JPH0127998B2 - - Google Patents

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Publication number
JPH0127998B2
JPH0127998B2 JP19587581A JP19587581A JPH0127998B2 JP H0127998 B2 JPH0127998 B2 JP H0127998B2 JP 19587581 A JP19587581 A JP 19587581A JP 19587581 A JP19587581 A JP 19587581A JP H0127998 B2 JPH0127998 B2 JP H0127998B2
Authority
JP
Japan
Prior art keywords
aeration
liquid
temperature
human waste
aeration tank
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
Application number
JP19587581A
Other languages
Japanese (ja)
Other versions
JPS5898187A (en
Inventor
Tomoyuki Shibata
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.)
Ebara Corp
Original Assignee
Ebara Corp
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 Ebara Corp filed Critical Ebara Corp
Priority to JP56195875A priority Critical patent/JPS5898187A/en
Publication of JPS5898187A publication Critical patent/JPS5898187A/en
Publication of JPH0127998B2 publication Critical patent/JPH0127998B2/ja
Granted 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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
    • 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

Description

【発明の詳細な説明】 本発明は家畜し尿処理に用いられる液面上の空
間に回転駆動されるカツタと散水形式の消泡器を
備えた曝気槽の運転方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method of operating an aeration tank that is used for treating livestock human waste and is equipped with a cutter that is rotatably driven in a space above the liquid level and a water spray type defoamer.

従来より汚水処理のピツト内に曝気装置を設置
し、汚水中に空気中の酸素を吹込んで汚水の浄化
処理を行うことが広く実施されている。
Conventionally, it has been widely practiced to install an aeration device in a sewage treatment pit and blow oxygen from the air into the sewage to purify the sewage.

ところで、従来濃度の濃い汚水、例えば牛、豚
の排泄物、し尿のみよりなる汚水等を曝気装置に
より処理する場合に送入せられた空気が浮上する
際泡となり、汚水面上に泡の層ができ、次第に増
大して汚水処理槽が密閉型の場合は上部空間に充
満し、汚水処理槽が開放型の場合は泡が地上にあ
ふれ出ることになり、衛生上、保守点検の点より
も好ましくない結果となることがある。
By the way, conventionally, when sewage with a high concentration, such as sewage consisting only of cow and pig excrement or human waste, is treated using an aeration device, the air introduced bubbles when it floats to the surface, creating a layer of bubbles on the surface of the sewage. If the sewage treatment tank is a closed type, the upper space will be filled with foam, and if the sewage treatment tank is an open type, the foam will overflow to the ground, making it more difficult for hygiene and maintenance inspection. This may lead to undesirable results.

泡が発生すると汚水処理槽の点検ができず、泡
を取除くのは容易なことではない。上記は一例を
示すものであるが、一般に汚水を曝気し、或は撹
拌すると泡の発生する場合がある。
Bubbles make it impossible to inspect the sewage treatment tank, and removing the bubbles is not easy. Although the above is an example, bubbles may generally be generated when wastewater is aerated or stirred.

然し泡は一方で曝気槽内の被処理液の保温のた
めに有用であり、又一方曝気によりバクテリアが
内生呼吸期に入ると被処理液体中のガス発生量も
多くなり、ガスを逃がす必要がでてくるので泡を
取除いてガスを逃がしてやる必要がある。
However, foam is useful for keeping the liquid to be treated in the aeration tank warm, and on the other hand, when bacteria enter the endogenous respiration phase due to aeration, the amount of gas generated in the liquid to be treated increases, and it is necessary to release the gas. Since bubbles will appear, it is necessary to remove the bubbles and allow the gas to escape.

実願昭56−153449号の考案曝気槽における消泡
装置は「汚水を溜めた槽中に空気を吹き込んで曝
気を行う曝気装置を備えた密閉した曝気槽上部の
上壁と曝気槽中の被処理液面間に回転駆動される
泡切りカツタと散水形式の消泡器を備えた曝気槽
における消泡装置。」であつて醗酵初期より腐熟
するまで適切な泡処理がなされ、又初期は適度の
泡を残すから被処理液の昇温を助け、醗酵日数を
短くすることも可能となる効果を生じている。
The defoaming device in the aeration tank devised in Utility Application No. 56-153449 is ``a closed upper wall of the aeration tank equipped with an aeration device that blows air into the tank that collects sewage and a covering inside the aeration tank. This is a foam defoaming device in an aeration tank that is equipped with a foam cutter that is rotated between the surface of the treated liquid and a water sprinkler type defoamer. This has the effect of helping to raise the temperature of the liquid to be treated and shortening the number of days required for fermentation.

