JP2002086170A - Preliminary fermentation device of fermentation bacteria for sewage treatment - Google Patents

Preliminary fermentation device of fermentation bacteria for sewage treatment

Info

Publication number
JP2002086170A
JP2002086170A JP2000279290A JP2000279290A JP2002086170A JP 2002086170 A JP2002086170 A JP 2002086170A JP 2000279290 A JP2000279290 A JP 2000279290A JP 2000279290 A JP2000279290 A JP 2000279290A JP 2002086170 A JP2002086170 A JP 2002086170A
Authority
JP
Japan
Prior art keywords
bacteria
tank
fermentation
pump
casing
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.)
Withdrawn
Application number
JP2000279290A
Other languages
Japanese (ja)
Inventor
Isamu Ito
勇 伊藤
Toru Hirayama
透 平山
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.)
KUJIRAOKA SANGYO KK
MONOTEKKU KK
Tokan Co Ltd
Original Assignee
KUJIRAOKA SANGYO KK
MONOTEKKU KK
Tokan Co Ltd
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 KUJIRAOKA SANGYO KK, MONOTEKKU KK, Tokan Co Ltd filed Critical KUJIRAOKA SANGYO KK
Priority to JP2000279290A priority Critical patent/JP2002086170A/en
Publication of JP2002086170A publication Critical patent/JP2002086170A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M23/00Constructional details, e.g. recesses, hinges
    • C12M23/52Mobile; Means for transporting the apparatus
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M27/00Means for mixing, agitating or circulating fluids in the vessel
    • C12M27/02Stirrer or mobile mixing elements
    • C12M27/04Stirrer or mobile mixing elements with introduction of gas through the stirrer or mixing element
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M41/00Means for regulation, monitoring, measurement or control, e.g. flow regulation
    • C12M41/12Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature

Abstract

PROBLEM TO BE SOLVED: To decrease time corresponding to treatment after introducing fermentation bacteria for cleaning treatment, quantity of use of the bacteria and to shorten time of fermentation treatment by equipping a portable preliminary culture device nearby a sewage treating tank and preliminarily cultivating various kinds of fermentation bacteria. SOLUTION: A fermenting tank 20, a heating apparatus 22, a drawing pump 30, various kinds of bacteria storing tanks 50a, 50b and 50c, and various kinds of bacteria supplying pump tanks 52a, 52b and 52c are equipped in a casing 10 with casters. Various kinds of hose connecting parts 32, 32b and 32c are arranged at the outer face of the casing 10.

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】この発明は中規模の汚水処理
装置に、近年多量に使用される嫌気性菌、好気性菌、そ
の他臭気除去菌などを予め、予備培養する装置に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a medium-scale sewage treatment apparatus for pre-cultivating anaerobic bacteria, aerobic bacteria, and other odor-removing bacteria used in large quantities in recent years.

【0002】[0002]

【従来の技術】近年中規模の汚水処理装置に於いても嫌
気性菌、好気性菌、これら混合菌若しくは嫌気・好気両
性菌(以下浄化処理発酵菌と云う)。臭気乃至消臭除去
発酵菌その他浄化施設や各種パイプなどに付着する付着
物を分解するいわゆるクリーニング菌などが多量に使用
されるようになってきている。ところが、この種の中規
模の汚水処理装置は5乃至30トン程度の処理槽(嫌気
性濾床槽、接触曝気槽など)が2乃至5槽並列に設置さ
れたものが殆どであり、前記各種処理菌を使用する場
合、これら処理槽に菌を直接投入するか、或いは前記処
理槽の一つを予備培養槽として使用している。従って、
予備培養槽の大きさは5トン乃至30トン入りと大き
い。よって前記投入する菌量も多くなり、また前記培養
槽に供給された汚水、糞尿などは菌の初期培養に適した
温度ではなく、菌が活性化するまで相当の時間を要し、
処理能力が低下し、これを補うには更に菌の使用量を増
加せざるをえず、処理コストを押し上げる。また、前記
の5乃至30トン槽を培養に適した温度まで加熱すると
なると、相当の熱エネルギ−を要し、汚水処理コストを
押し上げることになり現実的ではない。
2. Description of the Related Art In recent years, anaerobic bacteria, aerobic bacteria, mixed bacteria thereof, or anaerobic / aerobic bacteria (hereinafter referred to as purification fermentation bacteria) have been used even in a medium-scale sewage treatment apparatus. A large amount of fermentative bacteria that remove odors or deodorants, so-called cleaning bacteria that decompose adhering substances that adhere to purification facilities, various pipes, and the like have been used. However, most of this kind of medium-scale sewage treatment equipment is provided with 2 to 5 treatment tanks (anaerobic filter bed tank, contact aeration tank, etc.) of about 5 to 30 tons in parallel. When using the treated bacteria, the bacteria are directly introduced into these treatment tanks, or one of the treatment tanks is used as a preculture tank. Therefore,
The size of the preculture tank is as large as 5 to 30 tons. Therefore, the amount of bacteria to be added is also large, and the sewage, manure, and the like supplied to the culture tank are not at a temperature suitable for the initial culture of the bacteria, and require a considerable time until the bacteria are activated,
The processing capacity is reduced, and to compensate for this, the amount of bacteria used must be further increased, thereby increasing the processing cost. Further, if the 5 to 30 ton tank is heated to a temperature suitable for culturing, considerable heat energy is required, which increases the cost of sewage treatment, which is not realistic.

【0003】[0003]

【発明が解決しようとする課題】そこで、この発明は前
記各種の菌の初期において、菌の増殖によい条件を与
え、早期に活発な繁殖を開始し、これを処理槽に順次供
給して、菌の使用量を最小限に留め、且つ処理槽の能力
を向上させる装置を市場に提供し、既設の処理槽の近傍
に置き、単にホ−スで接続するだけで、各種菌使用の汚
水、糞尿処理装置にすることが出来るようにするためで
ある。
Therefore, the present invention provides good conditions for the growth of bacteria at the beginning of the various bacteria, starts vigorous propagation at an early stage, and sequentially supplies them to the treatment tank. Provide the market with a device that minimizes the amount of bacteria used and improves the capacity of the treatment tank. Place it near the existing treatment tank and simply connect it with a hose. This is to make it possible to use a manure processing device.

【0004】[0004]

【課題を解決するための手段】前記の課題を達成するた
めにこの特定発明は、キャスタ−付きのケ−シング内に
は培養槽処理液供給及び吐出パイプ、数個の発酵菌貯蔵
槽及びこれより発酵菌液を前記培養槽にそれぞれ供給す
る数個の菌供給ポンプ及び菌供給パイプ、培養槽に栄養
剤を供給する栄養剤貯蔵槽及び供給装置を備え、前記培
養槽に処理液を汲み揚げるポンプは前記ケーシング内乃
至この近傍に備えてあり、前記培養槽は円筒形であっ
て、その中心に垂直な中空回転軸を備え、この中空回転
軸には半径方向に突出した腕棒の先端には前記培養槽の
軸方向に長い撹拌板が固着してあり、この撹拌翼の外縁
は前記培養槽内周面の略全長おいて極接近乃至軽く接触
させてあり、前記中空回転軸の外端は空気供給源に接続
してあり、また前記中空回転軸の一部培養槽内の底近く
には空気吹き込みパイプが半径方向に突出して設けてあ
り、この空気吹き込みパイプは前記中空回転軸の中空孔
に連通させてあり、前記培養槽の外周面には加熱装置が
装備してあることを特徴とする汚水処理発酵菌の予備発
酵装置とする。
SUMMARY OF THE INVENTION In order to achieve the above-mentioned object, the present invention provides a processing tank for supplying and discharging a treatment liquid in a culture tank, a storage tank for several fermentation bacteria, It further comprises several bacteria supply pumps and bacteria supply pipes for supplying fermentation bacteria liquid to the culture tank, a nutrient storage tank and a supply device for supplying nutrients to the culture tank, and pumps the treatment liquid into the culture tank. A pump is provided in or near the casing, and the culture tank is cylindrical and has a hollow rotating shaft perpendicular to the center thereof, and the hollow rotating shaft has a tip end of a radially protruding arm bar. A stirring plate long in the axial direction of the culture tank is fixed, and the outer edge of the stirring blade is brought into extremely close or light contact with almost the entire length of the inner peripheral surface of the culture tank, and the outer end of the hollow rotary shaft is Is connected to an air supply and An air blowing pipe is provided protruding in the radial direction near the bottom of the part of the empty rotating shaft in the culture tank, and the air blowing pipe communicates with the hollow hole of the hollow rotating shaft. The surface is equipped with a heating device, which is a preliminary fermentation device for sewage treatment fermentation bacteria.

