JP4611120B2 - Wastewater recycling system - Google Patents

Wastewater recycling system Download PDF

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JP4611120B2
JP4611120B2 JP2005161245A JP2005161245A JP4611120B2 JP 4611120 B2 JP4611120 B2 JP 4611120B2 JP 2005161245 A JP2005161245 A JP 2005161245A JP 2005161245 A JP2005161245 A JP 2005161245A JP 4611120 B2 JP4611120 B2 JP 4611120B2
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treated water
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JP2006334491A (en
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英樹 高橋
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Yanmar Co Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Description

本発明は、生物反応処理する排水リサイクルシステムに関する。 The present invention relates to a waste water recycling system that biological reaction treatment.

一般に、有機系の工場排水を処理する排水リサイクルシステムとしては、排水を生物反応処理する排水処理施設を備え、この排水処理施設で処理した排水を、汚泥と分離し消毒した後に排出するように構成されたものが公知である(例えば、特許文献1参照)。そして、このように処理、排出された工場排水は、下水放流もしくは河川放流されている。   Generally, a wastewater recycling system for treating organic factory wastewater is equipped with a wastewater treatment facility that biologically treats wastewater, and the wastewater treated in this wastewater treatment facility is separated from sludge and disinfected before being discharged. Is known (for example, see Patent Document 1). The factory wastewater treated and discharged in this way is discharged into sewage or rivers.

例えば、タコ、イカナゴ等の魚介類を加工する水産加工場においても、魚介類を加工、洗浄した後に発生する洗浄排水を、前記排水リサイクルシステムにより処理している。また、加工後に魚介類の食品残渣が発生するが、かかる魚介類の食品残渣は、委託業者に依頼して産廃処理を行っているのが現状である。
特開2003−136091号公報
For example, even in a fish processing plant that processes seafood such as octopus and sea cucumber, cleaning wastewater generated after processing and washing seafood is processed by the wastewater recycling system. In addition, food residues of seafood are generated after processing, and in the current situation, such food residues of seafood are subjected to industrial waste processing by requesting a contractor.
JP 2003-136091 A

魚介類を加工する水産加工場においては、委託業者に魚介類の食品残渣処理を依頼しなければならず、産廃処分費が必要となる。また、処理された工場排水を下水放流している加工場においては、下水放流に伴う下水道使用料金が必要となる。また、水産加工場は、加工場の床面や魚介類等の1次洗浄を上水で行っているため、これらの洗浄に使用する水道使用料金も必要となっている。   In fisheries processing plants that process seafood, it is necessary to request a food residue treatment of seafood from a contractor, and industrial waste disposal costs are required. In addition, in a processing plant that discharges treated factory wastewater, a sewerage usage fee for sewage discharge is required. In addition, since the fishery processing plant performs primary cleaning of the processing plant floor, seafood and the like with clean water, a water usage fee for these cleaning is also required.

本発明は、魚介類等の産廃処分費、工場で使用される上水道および下水道使用料金のコスト削減を図ることを課題とする。   This invention makes it a subject to aim at the cost reduction of industrial waste disposal costs, such as seafood, and the water supply fee used in a factory, and a sewerage usage fee.

本発明は、前記課題に鑑みて排水リサイクルシステムとしてなされたもので、その特徴は、食品加工場内の排水が流入する排水調整槽と該排水調整槽から導入される排水を生物反応処理する生物反応槽とを備える排水処理施設と、食品残渣を粉砕して前記排水調整槽に供給する食品残渣処理装置と、前記生物反応槽で処理された排水を、汚泥から分離しさらに高度処理して再利用可能にする処理水リサイクル施設と、前記処理水リサイクル施設で再利用可能とされた処理水の水質を監視する処理水監視装置と、前記処理水監視装置の処理水が供給される処理水貯留槽とを備え、前記処理水監視装置は、前記処理水リサイクル施設で処理された処理水が導入される水質監視槽と、該水質監視槽内の処理水をサンプリングして、そのサンプリング水の水質を測定する水質自動測定装置と、測定されたサンプリング水の水質測定値と予め設定された水質基準値とを比較し、水質測定値が予め定められた水質基準値に達した際に、前記水質監視槽の処理水が処理水貯留槽に供給されるのを停止する制御装置とを備えたことにある。 The present invention has been made in the waste water recycling system in view of the above problems, its features, biological response processing waste water drainage food processing hall is introduced from the waste water regulation tank and the drainage regulating tank flowing A wastewater treatment facility comprising a biological reaction tank, a food residue treatment device that pulverizes food residues and supplies the wastewater adjustment tank, and wastewater treated in the biological reaction tank is separated from sludge and further processed. Treated water recycling facility to be reusable, treated water monitoring device for monitoring the quality of treated water reusable at the treated water recycling facility, and treatment to which treated water from the treated water monitoring device is supplied A water storage tank, and the treated water monitoring device samples the water quality monitoring tank into which the treated water treated in the treated water recycling facility is introduced, and the treated water in the water quality monitoring tank, When the water quality automatic measurement device that measures the water quality of the sample is compared with the measured water quality measurement value of the sampled water and the preset water quality standard value, and the water quality measurement value reaches the predetermined water quality standard value, And a control device for stopping the treated water in the water quality monitoring tank from being supplied to the treated water storage tank.