処が前述の考案では曝気槽上部に泡検知器を備
えて泡検知器により泡の状態を知り泡切りカツタ
と消泡器の運転を行つている。泡の発生量と、し
尿処理の堆肥化醗酵の過程は関係はあるとしても
泡の発生量と要求酸素量は密接な対応を示してお
らない。又、泡の発生にはばらつきがあり、制御
を行うには泡検知器を備えることがすぐれている
が泡検知器による堆肥化過程の検知制御には限界
がある。そこで上述の考案では曝気装置の運転は
手動制御となつている。
However, in the above-mentioned device, a bubble detector is installed at the top of the aeration tank, and the condition of the bubbles is determined by the bubble detector, and the bubble cutter and defoamer are operated. Although there is a relationship between the amount of foam generated and the process of composting and fermentation in human waste treatment, the amount of foam generated and the amount of oxygen required do not show a close correspondence. In addition, there are variations in the generation of bubbles, and although it is excellent to have a bubble detector for control, there are limits to the detection and control of the composting process using a bubble detector. Therefore, in the above-mentioned device, the operation of the aeration device is manually controlled.

本発明は上述したようにし尿処理において曝気
槽に曝気装置と泡切りカツタを備える泡切り機と
散液式の消泡器を備えるものにおいて曝気装置の
し尿処理の堆肥化過程に適応した適切な運転と、
し尿より発生する泡を適度に保温に利用するとと
もにガスの放散を行う如く消泡装置の適切な運転
を行える消泡装置を備える曝気槽の運転方法を得
ることを目的とするものである。
As described above, the present invention is an aeration tank equipped with an aeration device, a foam cutter equipped with a foam cutter, and a spray defoamer in the human waste treatment, and the present invention provides an appropriate method adapted to the composting process of the human waste treatment using the aeration device. driving and
The object of the present invention is to provide a method for operating an aeration tank equipped with an antifoaming device that can appropriately operate the antifoaming device so as to appropriately utilize foam generated from human waste for heat retention and dissipate gas.

本発明の第1の発明は泡切機と散液式の消泡器
と曝気装置を備えた曝気槽の運転方法であつて曝
気槽内にし尿を入れて曝気装置により曝気を行う
場合に、曝気槽内にし尿の温度を検知する温度検
知器を備え、温度検知器がし尿の温度を検知して
発生する信号により制御装置を介して堆肥化過程
の初期バクテリアが充分増殖し始める近傍温度に
達するまで曝気装置を連続運転することを特徴と
する消泡装置を備える曝気槽の運転方法である。
The first invention of the present invention is a method of operating an aeration tank equipped with a foam cutter, a liquid defoamer, and an aeration device, and when human waste is placed in the aeration tank and aeration is performed by the aeration device, The aeration tank is equipped with a temperature sensor that detects the temperature of human waste, and the signal generated when the temperature sensor detects the temperature of the human waste is sent via a control device to a temperature close to the point at which the initial bacteria in the composting process begin to grow sufficiently. This is a method of operating an aeration tank equipped with an antifoaming device, characterized in that the aeration device is continuously operated until the antifoaming device is reached.

本発明の第2の発明は泡切機と散液式の消泡器
と曝気装置を備えた曝気槽の運転方法であつて曝
気槽内にし尿を入れて曝気装置により曝気を行う
場合に、曝気槽内にし尿のPH値を検知する酸性度
検知器を備え、酸性度検知器がし尿のPH値を検知
して発生する信号により制御装置を介して堆肥化
過程の初期バクテリアが充分増殖し始める近傍温
度に達するまで曝気装置を連続運転することを特
徴とする消泡装置を備える曝気槽の運転方法であ
る。
The second invention of the present invention is a method of operating an aeration tank equipped with a foam cutter, a liquid defoamer, and an aeration device, and when human waste is placed in the aeration tank and aeration is performed by the aeration device, The aeration tank is equipped with an acidity detector that detects the pH value of human waste, and the signal generated when the acidity detector detects the pH value of human waste is sent via a control device to ensure that the initial bacteria in the composting process are sufficiently grown. This is a method of operating an aeration tank equipped with an antifoaming device, characterized in that the aeration device is continuously operated until the temperature reaches a temperature close to the starting temperature.