【0005】また前記の課題を達成するために前記汚水
処理発酵菌の予備発酵装置における前記ケ−シングはほ
ゞ密閉型であり、内部で第1室と第2室に分かれて区画
してあり、第1室には前記培養槽及び加熱装置を備え、
第2室には数個の発酵菌貯蔵槽と空気調和装置を備え、
第1室と第2室は空気流が遮断してあり、前記第2室の
外壁面には発酵菌貯蔵槽に通じる発酵菌供給口乃至発酵
菌供給時に開閉可能な扉が設けてあり、前記第1室の外
壁の一部には原液供給ホ−ス、処理水放出ホ−ス、ドレ
ン放出ホ−スのそれぞれの接続口が設けてあることを特
徴とすることが好ましい。
[0005] In order to achieve the above object, the casing in the preliminary fermentation apparatus for sewage treatment fermentation bacteria is substantially hermetic, and is divided into a first chamber and a second chamber. , The first chamber includes the culture tank and a heating device,
The second room is equipped with several fermentation bacteria storage tanks and an air conditioner,
The first chamber and the second chamber are shut off from the air flow, and the outer wall surface of the second chamber is provided with a fermentation bacterium supply port communicating with the fermentation germ storage tank or a door that can be opened and closed at the time of fermentation germ supply, It is preferable that connection ports for a stock solution supply hose, a treated water discharge hose, and a drain discharge hose are provided in a part of the outer wall of the first chamber.

【0006】また前記の課題を達成するために前記汚水
処理発酵菌の予備発酵装置の前記第2室の一部には、制
御装置が設けてあり、その操作盤面はケ−シング外面に
露出させてあり、制御装置内には処理液ポンプ及び循環
ポンプの発停止、加熱装置による培養槽の温度制御装
置、数個の菌供給ポンプの発停、空気供給源の発停止、
その他換気装置の発停、の入力部が装備してあることを
特徴とすることが好ましい。また前記の課題を達成する
ために、前記予備発酵装置の前記制御装置の操作盤面
は、ケーシング外面に露出させる代わりに、ケーシング
内に納めてあり、操作壁面に対応した部分のみに、独立
した操作壁面用開閉扉が設けてあることを特徴とする場
合もある。また前記の課題を達成するために前記の汚水
処理発酵菌の予備発酵装置における前記培養槽には循環
ポンプが循環パイプを介して連結してあることを特徴と
することが好ましい。また前記の課題を達成するために
前記の汚水処理発酵菌の予備発酵装置の前記汲み揚げポ
ンプは前記ケーシングの中の第1室内に設けてあること
を特徴とする。
In order to achieve the above object, a control device is provided in a part of the second chamber of the preliminary fermentation device for sewage treatment fermentation bacteria, and a control panel surface of which is exposed to an outer surface of the casing. In the control device, start and stop of the processing solution pump and circulation pump, temperature control device of the culture tank by heating device, start and stop of several bacteria supply pumps, start and stop of air supply source,
In addition, it is preferable that an input unit for starting and stopping the ventilation device is provided. Further, in order to achieve the above object, the operation panel surface of the control device of the preliminary fermentation apparatus is housed in a casing instead of being exposed to an outer surface of the casing, and only an independent operation is performed on a portion corresponding to an operation wall surface. In some cases, a door for a wall is provided. In order to achieve the above object, it is preferable that a circulation pump is connected to the culture tank in the preliminary fermentation apparatus for sewage treatment fermentation bacteria via a circulation pipe. In order to achieve the above object, the pump for pumping the fermentation apparatus for sewage treatment fermentation bacteria is provided in a first chamber in the casing.

【0007】発明の作用前記の特定発明において、これ
を使用するには、処理原液を採取及び予備培養液を放出
し易い場所に、この装置をキャスタ−を利用して移動し
固定する。次に、汲み揚げポンプがケーシング内にある
とき(請求項6記載の発明)ケ−シングの外面に設けて
ある原液供給ホ−ス、処理水放出ホ−ス、ドレン放出ホ
−スのそれぞれの接続口にそれぞれホ−スを接続し、こ
れらのそれぞれの他端を処理槽のうち最も上流側槽に垂
す。或いは前記処理槽よりも上流側の受液槽曝気沈砂
槽、流量調整槽であってもよい。汲み揚げポンプがケー
シング外にあるときは、この一次側のホースを前記原液
汲み揚げ槽に入れ、2次側のホースをケーシングに設け
た処理液供給パイプに接続する。而して、処理液ポンプ
を制御装置Cの操作部の入力部より運転指令し、これを
運転すると、前記ケ−シング外のホ−ス及びケ−シング
内のパイプ及び汲み揚げポンプを通して、処理槽の原液
は培養槽に連続して汲み込まれる。通常この種の処理槽
には運転開始時に、前記浄化処理発酵菌を投入する場合
もあり、これらの使用を阻げるものではない。前記培養
槽が所定量に達したときに、前記汲み揚げポンプを一旦
停止する。
Operation of the Invention In the above-mentioned specific invention, in order to use it, this apparatus is moved and fixed using a caster to a place where the stock solution for treatment is easily collected and the preculture solution is easily released. Next, when the pump is in the casing (invention of claim 6), each of the stock solution supply hose, treated water discharge hose and drain discharge hose provided on the outer surface of the casing is provided. The hoses are connected to the connection ports, respectively, and the other ends of the hoses are dropped to the most upstream one of the processing tanks. Alternatively, it may be a liquid receiving tank aeration sand settling tank or a flow rate adjusting tank upstream of the processing tank. When the pump is outside the casing, the primary side hose is put in the undiluted solution pumping tank, and the secondary side hose is connected to the processing liquid supply pipe provided in the casing. When the operation of the processing liquid pump is instructed from the input section of the operation unit of the control device C, and the operation is performed, the processing liquid is pumped through the hose outside the casing, the pipe in the casing and the pump. The stock solution in the tank is continuously pumped into the culture tank. Usually, this type of treatment tank may be charged with the above-mentioned purification-treated fermentation bacterium at the start of operation, which does not hinder the use thereof. When the culture tank reaches a predetermined amount, the pump is temporarily stopped.

【0008】次に入力部より加熱装置の電源をオンと
し、培養槽の温度を培養に適した温度まで加熱し、以後
使用終了までこの温度を維持するようにする。
Next, the power of the heating device is turned on from the input unit, the temperature of the culture tank is heated to a temperature suitable for culture, and this temperature is maintained until the end of use.

【0009】他方、それぞれの発酵菌貯蔵槽には通常そ
れぞれ相互に異種の発酵菌をケ−シングの外壁面にある
供給口より、或いは第2室の扉を開け供給する。次に、
浄化処理発酵菌を使用する場合は、これに対応する発酵
菌貯蔵槽の菌供給装置を作動させ、浄化処理発酵菌を培
養槽に供給する。同時に前記中空回転軸をそのモ−タに
より回転し、また空気供給源を作動させくて、前記中空
回転軸及び空気吹き込みパイプより、空気を培養槽の液
中に供給する。また、必要に応じて、栄養剤槽にも培養
栄養剤を供給し、この栄養剤供給装置も運転し、培養栄
養剤も培養槽に供給する。同時に、脱臭乃至消臭発酵菌
を使用するときは、浄化槽発酵菌と同様の方法で脱臭乃
至消臭発酵菌が貯蔵してある別の発酵菌貯蔵槽より、脱
臭乃至消臭発酵菌を培養槽に供給する。一般に、脱臭乃
至消臭発酵菌は他の菌に先立って供給する方が好まし
い。更に、浄化処理施設のクリーニング及び汚の減量化
対策として、前記従来の技術の項において述べたいわゆ
るクリーニング菌を一緒に投入し、培養槽内、各種パイ
プ、ホース及び各種の制御弁などに付着する付着物の発
生を防止する。前述の取り扱い方においては、運転初期
において、培養槽が一旦満杯になったとき、汲み揚げポ
ンプを一旦停止する方法を説明したが、この汲み揚げポ
ンプの運転及び循環ポンプの運転を継続し順次処理液を
浄化処理槽に戻す場合もあり、何れの方法をも採用し得
る。
On the other hand, different fermentation bacteria are usually supplied to the respective fermentation bacteria storage tanks through a supply port on the outer wall surface of the casing or by opening the door of the second chamber. next,
When the purified fermentation bacteria are used, the corresponding bacteria supply device of the fermentation bacteria storage tank is operated to supply the purified fermentation bacteria to the culture tank. At the same time, the hollow rotary shaft is rotated by the motor and an air supply source is operated to supply air into the culture tank from the hollow rotary shaft and the air blowing pipe. If necessary, the culture nutrient is also supplied to the nutrient tank, and the nutrient supply device is also operated to supply the culture nutrient to the culture tank. At the same time, when using a deodorizing or deodorizing fermentation bacterium, a deodorizing or deodorizing fermentation bacterium is cultured in another fermentation bacteria storage tank in which the deodorizing or deodorizing fermentation bacterium is stored in the same manner as the septic tank fermentation bacterium. To supply. Generally, it is preferable to supply the deodorized or deodorized fermentation bacteria prior to the other bacteria. Further, as a measure for cleaning the purification facility and reducing the amount of dirt, so-called cleaning bacteria described in the section of the related art are put together and adhere to the inside of the culture tank, various pipes, hoses and various control valves. Prevents the formation of deposits. In the above-mentioned handling method, in the early stage of the operation, when the culture tank is once full, the method of temporarily stopping the pump is described.However, the operation of the pump and the operation of the circulation pump are continued to sequentially process the pump. The liquid may be returned to the purification tank, and any of these methods can be adopted.

