JP2005013879A - Waste liquid treatment apparatus - Google Patents

Waste liquid treatment apparatus Download PDF

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Publication number
JP2005013879A
JP2005013879A JP2003182251A JP2003182251A JP2005013879A JP 2005013879 A JP2005013879 A JP 2005013879A JP 2003182251 A JP2003182251 A JP 2003182251A JP 2003182251 A JP2003182251 A JP 2003182251A JP 2005013879 A JP2005013879 A JP 2005013879A
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Prior art keywords
waste liquid
treatment
tank
treatment tank
treatment apparatus
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Pending
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JP2003182251A
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Japanese (ja)
Inventor
Shinten Natsuhara
伸展 夏原
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Toyo Giken Co Ltd
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Toyo Giken Co Ltd
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Priority to JP2003182251A priority Critical patent/JP2005013879A/en
Publication of JP2005013879A publication Critical patent/JP2005013879A/en
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  • Degasification And Air Bubble Elimination (AREA)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a simple and low-cost waste liquid treatment apparatus which can forcibly eliminate bubbles generated and accumulated when waste liquid is heated and concentrated, and makes the deterioration of waste liquid treatment capacity of the apparatus small due to a small temperature drop at the bubble elimination. <P>SOLUTION: In the waste liquid treatment apparatus where the waste liquid E stored in a treatment tank 1 is heated by a heating means 3 to be evaporated and concentrated, an air sucking means 4 and an air blowing means 6 which forcibly discharge evaporated material generated from the waste liquid E quickly to the outside of the treatment tank 1 are installed. The air sucking means 4 or the air blowing means 6 uses blowing air pressure to introduce outside air to the liquid surface of the waste liquid E or to blow air thereto, thereby forcibly eliminating the bubbles B accumulated on the liquid surface of the waste liquid E. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

【0001】
【発明の属する技術分野】
本発明は、廃液を加熱濃縮する廃液処理装置に関し、例えば、漬物、餡等の食品製造加工に伴って排出される廃液を加熱濃縮することにより廃液を減量化する廃液処理装置に関するものである。
【0002】
【従来の技術】
周知のとおり、廃液の処理方法の一つとして、処理槽に収容した廃液を加熱しその水分を蒸発させて廃液を濃縮し減量化することが行われている。ところが、処理する廃液の種類によっては、加熱濃縮時に廃液から多量の泡が発生し、これらの泡が液面に積層して処理槽から溢れ出す問題を生じることがあった。
【0003】
この問題に対処するため、従来、積層した泡が処理槽の所定高さに達したことを泡検知器で検知し、泡レベルがある程度下がるまで、廃液に対する加熱を弱めて新たな泡の発生を抑制する装置が提案されている(特許文献1参照)。
【0004】
しかしながら、この装置は、自然放熱により廃液の温度を低下させて泡の発生を抑制していたため、処理槽の断熱性が優れている程、泡レベルを下げるのに時間がかかり、この間の加熱抑制が装置の廃液処理能力を大幅に低下させてしまう難点があった。しかも、この装置は、積層している泡が自ら消滅するのを待たねばならないことから、消泡し難い廃液を処理する場合ほど、泡レベルを下げるのに時間がかかり、装置の廃液処理能力が損なわれていた。
【0005】
【特許文献1】
特開2000−61203号公報
【0006】
【発明が解決しようとする課題】