本発明の排水リサイクルシステムにおいて、食品残渣については、食品残渣処理装置で例えば100μm程度のペースト状まで摩砕し、排水処理施設に投入することにより、分解処理させる。排水処理施設で処理された処理水は、処理水リサイクル施設で高度処理することにより、加工場で1次洗浄水として利用できる。   In the wastewater recycling system of the present invention, food residues are decomposed by being ground to a paste of, for example, about 100 μm with a food residue treatment apparatus and put into a wastewater treatment facility. The treated water treated at the wastewater treatment facility can be used as the primary washing water at the processing plant by advanced treatment at the treated water recycling facility.

また、排水処理施設に食品残渣を投入することにより、流入負荷が高くなることが懸念されるが、加工場において、加工作業終了後の夜間や、加工作業時の流入負荷の低いときに、処理残渣を適宜投入することにより、流入負荷の変動を抑えることができる。   In addition, there is a concern that the inflow load will increase due to the introduction of food residues into the wastewater treatment facility, but at the processing site at night after the end of processing work or when the inflow load during processing work is low, By appropriately introducing the residue, fluctuations in the inflow load can be suppressed.

本発明の排水リサイクルシステムの前記処理水貯留槽は、前記処理水貯留槽に上水を補給する上水補給装置が設けられ、前記制御装置は、処理水貯留槽内の水が利用されて処理水貯留槽内の水が所定量よりも少なくなった場合に、前記上水補給装置が上水を処理水貯留槽内に補給するように制御する。かかる場合には、処理水貯留槽から安定した水の供給を行うことができる。 The treated water storage tank of the wastewater recycling system of the present invention is provided with a water supply device that replenishes the treated water storage tank with clean water, and the control device uses water in the treated water storage tank for processing. When the water in the water storage tank becomes less than a predetermined amount, the water supply device controls the water to be supplied into the treated water storage tank. In such a case, stable water can be supplied from the treated water storage tank.

本発明の排水リサイクルシステムの前記食品残渣処理装置は、食品残渣が投入される第1残渣粉砕手段と、該第1残渣粉砕手段よりもさらに細かく食品残渣を粉砕する第2残渣粉砕手段と、該第2残渣粉砕手段により粉砕された処理残渣を貯留する残渣貯留槽と、該残渣貯留槽から所定量の処理残渣を前記排水処理施設に供給する定量ポンプ装置とを備えている。そして、食品残渣は第1残渣粉砕手段および第2残渣粉砕手段により、効率よく迅速に所定の状態まで粉砕でき、処理残渣の所定量を定量ポンプ装置で排水処理施設に供給できる。   The food residue treatment apparatus of the wastewater recycling system of the present invention includes a first residue pulverizing unit into which a food residue is charged, a second residue pulverizing unit that pulverizes a food residue more finely than the first residue pulverizing unit, A residue storage tank for storing the processing residue pulverized by the second residue pulverizing means; and a metering pump device for supplying a predetermined amount of the processing residue from the residue storage tank to the wastewater treatment facility. The food residue can be efficiently and quickly pulverized to a predetermined state by the first residue pulverizing means and the second residue pulverizing means, and a predetermined amount of the processing residue can be supplied to the wastewater treatment facility by the metering pump device.

本発明によれば、食品加工残渣を加工場内の原水と混合し処分するため、産廃処分費の削減が可能となる。また、処理水を加工場内での1次洗浄水として利用できるため、上水道および下水道使用料金の削減が可能となる。   According to the present invention, the food processing residue is mixed with the raw water in the processing plant and disposed, so that the industrial waste disposal cost can be reduced. In addition, since the treated water can be used as the primary washing water in the processing plant, it is possible to reduce water and sewage usage charges.

本発明の実施の形態を図面に基づいて説明する。本実施の形態では、連続流入間欠曝気法により汚水処理を行う排水リサイクルシステムとして、例えばタコ、イカナゴ等の魚介類を加工する水産加工場における水産加工排水中水処理システムを例示する。   Embodiments of the present invention will be described with reference to the drawings. In the present embodiment, as a wastewater recycling system that performs sewage treatment by the continuous inflow intermittent aeration method, for example, an aquatic processing wastewater treatment system in a fishery processing plant that processes seafood such as octopus and squid.