【0010】培養槽の発酵が活発になったならば、増殖
した培養液を再び原液を採取した槽乃至処理槽に戻す。
このとき培養液を戻す量を概ね一定とし、培養槽内の液
面位が一定になるよう汲み揚げ量を調整することは当然
である。
When the fermentation in the culture tank becomes active, the grown culture solution is returned to the tank from which the stock solution was collected or the processing tank.
At this time, it is natural that the amount of the culture solution to be returned is substantially constant, and the pumping amount is adjusted so that the liquid level in the culture tank becomes constant.

【0011】前記培養槽においては、外周壁で加熱装置
により、加熱されるため、処理液中の成分の一部が内周
面に固着し、熱伝導を低下させる可能性があるが、前記
のこの発明の装置おいては、撹拌板が前記の構造である
から、培養槽の内壁面は常時撹拌板によって付着物は払
拭乃至掻きとられ、且つ撹拌されるから、加熱装置の熱
は有効に処理液に伝達し、熱伝導の低下は起らない。培
養槽にクリーニング菌を投入する場合には、これら培養
槽内周面に付着する固形物も分解してくれ、前記の攪拌
板と相俟って、これらを除去する作用を為す。
In the above-mentioned culture tank, since the outer peripheral wall is heated by a heating device, a part of the components in the processing solution may adhere to the inner peripheral surface and may reduce heat conduction. In the apparatus of the present invention, since the stirring plate has the above-described structure, the inner wall surface of the culture tank is constantly wiped or scraped off by the stirring plate, and the stirring is performed. The heat is transferred to the processing solution, and the heat conduction does not decrease. When a cleaning bacterium is introduced into the culture tank, the solid substances adhering to the inner peripheral surface of the culture tank are also decomposed, and work together with the above-mentioned stirring plate to remove them.

【0012】請求項2記載の発明に於いては、特定発明
の作用の他、ケ−シングが前述のように、第1室と第2
室にわかれ、発酵菌貯蔵槽と他の構成部分とは別の室に
分けてあり、第2室には空気調和装置が設けてあるか
ら、各種の発酵菌貯蔵槽が加熱装置で無闇に加熱される
おそれはないし、発酵菌貯蔵槽に発酵菌を補充すると
き、各発酵菌貯蔵槽の蓋、若しくは前記第2室の蓋を開
けたとしても、培養槽の臭気は第2室の扉や蓋の部分か
ら発散せず、作業環境が悪化しない。また寒冷地におい
ても、第2室は適温に保持されるから、凍結したり、冷
温下にならず、各種浄化処理発酵菌は繁殖機能の低下乃
至死滅することがない。
According to the second aspect of the present invention, in addition to the operation of the specific invention, the casing is formed in the first chamber and the second chamber as described above.
The fermentation bacteria storage tank and other components are divided into separate rooms, and the second room is equipped with an air conditioner. When replenishing the fermentation bacteria into the fermentation bacteria storage tank, even if the lid of each fermentation bacteria storage tank or the lid of the second chamber is opened, the odor of the culture tank does not affect the door of the second chamber or the like. Does not emanate from the lid and does not degrade the working environment. Also, even in cold regions, the second chamber is kept at an appropriate temperature, so that it does not freeze or cool, and the various fermentative bacteria for purification treatment do not decrease in the reproductive function or die.

【0013】請求項3記載の発明に於いては、請求項2
記載の発明の作用の他、加熱装置、空気供給装置など各
種運転機器は制御装置によって運転制御され、その操作
盤面がケ−シング外面に露出させてあるから、前述の各
種操作の条件設定及び操作などがケ−シング外面で行え
る。また前記制御装置は第2室内であるから、空気調和
装置により、第2室内は適度の温度と湿度である培養槽
から発生する湿気や腐食性ガスに曝されることなく、制
御機器、制御回路などが腐食しないし、貯蔵中の各種発
酵菌が増殖するおそれもない。請求項4記載の発明にお
いては、前記操作盤部分は独立した操作壁面用の扉内に
通常は納められているから、扉を閉じておけば、操作盤
面に外部の人が接触したりするおそれがなく、誤操作の
危険性が少ない。また操作室を管理外の人にいたずらさ
れるおそれもない。
According to the third aspect of the present invention, there is provided the second aspect.
In addition to the operation of the invention described above, the operation of various operating devices such as a heating device and an air supply device is controlled by a control device, and the operation panel surface is exposed to the outer surface of the casing. Can be performed on the outer surface of the casing. In addition, since the control device is in the second room, the air conditioner does not expose the second room to humidity or corrosive gas generated from the culture tank, which is at an appropriate temperature and humidity. Does not corrode, and there is no danger of various fermentation bacteria growing during storage. In the invention according to claim 4, since the operation panel portion is usually housed in the door for the independent operation wall, if the door is closed, there is a possibility that an outside person may contact the operation panel surface. No risk of erroneous operation. Further, there is no possibility that the operation room is tampered with by an unmanaged person.

【0014】請求項5記載の発明に於いては、他の請求
項記載の発明の作用の他、循環ポンプ及びそのパイプが
設けてあるから、前記の撹拌板の回転と相俟って、培養
槽内の発酵菌の繁殖が均一化する。また、循環ポンプの
二次側が切換弁によって、培養槽と、吐出パイプとに切
換られるから、循環ポンプを利用して、培養後の液を吐
出パイプを介して、処理槽に放出できる。
According to the fifth aspect of the present invention, in addition to the operation of the other aspects of the present invention, a circulating pump and its pipe are provided. Propagation of fermentation bacteria in the tank becomes uniform. Further, since the secondary side of the circulation pump is switched between the culture tank and the discharge pipe by the switching valve, the liquid after the culture can be discharged to the treatment tank through the discharge pipe using the circulation pump.

【0015】[0015]

【実施の形態】実施の形態 図1及び2に示すものであり、全ての請求項記載の発明
を含む実施の形態である。Aは本件の予備発酵装置であ
り、10はそのケ−シングであり、箱型形状であって、
例えば高さ約2m、幅80cm、奥行60cmとしてあ
る。これらの寸法に限定的な意味はない。ケ−シング1
0の中は第1室11と第2室12に区画パネル13で区
画され、更に全体として上中下の三段に支持枠14で区
切られている。前記第1室11と第2室12とは相互に
空気が流通しないように、前記区画パネル13で区画さ
れ、好ましくは区画パネル13は断熱材で形成すること
が好ましい。勿論第1室11又は第1室11及び第2室
12全部も断熱材で裏張する場合もある。前記第1室1
1はケ−シング10内の下段の一部と中段の大部分と上
段の全部によって形成してある。また第2室12は前記
下段の大部分と中段の一部によって形成してある。第1
室11の中段には培養槽20が設けられ、実施例におい
てこの容量は30リッターとした。これは縦型円筒形で
あり、その外周面21には加熱装置22が取り付けてあ
る。また培養槽20中心軸線位置には垂直な中空回転軸
23が設けてあり、前記培養槽20の上に設けたモ−タ
24と適当な減速装置(図示していない)を介して接続
してある。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment shown in FIGS. 1 and 2 is an embodiment including all the claimed inventions. A is the pre-fermentation apparatus of the present case, 10 is its casing, and is box-shaped,
For example, the height is about 2 m, the width is 80 cm, and the depth is 60 cm. These dimensions are not limiting. Case 1
The inside of 0 is partitioned by a partition panel 13 into a first chamber 11 and a second chamber 12, and further divided into a three-stage upper, middle, lower section as a whole by a support frame 14. The first chamber 11 and the second chamber 12 are partitioned by the partition panel 13 so that air does not flow between each other. Preferably, the partition panel 13 is formed of a heat insulating material. Of course, the first chamber 11 or all of the first chamber 11 and the second chamber 12 may be lined with a heat insulating material. The first room 1
1 is formed by a part of the lower stage, the majority of the middle stage, and the entire upper stage in the casing 10. The second chamber 12 is formed by a large part of the lower stage and a part of the middle stage. First
A culture tank 20 is provided in the middle stage of the chamber 11, and in this example, the capacity was 30 liters. This is a vertical cylindrical shape, and a heating device 22 is attached to an outer peripheral surface 21 thereof. A vertical hollow rotary shaft 23 is provided at the center axis position of the culture tank 20, and is connected to a motor 24 provided on the culture tank 20 via a suitable speed reducer (not shown). is there.