本発明は、従来の加熱濃縮による廃液処理装置に上記のような難点があったことに鑑みて為されたもので、廃液の液面に積層する泡を即座に強制消泡することができ、しかも、消泡時における廃液自体の温度低下が少なくて装置の廃液処理能力が大幅に低下することのない構造簡素で安価な廃液処理装置を提供することにある。
【0007】
【課題を解決するための手段】
本発明は、処理槽に収容された廃液を加熱手段により加熱して該廃液を蒸発させて濃縮する廃液処理装置であって、
該処理槽で発生する蒸発物を吸引する吸気手段を備え、該吸気手段の吸引圧を利用して該廃液の液面に外気を導き、該吸気手段により該蒸発物を該外気と共に強制排気することを特徴とする。
【0008】
また、本発明は、処理槽に収容された廃液を加熱手段により加熱して該廃液を蒸発させて濃縮する廃液処理装置であって、
該廃液の液面に対し送風する送風手段を備え、該送風手段の送風圧を利用して該処理槽で発生する蒸発物を該外気と共に強制排気することを特徴とする。
【0009】
更に本発明は、前記処理槽の上部が開放されていることを特徴とする。
【0010】
更にまた、本発明は前記処理槽の上部が開放されており、前記吸気手段が該処理槽の開放部に対し開閉可能に昇降する排気フードを備えていることを特徴とする。
【0011】
更にまた、本発明は、前記処理槽の廃液に上方から未処理の廃液を散布する散布手段を備えたことを特徴とする。
【0012】
更にまた、本発明は、前記加熱手段が蒸気を発生させる蒸気ボイラと、前記処理槽1の槽内に配設され、該蒸気を通す蒸気管とから成ることを特徴とする。
【0013】
【発明の実施の形態】
以下、本発明の実施の形態に係る廃液処理装置について、図1を参照しながら説明する。なお、本実施形態では、漬物(べったら漬け)を製造する際に排出される廃液を処理する例を説明している。この廃液は糖分を多く含んでおり、加熱濃縮時に発泡した泡は、自然消滅し難く液面に積層し易い。
【0014】
図1において符号1で指示するものは、処理すべき廃液Eを収容する処理槽である。処理槽1はその上部が開放されて開放部が形成されており、底部には排出孔11が設けられている。排出孔11にはバルブ13を備えた排出管12が接続され、バルブ13を開閉して処理済みの廃液を排出することができる。また、処理槽1には断熱材が周設されており、加熱された廃液Eを保温する。
【0015】
符号2で指示するものは、廃液を上記処理槽1へ供給するための供給手段である。供給手段2は、未処理の廃液を貯留する貯留槽21と、貯留槽21の廃液を供給管23を通して散布手段24へ圧送するポンプ22とから構成されている。散布手段24は、多数の噴出孔を備えた環状パイプ材から構成され、処理槽1の開放部に沿って配設されている。ポンプ22により圧送された廃液を多数の噴出孔から噴出させることによって、未処理の廃液を処理槽1の廃液Eに対して上方から散布する。
【0016】
符号3で指示するものは、上記処理槽1内の廃液Eを加熱するための加熱手段である。本実施形態の加熱手段3は、蒸気を発生させる蒸気ボイラ31と、この蒸気を通す蒸気管32とから構成されている。この蒸気管32は処理槽1の底部において槽内に臨んで配設されており、蒸気の熱によって処理槽1内の廃液Eを蒸気管32を介して加熱する。なお、処理槽1内の蒸気管32の長さ、径、位置等は、処理槽1の廃液容量、廃液Eの種類等を考慮して種々の設計変更が可能である。
【0017】
符号4で指示するものは、処理槽1の廃液Eから発生する蒸発物を吸引するための吸気手段である。本実施形態の吸気手段4は、処理槽1の上方に配設された吸気ダクト41と、吸気ダクト41に接続された吸気ファン42と、吸気ダクト41の下端に配設された排気フード43とから構成されている。吸気手段4は、図示しない固定フレームに上下動可能に設けられ、処理槽1の開放部に対し昇降可能に構成されている。そして、この吸気手段4を最下降させたとき、排気フード43で処理槽1の開放部を閉じることができる。なお、吸気手段4の吸気ダクト41及び吸気ファン42を固定し、吸気ダクト41に図示しない可撓性パイプを介して排気フード43を配設することによって、この排気フード43のみを処理槽1に対して上下動可能に構成しても良い。
【0018】
以下、本実施形態の廃液処理装置による廃液Eの処理作業を説明する。
【0019】
まず、処理槽1内へ未処理の廃液を供給し、この廃液を加熱手段3で加熱して廃液Eの濃縮処理を開始する。廃液Eの液温が上昇することによって廃液Eから蒸発物が発生するとともに、泡Bが発生して廃液Eの液面に積層し始める。このとき、吸気手段4を作動させ、この吸気手段4で蒸発物を吸引しながら、その吸引圧を利用して廃液Eの液面に外気を導く。この外気が廃液Eの液面に積層する泡Bに接触し、その際の風圧および泡の温度低下によって泡Bが消泡される。
【0020】
図1に示すように、泡Bを消泡する外気は、吸気手段4の排気フード43と処理槽1の開放部との隙間を通って廃液Eの液面に導かれる。したがって、泡Bに接触する外気の流量・流速は、吸気ファン42の吸引力、及び排気フード43と処理槽1の開放部との間隔を変更することによって適宜調節することができる。したがって、例えば、加熱濃縮時に発泡しない廃液や、発泡してもすぐに自然消滅して泡が積層しない廃液を処理する場合等には、保温のため、排気フード43を最下降させて処理槽1の開放部を閉じた状態で廃液処理を行うことが可能である。
【0021】
こうして外気で泡Bを消泡しながら廃液Eの加熱濃縮を進めてゆき、廃液Eが所定濃度まで濃縮したとき、供給手段2を作動させ、未処理の廃液を処理槽1へ供給する。本実施形態の廃液処理装置は、散布手段24によって未処理の廃液を処理槽1の廃液Eに対し上方から散布して供給することができるので、この散布廃液を泡Bに接触させることによっても泡Bを消泡することができる。したがって、加熱濃縮中に未処理の廃液の散布供給を行なっても良い。
【0022】
そして、処理槽1での廃液Eの加熱濃縮を終了するときには、処理槽1の底部のバルブ13を開いて排出孔11から処理済みの濃縮廃液を排出する。
【0023】
以上のように、本実施形態の廃液処理装置によれば、廃液Eから発生する蒸発物を吸気手段4により積極的に吸引することができるので、加熱濃縮時の蒸発物を速やかに処理槽1の外部へ強制排気することができる。しかも、この吸気手段4の吸引力によって処理槽1内をある程度、減圧状態に保つことができるので、廃液Eの蒸発を促進させることができ、装置の廃液処理能力を向上させることができる。
【0024】