第1図は本発明の実施例を示すフローシートで
ある。曝気槽1の槽底には全体を2で示す曝気装
置、全体を3で示す水中モータポンプが設置せら
れる。
FIG. 1 is a flow sheet showing an embodiment of the present invention. At the bottom of the aeration tank 1, an aeration device, generally indicated by 2, and a submersible motor pump, generally indicated by 3, are installed.

曝気装置2は上部にモータ4をその下方にポン
プ5を備えている。ポンプ5の吐出口にはノズル
本体7が接続されており、ノズル本体7にデイフ
ユーザ8が一直線になるように接続されている。
ノズル本体7には図示されないノズルが設けられ
ており、またノズルの開口近傍の空気室で開口す
る空気導入のための直管の空気導入管9が接続さ
れており、空気導入管9は曝気槽1の上壁を挿通
して空気導入管9の他端が泡切り機の外筒11の
出口通路に連結されている。
The aeration device 2 includes a motor 4 at the top and a pump 5 below. A nozzle body 7 is connected to the discharge port of the pump 5, and a diff user 8 is connected to the nozzle body 7 in a straight line.
The nozzle body 7 is provided with a nozzle (not shown), and is connected to a straight air introduction pipe 9 for introducing air that opens in an air chamber near the opening of the nozzle, and the air introduction pipe 9 is connected to an aeration tank. 1, and the other end of the air introduction pipe 9 is connected to the outlet passage of the outer cylinder 11 of the bubble cutter.

泡切り機10は外筒11内にモータ12を外筒
11と間隙をおいて備えており、上壁の外部に固
定せられたベース13に外筒11、モータ12が
固定され、モータ12のモータ軸はベース13中
を挿通して軸端には曝気槽1中の液面より離れた
位置に泡切りの羽根翼を備えた泡切りカツタ14
が固定されている。外筒11の上部は外筒11の
穴より消音器15を介して大気中に通じている。
The foam cutter 10 includes a motor 12 in an outer cylinder 11 with a gap between the outer cylinder 11 and the outer cylinder 11. The outer cylinder 11 and the motor 12 are fixed to a base 13 fixed to the outside of the upper wall. The motor shaft passes through the base 13, and a foam cutter 14 is provided at the end of the shaft with a foam cutter blade located away from the liquid level in the aeration tank 1.
is fixed. The upper part of the outer cylinder 11 communicates with the atmosphere from a hole in the outer cylinder 11 via a muffler 15.

水中モータポンプ3は通常の水中モータポンプ
と同様モータ16の下部にポンプ17が連結さ
れ、ポンプ17の吐出口には吐出管18が連結さ
れ、吐出管18は上壁を挿通してT接手19に連
結され、T接手19の両側は開閉弁20,21が
固定されている。開閉弁20にはエルボを連結し
た下向の出口管22が固定され、出口管22端に
は消泡器23が固定されている。消泡器23は出
口管22の開口端と間隔をおいて傘状散液板を設
けたもので出口管22より噴出する液体は散液板
に当つて曝気槽1の液面広くに液体を散布して消
泡を行うものである。
The submersible motor pump 3 has a pump 17 connected to the lower part of a motor 16 like a normal submersible motor pump, and a discharge pipe 18 is connected to the discharge port of the pump 17, and the discharge pipe 18 is inserted through the upper wall and connected to a T-joint 19. On-off valves 20 and 21 are fixed to both sides of the T-joint 19. A downward outlet pipe 22 connected to an elbow is fixed to the on-off valve 20, and a defoamer 23 is fixed to the end of the outlet pipe 22. The defoamer 23 is equipped with an umbrella-shaped liquid scattering plate spaced apart from the open end of the outlet pipe 22, and the liquid ejected from the outlet pipe 22 hits the liquid scattering plate and spreads the liquid over a wide liquid surface in the aeration tank 1. It is used to defoam by spraying.

上壁には検知器24が取付けられていて曝気槽
1内の被処理液体の状態を示す指標の温度又はPH
を検知するようになつている。
A detector 24 is attached to the upper wall and measures the temperature or pH of the liquid in the aeration tank 1.
It is now possible to detect

即ち、検知器24は温度検知器又は酸性度検知
器である。
That is, the detector 24 is a temperature detector or an acidity detector.