図1は、本実施形態に係る水産加工排水中水処理システムの概略システムを示す図である。この図に示すように、水産加工排水中水処理システム1は、排水処理施設2と、食品残渣処理装置3と、処理水リサイクル施設4と、処理水監視装置6および処理水貯留槽7とから主構成されている。   FIG. 1 is a diagram showing a schematic system of a fishery processing wastewater-in-water treatment system according to this embodiment. As shown in this figure, an aquatic processing wastewater-in-water treatment system 1 includes a wastewater treatment facility 2, a food residue treatment device 3, a treated water recycling facility 4, a treated water monitoring device 6, and a treated water storage tank 7. The main composition is.

排水処理施設2は、水産加工場で発生した排水(例えば、魚介類を洗浄したり、加工場の床面等を洗浄した排水)が流入される排水調整槽21と、この排水調整槽21に設置された排水送液ポンプP1により、排水調整槽21から排水が導入される生物反応槽23と、排水調整槽21内の排水に含まれる有機物を測定する測定装置27とを備えている。この測定装置27は、例えば、TOC測定器であって、TOC(Total Organic Carbon:全有機炭素)の値を測定するものである。   The wastewater treatment facility 2 includes a drainage adjustment tank 21 into which wastewater generated at a fishery processing plant (for example, wastewater from which seafood is washed or floor surface of a processing plant) is introduced, and the drainage adjustment tank 21 A biological reaction tank 23 into which drainage is introduced from the drainage adjustment tank 21 and a measuring device 27 that measures organic substances contained in the wastewater in the drainage adjustment tank 21 are provided by the installed drainage pump P1. This measuring device 27 is, for example, a TOC measuring device, and measures the value of TOC (Total Organic Carbon).

排水調整槽21の排水送液ポンプP1と生物反応槽23とは、排水送液管25により接続されており、この排水送液管25には、浮遊物等の異物を除去するベルトスクリーン26が介在されている。   The drainage liquid feed pump P1 and the biological reaction tank 23 of the drainage adjustment tank 21 are connected by a drainage liquid feed pipe 25. The drainage liquid feed pipe 25 has a belt screen 26 for removing foreign matters such as floating substances. Intervened.

前記生物反応槽23は、曝気ブロワB1により、内部の溶存酸素(DO)を制御するようになっている。生物反応処理としては、曝気ブロワB1を停止状態にする嫌気工程と曝気ブロワB1を駆動状態にする好気工程とを交互に切り換えて、排水の脱窒や脱リンが行われる。つまり、排水中に含まれる窒素化合物が好気工程において活性汚泥により酸化されて硝酸性窒素になり、その後、嫌気工程に切り換えられることによって硝酸性窒素から酸素を奪って窒素ガスを発生させ、これによって脱窒が行われる。また、嫌気工程において活性汚泥からリンが一旦放出され、その後、好気工程に切り換えられることによって活性汚泥にリンを過剰採取させることにより脱リンが行われる。   The biological reaction tank 23 controls internal dissolved oxygen (DO) by the aeration blower B1. As the biological reaction process, drainage denitrification and dephosphorization are performed by alternately switching between an anaerobic process for stopping the aeration blower B1 and an aerobic process for driving the aeration blower B1. In other words, the nitrogen compounds contained in the wastewater are oxidized by activated sludge in the aerobic process to become nitrate nitrogen, and then switched to the anaerobic process to remove oxygen from nitrate nitrogen and generate nitrogen gas. Denitrification is performed by Further, phosphorus is once released from the activated sludge in the anaerobic process, and thereafter, the phosphorus is removed by excessively collecting phosphorus in the activated sludge by switching to the aerobic process.

食品残渣処理装置3は、第1残渣粉砕手段としてのチョッパー31と、第2残渣粉砕手段としての摩砕機32と、残渣貯留槽33と、定量ポンプ装置34とを備えている。チョッパー31は投入される食品残渣(魚介類残渣)を所定荒さに破砕する装置である。摩砕機32は、チョッパー31により破砕処理された魚介類残渣が投入されるホッパー32aを有し、投入された魚介類残渣を、更に細かく例えば100μm程度のペースト状まで摩砕する(すり潰す)装置である。   The food residue treatment apparatus 3 includes a chopper 31 as a first residue grinding means, a grinder 32 as a second residue grinding means, a residue storage tank 33, and a metering pump device 34. The chopper 31 is a device that crushes the input food residue (seafood residue) to a predetermined roughness. The attritor 32 has a hopper 32a into which the seafood residue crushed by the chopper 31 is charged. It is.

残渣貯留槽33は、摩砕機32により摩砕された処理済残渣が投入され且つ処理済残渣を貯留しておく槽である。定量ポンプ装置34は、前記残渣貯留槽33内の処理済残渣を前記排水調整槽21に所定量供給するための装置である。   The residue storage tank 33 is a tank in which the processed residue ground by the grinder 32 is charged and the processed residue is stored. The metering pump device 34 is a device for supplying a predetermined amount of the treated residue in the residue storage tank 33 to the drainage adjustment tank 21.