また、本実施形態の廃液処理装置によれば、吸気手段4の吸引圧を利用して廃液Eの液面に外気を導き、この外気を泡Bに接触させて泡Bを即座に強制消泡することができる。したがって、従来装置のように、積層した泡が自然消滅して泡レベルが下がるのを廃液の液温を低下させて待つ必要もなく、この消泡工程によって装置の廃液処理能力が大幅に低下するようなこともない。
【0025】
更にまた、本実施形態の廃液処理装置によれば、外気で泡を強制消泡することができるので、消泡時に廃液Eに対する加熱を抑制する必要がなく、廃液に対する加熱をそのまま続行することが可能である。しかも、外気との接触も廃液Eの液面に積層した泡Bに対して限定的に行なわれるので、外気導入による廃液それ自体の温度低下も少なく、従来装置のように廃液処理能力が大幅に低下することもない。
【0026】
更にまた、本実施形態の廃液処理装置は、廃液Eの蒸発を促進する吸気手段4を、泡Bの消泡手段として同時利用しているので、装置構成を極めて簡素化することができ、廃液処理能力に優れた廃液処理装置を、頗る安価に市場に提供することができる。
【0027】
以上、本発明の一実施形態について説明したが、本発明に係る廃液処理装置はその他の形態でも実施し得るものである。
【0028】
例えば、上記実施形態では、上部を開放した処理槽1の上方に吸気手段4を昇降可能に設け、排気フード43と処理槽1の開放部との隙間を通して外気を導くようにしているが、図2に示すように、処理槽5の上部に直接、吸気手段4の吸気ダクト41を接続し、この処理槽5に開設した外気取入口51を通して外気を導くようにしても良い。このことで、装置構成を更に簡素化することができる。この場合、外気の流量等の調節は、吸気ファン42の吸引力を変更することで行なうことができる。
【0029】
また、上記実施形態では、供給手段2の散布手段24を多数の噴出孔を備えた環状パイプ材で構成しているが、勿論これに限定されるものではなく、同じく図2に示すように、散布手段25を多数の噴出孔を備えた円筒部材で構成しても良い。また、処理槽5内に複数の散布手段25を配設しても良い。
【0030】
更にまた、上記実施形態では、上部を開放した処理槽1の上方に吸気手段4を設けているが、図3に示すように、吸気手段の代わりに、廃液Eの液面に対し送風する送風手段6を設けても良い。この送風手段6は、処理槽1の上方に配設された送風ダクト61と、この送風ダクト61に接続された送風ファン62とから構成されている。廃液Eを加熱して泡Bが液面に積層し始めたとき、送風ファン62を作動させて廃液Eの液面に対して送風し、その際の風圧および泡の温度低下によって泡Bを消泡する。そして、この送風手段6の送風圧を利用して処理槽1で発生する蒸発物を速やかに強制排気するのである。なお、廃液Eの液面に対する送風は、例えば、冷風で行なっても良く、温風で行なっても良い。泡Bの消泡効果、装置の廃液処理能力等を考慮して種々の変更が可能である。
【0031】
この実施変形例の廃液処理装置においても、加熱濃縮時の蒸発物を速やかに処理槽1の外部へ強制排気することができるので、廃液Eの蒸発を促進させることができ、装置の廃液処理能力を向上させることができる。そして、送風手段6の送風を泡Bに接触させて泡Bを即座に強制消泡することができ、また、必ずしも消泡時に廃液Eに対する加熱を抑制する必要がないので、従来装置のように消泡時に廃液処理能力が大幅に低下するようなこともない。
【0032】
更にまた、上記実施形態では、廃液Eを加熱する加熱手段3として、蒸気ボイラ31で得た蒸気熱を利用しているが、本発明は決してこれに限定されるものではなく、例えば、処理槽1の槽内に配設した電熱ヒータで廃液Eを加熱したり、処理槽1を電磁誘導加熱して廃液Eを加熱したり、処理槽1を外側からガス燃焼熱で加熱して廃液Eを加熱するようにしても良い。
【0033】
更にまた、上記実施形態では、漬物を製造する際に排出される廃液Eを処理する例を説明しているが、勿論これに限定されるものではなく、例えば、畜産、食肉加工時に排出される廃液や屎尿、機械洗浄液等の工業廃液等の各種廃液の処理に適用することが可能である。
【0034】
本発明は、その趣旨を逸脱しない範囲内で当業者の知識に基づき種々の改良、変更、修正を加えた態様で実施し得るものである。また、同一の作用又は効果が生じる範囲内で、何れかの発明特定事項を他の技術に置換した形態で実施しても良く、また、一体に構成されている発明特定事項を複数の部材から構成しても、複数の部材から構成されている発明特定事項を一体に構成した形態で実施しても良い。
【0035】
【発明の効果】
以上のように、本発明に係る廃液処理装置によれば、廃液から発生する蒸発物を、吸気手段または送風手段によって速やかに処理槽の外部へ強制排気することができるので、廃液の蒸発を促進させることができ、装置の廃液処理能力を向上させることができる。
【0036】
しかも、吸気手段の吸引圧または送風手段の送風圧を利用して、廃液の液面に外気を導くか送風するかして、廃液の液面に積層する泡を即座に強制消泡することができるので、従来装置のように、積層した泡が自然消滅して泡レベルが下がるのを廃液自体の温度を低下させて待つ必要もなく、この消泡工程によって装置の廃液処理能力が大幅に低下するようなこともない。
【0037】
更にまた、このように廃液の液面に積層する泡を即座に強制消泡することができるので、消泡時に廃液に対する加熱を抑制する必要がなく、廃液に対する加熱をそのまま続行することが可能である。しかも、外気の導入または送風も、廃液の液面に積層した泡に対して限定的に行なわれるので、消泡時の廃液自体の温度低下も少なく、従来装置のように廃液処理能力が大幅に低下することもない。
【0038】
更にまた、本実施形態の廃液処理装置は、廃液の蒸発を促進する吸気手段又は送風手段を、泡の消泡手段として同時利用しているので、装置構成を極めて簡素化することができ、廃液処理能力に優れた廃液処理装置を、頗る安価に市場に提供することができる。
【図面の簡単な説明】
【図1】本発明の廃液処理装置の部分断面正面図である。
【図2】本発明の変形例の廃液処理装置の部分断面正面図である。
【図3】本発明の他の変形例の廃液処理装置の部分断面正面図である。
【符号の説明】
E 廃液
B 泡
1 処理槽
11 排出孔
12 排出管
13 バルブ
2 供給手段
21 貯留槽
22 ポンプ
23 供給管
24 散布手段
25 散布手段
3 加熱手段
31 蒸気ボイラ
32 蒸気管
4 吸気手段
41 吸気ダクト
42 吸気ファン
43 排気フード
5 処理槽
51 外気取入口
6 送風手段
61 送風ダクト
62 送風ファン