開閉弁21には次の工程の二次貯留槽への配管
25又は堆肥化したふん尿をタンク車へ移し換え
るためのタンク車との接続をする管接手等が接続
させる。
The on-off valve 21 is connected to a pipe 25 to a secondary storage tank for the next process or a pipe joint for connection to a tank car for transferring composted manure to a tank car.

泡切り機10は実願昭56−79472号にかゝわる
考案のものでモータ12の発生熱の有効利用を計
ることができるもので好適であるが限定されるも
のではない。26は曝気槽1へ牛豚のふん尿の一
次処理された液が送入される送液管である。検知
器24よりはマイコン等の制御装置27へ配線さ
れている。制御装置27は検知器24から送られ
る信号を判別して曝気装置2、水中モータポンプ
3、泡切り機10を制御する指令を出すもので該
指令による制御信号は増幅回路28に送られて増
幅され、増幅回路28は出力回路29を開閉すよ
うになつている。出力回路29は曝気装置2のモ
ータ4、水中モータポンプ3のモータ16、泡切
り機10のモータ12へ夫々電力を供給するもの
である。
The foam cutter 10 is a device based on Utility Model Application No. 56-79472, which is suitable for effectively utilizing the heat generated by the motor 12, but is not limited thereto. Reference numeral 26 denotes a liquid supply pipe through which a primarily treated liquid of cow and pig excreta is sent to the aeration tank 1. The detector 24 is wired to a control device 27 such as a microcomputer. The control device 27 discriminates the signal sent from the detector 24 and issues commands to control the aeration device 2, submersible motor pump 3, and bubble cutter 10. The control signal according to the command is sent to the amplifier circuit 28 and amplified. The amplifier circuit 28 is configured to open and close the output circuit 29. The output circuit 29 supplies electric power to the motor 4 of the aeration device 2, the motor 16 of the submersible motor pump 3, and the motor 12 of the bubble cutter 10, respectively.

第2図は横軸に曝気槽1へし尿の液分(以下単
に液30と称する場合がある)を入れてからの経
過日数を示し、縦軸は液30の液温、PH、及び曝
気槽1の周囲の気温を示す線図である。
In Figure 2, the horizontal axis shows the number of days that have passed since the human waste liquid (hereinafter sometimes simply referred to as liquid 30) was added to the aeration tank 1, and the vertical axis shows the temperature and pH of liquid 30, and the aeration tank. FIG. 1 is a diagram showing the temperature around No. 1. FIG.