処理水リサイクル施設4は、生物反応槽23で処理された排水を、汚泥から分離し、さらに高度処理して中水としてリサイクルできるようにする施設で、膜分離槽40、活性炭原水槽41、活性炭吸着塔42、紫外線殺菌装置43とを備えている。   The treated water recycling facility 4 is a facility that separates the wastewater treated in the biological reaction tank 23 from sludge and further recycles it as intermediate water through advanced treatment. The membrane separation tank 40, the activated carbon raw water tank 41, the activated carbon An adsorption tower 42 and an ultraviolet sterilizer 43 are provided.

膜分離槽40は、槽内に膜ユニット45が設けられている。膜ユニット45は、例えば平膜形状のエレメントが複数枚間隔を空けて配列された構成となっており、この平膜により汚泥と処理水を固液分離できるようになっている。膜ユニット45を構成する膜エレメント形状は平膜以外に中空糸状のものが、また膜材質も有機、無機いずれも使用可能である。膜ユニット45を生物反応槽23内に設置すること、および槽外設置の管状膜を使用することにより膜分離槽を不要とすることも可能である。   The membrane separation tank 40 is provided with a membrane unit 45 in the tank. The membrane unit 45 has, for example, a configuration in which a plurality of flat membrane-shaped elements are arranged at intervals, and sludge and treated water can be separated into solid and liquid by this flat membrane. The shape of the membrane element constituting the membrane unit 45 may be a hollow fiber shape other than a flat membrane, and the membrane material may be either organic or inorganic. It is also possible to eliminate the need for a membrane separation tank by installing the membrane unit 45 in the biological reaction tank 23 and using a tubular membrane installed outside the tank.

膜分離槽40と生物反応槽23とは、排水取出管50および排水戻管51によって互いに接続されている。なお、排水取出管50は生物反応槽23のポンプP2と接続され、膜分離槽40と生物反応槽23と間で汚泥が循環できるようになっている。膜ユニット45と活性炭原水槽41とは、膜濾過ポンプP3が介在された処理水取出管53によって接続されている。膜ユニット45には、エア供給管55を介して膜ブロアB2からエアが気泡となって供給され、汚泥が膜ユニット45に滞留するのを防止するようになっている。   The membrane separation tank 40 and the biological reaction tank 23 are connected to each other by a drainage extraction pipe 50 and a drainage return pipe 51. The drainage pipe 50 is connected to the pump P2 of the biological reaction tank 23 so that sludge can be circulated between the membrane separation tank 40 and the biological reaction tank 23. The membrane unit 45 and the activated carbon raw water tank 41 are connected by a treated water take-out pipe 53 with a membrane filtration pump P3 interposed therebetween. Air is supplied as bubbles from the membrane blower B <b> 2 to the membrane unit 45 through the air supply pipe 55, and sludge is prevented from staying in the membrane unit 45.

活性炭原水槽41には、活性炭原水ポンプP5が設けられ、活性炭原水槽41に貯留された処理水は、活性炭原水ポンプP5により処理水移送管56を介して活性炭吸着塔42に供給される。活性炭吸着塔42は、供給された処理水から臭気、色等の生物反応槽23で処理しきれなかった微量有機物成分(以下、微量有機物成分という。)を吸着除去する装置である。活性炭吸着塔42から出た処理水は、処理水移送管57を介して紫外線殺菌装置43に導入される前に、薬品タンク45内の薬液で塩素消毒されるようになっている。紫外線殺菌装置43は、塩素消毒された処理水がこの装置内を通流する際に、この処理水に紫外線を照射することにより、水中のバクテリア等の殺菌が行われ、処理水を清浄化する。   The activated carbon raw water tank 41 is provided with an activated carbon raw water pump P5, and the treated water stored in the activated carbon raw water tank 41 is supplied to the activated carbon adsorption tower 42 via the treated water transfer pipe 56 by the activated carbon raw water pump P5. The activated carbon adsorption tower 42 is an apparatus that adsorbs and removes trace organic components (hereinafter referred to as trace organic components) that could not be processed in the biological reaction tank 23 such as odor and color from the supplied treated water. The treated water discharged from the activated carbon adsorption tower 42 is sterilized with a chemical solution in the chemical tank 45 before being introduced into the ultraviolet sterilizer 43 through the treated water transfer pipe 57. When the sterilized treated water flows through the apparatus, the ultraviolet sterilizer 43 irradiates the treated water with ultraviolet rays, thereby sterilizing bacteria in the water and purifying the treated water. .

