溝形式の浄化槽 6…曝気・攪拌装置 7…処理水取出し装置 8…汚泥取出し装置 9…粗い浮遊固形物)除去装置 10…溶存酸素濃度計・酸化還元電位計・pH計等のセ
ンサー 11…制御盤 12…活性汚泥液
DESCRIPTION OF SYMBOLS 1 ... Pig house 2 ... Building 3 ... Pig bun 4 ... Floor where manure and washing water, such as a snowboard, fall naturally 5 ... Oxidation groove type purification tank under the floor 6 ... Aeration / stirring device 7 ... Treated water removal device 8 ... Sludge removal device 9 ... Coarse suspended solids) removal device 10 ... Sensors such as dissolved oxygen concentration meter, redox potential meter and pH meter 11 ... Control panel 12 ... Activated sludge liquid

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 2B101 AA04 CA08 CB04 EB13 4D006 GA07 HA93 KA02 KB22 KB23 PA01 PB08 PC63 4D029 AA03 AA04 AA09 AB05 BB04 BB10 DD03 4D040 BB54 BB67 BB91 BB92  ──────────────────────────────────────────────────続 き Continued on the front page F term (reference) 2B101 AA04 CA08 CB04 EB13 4D006 GA07 HA93 KA02 KB22 KB23 PA01 PB08 PC63 4D029 AA03 AA04 AA09 AB05 BB04 BB10 DD03 4D040 BB54 BB67 BB91 BB92

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】 床が細い隙間(スリット)のあるコンク
リートスノコまたは網目状の隙間のある金属あるいは合
成樹脂によって構成され、その隙間から排泄された糞尿
や洗い水が落下する豚舎において、該床下に床から落下
した糞尿や洗い水を受ける酸化溝(オキシデーションデ
ィッチ)形式の活性汚泥法浄化槽を設置したことを特徴
とする豚舎。
1. A pig barn in which a floor is made of concrete saw with a narrow gap (slit) or metal or synthetic resin having a mesh-shaped gap, and excrement and washing water excreted from the gap fall under the floor. A pig house equipped with an activated sludge process septic tank of the oxidation ditch type, which receives excrement and washing water dropped from the floor.
【請求項2】 前記浄化槽はBOD容積負荷0.1〜
0.3kg/m・日の容量である請求項1記載の豚
舎。
2. The septic tank has a BOD volume load of 0.1 to 2.
The piggery according to claim 1, wherein the capacity is 0.3 kg / m 3 · day.
【請求項3】 前記浄化槽は、付帯装置として、曝気の
時間や強度を制御できる曝気・攪拌装置、処理水の取出
し装置、糞に含まれる未消化の餌かすなどの粗い浮遊固
形物の除去装置及び余剰活性汚泥の抜取装置を備えてい
る請求項1記載の豚舎。
3. The septic tank, as an auxiliary device, an aeration / stirring device capable of controlling the time and intensity of aeration, a device for removing treated water, and a device for removing coarse suspended solids such as undigested food waste contained in feces. The piggery according to claim 1, further comprising a device for extracting excess activated sludge.
【請求項4】 前記浄化槽の運転は、曝気・攪拌時間
(好気条件)、曝気停止・静置・活性汚泥沈澱時間
(嫌気条件)、処理水の上澄み取出し時間を区切って
繰り返す間欠曝気の回分式にて行われる請求項3記載の
豚舎。
4. The operation of the septic tank includes batching of intermittent aeration repeated by dividing aeration / agitating time (aerobic condition), aeration stop / standing, activated sludge sedimentation time (anaerobic condition), and supernatant removal time of treated water. The piggery according to claim 3, which is performed by a formula.
【請求項5】 前記浄化槽の運転は、曝気・攪拌を連続
して行う請求項3記載の豚舎。
5. The piggery according to claim 3, wherein the operation of the septic tank performs aeration and stirring continuously.
【請求項6】 処理水の取出し装置がポンプあるいは排
水弁であって、これを用いて曝気停止・静置・汚泥沈澱
時間後の上澄み処理水を取出す請求項4記載の豚舎。
6. The piggery according to claim 4, wherein the treated water take-out device is a pump or a drain valve, and uses this to take out the supernatant treated water after aeration stoppage, standing, and sludge sedimentation time.
【請求項7】 処理水の取出し装置が精密濾過膜であっ
て、これを浄化槽の中または別に設けた槽に設置してあ
る請求項5記載の豚舎。
7. The piggery according to claim 5, wherein the device for taking out the treated water is a microfiltration membrane, which is installed in a septic tank or a separately provided tank.
【請求項8】 前記浄化槽に更に溶存酸素濃度計、酸化
還元電位計及び水素イオン濃度計を備えている請求項3
記載の豚舎。
8. The purifying tank further comprises a dissolved oxygen concentration meter, an oxidation-reduction potentiometer, and a hydrogen ion concentration meter.
Pig house described.
JP2000271350A 2000-09-07 2000-09-07 Pigpen Pending JP2002084908A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000271350A JP2002084908A (en) 2000-09-07 2000-09-07 Pigpen