送液管26より曝気槽1に満たされた液30は
第2図に示すように液温も気温とほぼ等しいかわ
ずかに高く21℃と低く、液30中のバクテリアも
有機物を捕捉する準備時間が必要であり、又充分
なバクテリア増殖に必要な温度に達していない。
液30の当初の温度は従つて冬期は更に低い訳で
ある。そこで制御装置27よりの指令は増幅回路
28、出力回路29を介してモータ4,12へ送
られ曝気装置2は運転され、モータ12はカツタ
14を回転させる。曝気に必要な空気は消音器1
5―外筒11―空気導入管9―ノズル本体7と吸
込まれ、デイフユーザ8にてポンプ5により吐出
された液体に巻込まれて液30中へ放散される。
液30中に入つた空気中の酸素は一部液中へ溶け
込むが残りは泡となつて液30の上面に上昇す
る。液30は濃度の高いし尿であるから液面上に
は泡が消滅しないで泡層を生ずる。曝気空気は外
筒11中でモータ12を冷却し、空気は暖められ
る。従つて液温より高い空気により当初は液30
は加熱される。最初より液温が20〜30℃位になる
までは液温が20〜30℃の何れかになりバクテリア
の増殖の条件を準備するためで曝気による撹拌に
よる流体摩擦により液30は昇温する。かくして
実例としての第2図に示すように温度約30℃前後
になるとバクテリアの増殖も急激に増加する段階
に入る。処がバクテリアが急激に増加する段階と
なつても要求酸素量は総量は多くないのでその
まゝ曝気装置2を運転すると曝気装置2は要求酸
素量がバクテリアが内生呼吸をする後半の段階の
最大酸素要求量に見合つて設けられているから過
曝気となつてバクテリアは死滅する。そこで検知
器24が液温30℃を検知するとその信号は制御装
置27に送られ制御装置27はモータ4を断続運
転をする指令を出し、増幅回路28、出力回路2
9を介してモータ4は例えば2時間運転、1時間
停止の断続運転に入り、酸素供給量は制限され適
度の酸素がバクテリアに与えられる。
As shown in Fig. 2, the temperature of the liquid 30 filled into the aeration tank 1 from the liquid pipe 26 is as low as 21°C, which is almost equal to or slightly higher than the air temperature, and the preparation time for the bacteria in the liquid 30 to capture organic matter. temperature required for sufficient bacterial growth.
The initial temperature of the liquid 30 is therefore lower in winter. Therefore, a command from the control device 27 is sent to the motors 4 and 12 via the amplifier circuit 28 and the output circuit 29, the aeration device 2 is operated, and the motor 12 rotates the cutter 14. The air required for aeration is silenced by silencer 1.
5-outer cylinder 11-air introduction pipe 9-nozzle body 7, and is drawn into the liquid discharged by the pump 5 in the diffuser 8 and dispersed into the liquid 30.
Part of the oxygen in the air that has entered the liquid 30 dissolves into the liquid, but the rest rises to the top of the liquid 30 in the form of bubbles. Since the liquid 30 is highly concentrated human waste, the bubbles do not disappear and form a foam layer on the liquid surface. The aeration air cools the motor 12 in the barrel 11 and the air is warmed. Therefore, due to the air having a higher temperature than the liquid temperature, the liquid temperature initially becomes 30.
is heated. From the beginning until the liquid temperature reaches about 20 to 30°C, the temperature of the liquid 30 increases due to fluid friction caused by agitation due to aeration in order to prepare conditions for bacterial growth. Thus, as shown in Figure 2 as an example, when the temperature reaches around 30°C, bacterial growth rapidly increases. However, even when bacteria rapidly increase, the total amount of oxygen required is not large, so if the aeration device 2 is operated as it is, the amount of oxygen required will be the same as in the latter half of the stage when bacteria undergo endogenous respiration. Since it is set to meet the maximum oxygen demand, it causes overaeration and kills bacteria. Therefore, when the detector 24 detects a liquid temperature of 30°C, the signal is sent to the control device 27, which issues a command to operate the motor 4 intermittently.
9, the motor 4 enters intermittent operation, for example, running for 2 hours and stopping for 1 hour, and the amount of oxygen supplied is limited so that an appropriate amount of oxygen is given to the bacteria.

一方泡切り機10は運転したまゝであつたから
生じた泡は泡切り機10のカツタ14により液化
される。カツタによる消泡作用はカツタの回転す
る近くに限られるから液30の液面よりカツタ1
4が離れているから泡層は液面上に残つている。
従つて液温が充分に上昇し、且つ液30中より発
生するガスの量が多くない間は泡切り機10を運
転する。即ち液温20〜30℃、第2図の実例では約
30℃まで泡切り機10を連続運転する。
On the other hand, since the foam cutter 10 remained in operation, the foam generated is liquefied by the cutter 14 of the foam cutter 10. Since the defoaming effect of the cutter is limited to the area near where the cutter rotates, the cutter 1 is lower than the liquid level of the liquid 30.
4 is far apart, so the foam layer remains on the liquid surface.
Therefore, the bubble remover 10 is operated until the liquid temperature has risen sufficiently and the amount of gas generated from the liquid 30 is not large. In other words, the liquid temperature is 20 to 30℃, and in the example shown in Figure 2, it is approximately
The bubble cutter 10 is operated continuously up to 30°C.