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a waste liquid processing apparatus that heats and concentrates a waste liquid, for example, a waste liquid processing apparatus that reduces the amount of waste liquid by heating and concentrating the waste liquid that is discharged during food manufacturing processing such as pickles and strawberries.
[0002]
[Prior art]
As is well known, as one of the methods for treating the waste liquid, the waste liquid stored in the treatment tank is heated to evaporate the water, thereby concentrating the waste liquid to reduce the volume. However, depending on the type of waste liquid to be treated, a large amount of bubbles may be generated from the waste liquid during heating and concentration, and these bubbles may accumulate on the liquid surface and overflow from the treatment tank.
[0003]
In order to cope with this problem, it is conventionally detected by the foam detector that the stacked foam has reached the predetermined height of the processing tank, and until the foam level drops to some extent, the heating to the waste liquid is weakened to generate new foam. The apparatus which suppresses is proposed (refer patent document 1).
[0004]
However, since this device reduced the temperature of the waste liquid by natural heat dissipation and suppressed the generation of bubbles, the better the heat insulation of the treatment tank, the longer it took to lower the bubble level, and the suppression of heating during this period However, there has been a problem that the waste liquid processing capacity of the apparatus is greatly reduced. In addition, since this device must wait for the foams that have been deposited to disappear by itself, it takes longer to lower the bubble level when processing waste liquids that are difficult to defoam. It was damaged.
[0005]
[Patent Document 1]
Japanese Patent Laid-Open No. 2000-61203
[Problems to be solved by the invention]
The present invention was made in view of the above-mentioned drawbacks in the conventional waste liquid treatment equipment by heat concentration, and can immediately and forcibly defoam the bubbles laminated on the liquid surface of the waste liquid, In addition, it is an object of the present invention to provide a waste liquid treatment apparatus having a simple structure and low cost, in which the temperature of the waste liquid itself during defoaming is small and the waste liquid treatment capability of the apparatus is not significantly reduced.
[0007]
[Means for Solving the Problems]
The present invention is a waste liquid treatment apparatus for concentrating by evaporating the waste liquid by heating the waste liquid stored in the treatment tank by a heating means,
Intake means for sucking evaporant generated in the treatment tank is provided, and outside air is guided to the liquid level of the waste liquid using suction pressure of the intake means, and the evaporate is forcibly exhausted together with the outside air by the intake means. It is characterized by that.