処理水監視装置6は、処理水移送管58を介して紫外線殺菌装置43と接続された水質監視槽60と、水質自動測定装置61とを備えている。水質監視槽60には、サンプリングポンプP6が設けられ、このサンプリングポンプP6は、サンプリング水用管62を介して、水質監視槽60内の処理水を水質自動測定装置61に供給する。なお、チラーユニット63により水質監視槽60内の処理水は、精度の高い水温制御が行われている。水質監視槽60は、冷水移送ポンプP7が介在された中水用管65により、処理水貯留槽7と接続されており、水質監視槽60内の処理水は処理水貯留槽7に供給されるようになっている。なお、処理水貯留槽7内の処理水は加工場内の使用に応じた量が供給される。   The treated water monitoring device 6 includes a water quality monitoring tank 60 connected to the ultraviolet sterilizer 43 through a treated water transfer pipe 58 and a water quality automatic measuring device 61. The water quality monitoring tank 60 is provided with a sampling pump P 6, and the sampling pump P 6 supplies treated water in the water quality monitoring tank 60 to the water quality automatic measuring device 61 via the sampling water pipe 62. The treated water in the water quality monitoring tank 60 is subjected to highly accurate water temperature control by the chiller unit 63. The water quality monitoring tank 60 is connected to the treated water storage tank 7 by a middle water pipe 65 with a cold water transfer pump P7 interposed therebetween, and the treated water in the water quality monitoring tank 60 is supplied to the treated water storage tank 7. It is like that. The treated water in the treated water storage tank 7 is supplied in an amount corresponding to the use in the processing plant.

水質自動測定装置61は、水質監視槽60内の処理水をサンプリングして、その性状を常時測定する。また、水質自動測定装置61には、前記活性炭原水ポンプP5、冷水移送ポンプP7および前記定量ポンプ装置34を制御する制御装置66が設けられている。即ち、この制御装置66は、測定されたサンプリング水の水質測定値と予め設定された水質基準値とを比較し、水質測定値が水質基準値に達したと判断した場合は、活性炭原水ポンプP5および冷水移送ポンプP7を停止し、処理水貯留槽7への処理水の投入を停止するようになっている。   The automatic water quality measuring device 61 samples the treated water in the water quality monitoring tank 60 and constantly measures its properties. The automatic water quality measuring device 61 is provided with a control device 66 that controls the activated carbon raw water pump P5, the cold water transfer pump P7, and the metering pump device 34. In other words, the control device 66 compares the measured water quality measurement value of the sampled water with a preset water quality reference value, and if it is determined that the water quality measurement value has reached the water quality reference value, the activated carbon raw water pump P5 And the cold water transfer pump P7 is stopped, and the input of the treated water to the treated water storage tank 7 is stopped.

また、制御装置66は、前記TOC測定器27からの情報に基づいて得られた測定TOC値と、設定TOC値とを比較し、測定TOC値が設定TOC値と略一致するか、あるいは設定TOC値に所定の範囲を持たせておいて、その範囲内に測定TOC値が入るように、定量ポンプ装置34を制御して、処理残渣の排水調整槽21への投入量を調整する。   Further, the control device 66 compares the measured TOC value obtained based on the information from the TOC measuring device 27 with the set TOC value, and the measured TOC value substantially matches the set TOC value or the set TOC. A predetermined range is given to the value, and the metering pump device 34 is controlled so that the measured TOC value falls within the range, thereby adjusting the amount of treatment residue input to the drainage adjustment tank 21.

処理水貯留槽7には上水が上水補給装置75から適宜補給できるように、上水用管70が接続されている。この上水用管70には電磁弁71が設けられており、通常は電磁弁71は閉塞されている。また、処理水貯留槽7の水は、逆洗ポンプP8の動作により処理水戻し管72を介して活性炭吸着塔42に供給され、逆洗に使用される。なお、電磁弁71および逆洗ポンプP8の動作は、前記制御装置66が行うようにできる。   The treated water storage tank 7 is connected with a water supply pipe 70 so that clean water can be appropriately supplied from a water supply device 75. The water pipe 70 is provided with an electromagnetic valve 71, and the electromagnetic valve 71 is normally closed. Further, the water in the treated water storage tank 7 is supplied to the activated carbon adsorption tower 42 through the treated water return pipe 72 by the operation of the backwash pump P8 and used for backwashing. The operation of the solenoid valve 71 and the backwash pump P8 can be performed by the control device 66.

次に、以上の構成からなる水産加工排水中水処理システムの処理工程について、図2を参照しながら説明する。   Next, processing steps of the fishery processing wastewater-in-water treatment system having the above-described configuration will be described with reference to FIG.

食品加工場が24時間操業でない場合
先ず、魚介類残渣投入工程について説明する。作業者は、食品加工場で発生した魚介類残渣をチョッパー31に投入する。魚介類残渣は、チョッパー31で粉砕された後に、摩砕機32によりペースト状の100μm程度以下まですり潰され、自動的に残渣貯留槽33に投入される。この魚介類残渣のチョッパー31への投入作業は、所定の時間(例えば、作業終了後の清掃時)に行う。
When the food processing plant is not operated for 24 hours First, the seafood residue charging process will be described. The worker inputs the seafood residue generated at the food processing plant into the chopper 31. After the seafood residue is pulverized by the chopper 31, it is crushed to about 100 μm or less by a grinder 32 and automatically put into the residue storage tank 33. The operation of putting the seafood residue into the chopper 31 is performed for a predetermined time (for example, at the time of cleaning after completion of the operation).