かくしてモータ4が断続運転に入ると同時、又
は更に液30の温度が上昇して液温が40〜50℃と
なりバクテリアの量も最も多くなり泡の発生も多
くなると検知器24は液温約40℃〜約50℃の設定
値を検知してその信号は制御装置27に送られ
る。制御装置27は泡切り機10のモータ12を
断電し、水中モータポンプ3のモータ16に通電
指令を出し、増幅回路28、出力回路29を介し
てモータ12は消勢され、モータ16は附勢され
ポンプ17は駆動され、ポンプ17は液30を吸
込んで吐出管18にて送り出しT接手19、予め
開かれている開閉弁20、出口管22をとおり消
泡器23で散水して液30上の泡を消滅させる。
散液式の消泡器23は散液範囲について泡を完全
に消滅させる。この時点では液30の状態はバク
テリアが最大量に達する過程であつて、醗酵熱も
増大しているので保温の必要がなく、液30中か
ら発生する蒸気を含むガスが多くなるので放散の
必要がでてくる。液30の温度が更に上昇して40
〜50℃になりバクテリアが自生呼吸をするように
なると酸素要求量も最大近くに達するそこで検知
器24が該温度40〜50℃の何れかの値を検知する
とその信号は制御装置27へ送られて制御装置2
7は増幅回路28、出力回路29を介してモータ
4を連続運転に切換え、連続して曝気が行われ
る。もしくは液30の状態によりこの段階では有
機物量も減少するので曝気装置2の断続運転を続
ける場合もある。液温が約50℃位になると醗酵熱
のみで温度は上昇するから大気をそのまゝ取り入
れてもよい。この状態で曝気槽は稼動され液面上
よりは蒸気を含むガスが盛んに発生する。一方泡
の発生も多いが消泡器23により消滅させられる
のでガスの放散を邪げられることはない。尚又散
水により表面曝気が行われる。又、散水形式の消
泡器による消泡効果は著しいので液面上に全く泡
を残さないことになり、尚そのように消泡するこ
とが液30によつては不要な場合もあるのでモー
タ12と16を交互に運転して泡の発生を適度に
して動力費の節減も計るようにする。
Thus, at the same time as the motor 4 enters intermittent operation, or when the temperature of the liquid 30 rises further and the liquid temperature reaches 40 to 50°C, the amount of bacteria becomes the largest and the generation of bubbles increases, the detector 24 detects that the liquid temperature is about 40°C. A set value of .degree. C. to about 50.degree. C. is detected and the signal is sent to the control device 27. The control device 27 de-energizes the motor 12 of the bubble cutter 10, issues an energization command to the motor 16 of the submersible motor pump 3, de-energizes the motor 12 via the amplifier circuit 28 and output circuit 29, and de-energizes the motor 16. The pump 17 sucks in the liquid 30 and sends it out through the discharge pipe 18 through the T-joint 19, the previously opened on-off valve 20, and the outlet pipe 22, and is sprayed with water by the defoamer 23 to form the liquid 30. Disappear the bubbles on top.
The liquid spray type defoamer 23 completely extinguishes foam within the liquid spray range. At this point, the liquid 30 is in the process of reaching its maximum amount of bacteria, and the heat of fermentation is also increasing, so there is no need to keep it warm, and the amount of gas containing steam generated from the liquid 30 is increasing, so it is necessary to dissipate it. comes out. The temperature of liquid 30 further increases to 40
When the temperature reaches ~50°C and bacteria begin to breathe naturally, the amount of oxygen required also reaches its maximum.When the detector 24 detects a temperature between 40 and 50°C, the signal is sent to the control device 27. control device 2
7, the motor 4 is switched to continuous operation via the amplifier circuit 28 and the output circuit 29, and aeration is performed continuously. Alternatively, depending on the state of the liquid 30, the amount of organic matter also decreases at this stage, so the aeration device 2 may continue to be operated intermittently. When the temperature of the liquid reaches about 50℃, the temperature will rise due to fermentation heat alone, so you can just take in the atmosphere. In this state, the aeration tank is operated and a large amount of gas containing steam is generated above the liquid level. On the other hand, although many bubbles are generated, they are eliminated by the defoamer 23, so that gas dissipation is not hindered. Surface aeration is also performed by water sprinkling. In addition, since the defoaming effect of the water sprinkler type defoamer is so remarkable that no foam is left on the liquid surface, such defoaming may not be necessary depending on the liquid 30, so the motor 12 and 16 are operated alternately to moderate the generation of foam and to reduce power costs.

かくして腐熟が完了するとモータ4,12,1
6は断電され、開閉弁20を閉じ開閉弁21を開
いて液30はポンプ17により汲み出され配管2
5より送り出される。
When ripening is completed in this way, the motors 4, 12, 1
6 is cut off, the on-off valve 20 is closed and the on-off valve 21 is opened, and the liquid 30 is pumped out by the pump 17 to the pipe 2.
Sent from 5.