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000271350A JP2002084908A (en) 2000-09-07 2000-09-07 Pigpen

Publications (1)

Publication Number Publication Date
JP2002084908A true JP2002084908A (en) 2002-03-26

Family

ID=18757655

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000271350A Pending JP2002084908A (en) 2000-09-07 2000-09-07 Pigpen

Country Status (1)

Country Link
JP (1) JP2002084908A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006102579A (en) * 2004-10-01 2006-04-20 Matsushita Electric Ind Co Ltd Parlor waste water treatment system
JP2006159046A (en) * 2004-12-06 2006-06-22 Tohoku Univ Method for determining state of operation of water treatment facilities by microorganism community analysis
JP2008264696A (en) * 2007-04-20 2008-11-06 Ooita Ken Biological purification treatment method of sewage from cattle house using white distilled liquor production waste liquid
CN101849511A (en) * 2010-06-02 2010-10-06 黑龙江洛东生物技术有限公司 Padding for biological fermentation bed, preparation and application thereof
CN104365490A (en) * 2014-11-04 2015-02-25 覃能明 Cleaning-free and washing-free method of pigpen
CN106719009A (en) * 2017-01-26 2017-05-31 广西宏华生物实业股份有限公司 A kind of energy-saving environment-protecting pig house
CN107750966A (en) * 2017-11-17 2018-03-06 北京昊业同宇科技有限公司 A kind of flushing-free ecological environmental protection pig house
CN109042353A (en) * 2018-08-03 2018-12-21 安徽省强家庄生态农业有限公司 A kind of dry clear formula excrement storage and handling facility of one-storey house formula pig house

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006102579A (en) * 2004-10-01 2006-04-20 Matsushita Electric Ind Co Ltd Parlor waste water treatment system
JP2006159046A (en) * 2004-12-06 2006-06-22 Tohoku Univ Method for determining state of operation of water treatment facilities by microorganism community analysis
JP2008264696A (en) * 2007-04-20 2008-11-06 Ooita Ken Biological purification treatment method of sewage from cattle house using white distilled liquor production waste liquid
CN101849511A (en) * 2010-06-02 2010-10-06 黑龙江洛东生物技术有限公司 Padding for biological fermentation bed, preparation and application thereof
CN104365490A (en) * 2014-11-04 2015-02-25 覃能明 Cleaning-free and washing-free method of pigpen
CN106719009A (en) * 2017-01-26 2017-05-31 广西宏华生物实业股份有限公司 A kind of energy-saving environment-protecting pig house
CN107750966A (en) * 2017-11-17 2018-03-06 北京昊业同宇科技有限公司 A kind of flushing-free ecological environmental protection pig house
CN109042353A (en) * 2018-08-03 2018-12-21 安徽省强家庄生态农业有限公司 A kind of dry clear formula excrement storage and handling facility of one-storey house formula pig house

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