[0008]
Further, the present invention is a waste liquid treatment apparatus for concentrating by evaporating the waste liquid by heating the waste liquid stored in the treatment tank by a heating means,
A blower for blowing air to the liquid level of the waste liquid is provided, and the evaporant generated in the treatment tank is forcibly exhausted together with the outside air by using the blower pressure of the blower.
[0009]
Furthermore, the present invention is characterized in that the upper part of the treatment tank is opened.
[0010]
Furthermore, the present invention is characterized in that the upper part of the processing tank is opened, and the intake means includes an exhaust hood that moves up and down so as to be openable and closable with respect to the open part of the processing tank.
[0011]
Furthermore, the present invention is characterized by comprising spraying means for spraying untreated waste liquid from above into the waste liquid of the treatment tank.
[0012]
Furthermore, the present invention is characterized in that the heating means includes a steam boiler that generates steam, and a steam pipe that is disposed in the tank of the processing tank 1 and passes the steam.
[0013]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, a waste liquid treatment apparatus according to an embodiment of the present invention will be described with reference to FIG. In the present embodiment, an example is described in which the waste liquid discharged when manufacturing pickles (pickles pickled) is processed. This waste liquid contains a large amount of sugar, and bubbles foamed at the time of heating and concentration are unlikely to disappear spontaneously and are easily laminated on the liquid surface.
[0014]
In FIG. 1, what is indicated by reference numeral 1 is a processing tank for storing waste liquid E to be processed. The processing tank 1 is open at the top to form an open portion, and a discharge hole 11 is provided at the bottom. A discharge pipe 12 having a valve 13 is connected to the discharge hole 11, and the treated waste liquid can be discharged by opening and closing the valve 13. In addition, a heat insulating material is provided around the processing tank 1 to keep the heated waste liquid E warm.
[0015]
What is indicated by reference numeral 2 is a supply means for supplying waste liquid to the treatment tank 1. The supply means 2 includes a storage tank 21 that stores untreated waste liquid, and a pump 22 that pumps the waste liquid of the storage tank 21 to the spraying means 24 through the supply pipe 23. The spraying means 24 is composed of an annular pipe material having a large number of ejection holes, and is disposed along the open portion of the processing tank 1. By discharging the waste liquid pumped by the pump 22 from a large number of ejection holes, the untreated waste liquid is sprayed onto the waste liquid E in the treatment tank 1 from above.
[0016]
What is indicated by reference numeral 3 is a heating means for heating the waste liquid E in the processing tank 1. The heating means 3 of this embodiment includes a steam boiler 31 that generates steam and a steam pipe 32 through which the steam passes. The steam pipe 32 is disposed at the bottom of the processing tank 1 so as to face the tank, and the waste liquid E in the processing tank 1 is heated via the steam pipe 32 by the heat of the steam. The length, diameter, position, and the like of the steam pipe 32 in the processing tank 1 can be variously changed in consideration of the waste liquid capacity of the processing tank 1, the type of the waste liquid E, and the like.
[0017]
What is indicated by reference numeral 4 is an intake means for sucking evaporate generated from the waste liquid E in the treatment tank 1. The intake means 4 of the present embodiment includes an intake duct 41 disposed above the processing tank 1, an intake fan 42 connected to the intake duct 41, and an exhaust hood 43 disposed at the lower end of the intake duct 41. It is composed of The intake means 4 is provided on a fixed frame (not shown) so as to be movable up and down, and is configured to be movable up and down with respect to the open portion of the processing tank 1. When the intake means 4 is lowered to the lowest position, the exhaust hood 43 can close the open portion of the processing tank 1. The intake duct 41 and the intake fan 42 of the intake means 4 are fixed, and the exhaust hood 43 is disposed in the intake duct 41 via a flexible pipe (not shown), so that only the exhaust hood 43 is placed in the processing tank 1. On the other hand, it may be configured to be movable up and down.
[0018]
Hereinafter, the processing operation of the waste liquid E by the waste liquid processing apparatus of this embodiment will be described.
[0019]
First, untreated waste liquid is supplied into the treatment tank 1, and this waste liquid is heated by the heating means 3 to start the concentration process of the waste liquid E. As the liquid temperature of the waste liquid E rises, an evaporant is generated from the waste liquid E, and bubbles B are generated and start to be stacked on the liquid surface of the waste liquid E. At this time, the suction means 4 is operated, and the suction means 4 sucks evaporate, and the outside pressure is guided to the liquid level of the waste liquid E using the suction pressure. The outside air comes into contact with the bubbles B stacked on the liquid surface of the waste liquid E, and the bubbles B are defoamed by the wind pressure and the temperature drop of the bubbles.