【0016】前記中空回転軸23の一部であり、前記培
養槽20内の位置には半径方向に延びる腕杆25が上下
2本を一組として、少なくとも2組設けてあり、上下の
一組の腕杆25には縦方向に長い撹拌板26がそれぞれ
固着してある。撹拌板26が剛性の高い材質よりなると
き、その外縁26aは培養槽20の円筒部の内周面に極
接近(5mm以下)して設けてあり、撹拌板26が若干
可撓性を有する材質の場合、その外縁26aは円筒部の
内周面に接触させてある。中空回転軸23の下端近くに
は空気吹き込みパイプ27が半径方向に吐出させてあ
り、この上面には多数の空気吹き出し孔28が穿設して
あり、この空気吹き込みパイプ27は前記中空回転軸2
3の中空孔23aに連通させてある。
At least two sets of upper and lower arm rods 25 are provided at a position in the culture tank 20 as a part of the hollow rotary shaft 23 and two sets of upper and lower arms are provided. Each of the arm rods 25 has a vertically long stirring plate 26 fixed thereto. When the stirring plate 26 is made of a material having high rigidity, its outer edge 26a is provided very close to (5 mm or less) the inner peripheral surface of the cylindrical portion of the culture tank 20, and the stirring plate 26 is made of a material having a slight flexibility. In this case, the outer edge 26a is in contact with the inner peripheral surface of the cylindrical portion. Near the lower end of the hollow rotary shaft 23, an air blowing pipe 27 is discharged in the radial direction, and a large number of air blowing holes 28 are formed on the upper surface thereof.
3 is communicated with the hollow hole 23a.

【0017】前記培養槽20に処理液を汲揚げる汲揚げ
ポンプ30は前記第1室11の下段に設けてあり、この
一次側の吸引パイプ31aの先端はケ−シング10の下
部に設けてあるホ−ス接続部32に連結してあり、二次
側の汲み揚げパイプ31bは培養槽20の蓋33に接続
してある。前記吸引パイプ31aと汲み揚げパイプ31
bによって処理液供給パイプ31を構成している。汲み
揚げポンプ30の最大汲み揚げ量は0.5リッター/分
のものを用いた。汲み揚げポンプ30はケーシング10
内に設けておくことが好ましいが、ケーシング10外に
設けてもよいし、従前の浄化処理槽に用いられているポ
ンプを切換えて接続しても、請求項1記載の発明の実施
の形態に含まれる。ケーシング10の下部には、更に2
つのホース接続部32b、32cが設けてあり、その一
つはケーシング10内において、ドレーン本管35に、
他の一つは処理液放水パイプ36が接続してある。
A pump 30 for pumping the processing solution into the culture tank 20 is provided at the lower stage of the first chamber 11, and the tip of the suction pipe 31a on the primary side is provided below the casing 10. The secondary side pumping pipe 31 b is connected to the hose connection part 32, and is connected to the lid 33 of the culture tank 20. The suction pipe 31a and the pumping pipe 31
b constitutes a processing liquid supply pipe 31. The maximum pumping amount of the pump 30 was 0.5 liter / min. The pump 30 is a casing 10
It is preferable that the pump is provided inside the casing 10, but it may be provided outside the casing 10, or the pump used in the conventional purification treatment tank may be switched and connected to the embodiment of the invention according to claim 1. included. In the lower part of the casing 10, two more
One hose connection part 32b, 32c is provided, one of which is connected to the drain main pipe 35 in the casing 10.
The other one is connected to a processing liquid discharge pipe 36.

【0018】前記培養槽20には、処理液循環ポンプ3
7及びこの一次側には、培養槽20の底部に連なる一次
側循環用パイプ38がまた二次側には、二次側循環用パ
イプ39が接続してあり、切換弁40を介して、培養槽
20の前記蓋33に接続してある。この処理液循環ポン
プ37の出力は、2リットル/分乃至2.5リットル/
分あれば充分である。切換弁40の他方は前記処理液放
出パイプ36を介して、ホース接続部の一つの32Bに
接続してある。従って前記切換弁40は液面制御の機能
も有する。
The culture tank 20 has a treatment liquid circulation pump 3
7 and the primary side thereof, a primary-side circulation pipe 38 connected to the bottom of the culture tank 20 is connected to the secondary side, and a secondary-side circulation pipe 39 is connected to the secondary side. It is connected to the lid 33 of the tank 20. The output of the processing liquid circulation pump 37 is 2 liters / minute to 2.5 liters / minute.
All you need is enough. The other end of the switching valve 40 is connected to one of the hose connection portions 32B via the processing liquid discharge pipe 36. Therefore, the switching valve 40 also has a function of controlling the liquid level.

【0019】前記培養タンク20には更にオーバーフロ
ーパイプ41、ドレーンパイプ42が接続してあり、こ
れらは、前記ドレーン本管35に接続してある。ハウジ
ング10内の第1室11の上段位置において、つまり蓋
33の上方には空気ポンプ44が設けてあり、この空気
ポンプ44の二次側は前記中空回転軸23に適宜のジョ
イントを介して接続してある。その他、図示していない
が、液面計を設け、液面位が許容範囲以下になれば、前
記切換弁40を培養槽30側にして、培養液がより多く
循環するようにし、許容範囲となれば、元の状態に戻
す。これらの操作も制御装置をCによって行う。更に前
記第1室11の上段位置には栄養剤貯蔵槽45が設けて
ある。通常栄養剤としては、グルタミン酸ソーダ、ソル
ビトールなどの顆粒物を用いる。栄養剤供給装置46と
しては図示の態様においては、スクリューフィーダを用
いた。この供給能力は0.2グラム乃至2グラム/分の
供給能力のあるものを用いた。
The culture tank 20 is further connected with an overflow pipe 41 and a drain pipe 42, which are connected to the drain main pipe 35. An air pump 44 is provided at an upper position of the first chamber 11 in the housing 10, that is, above the lid 33, and a secondary side of the air pump 44 is connected to the hollow rotary shaft 23 via an appropriate joint. I have. In addition, although not shown, a liquid level gauge is provided, and when the liquid level falls below the allowable range, the switching valve 40 is set to the culture tank 30 side so that the culture liquid circulates more, and the allowable range is set. If it does, return it to its original state. These operations are also performed by the control device C. Further, a nutrient storage tank 45 is provided at an upper position of the first chamber 11. Usually, granules such as sodium glutamate and sorbitol are used as nutritional supplements. In the illustrated embodiment, a screw feeder is used as the nutrient supply device 46. The supply capacity was 0.2 g to 2 g / min.

【0020】前記第2室12の下段には、発酵菌貯蔵槽
50a、50b、50cが複数槽設けてあり、第2室1
2の扉51を開け、それぞれの発酵菌貯蔵槽に発酵菌液
がそれぞれ供給できるようにしてある。各発酵菌貯蔵槽
50a、50b、50cの蓋を第2室12のハウジング
10の外壁面にそれぞれ独立に設け、ケーシング10外
より発酵菌が直接目的の発酵菌貯蔵槽50a、50b、
50cに投入できるようにする場合もある。
In the lower part of the second chamber 12, a plurality of fermentation bacteria storage tanks 50a, 50b and 50c are provided.
The second door 51 is opened so that the fermentation bacteria solution can be supplied to each fermentation bacteria storage tank. The lids of the fermentation bacteria storage tanks 50a, 50b, and 50c are provided independently on the outer wall surface of the housing 10 of the second chamber 12, and the fermentation bacteria storage tanks 50a, 50b,
In some cases, it may be possible to put it into 50c.