排水調整槽21には、食品加工場で発生した工場洗浄排水が適宜流入する。このとき、排水調整槽21に設置されたTOC測定器27は、流入有機物の量を測定し、制御装置66は、その情報に基づいて、食品加工場からの排水処理負荷に応じてすり潰した残渣の投入量を調整する。具体的には、TOC測定器27でTOCの値を測定し、その情報が制御装置66に送られ、制御装置66はその情報に基づいて得られた測定TOC値と設定TOC値とを比較する。制御装置66は、測定TOC値が設定TOC値に達している場合(測定値以上の場合)には、食品加工場からの排水処理負荷(流入負荷)が大きいと判断し、定量ポンプ装置34を制御して、残渣貯留槽33内の処理残渣の排水調整槽21への投入量を少なくしたり、停止したりする。   The factory cleaning wastewater generated at the food processing plant appropriately flows into the wastewater adjustment tank 21. At this time, the TOC measuring device 27 installed in the drainage adjustment tank 21 measures the amount of inflowing organic matter, and the control device 66 is based on the information, and the residue ground according to the wastewater treatment load from the food processing plant Adjust the input amount. Specifically, the TOC measuring device 27 measures the TOC value, and the information is sent to the control device 66. The control device 66 compares the measured TOC value obtained based on the information with the set TOC value. . When the measured TOC value reaches the set TOC value (when the measured TOC value is greater than or equal to the measured value), the control device 66 determines that the wastewater treatment load (inflow load) from the food processing plant is large, and the metering pump device 34 is By controlling, the amount of treatment residue in the residue storage tank 33 to the drainage adjustment tank 21 is reduced or stopped.

測定TOC値が設定TOC値に達していない場合(未満の場合)には、制御装置66は、食品加工場からの排水処理負荷が小さいと判断し、残渣貯留槽33内の処理残渣を定量ポンプ装置34により一定量排水調整槽21へ供給する。かかる場合には、測定TOC値が設定TOC値と略一致するまで処理残渣を供給したり、設定TOC値の範囲内で定量ポンプ装置34を制御したりする。これにより、排水調整槽21への流入負荷を均一にし、安定した生物処理を行うことができる。   When the measured TOC value does not reach the set TOC value (if less), the control device 66 determines that the wastewater treatment load from the food processing plant is small, and the treatment residue in the residue storage tank 33 is metered into the metering pump. A certain amount is supplied to the drainage adjustment tank 21 by the device 34. In such a case, the processing residue is supplied until the measured TOC value substantially matches the set TOC value, or the metering pump device 34 is controlled within the range of the set TOC value. Thereby, the inflow load to the drainage adjustment tank 21 can be made uniform, and stable biological treatment can be performed.

次に、生物処理工程および処理水浄化工程について説明する。排水調整槽21内の排水(残渣貯留槽33から供給された処理残渣を含む場合がある。)は、排水送液ポンプP1により生物反応槽23に供給される。生物反応槽23において活性汚泥による生物反応処理によって脱窒や脱リン処理が行われ、膜分離槽40へ導入された汚泥から処理水のみを濾過し、処理水を活性炭原水槽41に導入する。活性炭原水槽41内の処理水は、活性炭吸着塔42に供給され、この活性炭吸着塔42で微量有機物成分の効果的な吸着除去が行われる。微量有機物成分が除去された処理水は、塩素消毒された後に紫外線殺菌装置43で殺菌処理される。   Next, the biological treatment process and the treated water purification process will be described. Drainage in the drainage adjustment tank 21 (which may include processing residues supplied from the residue storage tank 33) is supplied to the biological reaction tank 23 by the wastewater feed pump P1. In the biological reaction tank 23, denitrification and dephosphorization processes are performed by biological reaction treatment with activated sludge. Only the treated water is filtered from the sludge introduced into the membrane separation tank 40, and the treated water is introduced into the activated carbon raw water tank 41. The treated water in the activated carbon raw water tank 41 is supplied to the activated carbon adsorption tower 42, and the activated carbon adsorption tower 42 effectively removes and removes trace organic components. The treated water from which the trace organic substance component has been removed is sterilized by the ultraviolet sterilizer 43 after being sterilized with chlorine.