[0020]
As shown in FIG. 1, the outside air that eliminates the bubbles B is guided to the liquid level of the waste liquid E through the gap between the exhaust hood 43 of the intake means 4 and the open portion of the treatment tank 1. Therefore, the flow rate / flow velocity of the outside air contacting the bubbles B can be adjusted as appropriate by changing the suction force of the intake fan 42 and the interval between the exhaust hood 43 and the open portion of the treatment tank 1. Therefore, for example, when processing waste liquid that does not foam during heat concentration, or waste liquid that does not immediately stack and foam does not stack even after foaming, the exhaust hood 43 is moved down to keep the treatment tank 1 warm. It is possible to perform the waste liquid treatment in a state where the open portion is closed.
[0021]
In this way, heating and concentration of the waste liquid E is proceeded while the bubbles B are defoamed by the outside air, and when the waste liquid E is concentrated to a predetermined concentration, the supply means 2 is operated to supply the untreated waste liquid to the treatment tank 1. The waste liquid treatment apparatus of this embodiment can supply unprocessed waste liquid to the waste liquid E in the treatment tank 1 from above by the spraying means 24 and supply the waste liquid E by bringing the sprayed waste liquid into contact with the bubbles B. Bubble B can be defoamed. Therefore, the untreated waste liquid may be sprayed and supplied during the heat concentration.
[0022]
When the heat concentration of the waste liquid E in the treatment tank 1 is finished, the valve 13 at the bottom of the treatment tank 1 is opened to discharge the treated concentrated waste liquid from the discharge hole 11.
[0023]
As described above, according to the waste liquid treatment apparatus of the present embodiment, since the evaporant generated from the waste liquid E can be actively sucked by the intake means 4, the evaporant at the time of heating and concentration can be quickly treated. Can be forced to the outside. Moreover, since the inside of the processing tank 1 can be kept in a reduced pressure state to some extent by the suction force of the intake means 4, the evaporation of the waste liquid E can be promoted, and the waste liquid processing capability of the apparatus can be improved.
[0024]
Further, according to the waste liquid treatment apparatus of the present embodiment, the outside air is guided to the liquid surface of the waste liquid E by using the suction pressure of the suction means 4, and the outside air is brought into contact with the bubbles B so that the bubbles B are immediately forcibly removed. can do. Therefore, unlike the conventional apparatus, there is no need to wait for the liquid temperature of the waste liquid to be lowered and the foam level to drop naturally, and this defoaming process greatly reduces the waste liquid processing capacity of the apparatus. There is no such thing.
[0025]
Furthermore, according to the waste liquid treatment apparatus of the present embodiment, it is possible to forcibly defoam bubbles with the outside air, so there is no need to suppress heating of the waste liquid E during defoaming, and heating of the waste liquid can be continued as it is. Is possible. In addition, since the contact with the outside air is also limited to the bubbles B stacked on the liquid surface of the waste liquid E, the temperature of the waste liquid itself due to the introduction of the outside air is small, and the waste liquid treatment capacity is greatly increased as in the conventional apparatus. There is no decline.
[0026]
Furthermore, since the waste liquid treatment apparatus of the present embodiment uses the air intake means 4 for promoting the evaporation of the waste liquid E at the same time as the defoaming means for the bubbles B, the apparatus configuration can be greatly simplified. It is possible to provide a waste liquid treatment apparatus having an excellent processing capacity to the market at a much lower cost.
[0027]
Although one embodiment of the present invention has been described above, the waste liquid treatment apparatus according to the present invention can be implemented in other forms.
[0028]
For example, in the above embodiment, the intake means 4 is provided so as to be able to move up and down above the processing tank 1 with the upper part opened, and the outside air is guided through the gap between the exhaust hood 43 and the open part of the processing tank 1. 2, the intake duct 41 of the intake means 4 may be directly connected to the upper portion of the processing tank 5, and the outside air may be guided through the outside air inlet 51 opened in the processing tank 5. This can further simplify the apparatus configuration. In this case, adjustment of the flow rate or the like of the outside air can be performed by changing the suction force of the intake fan 42.
[0029]
Moreover, in the said embodiment, although the spreading | diffusion means 24 of the supply means 2 is comprised with the annular pipe material provided with many ejection holes, of course, it is not limited to this, As also shown in FIG. You may comprise the spreading | diffusion means 25 with the cylindrical member provided with many ejection holes. Further, a plurality of spraying means 25 may be disposed in the processing tank 5.
[0030]
Furthermore, in the above embodiment, the intake means 4 is provided above the treatment tank 1 with the upper part opened. However, as shown in FIG. Means 6 may be provided. The blowing unit 6 includes a blower duct 61 disposed above the processing tank 1 and a blower fan 62 connected to the blower duct 61. When the waste liquid E is heated and the bubbles B start to be laminated on the liquid surface, the blower fan 62 is operated to blow air to the liquid surface of the waste liquid E, and the bubbles B are extinguished by the wind pressure and the bubble temperature drop at that time. Foam. And the evaporant which generate | occur | produces in the processing tank 1 is forcedly exhausted rapidly using the ventilation pressure of this ventilation means 6. FIG. Note that the air blowing to the liquid level of the waste liquid E may be performed by, for example, cold air or hot air. Various changes can be made in consideration of the defoaming effect of the bubbles B, the waste liquid treatment capability of the apparatus, and the like.