検知器24液30のPHを検知するものである場
合は液温とPHが関連をもつので温度に相当するPH
をもつて上述した処と同様の制御を行うものであ
る。第2図に示すように温度が約30℃に対応した
PHは8.0で最初の飽和状態にあるのでそれよりも
若干小さいPH8近傍で曝気装置2は断続運転に切
換えられる。温度40〜50℃間の例えば温度42℃に
対応したPHは8.2であるからPH8.2で泡切り機10
を止め消泡器23に送液する。温度約45℃に対応
するPHは8.4であるが飽和状態にあるからPH8.4よ
り小さいPH8.4近傍で曝気装置2を連続運転に切
換える。もしくは有機物量が減少しているときは
断続運転を続ける。
If the detector is to detect the PH of the liquid 30, the liquid temperature and PH are related, so the PH that corresponds to the temperature
The control is similar to that described above. As shown in Figure 2, the temperature corresponded to approximately 30℃.
Since the pH is in the initial saturated state at 8.0, the aeration device 2 is switched to intermittent operation when the pH is slightly lower than 8.0. For example, the pH corresponding to a temperature of 42℃ between 40 and 50℃ is 8.2.
is stopped and the liquid is sent to the defoamer 23. The pH corresponding to a temperature of about 45° C. is 8.4, but it is in a saturated state, so the aeration device 2 is switched to continuous operation at around PH8.4, which is lower than PH8.4. Alternatively, continue intermittent operation when the amount of organic matter is decreasing.

以上のように本発明の泡切機、散液形式の消泡
器、曝気装置を備える曝気槽の運転方法によれば
バクテリアの増殖の準備期には泡切機の作用によ
り泡が適度に液面上に残り曝気装置は連続運転さ
れ昇温する。尚又泡切機のモータの入力は曝気槽
内へ熱として移転する。バクテリアの増殖期に入
ると過曝気をしないように断続運転し、同時に温
度上昇も計る必要があるから、泡切機は運転さ
れ、泡は残される。バクテリア量が最大量近くに
なると泡切機は停止され散水形式の消泡器でもつ
て液面上の泡を消滅するか、泡切機と消泡器を交
互に作用させて液中のガスを逃げ易くする。この
時分には醗酵熱により液温は保たれるから特に保
温を計る必要もなくなる。ついで40〜50℃位の液
温になると要求酸素量が最も多くなるので連続曝
気されるか有機物残量によつては断続曝気が継続
される。このような過程が自動で行われ家畜し尿
の曝気処理が最適な過程で行われる。
As described above, according to the method of operating an aeration tank equipped with a foam cutter, a liquid defoamer, and an aeration device according to the present invention, during the preparatory period for bacterial growth, the action of the foam cutter allows the foam to be properly liquefied. The aeration equipment remaining on the surface is operated continuously and the temperature rises. Additionally, the input to the foam cutter motor is transferred as heat into the aeration tank. When the bacteria enters the growth phase, it is necessary to operate intermittently to prevent overaeration and at the same time measure the temperature rise, so the foam cutter is operated and the foam is left behind. When the amount of bacteria approaches the maximum amount, the bubble cutter is stopped and either a water spray type defoamer is used to extinguish the bubbles on the liquid surface, or the bubble cutter and defoamer are operated alternately to eliminate the gas in the liquid. Make it easier to escape. At this time, the temperature of the liquid is maintained by the fermentation heat, so there is no need to keep it warm. Then, when the liquid temperature reaches about 40 to 50°C, the amount of oxygen required is the highest, so continuous aeration is carried out, or depending on the amount of organic matter remaining, intermittent aeration is continued. This process is carried out automatically, and the aeration treatment of livestock human waste is carried out in an optimal manner.

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

第1図は本発明の実施例を説明するフローシー
ト、第2図は第1図において堆肥化経過日数とし
尿の状態の関係を表わす線図である。 1……曝気槽、2……曝気装置、3……水中モ
ータポンプ、4……モータ、5……ポンプ、7…
…ノズル本体、8……デイフユーザ、9……空気
導入管、10……泡切り機、11……外筒、12
……モータ、13……ベース、14……泡切りカ
ツタ、15……消音器、16……モータ、17…
…ポンプ、18……吐出管、19……T接手、2
0……開閉弁、21……開閉弁、22……出口
管、23……消泡器、24……検知器、25……
配管、26……送液管、27……制御装置、28
……増幅回路、29……出力回路、30……液。
FIG. 1 is a flow sheet explaining an embodiment of the present invention, and FIG. 2 is a diagram showing the relationship between the number of days elapsed after composting and the condition of human urine in FIG. 1. 1... Aeration tank, 2... Aeration device, 3... Submersible motor pump, 4... Motor, 5... Pump, 7...
... Nozzle body, 8 ... Diffusion user, 9 ... Air introduction pipe, 10 ... Bubble cutter, 11 ... Outer cylinder, 12
... Motor, 13 ... Base, 14 ... Foam cutter, 15 ... Silencer, 16 ... Motor, 17 ...
...Pump, 18...Discharge pipe, 19...T joint, 2
0... On-off valve, 21... On-off valve, 22... Outlet pipe, 23... Defoamer, 24... Detector, 25...
Piping, 26...Liquid feeding pipe, 27...Control device, 28
...Amplification circuit, 29...Output circuit, 30...Liquid.