【0021】前記発酵菌貯蔵槽50a、50b、50c
に菌供給パイプ51a、51b、51cが接続してあ
り、中間に菌供給ポンプ52a、52b、52cを介し
て、前記培養槽の蓋33に接続し、菌供給ポンプ52
a、52b、52cで供給した菌が、培養槽20に投入
できるものであり、菌供給ポンプ52a、52b、52
cの出力に応じた菌が連続乃至間欠的に供給できるもの
である。これら菌供給ポンプ52a、52b及び52c
の吐出量の改定及び運転制御は、制御装置Cによって行
う。これら菌供給ポンプ52a、52b、52cは、前
記第1室11中に設けてある。これら菌供給ポンプ52
a、52b、52cの最大吐出量は30cc/分までの
範囲で適宜変更できるものである。
The fermentation bacteria storage tanks 50a, 50b, 50c
Are connected to the lid 33 of the culture tank via the bacterial supply pumps 52a, 52b, 52c, and the bacterial supply pumps 52a, 52b, 52c.
The bacteria supplied by a, 52b, 52c can be put into the culture tank 20, and the bacteria supply pumps 52a, 52b, 52c
Bacteria corresponding to the output of c can be supplied continuously or intermittently. These bacteria supply pumps 52a, 52b and 52c
The revision of the discharge amount and the operation control are performed by the control device C. These bacteria supply pumps 52a, 52b, 52c are provided in the first chamber 11. These bacteria supply pumps 52
The maximum discharge rates of a, 52b, and 52c can be appropriately changed within a range of up to 30 cc / min.

【0022】前記制御装置Cは、ケーシング10の中段
第2室12中に設けてある。通常ケーシング10の外側
から填め込まれており、第1室11中の腐蝕性の有害な
ガスに曝されないようにしてある。制御装置Cの操作盤
55はケーシング10の外壁面に露出しており、各種モ
ータの発停、各種ポンプの吐出量の設定、加熱装置22
の温度設定、液面水位制御、各種切換弁の切換などを行
うノブ若しくはスイッチその他テンキーなどの入力部が
設けてある。図に示す実施の形態においては、前記操作
盤55に相当する部分のみに別個の独立した操作盤面用
開閉扉56をハウジング10に設け、操作するときにの
みこれを開け、この装置の継続的運転時及び不使用時に
は、この扉56を閉じておけば、作業者の無意識な接触
や、いたずらで誤作動を起こすことがない。
The control device C is provided in the middle second chamber 12 of the casing 10. Usually, it is inserted from the outside of the casing 10 so as not to be exposed to corrosive and harmful gas in the first chamber 11. The operation panel 55 of the control device C is exposed on the outer wall surface of the casing 10, and starts and stops various motors, sets the discharge amounts of various pumps, and controls the heating device 22.
An input unit such as a knob or switch or a numeric keypad for setting the temperature of the liquid, controlling the liquid level, and switching various switching valves is provided. In the embodiment shown in the drawings, a separate and independent operation panel surface opening / closing door 56 is provided in the housing 10 only at a portion corresponding to the operation panel 55, and is opened only when the operation is performed. When the door 56 is closed at the time of use and at the time of non-use, there is no unintentional contact of the operator and no malfunction due to mischief.

【0023】その他、第1室11の上部には換気扇60
が設けてあり、脱臭、消臭発酵菌を使用しない場合、こ
の一次又は二次側に、活性炭などの脱臭剤を充填した脱
臭器乃至脱臭装置(図示していない)を付加しておく場
合もある。また、第2室例えば第1室11と第2室12
の区画パネルに、空気調和装置58が設けてあり、第2
室の室温が上昇し過ぎないようにしてある。例えば、ペ
ルティエ効果(Peltier effect)を利用した電子空気
調和装置58とする。ケーシング10の一部と前記培養
槽20の外周壁の一部相対する部分には透明ガラスより
なる第1、第2の観察窓15及び29が設けてあり、ケ
ーシング10の外側から培養槽20の中の状態が観察で
きるようにしてある。
In addition, a ventilation fan 60 is provided above the first chamber 11.
When deodorizing and deodorizing fermentation bacteria are not used, a deodorizer or a deodorizing device (not shown) filled with a deodorant such as activated carbon may be added to the primary or secondary side. is there. A second chamber, for example, a first chamber 11 and a second chamber 12
An air conditioner 58 is provided on the partition panel of
The room temperature is kept from rising too high. For example, the electronic air conditioner 58 uses the Peltier effect. First and second observation windows 15 and 29 made of transparent glass are provided in a part of the casing 10 and a part of the outer peripheral wall of the culture tank 20 opposed to each other. The inside state can be observed.

【0024】実施の形態の作用及び効果 浄化処理発酵菌を培養する場合を説明する。操作盤55
を操作して、例えば原液受け槽61などから原液を汲み
揚げポンプ30を作動させ培養槽20に源液を汲み揚げ
る。処理すべき汚水(原液)は通常相当の臭気を伴うた
め、前記原液の汲み揚げ前若しくはその途中より、前記
三つの発酵菌貯蔵槽50cに臭気発生防止菌を供給し、
これに対応した菌供給ポンプ51cを作動させ、改めて
定められた臭気発生防止菌を培養槽20に投入する。
Operation and effect of the embodiment A case where a purified fermentative bacterium is cultured will be described. Operation panel 55
Is operated to pump the undiluted solution from, for example, the undiluted solution receiving tank 61 and operate the pump 30 to pump the undiluted solution into the culture tank 20. The sewage (stock solution) to be treated usually has a considerable odor, so the odor generation preventing bacteria are supplied to the three fermentation bacteria storage tanks 50c before or during the pumping of the stock solution,
The germ supply pump 51c corresponding to this is operated, and the odor generation preventing bacterium newly determined is thrown into the culture tank 20.

【0025】前記培養槽20に原液が満杯になれば、ま
ず汲み揚げポンプ30を停止し、臭気発生防止菌の培養
に最適な温度、通常は培養槽20内の温度が25℃〜3
0℃になるように加熱装置22により過熱すると共に、
中空回転軸23をモータ24によって回転させ、空気ポ
ンプ43により、曝気攪拌培養槽20内の原液と臭気発
生防止菌とが充分に混合されるよう、攪拌板26によっ
て攪拌する。これらの操作も操作盤55よりの操作で行
う。
When the undiluted solution is filled in the culture tank 20, the pump 30 is first stopped, and the temperature optimal for cultivation of the odor preventing bacteria, usually the temperature in the culture tank 20 is 25 ° C to 3 ° C.
While being heated by the heating device 22 so as to be 0 ° C.,
The hollow rotary shaft 23 is rotated by the motor 24, and is stirred by the stirring plate 26 by the air pump 43 so that the undiluted solution in the aeration and stirring culture tank 20 and the odor generation preventing bacteria are sufficiently mixed. These operations are also performed by operating the operation panel 55.

【0026】臭気発生防止菌の初期培養において、栄養
剤を必要とするときは、栄養剤供給装置46を作動させ
て栄養剤貯蔵槽45に予め貯蔵してあるグルタミン酸ソ
ーダ、ソルビトールなどを定められた量投入する。これ
ら栄養剤は一般に凍結乾燥されており、吸湿性があるか
ら一回に投入する量、その都度栄養剤貯蔵槽45に供給
するようにする。
When nutrients are required in the initial cultivation of the odor-preventing bacteria, the nutrient supply device 46 is operated to determine sodium glutamate, sorbitol, etc., which are stored in the nutrient storage tank 45 in advance. Inject quantity. These nutrients are generally freeze-dried and have a hygroscopic property, so that they are supplied to the nutrient storage tank 45 each time they are injected.