[0031]
Also in the waste liquid treatment apparatus according to this embodiment, since the evaporate at the time of heating and concentration can be forcibly exhausted to the outside of the treatment tank 1, evaporation of the waste liquid E can be promoted, and the waste liquid treatment capacity of the apparatus Can be improved. And since the ventilation of the ventilation means 6 is made to contact the bubble B and the bubble B can be immediately forced to defoam, and it is not always necessary to suppress the heating to the waste liquid E during the defoaming, as in the conventional device The waste liquid treatment capacity is not significantly reduced during defoaming.
[0032]
Furthermore, in the said embodiment, although the steam heat obtained with the steam boiler 31 is utilized as the heating means 3 which heats the waste liquid E, this invention is never limited to this, For example, a processing tank The waste liquid E is heated by an electric heater disposed in the tank 1, the waste liquid E is heated by electromagnetic induction heating of the treatment tank 1, or the waste liquid E is heated by gas combustion heat from the outside. You may make it heat.
[0033]
Furthermore, although the said embodiment demonstrated the example which processes the waste liquid E discharged | emitted when manufacturing pickles, of course, it is not limited to this, For example, it discharge | emits at the time of livestock production and meat processing The present invention can be applied to the treatment of various waste liquids such as waste liquids, manure, and industrial waste liquids such as machine cleaning liquids.
[0034]
The present invention can be implemented in a mode in which various improvements, changes, and modifications are made based on the knowledge of those skilled in the art without departing from the spirit of the present invention. In addition, within a range where the same action or effect is produced, any invention specific matter may be replaced with another technology, and the integrally configured invention specific matter may be made up of a plurality of members. Even if comprised, you may implement with the form which comprised the invention specific matter comprised from the several member integrally.
[0035]
【The invention's effect】
As described above, according to the waste liquid treatment apparatus according to the present invention, the evaporant generated from the waste liquid can be forcibly exhausted to the outside of the treatment tank quickly by the intake means or the air blowing means, thus promoting the evaporation of the waste liquid. It is possible to improve the waste liquid processing capacity of the apparatus.
[0036]
In addition, by using the suction pressure of the suction means or the blowing pressure of the blowing means, the outside air is guided or blown to the liquid level of the waste liquid, and the bubbles stacked on the liquid level of the waste liquid can be immediately forcibly defoamed. This eliminates the need to lower the temperature of the waste liquid itself and wait for the foam to drop naturally and reduce the foam level, unlike the conventional equipment. This defoaming process significantly reduces the waste liquid treatment capacity of the equipment. There is nothing to do.
[0037]
Furthermore, since the bubbles stacked on the liquid surface of the waste liquid can be forcibly defoamed immediately in this way, it is not necessary to suppress the heating of the waste liquid at the time of defoaming, and the heating to the waste liquid can be continued as it is. is there. Moreover, since the introduction or blowing of outside air is also limited to the bubbles stacked on the liquid surface of the waste liquid, there is little temperature drop of the waste liquid itself at the time of defoaming, and the waste liquid processing capacity is greatly increased as in the conventional device. There is no decline.
[0038]
Furthermore, since the waste liquid treatment apparatus of the present embodiment uses the air intake means or the air blowing means for promoting the evaporation of the waste liquid at the same time as the foam defoaming means, the apparatus configuration can be greatly simplified. It is possible to provide a waste liquid treatment apparatus having an excellent processing capacity to the market at a much lower cost.
[Brief description of the drawings]
FIG. 1 is a partial cross-sectional front view of a waste liquid treatment apparatus of the present invention.
FIG. 2 is a partial cross-sectional front view of a waste liquid treatment apparatus according to a modification of the present invention.
FIG. 3 is a partial cross-sectional front view of a waste liquid treatment apparatus according to another modification of the present invention.
[Explanation of symbols]
E Waste liquid B Bubble 1 Processing tank 11 Discharge hole 12 Discharge pipe 13 Valve 2 Supply means 21 Storage tank 22 Pump 23 Supply pipe 24 Dispersion means 25 Dispersion means 3 Heating means 31 Steam boiler 32 Steam pipe 4 Intake means 41 Intake duct 42 Intake fan 42 43 Exhaust hood 5 Treatment tank 51 Outside air intake 6 Blower means 61 Blower duct 62 Blower fan

Claims (6)

処理槽に収容された廃液を加熱手段により加熱して該廃液を蒸発させて濃縮する廃液処理装置であって、
該処理槽で発生する蒸発物を吸引する吸気手段を備え、該吸気手段の吸引圧を利用して該廃液の液面に外気を導き、該吸気手段により該蒸発物を該外気と共に強制排気することを特徴とした廃液処理装置。
A waste liquid treatment apparatus that heats waste liquid stored in a treatment tank by heating means to evaporate the waste liquid and concentrates the waste liquid,
Intake means for sucking evaporant generated in the treatment tank is provided, and outside air is guided to the liquid level of the waste liquid using suction pressure of the intake means, and the evaporate is forcibly exhausted together with the outside air by the intake means. Waste liquid treatment equipment characterized by that.