Claims (1)

【特許請求の範囲】 1 泡切機と散液式の消泡器と曝気装置を備えた
曝気槽の運転方法であつて曝気槽内にし尿を入れ
て曝気装置により曝気を行う場合に、曝気槽内に
し尿の温度を検知する温度検知器を備え、温度検
知器がし尿の温度を検知して発生する信号により
制御装置を介して堆肥化過程の初期バクテリアが
充分増殖し始める近傍温度に達するまで曝気装置
を連続運転することを特徴とする消泡装置を備え
る曝気槽の運転方法。 2 泡切機と散液式の消泡器と曝気装置を備えた
曝気槽の運転方法であつて曝気槽内にし尿を入れ
て曝気装置により曝気を行う場合に、曝気槽内に
し尿のPH値を検知する酸性度検知器を備え、酸性
度検知器がし尿のPH値を検知して発生する信号に
より制御装置を介して堆肥化過程の初期バクテリ
アが充分増殖し始める近傍温度に達するまで曝気
装置を連続運転することを特徴とする消泡装置を
備える曝気槽の運転方法。
[Claims] 1. A method for operating an aeration tank equipped with a foam cutter, a liquid defoamer, and an aeration device, in which human waste is placed in the aeration tank and aeration is performed by the aeration device. The tank is equipped with a temperature sensor that detects the temperature of the human waste, and a signal generated when the temperature sensor detects the temperature of the human waste is sent via a control device to reach a temperature close to the point at which the initial bacteria in the composting process begin to sufficiently proliferate. A method for operating an aeration tank equipped with an antifoaming device, characterized by continuously operating the aeration device until 2. A method of operating an aeration tank equipped with a foam cutter, a liquid defoamer, and an aeration device, and when human waste is placed in the aeration tank and aeration is performed by the aeration device, the PH of the human waste in the aeration tank is Equipped with an acidity detector that detects the pH value of human waste, the acidity detector detects the pH value of human waste and generates a signal that is used to control the aeration until the temperature reaches a temperature close to the point at which the initial bacteria in the composting process begin to grow sufficiently. A method of operating an aeration tank equipped with an antifoaming device, characterized in that the device is operated continuously.
JP56195875A 1981-12-04 1981-12-04 Operation of aerating cell equipped with defoaming means Granted JPS5898187A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56195875A JPS5898187A (en) 1981-12-04 1981-12-04 Operation of aerating cell equipped with defoaming means

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56195875A JPS5898187A (en) 1981-12-04 1981-12-04 Operation of aerating cell equipped with defoaming means

Publications (2)

Publication Number Publication Date
JPS5898187A JPS5898187A (en) 1983-06-10
JPH0127998B2 true JPH0127998B2 (en) 1989-05-31

Family

ID=16348434

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56195875A Granted JPS5898187A (en) 1981-12-04 1981-12-04 Operation of aerating cell equipped with defoaming means

Country Status (1)

Country Link
JP (1) JPS5898187A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2557670B2 (en) * 1987-11-21 1996-11-27 ゼオラケミカル株式会社 Animal husbandry waste disposal device
KR20020066721A (en) * 2001-02-13 2002-08-21 이명규 A Livestock Sewage Treatment Unit of Continuous Typed and Method thereof
JP2006075782A (en) * 2004-09-13 2006-03-23 Shin Meiwa Ind Co Ltd Foam suppressing unit of aeration tank and garbage treatment apparatus having the unit

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5541840A (en) * 1978-09-19 1980-03-24 Toyo Kuriin Kagaku Kk Aerobic, high temperature fermentation treatment of sewage and system therefor

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6131609Y2 (en) * 1978-10-09 1986-09-13
JPS575109Y2 (en) * 1979-02-21 1982-01-30

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5541840A (en) * 1978-09-19 1980-03-24 Toyo Kuriin Kagaku Kk Aerobic, high temperature fermentation treatment of sewage and system therefor

Also Published As

Publication number Publication date
JPS5898187A (en) 1983-06-10

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