【0027】培養槽20内がより均一に発酵菌が繁殖す
るように処理循環ポンプ37を運転し、培養槽20の一
部の処理水をその底部近傍より抜き取り、循環ポンプ3
7切換弁40を通り、培養槽20上部より再度培養槽2
0中に注入し、培養処理液を循環させる。培養液を浄化
処理槽に戻す流量を予め定め、この量汲み揚げポンプ3
0で汲み揚げるようにする。培養槽20内の液位は図示
してない液面計で検出し、この出力信号により、切換弁
40を循環と排出の何れかに選択し許容範囲に培養槽2
0内の液面が保たれるようにする。この場合は汲み揚げ
ポンプ30は連続運転となる。次に三つの発酵菌貯蔵槽
の内、例えば一つの発酵菌貯蔵槽50aに浄化処理槽発
酵菌液を供給する。前記発酵菌貯蔵槽50aに対応する
菌供給ポンプ51aを操作盤55よりの指令により作動
させて、前述の浄化処理液発酵菌を培養槽20に供給す
る。前述の浄化処理発酵菌供給量及びその流量などは制
御装置Cの入力部より予め設定しておく。更に栄養剤を
補充する必要があるときは、これを補充する。循環ポン
プ37運転、空気ポンプ43、攪拌板26の運転中に浄
化処理発酵菌を投入後、約1時間汲み揚げポンプ30の
運転を再開すると共に、培養槽20から処理液の一部を
循環ポンプ37及び切換弁40を通り及び処理液放出パ
イプ36若しくはオーバーフロー41を処理槽若しくは
これよりも上流側の適宜の槽に培養液を順次戻す。
The processing circulation pump 37 is operated so that fermentation bacteria can be propagated more evenly in the culture tank 20, and a part of the treated water in the culture tank 20 is drawn out from near the bottom thereof.
7 through the switching valve 40 and from the upper part of the culture tank 20 to the culture tank 2 again.
0, and the culture solution is circulated. The flow rate at which the culture solution is returned to the purification tank is determined in advance, and the pump 3
Try to pump at 0. The liquid level in the culture tank 20 is detected by a liquid level meter (not shown), and the output valve selects the switching valve 40 to either circulation or discharge and sets the culture tank 2 within an allowable range.
The liquid level in 0 is maintained. In this case, the pump 30 operates continuously. Next, the fermentation bacterium liquid in the purification treatment tank is supplied to, for example, one fermentation germ storage tank 50a among the three fermentation germ storage tanks. The bacteria supply pump 51a corresponding to the fermentation bacteria storage tank 50a is operated according to a command from the operation panel 55 to supply the above-mentioned purified liquid fermentation bacteria to the culture tank 20. The supply amount and the flow rate of the above-mentioned purification fermentation bacteria are set in advance from the input unit of the control device C. If it is necessary to replenish nutrients, they are replenished. After introducing the purified fermentation bacteria during the operation of the circulation pump 37, the air pump 43, and the stirring plate 26, the pumping pump 30 is restarted for about 1 hour, and a part of the processing solution is circulated from the culture tank 20 by the circulation pump. The culture solution is sequentially returned to the treatment tank or an appropriate tank upstream from the treatment liquid discharge pipe 36 or the overflow 41 through the 37 and the switching valve 40.

【0028】或いは処理液循環ポンプ37の二次側循環
パイプに設けた切換弁40を吐出側に切換え、処理液を
順次ドレーン本管35又は別個の処理液放出パイプ36
を利用して、処理槽若しくはこれよりも上流側の適宜の
槽に培養液を順次戻す。
Alternatively, the switching valve 40 provided on the secondary side circulation pipe of the processing liquid circulation pump 37 is switched to the discharge side, and the processing liquid is sequentially drained to the drain main pipe 35 or a separate processing liquid discharge pipe 36.
, The culture solution is sequentially returned to the treatment tank or an appropriate tank upstream of the treatment tank.

【0029】第1室11は概ね密閉型とする場合もある
が、温緩地においては、底面パネルと頂面パネルは、防
虫網パネルとし、第1室11の室内温度が上昇すぎない
ようにする場合もある。培養槽30から排出する湿気は
換気扇57により外部に放出する。前述の通り、底面パ
ネル、頂面パネルが防虫網パネルの場合は必ずしも換気
扇57は必要ではない。
Although the first chamber 11 may be of a closed type in general, in a temperate area, the bottom panel and the top panel are made of insect screen panels so that the room temperature of the first chamber 11 does not rise excessively. In some cases. Moisture discharged from the culture tank 30 is released to the outside by a ventilation fan 57. As described above, when the bottom panel and the top panel are insect screen panels, the ventilation fan 57 is not necessarily required.

【0030】第2室12の室温は各種の浄化処理発酵菌
が活動を開始したり、凍結したりして、その繁殖能が劣
化乃至死滅しない温度範囲に保つよう、前記空気調和装
置58及び制御装置Cによって制御する室温は5℃乃至
20℃が好ましい。寒冷地や、冬期など、外気が低温す
ぎるときは、第2室を暖める熱源は、第1室11より、
熱だけを受け、通気はしないよう、前記空気調和装置5
8は前述の通り、ペルティエ効果利用の電子式空気調和
装置としてある。この発明の装置においては、予備培養
を行うので、各種発酵菌は、培養槽20中において、凡
そ100倍乃至1000倍に増殖する。
The air conditioner 58 and the controller are controlled so that the room temperature of the second chamber 12 is maintained within a temperature range in which the fermentative bacteria of various purification treatments start or freeze and their reproductive ability does not deteriorate or die. The room temperature controlled by the device C is preferably 5 ° C to 20 ° C. When the outside air is too low, such as in a cold region or in winter, the heat source for warming the second room is from the first room 11,
The air conditioner 5 receives only heat and does not ventilate.
As described above, reference numeral 8 denotes an electronic air conditioner utilizing the Peltier effect. In the apparatus of the present invention, since the preliminary culture is performed, the various fermentation bacteria multiply in the culture tank 20 approximately 100 to 1000 times.

【0031】汚水処理施設における嫌気性濾床槽及び接
触曝気槽内での浄化処理発酵菌の発酵が通常の発酵状態
に達したならば、この発明の装置を一時停止してもよ
く、冬季や寒冷地においてはこれら嫌気性濾床槽及び接
触曝気槽内の液を発酵に最適温度まで上昇せず、発酵が
不充分な場合には本件装置を連続運転し、これらは予備
発酵を継続して順次培養後の液をの供給を継続する。嫌
気性濾床槽及び接触瀑気槽内の液を発酵に最適温度まで
加熱する熱源としては廃棄物焼却炉の廃熱などを利用す
る事が好ましい。この発明の装置を長時間停止する場合
は制御装置その他電気系機器以外の機器は水洗し、洗滌
後の水はドレーン本管35に集められケーシング10外
に放出する。
When the fermentation of the purified fermentative bacteria in the anaerobic filter bed tank and the contact aeration tank in the sewage treatment plant reaches a normal fermentation state, the apparatus of the present invention may be temporarily stopped, and the apparatus may be used in winter or in winter. In cold regions, the liquid in these anaerobic filter bed tanks and contact aeration tanks does not rise to the optimum temperature for fermentation.If fermentation is not sufficient, the device is continuously operated, and these The supply of the liquid after the culture is continued. As a heat source for heating the liquid in the anaerobic filter bed tank and the contact water tank to an optimum temperature for fermentation, it is preferable to use waste heat of a waste incinerator or the like. When the device of the present invention is stopped for a long time, the control device and other devices other than the electrical devices are washed with water, and the washed water is collected in the drain main pipe 35 and discharged out of the casing 10.

【0032】この装置を利用する汚水浄化施設の一例を
図7に示す。この装置は農業集落廃水処理施設として通
常用いられているものの一種で汚水の流れを示すフロー
チャートである。上流側より受液槽乃至曝気沈砂槽6
0、流量調整槽61が設けてある。この流量調整槽61
より本件発明の予備培養装置に原液を汲み揚げ、嫌気性
濾床槽62の最上流槽に培養後の液を戻すようにし、嫌
気性濾床槽62を通過した液を曝気槽63に流入させ
る。更に沈殿槽64で固形物を沈殿させ上澄み液を消毒
して放流する。前記嫌気性濾床槽62、嫌気性濾床槽6
2及び沈殿槽64で発生した沈殿物は汚水と分離し、沈
殿物は肥料に,汚水は沈殿槽64に戻す。
FIG. 7 shows an example of a sewage purification facility using this apparatus. This apparatus is a flow chart showing the flow of sewage, which is a kind of one usually used as an agricultural settlement wastewater treatment facility. From the upstream side, receiving tank or aeration sand settling tank 6
0, a flow regulating tank 61 is provided. This flow control tank 61
The undiluted solution is further pumped up to the pre-culture device of the present invention, and the liquid after the culture is returned to the uppermost stream tank of the anaerobic filter bed tank 62, and the liquid passed through the anaerobic filter bed tank 62 flows into the aeration tank 63. . Further, solids are settled in the settling tank 64, and the supernatant is disinfected and discharged. The anaerobic filter bed tank 62 and the anaerobic filter bed tank 6
2 and the sediment generated in the sedimentation tank 64 are separated from the wastewater, the sediment is returned to the fertilizer, and the wastewater is returned to the sedimentation tank 64.

