JP2012170878A - Wastewater sterilization system - Google Patents

Wastewater sterilization system Download PDF

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JP2012170878A
JP2012170878A JP2011034874A JP2011034874A JP2012170878A JP 2012170878 A JP2012170878 A JP 2012170878A JP 2011034874 A JP2011034874 A JP 2011034874A JP 2011034874 A JP2011034874 A JP 2011034874A JP 2012170878 A JP2012170878 A JP 2012170878A
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drainage
tank
water
line
sealed
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JP5794789B2 (en
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Hiroyuki Nakajima
啓之 中島
Koji Kashima
光司 鹿島
Kazutomo Isono
一智 磯野
Shigeo Honda
重夫 本田
Takashi Kachi
隆 加地
Naohiko Igawa
直彦 井川
Takayuki Todate
貴之 戸館
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Asahi Kogyosha Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a wastewater sterilization system that can reduce heating energy and the amount of water used and moreover prevent a leakage of a pollution source contained in air when carrying out evacuation.SOLUTION: Wastewater Wd in a drain tank 10 is evacuated and led into a sealed tank 13, and then the wastewater in the sealed tank 13 is maintained to high temperature and high pressure and sterilized. A water seal type vacuum pump 20 is connected to the sealed tank 13, and a storage tank 15 is connected to the sealed tank 13 through a drain line 14. A wastewater heating heat exchanger 24 exchanging heat between treated water Wt after sterilization treatment and the wastewater Wd in the drain tank 10 is connected to the drain line 14, and a treated water circulation line 21 supplying and circulating the treated water Wt in the storage tank 15 to the water seal type vacuum pump 20 is connected to the storage tank 15.

Description

本発明は、バイオハザード施設等から排出される排水を高温高圧で滅菌処理するための排水滅菌システムに関するものである。   The present invention relates to a wastewater sterilization system for sterilizing wastewater discharged from a biohazard facility or the like at high temperature and pressure.

遺伝子組み換え植物工場などバイオハザード施設や医療施設、動物などを扱う実験研究施設、食品・医療品施設から排出される排水中には、遺伝子組み換え植物片や遺伝子組み換え細胞、病原菌、動植物細胞等の各種汚染源が活性状態のまま含んでいる。これらの活性状態の汚染源を含んだ排水の外部への漏出を防止するためには、各種汚染源を滅菌処理して外部に排水する必要がある。   Biohazard facilities such as genetically modified plant factories, medical facilities, experimental research facilities that handle animals, etc., wastewater discharged from food and medical facilities, various types of genetically modified plant fragments, genetically modified cells, pathogenic bacteria, animal and plant cells, etc. Contained in an active state. In order to prevent the discharge of the wastewater containing these active contamination sources to the outside, it is necessary to sterilize the various pollution sources and drain them to the outside.

この排水の滅菌処理は、特許文献1に示されるように、培養液等の排水をフィルタを通して植物片や細胞を捕捉して排水し、その後植物片や細胞を捕捉したフィルタに高温・高圧の蒸気を供給して植物片や細胞を不活化して滅菌処理することが提案されている。しかし、フィルタで植物片や細胞を捕捉するためには、フィルタサイズの問題があり、また高温高圧の蒸気をフィルタに供給すると、滅菌後に蒸気がドレンとして大量に発生してしまう問題がある。   In this wastewater sterilization process, as shown in Patent Document 1, wastewater such as a culture solution is captured and drained by capturing plant fragments and cells through a filter, and then high-temperature and high-pressure steam is applied to the filter capturing the plant fragments and cells. Has been proposed to inactivate plant pieces and cells to sterilize them. However, in order to capture plant pieces and cells with a filter, there is a problem of the filter size, and when high-temperature and high-pressure steam is supplied to the filter, there is a problem that a large amount of steam is generated as drainage after sterilization.

特許文献2は、排水を密閉タンク内に導入し、密閉タンク内を高温高圧に保って排水を直接滅菌処理するもので、各種汚染された排水中に含まれる汚染源を排水毎処理するため、より安全な滅菌処理システムとすることが可能である。   Patent Document 2 introduces wastewater into a sealed tank, maintains the inside of the sealed tank at high temperature and high pressure, and directly sterilizes the wastewater. In order to treat each pollution source contained in various contaminated wastewater, It is possible to provide a safe sterilization system.

この滅菌処理システムを図2により説明する。   This sterilization system will be described with reference to FIG.