次に、処理水監視工程について説明する。紫外線殺菌装置43で殺菌処理された処理水は、水質監視槽60に導入される。水質自動測定装置61は、水質監視槽60内の処理水のサンプリングを行う。制御装置66は、処理水の水質測定値が水質基準値に達していない(未満である)場合には、水質は良好であると判断し処理水貯留槽7への処理水の供給を継続させる。   Next, the treated water monitoring process will be described. The treated water sterilized by the ultraviolet sterilizer 43 is introduced into the water quality monitoring tank 60. The water quality automatic measuring device 61 samples the treated water in the water quality monitoring tank 60. The control device 66 determines that the water quality is good when the measured quality value of the treated water does not reach (below) the water quality reference value, and continues to supply the treated water to the treated water storage tank 7. .

また、制御装置66は、処理水の水質測定値が水質基準値に達した(以上である)と判断した場合には、処理水貯留槽7への処理水の投入を停止させる。処理水貯留槽7へ処理水が供給されないために、投入処理水貯留槽7内の水が所定量よりも少なくなった場合には、電磁弁71を開放して上水を所定量まで補給する。また、排水調整槽21へ処理残渣の投入が行われている場合に、制御装置66は、定量ポンプ装置34を制御して排水調整槽21への処理残渣の投入も停止する。   In addition, when the control device 66 determines that the measured water quality value has reached (or is more than) the water quality reference value, the control device 66 stops the input of the treated water into the treated water storage tank 7. Since treated water is not supplied to the treated water storage tank 7, when the amount of water in the input treated water storage tank 7 becomes less than a predetermined amount, the electromagnetic valve 71 is opened to replenish water to a predetermined amount. . In addition, when the processing residue is input to the drainage adjustment tank 21, the control device 66 controls the metering pump device 34 to stop the processing residue input to the drainage adjustment tank 21.

食品加工場が操業を停止し排水調整槽21への排水流入のない夜間は、測定TOC値が設定TOC値に達しないため、制御装置66は、定量ポンプ装置34を制御して昼間にすり潰しておいた残渣貯留槽33内の処理残渣を、排水調整槽21へ自動定量供給する。これにより、食品加工場が操業を停止していても、排水調整槽21への流入負荷を均一にし、安定した排水処理を行うことができる。   At night when the food processing plant stops operating and there is no inflow of drainage into the drainage adjustment tank 21, the measured TOC value does not reach the set TOC value. Therefore, the control device 66 controls the metering pump device 34 and grinds it during the daytime. The processing residue in the residue storage tank 33 is automatically supplied to the drainage adjustment tank 21 in a fixed amount. Thereby, even if the food processing plant has stopped the operation, the inflow load into the drainage adjustment tank 21 can be made uniform, and stable drainage treatment can be performed.

食品加工場が24時間操業の場合には、常時洗浄排水が排水調整槽21に流入することになる。制御装置66は、前記同様に定量ポンプ装置34を制御して排水調整槽21への処理残渣の投入量を調整することにより、排水調整槽21への流入負荷を均一にし、安定した排水処理を行うことができる。   When the food processing plant is operated for 24 hours, the cleaning wastewater always flows into the drainage adjustment tank 21. The control device 66 controls the metering pump device 34 in the same manner as described above to adjust the amount of treatment residue input to the drainage adjustment tank 21, thereby making the inflow load into the drainage adjustment tank 21 uniform and stable drainage treatment. It can be carried out.

食品残渣のすり潰しおよび機器洗浄には水の投入が必要となるが、ここで使用する水は本システムから得られる処理水貯留槽7内の処理水を中水として利用する。また、処理水貯留槽7内に処理水は、食品加工場内での床面等の1次洗浄水として利用するため、上水道および下水道使用料金の削減が可能となる。しかも、食品残渣を食品加工場内の汚水として洗浄排水と混合し処分するため、産廃処分費の削減が可能となる。   Water is required to grind food residues and clean the equipment, but the water used here uses treated water in the treated water storage tank 7 obtained from this system as intermediate water. Further, since the treated water in the treated water storage tank 7 is used as a primary cleaning water for a floor surface or the like in the food processing plant, it is possible to reduce water and sewerage usage charges. In addition, since the food residue is disposed as waste water in the food processing plant and mixed with the cleaning wastewater, the industrial waste disposal cost can be reduced.

なお、本発明はこれに限らず、前記実施の形態では、生物反応槽23で処理された処理水を、膜分離槽40で濾過する構成であったが、膜分離槽40に代えて沈殿槽を採用することも可能であり、排水リサイクルシステムは、前記実施の形態に限定されるものではない。しかも、加工される食品もタコ、イカナゴ等の魚介類に限定されるものではない。   Note that the present invention is not limited to this, and in the above-described embodiment, the treated water treated in the biological reaction tank 23 is filtered by the membrane separation tank 40. The waste water recycling system is not limited to the above embodiment. Moreover, the processed food is not limited to seafood such as octopus and squid.