【0033】[0033]

【発明の効果】請求項1及び6記載の特定発明において
は、装置全体がキャスター及び移動固定自在であるか
ら、この装置自体を汚泥汚物処理装置の尤も必要な場所
に移動し、汲み揚げるべき液槽にホースで接続し、この
装置内の汲み揚げポンプによって、培養槽に処理液を汲
み揚げることができる。殊に比較的小容量(通常の処理
槽に対して)の培養槽において、最適条件で各種発酵菌
を予備培養するため、この中で前記各種発酵菌は仮死状
態乃至増殖停止状態から活発な増殖状態となり、短時間
(1時間乃至2時間)のうちに100倍乃至1000倍
程度にまで増殖する。
According to the first and sixth aspects of the present invention, since the entire apparatus is caster and movable and can be fixed freely, the apparatus itself is moved to a place where the sludge waste treatment apparatus is required, and the liquid to be pumped is lifted. It is connected to a tank by a hose, and the processing liquid can be pumped into the culture tank by the pump in this apparatus. In particular, since various fermentation bacteria are precultured under optimum conditions in a culture tank having a relatively small capacity (relative to a normal treatment tank), the various fermentation bacteria actively grow from a suspended state or a growth stopped state. It grows to about 100 to 1000 times in a short time (1 to 2 hours).

【0034】而して、これを処理槽に戻すから、実質的
に各種発酵菌を直接処理槽に投入する量方法に比較し、
各種発酵菌の量を従来の量の1/100乃至1/100
0の量で従来の量と同等の効果が得られる。また同一の
装置を利用し、嫌気性発酵菌と好気性発酵菌の培養も、
単に培養槽の中空回転軸及び空気吹き込みパイプに空気
ポンプより空気を供給するか供給しないかの選択によっ
て行える。
Since this is returned to the treatment tank, it is practically compared with a method in which various fermentation bacteria are directly introduced into the treatment tank.
Reduce the amount of various fermentation bacteria to 1/100 to 1/100 of the conventional amount
An amount equal to 0 has the same effect as the conventional amount. In addition, using the same equipment, cultivation of anaerobic fermentation bacteria and aerobic fermentation bacteria,
It can be performed simply by selecting whether or not to supply air from the air pump to the hollow rotary shaft of the culture tank and the air blowing pipe.

【0035】また前述の培養槽には加熱装置を備えてお
り、前述の攪拌板の回転と相俟って、培養槽中の液は培
養に最適な温度にすることができるし、処理液中の挟雑
物が培養槽外周壁内面に固着するおそれもない。
Further, the above-mentioned culture tank is provided with a heating device, and the liquid in the culture tank can be adjusted to an optimum temperature for the culture, in combination with the rotation of the above-mentioned stirring plate. There is no possibility that the contaminants of the above will adhere to the inner surface of the outer peripheral wall of the culture tank.

【0036】請求項2記載の発明においては、前述の効
果に加え前述のようにケーシングが第1室と第2室に区
画され、各構成する装置を前述のように配設したから、
第2室中の各種発酵菌貯蔵槽は第1室の培養槽の加熱に
係らず、これら菌が発酵する程には加熱されず、菌の過
加熱は起こらない。またケーシングの外面には原液供給
ホースなど各種ホースが接続口に接続離反可能に設けて
あるから、これら各種ホースの着脱も容易である。
According to the second aspect of the present invention, in addition to the above-described effects, the casing is divided into the first chamber and the second chamber as described above, and the constituent devices are disposed as described above.
Regardless of the heating of the culture tank in the first chamber, the various fermentation bacteria storage tanks in the second chamber are not heated to such an extent that these bacteria ferment, and the bacteria do not overheat. In addition, since various hoses such as a stock solution supply hose are provided on the outer surface of the casing so as to be connected to and disconnected from the connection port, it is easy to attach and detach these various hoses.

【0037】請求項3記載の発明においては、第2室に
制御装置及び空気調和装置が設けてあるから、制御装置
が培養槽より発生する高湿気や、腐蝕性ガスに曝される
ことがない、勿論前述の各種貯蔵槽も最適条件に保たれ
る。また制御装置の操作盤はケーシング外壁面と露出さ
せてあるから、ケーシングの外壁面において、各種の操
作、指令、設定などが行える。
According to the third aspect of the present invention, since the control device and the air conditioner are provided in the second chamber, the control device is not exposed to high humidity or corrosive gas generated from the culture tank. Of course, the above-mentioned various storage tanks are also kept under optimal conditions. Further, since the operation panel of the control device is exposed to the outer wall surface of the casing, various operations, commands, settings, and the like can be performed on the outer wall surface of the casing.

【0038】請求項4記載の発明においては操作盤部分
は専用の開閉扉が設けられているから、閉じておけば、
操作盤面が外部に露出せず、各操作部が作業者の無意識
の接触や、部外者によるいたずらによって誤作動を起こ
すおそれがない。
According to the fourth aspect of the present invention, the operation panel is provided with a dedicated opening / closing door.
The operation panel surface is not exposed to the outside, and there is no possibility that each operation unit may malfunction due to unconscious contact of an operator or tampering by an outsider.

【0039】請求項5記載の発明においては、更に前記
培養槽には汲み揚げポンプとは別個の循環ポンプ及びこ
れらのパイプラインを設けたから、培養槽中の液は更に
攪拌されるし、切換弁の操作により、汲み揚げポンプを
運転しながら、これと独立して、目的に応じた吐出量
で、予備で培養した液を処理槽に吐出することができ
る。請求項6記載の発明においては汲み揚げポンプ30
はケーシング10の中に設けあるから、外部のポンプを
利用する必要はなく段取りが容易である。
According to the fifth aspect of the present invention, the culturing tank is further provided with a circulating pump separate from the pumping pump and these pipelines, so that the liquid in the culturing tank is further stirred and the switching valve is provided. By operating the pump, the pre-cultured liquid can be discharged into the treatment tank independently of the pump while operating the pump. In the invention according to claim 6, the pump 30
Is provided in the casing 10, so that it is not necessary to use an external pump and the setup is easy.

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

【図1】全体の外観正面図である。FIG. 1 is a front view of the entire appearance.

【図2】全体の外観側面図である。FIG. 2 is a side view of the entire appearance.

【図3】ケーシング縦断正面概略図である。FIG. 3 is a schematic vertical front view of a casing.

【図4】ケーシング縦断側面概略図である。FIG. 4 is a schematic vertical sectional side view of a casing.

【図5】全体の配管系統図である。FIG. 5 is an overall piping system diagram.

【図6】培養槽部の断面図である。FIG. 6 is a sectional view of a culture tank.

【図7】この発明の装置を利用した汚水処理施設の一例
のフローチャートである。
FIG. 7 is a flowchart of an example of a sewage treatment facility using the apparatus of the present invention.

【符号の説明】[Explanation of symbols]

10 ケーシング 11 第1室 12 第2室 13 区画パネル 14 支持枠 15 第1観察窓 20 培養槽 21 外周面 22 加熱装置 23 中空回転軸 23a 中空孔 24 モータ 25 腕杆 26 攪拌板 26a 外縁 27 空気吹き込みパイプ 28 空気吹き出し孔 29 第2観察窓 30 汲み揚げポンプ 31 処理液供給パイプ 31a 吸い揚げパイプ 31b 汲み揚げパイプ 32a ホース接続部 32b ホース接続部 32c ホース接続部 33 蓋 35 ドレーン本管 36 処理液放出パイプ 37 処理液循環ポンプ 38 一次側循環用パイプ 39 二次側循環用パイプ 40 自動液面コントロール弁 41 オーバーフローパイプ 42 ドレーンパイプ 43 空気ポンプ 45 栄養剤貯蔵槽 46 栄養剤供給装置 50a、50b、50c 発酵菌貯蔵槽 51a、51b、51c 菌供給パイプ 52a、52b、52c 菌供給ポンプ 55 操作盤 56 開閉扉 57 換気扇 58 空気調和装置 DESCRIPTION OF SYMBOLS 10 Casing 11 1st chamber 12 2nd chamber 13 Division panel 14 Support frame 15 1st observation window 20 Culture tank 21 Outer peripheral surface 22 Heating device 23 Hollow rotating shaft 23a Hollow hole 24 Motor 25 Arm rod 26 Stirring plate 26a Outer edge 27 Air blowing Pipe 28 Air outlet hole 29 Second observation window 30 Pumping pump 31 Treatment liquid supply pipe 31a Suction pipe 31b Pumping pipe 32a Hose connection part 32b Hose connection part 32c Hose connection part 33 Cover 35 Drain main pipe 36 Treatment liquid discharge pipe 37 Treatment liquid circulation pump 38 Primary side circulation pipe 39 Secondary side circulation pipe 40 Automatic liquid level control valve 41 Overflow pipe 42 Drain pipe 43 Air pump 45 Nutrient storage tank 46 Nutrient supply device 50a, 50b, 50c Fermenting bacteria Storage tank 51a 51b, 51c bacteria feed pipe 52a, 52b, 52c bacteria feed pump 55 operation panel 56 door 57 Ventilator 58 air conditioner