処理槽に収容された廃液を加熱手段により加熱して該廃液を蒸発させて濃縮する廃液処理装置であって、
該廃液の液面に対し送風する送風手段を備え、該送風手段の送風圧を利用して該処理槽で発生する蒸発物を該外気と共に強制排気することを特徴とした廃液処理装置。
A waste liquid treatment apparatus that heats waste liquid stored in a treatment tank by a heating means to evaporate the waste liquid and concentrate the waste liquid,
A waste liquid treatment apparatus comprising a blower for blowing air to the liquid surface of the waste liquid, and forcibly exhausting the evaporate generated in the treatment tank together with the outside air by using the blow pressure of the blower.
前記処理槽の上部が開放されている請求項1又は請求項2記載の廃液処理装置。The waste liquid treatment apparatus according to claim 1 or 2, wherein an upper part of the treatment tank is opened. 前記処理槽の上部が開放されており、前記吸気手段が該処理槽の開放部に対し開閉可能に昇降する排気フードを備えている請求項1記載の廃液処理装置。The waste liquid treatment apparatus according to claim 1, wherein an upper portion of the treatment tank is open, and the intake means includes an exhaust hood that moves up and down in an openable and closable manner with respect to the open portion of the treatment tank. 前記処理槽の廃液に上方から未処理の廃液を散布する散布手段を備えた請求項1乃至請求項4の何れかに記載の廃液処理装置。The waste liquid processing apparatus according to any one of claims 1 to 4, further comprising spraying means for spraying untreated waste liquid from above into the waste liquid in the treatment tank. 前記加熱手段が、蒸気を発生させる蒸気ボイラと、前記処理槽1の槽内に配設され、該蒸気を通す蒸気管とから成る請求項1乃至請求項5記載の廃液処理装置。The waste liquid treatment apparatus according to any one of claims 1 to 5, wherein the heating means includes a steam boiler that generates steam and a steam pipe that is disposed in the tank of the processing tank 1 and passes the steam.
JP2003182251A 2003-06-26 2003-06-26 Waste liquid treatment apparatus Pending JP2005013879A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101165813B1 (en) 2011-12-23 2012-07-16 주식회사 에이치엔 Evaporator for removing bubble
KR101438681B1 (en) 2014-06-13 2014-09-12 다운환경 (주) Evaporation condensation apparatus having foam control structure
CN118356798A (en) * 2024-06-20 2024-07-19 山东中航天业科技有限公司 Industrial flue gas desulfurization carbon fixing device and method

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JPS5725788U (en) * 1980-07-17 1982-02-10
JPS5749897A (en) * 1980-09-10 1982-03-24 Japan Atomic Energy Res Inst Liquid waste processing device
JPS60168583A (en) * 1984-02-13 1985-09-02 Sekine:Kk Apparatus for diffusing purified water
JPS6371696A (en) * 1986-09-13 1988-04-01 株式会社東芝 Concentrator for radioactive waste liquor
JPH0788469A (en) * 1993-09-21 1995-04-04 Tokai Sanki Kk Apparatus and method for treating waste solution and water-soluble waste paint
JPH07194964A (en) * 1993-12-28 1995-08-01 Yasutarou Masuda Method for bringing liquid into contact with gas
JPH09206737A (en) * 1996-02-02 1997-08-12 Konica Corp Evaporating-concentrating device for photographic waste fluid

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5725788U (en) * 1980-07-17 1982-02-10
JPS5749897A (en) * 1980-09-10 1982-03-24 Japan Atomic Energy Res Inst Liquid waste processing device
JPS60168583A (en) * 1984-02-13 1985-09-02 Sekine:Kk Apparatus for diffusing purified water
JPS6371696A (en) * 1986-09-13 1988-04-01 株式会社東芝 Concentrator for radioactive waste liquor
JPH0788469A (en) * 1993-09-21 1995-04-04 Tokai Sanki Kk Apparatus and method for treating waste solution and water-soluble waste paint
JPH07194964A (en) * 1993-12-28 1995-08-01 Yasutarou Masuda Method for bringing liquid into contact with gas
JPH09206737A (en) * 1996-02-02 1997-08-12 Konica Corp Evaporating-concentrating device for photographic waste fluid

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101165813B1 (en) 2011-12-23 2012-07-16 주식회사 에이치엔 Evaporator for removing bubble
KR101438681B1 (en) 2014-06-13 2014-09-12 다운환경 (주) Evaporation condensation apparatus having foam control structure
CN118356798A (en) * 2024-06-20 2024-07-19 山东中航天业科技有限公司 Industrial flue gas desulfurization carbon fixing device and method

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