本発明に係る一実施の形態の水産加工排水中水処理システムの概略構成を示図である。It is a figure showing a schematic structure of an aquatic processing drainage middle water treatment system of one embodiment concerning the present invention. 同水産加工排水中水処理システムのフローを示す図である。It is a figure which shows the flow of the same fisheries processing wastewater middle water treatment system.

符号の説明Explanation of symbols

1 水産加工排水中水処理システム(排水リサイクルシステム)
2 排水処理施設
3 食品残渣処理装置
4 処理水リサイクル施設
6 処理水監視装置
7 処理水貯留槽
31 チョッパー(第1残渣粉砕手段)
32 摩砕機(第2残渣粉砕手段)
33 残渣貯留槽
34 定量ポンプ装置
66 制御装置
1 Fishery processing wastewater wastewater treatment system (drainage recycling system)
2 Wastewater treatment facility 3 Food residue treatment device 4 Treated water recycling facility 6 Treated water monitoring device 7 Treated water storage tank 31 Chopper (first residue grinding means)
32 Mill (second residue grinding means)
33 Residue storage tank 34 Metering pump device 66 Control device

Claims (3)

食品加工場内の排水が流入する排水調整槽と該排水調整槽から導入される排水を生物反応処理する生物反応槽とを備える排水処理施設と、
食品残渣を粉砕して前記排水調整槽に供給する食品残渣処理装置と、
前記生物反応槽で処理された排水を、汚泥から分離しさらに高度処理して再利用可能にする処理水リサイクル施設と、
前記処理水リサイクル施設で再利用可能とされた処理水の水質を監視する処理水監視装置と、
前記処理水監視装置の処理水が供給される処理水貯留槽とを備え、
前記処理水監視装置は、前記処理水リサイクル施設で処理された処理水が導入される水質監視槽と、該水質監視槽内の処理水をサンプリングして、そのサンプリング水の水質を測定する水質自動測定装置と、測定されたサンプリング水の水質測定値と予め設定された水質基準値とを比較し、水質測定値が予め定められた水質基準値に達した際に、前記水質監視槽の処理水が処理水貯留槽に供給されるのを停止する制御装置とを備えたことを特徴とする排水リサイクルシステム。
A wastewater treatment facility comprising a wastewater adjustment tank into which wastewater in the food processing plant flows and a biological reaction tank that biologically treats the wastewater introduced from the wastewater adjustment tank;
A food residue treatment apparatus for crushing food residue and supplying the wastewater adjustment tank;
A treated water recycling facility that separates wastewater treated in the biological reaction tank from sludge and further treats it for reuse.
A treated water monitoring device for monitoring the quality of treated water reusable at the treated water recycling facility;
A treated water storage tank to which treated water of the treated water monitoring device is supplied,
The treated water monitoring device includes a water quality monitoring tank into which treated water treated at the treated water recycling facility is introduced, and samples the treated water in the water quality monitoring tank, and measures the quality of the sampled water. The measurement device compares the measured water quality value of the sampled water with a preset water quality reference value, and when the measured water quality value reaches a predetermined water quality reference value, the treated water in the water quality monitoring tank And a control device for stopping the supply of water to the treated water storage tank.
前記処理水貯留槽に上水を補給する上水補給装置が設けられ、前記制御装置は、処理水貯留槽内の水が利用されて処理水貯留槽内の水が所定量よりも少なくなった場合に、前記上水補給装置が上水を処理水貯留槽内に補給するように制御する請求項1に記載の排水リサイクルシステム。   A water supply device for replenishing the treated water storage tank is provided, and the control device uses water in the treated water storage tank so that the water in the treated water storage tank is less than a predetermined amount. The waste water recycling system according to claim 1, wherein the water supply device controls the water to be supplied into the treated water storage tank. 前記食品残渣処理装置は、食品残渣が投入される第1残渣粉砕手段と、該第1残渣粉砕手段によりもさらに細かく食品残渣を粉砕する第2残渣粉砕手段と、該第2残渣粉砕手段により粉砕された処理残渣を貯留する残渣貯留槽と、該残渣貯留槽から所定量の処理残渣を前記排水処理施設に供給する定量ポンプ装置とを備えている請求項1又は2に記載の排水リサイクルシステム。   The food residue treatment apparatus includes a first residue pulverizing unit into which a food residue is charged, a second residue pulverizing unit that further finely pulverizes the food residue by the first residue pulverizing unit, and a pulverization by the second residue pulverizing unit. The waste water recycling system of Claim 1 or 2 provided with the residue storage tank which stores the processed residue, and the metering pump apparatus which supplies the predetermined amount of processing residue from this residue storage tank to the said waste water treatment facility.
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US9611161B2 (en) 2013-12-05 2017-04-04 Mitsubishi Hitachi Power Systems, Ltd. Circulating water utilization system
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US10315930B2 (en) 2013-12-05 2019-06-11 Mitsubishi Hitachi Power Systems, Ltd. Method and system for remotely monitoring a group of circulating-water utilization systems
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