───────────────────────────────────────────────────── フロントページの続き (72)発明者 伊藤 勇 福島県いわき市東田町塩田2−3 (72)発明者 平山 透 福島県いわき市好間町下好間叶田15 Fターム(参考) 4B029 AA02 BB02 BB06 CC01 DB01 DB11 DB19 DD06  ────────────────────────────────────────────────── ─── Continued on the front page (72) Inventor Isamu Isoh 2-3, Shioda, Higashida-cho, Iwaki-shi, Fukushima (72) Inventor Toru Hirayama 15 Kanoda, Shimo-yoshima, Iwaki-shi, Fukushima F-term (reference) 4B029 AA02 BB02 BB06 CC01 DB01 DB11 DB19 DD06

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】キャスタ−付きのケ−シング内には培養槽
処理液供給及び吐出パイプ、数個の発酵菌貯蔵槽及びこ
れより発酵菌液を前記培養槽にそれぞれ供給する数個の
菌供給ポンプ及び菌供給パイプ、培養槽に栄養剤を供給
する栄養剤貯蔵槽及び供給装置を備え、前記培養槽に処
理液を汲み揚げるポンプは前記ケーシング内乃至この近
傍に備えてあり、 前記培養槽は円筒形であって、その中心に垂直な中空回
転軸を備え、この中空回転軸には半径方向に突出した腕
棒の先端には前記培養槽の軸方向に長い撹拌板が固着し
てあり、この撹拌板の外縁は前記培養槽内周面の略全高
長おいて極接近乃至軽く接触させてあり、 前記中空回転軸の外端は前記ケ−シング内に装備してあ
る空気供給源に接続してあり、また前記中空回転軸の一
部培養槽内の底近くには空気吹き込みパイプが半径方向
に突出して設けてあり、この空気吹き込みパイプは前記
中空回転軸の中空孔に連通させてあり、 前記培養槽の外周面には加熱装置が装備してあることを
特徴とする汚水処理発酵菌の予備発酵装置。
1. A feeder and a discharge pipe for treating liquid in a culture tank, a storage tank for several fermentation bacteria, and a supply of several bacteria for supplying a fermentation bacteria solution to the culture tank in a casing with casters. A pump and a bacterium supply pipe, a nutrient storage tank and a supply device for supplying nutrients to the culture tank, and a pump for pumping the treatment liquid into the culture tank is provided in or near the casing; It is cylindrical and has a hollow rotary shaft perpendicular to the center thereof, and a stir plate long in the axial direction of the culture tank is fixed to the tip of an arm rod protruding in the radial direction on the hollow rotary shaft, The outer edge of the agitating plate is extremely close to or lightly in contact with the inner peripheral surface of the culture tank at substantially the entire height, and the outer end of the hollow rotary shaft is connected to an air supply source provided in the casing. And a part of the hollow rotary shaft in the culture tank. An air blowing pipe is provided near the bottom so as to protrude in the radial direction. The air blowing pipe communicates with a hollow hole of the hollow rotary shaft, and a heating device is provided on an outer peripheral surface of the culture tank. Preliminary fermentation apparatus for sewage treatment fermentation bacteria.
【請求項2】前記ケ−シングはほゞ密閉型であり、内部
で第1室と第2室に分かれて区画してあり、第1室には
前記培養槽及び加熱装置を備え、第2室には数個の発酵
菌貯蔵槽と空気調和装置を備え、第1室と第2室は空気
流が遮断してあり、前記第2室の外壁面には発酵菌貯蔵
槽に通じる発酵菌供給口乃至発酵菌供給時に開閉可能な
扉が設けてあり、前記第1室の外壁の一部には原液供給
ホ−ス、処理水放出ホ−ス、ドレン放出ホ−スのそれぞ
れの接続口が設けてあることを特徴とする請求項1記載
の汚水処理発酵菌の予備発酵装置。
2. The casing is of a substantially hermetic type, and is internally divided into a first chamber and a second chamber. The first chamber is provided with the culture tank and a heating device. The room is provided with several fermentation bacteria storage tanks and an air conditioner, the first and second chambers are shut off from the air flow, and the outer wall of the second chamber has fermentation bacteria communicating with the fermentation bacteria storage tank. A supply port or a door that can be opened and closed when the fermentation bacteria are supplied is provided, and a connection port for a stock solution supply hose, a treated water discharge hose, and a drain discharge hose is provided on a part of the outer wall of the first chamber. The preliminary fermentation apparatus for sewage treatment fermentation bacteria according to claim 1, wherein:
【請求項3】前記第2室の一部には、制御装置及び空気
調和装置が設けてあり、その操作盤面はケ−シング外面
に露出させてあり、制御装置には処理液ポンプ及び循環
ポンプの発停止、加熱装置による培養槽の温度制御装
置、数個の菌供給ポンプの発停、空気供給源の発停止、
その他換気装置の発停、の入力部が装備してあることを
特徴とする請求項2記載の汚水処理発酵菌の予備発酵装
置。
3. A control device and an air conditioner are provided in a part of the second chamber, and an operation panel surface of the control device is exposed to an outer surface of the casing, and a processing liquid pump and a circulation pump are provided in the control device. Start and stop, temperature control device of culture tank by heating device, start and stop of several bacteria supply pump, start and stop of air supply source,
3. The preliminary fermentation apparatus for sewage treatment fermenters according to claim 2, further comprising an input section for starting and stopping the ventilation device.
【請求項4】前記制御装置の操作盤面は、ケーシング外
面に露出させる代わりに、ケーシング内に納めてあり、
操作壁面に対応した部分のみに、独立した操作壁面用開
閉扉が設けてあることを特徴とする請求項3記載の汚水
処理発酵菌の予備発酵装置。
4. An operation panel surface of the control device is housed in a casing instead of being exposed on an outer surface of the casing.
The preliminary fermentation apparatus for sewage-treated fermentation bacteria according to claim 3, wherein an independent operation wall opening / closing door is provided only in a portion corresponding to the operation wall surface.
【請求項5】前記培養槽には循環ポンプが循環パイプを
介して連結してあり、循環ポンプの二次側は培養槽と、
ドレーン本管乃至排出パイプに切換弁を介して接続して
あることを特徴とする請求項1、2、3または4記載の
汚水処理発酵菌の予備発酵装置。
5. A circulating pump is connected to the culturing tank via a circulating pipe, and a secondary side of the circulating pump is connected to the culturing tank.
5. The pre-fermentation apparatus for sewage-treated fermentative bacteria according to claim 1, wherein the apparatus is connected to a drain main pipe or a discharge pipe via a switching valve.
【請求項6】前記汲み揚げポンプは前記ケーシングの中
の第1室内に設けてあることを特徴とする請求項1、
2、3、4または5記載の汚水処理発酵菌の予備発酵装
置。
6. The pump according to claim 1, wherein said pump is provided in a first chamber in said casing.
A preliminary fermentation apparatus for a sewage treatment fermenter according to 2, 3, 4 or 5.
JP2000279290A 2000-09-14 2000-09-14 Preliminary fermentation device of fermentation bacteria for sewage treatment Withdrawn JP2002086170A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000279290A JP2002086170A (en) 2000-09-14 2000-09-14 Preliminary fermentation device of fermentation bacteria for sewage treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000279290A JP2002086170A (en) 2000-09-14 2000-09-14 Preliminary fermentation device of fermentation bacteria for sewage treatment

Publications (1)

Publication Number Publication Date
JP2002086170A true JP2002086170A (en) 2002-03-26

Family

ID=18764316

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000279290A Withdrawn JP2002086170A (en) 2000-09-14 2000-09-14 Preliminary fermentation device of fermentation bacteria for sewage treatment

Country Status (1)

Country Link
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007075786A (en) * 2005-09-16 2007-03-29 Sharp Corp Water treatment method, micro-nano bubble microorganism activating unit and water treatment apparatus
JP2012055827A (en) * 2010-09-08 2012-03-22 Nippon Mizushori Giken:Kk Culture device and culture system
CN116200245A (en) * 2023-04-28 2023-06-02 广东圣蜜生物科技有限公司 Production equipment and process of skin care product stock solution with natural anti-corrosion function

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007075786A (en) * 2005-09-16 2007-03-29 Sharp Corp Water treatment method, micro-nano bubble microorganism activating unit and water treatment apparatus
JP4648140B2 (en) * 2005-09-16 2011-03-09 シャープ株式会社 Water treatment method, micro-nano bubble microbial activity unit and water treatment apparatus
JP2012055827A (en) * 2010-09-08 2012-03-22 Nippon Mizushori Giken:Kk Culture device and culture system
CN116200245A (en) * 2023-04-28 2023-06-02 广东圣蜜生物科技有限公司 Production equipment and process of skin care product stock solution with natural anti-corrosion function

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