図2の滅菌処理システムは、植物工場などからの培養液などの排水を貯留する排水タンク40と、排水タンク40内の排水を真空吸引し、これを高温高圧で滅菌処理する密閉タンク41と、密閉タンク41内を真空引きする水封式真空ポンプ42とから主に構成される。   The sterilization system of FIG. 2 includes a drain tank 40 that stores wastewater such as a culture solution from a plant factory and the like, a sealed tank 41 that vacuums the drainage in the drain tank 40 and sterilizes it at high temperature and high pressure, A water-sealed vacuum pump 42 that evacuates the sealed tank 41 is mainly configured.

ここで排水タンク40は、ハザード管理区域内の植物工場内に設けられ、また密閉タンク41と水封式真空ポンプ42とは、植物工場と仕切られ、同じくハザード管理区域内の機械室に設けられている。   Here, the drainage tank 40 is provided in the plant factory in the hazard management area, and the sealed tank 41 and the water-sealed vacuum pump 42 are separated from the plant factory, and are also provided in the machine room in the hazard management area. ing.

この滅菌処理システムにおいては、排水タンク40内の排水を密閉タンク41に吸引する吸引ライン43の開閉弁44を閉じると共に密閉タンク41の排水ライン45の開閉弁46を閉じ、水封式真空ポンプ42を駆動して密閉タンク41内を真空引きする。この真空引きの際に、水道水等の給水を給水ライン47から水封式真空ポンプ42に供給し、水封式真空ポンプ42の真空シール、回転部の潤滑、摺動部の冷却を行い、密閉タンク41内の空気を吸引し、これを、水封式真空ポンプ42下流側の給水ライン47から給水と共に排水ライン45に排水する。   In this sterilization system, the open / close valve 44 of the suction line 43 that sucks the waste water in the drain tank 40 into the sealed tank 41 is closed and the open / close valve 46 of the drain line 45 of the sealed tank 41 is closed, and the water-sealed vacuum pump 42. To evacuate the sealed tank 41. During this evacuation, water such as tap water is supplied from the water supply line 47 to the water ring vacuum pump 42, the vacuum seal of the water ring vacuum pump 42, lubrication of the rotating part, cooling of the sliding part, The air in the sealed tank 41 is sucked and discharged from the water supply line 47 on the downstream side of the water-sealed vacuum pump 42 to the drainage line 45 together with the water supply.

密閉タンク41を真空引きした後、開閉弁44を開くことで、排水タンク40内の排水が密閉タンク41に吸引され、その後開閉弁44を閉じ、ヒータ48にて密閉タンク41内の排水を121℃(約0.2MPa)に加熱して高温高圧状態とし、これを約20分間保つことで、排水中の汚染源が滅菌処理される。滅菌処理後は、排水ライン45の開閉弁46を開くことで、密閉タンク41内の排水が排出される。この際、排水は高温のため、給水ライン47から分岐した冷水ライン49から冷水(水道水)を排水ライン45に供給し、排水の温度を、一般排水系に流してもよい耐熱温度以下(例えば60℃以下)に下げて排水を行う。   After the sealed tank 41 is evacuated, the on-off valve 44 is opened, whereby the waste water in the drain tank 40 is sucked into the sealed tank 41, and then the on-off valve 44 is closed, and the heater 48 discharges the waste water in the sealed tank 41 to 121. By heating to ℃ (about 0.2 MPa) to a high temperature and high pressure state and keeping this for about 20 minutes, the contamination source in the waste water is sterilized. After the sterilization treatment, the drainage in the sealed tank 41 is discharged by opening the on-off valve 46 of the drainage line 45. At this time, since the waste water is at a high temperature, cold water (tap water) is supplied from the cold water line 49 branched from the water supply line 47 to the drain line 45, and the temperature of the waste water is allowed to flow to the general drainage system or less (for example, Drain at a temperature below 60 ° C.

滅菌処理後の密閉タンク41内の排水は、自身の圧力で排出されるが、排出と共に密閉タンク41内が負圧となるため、空気導入弁50を開いて密閉タンク41内に空気を導入して排出する。滅菌処理後の排水を排水した後は、再度水封式真空ポンプ42で真空引きして上述のように滅菌処理を行う。   Waste water in the sealed tank 41 after sterilization is discharged at its own pressure, but since the inside of the sealed tank 41 becomes negative pressure with the discharge, the air introduction valve 50 is opened to introduce air into the sealed tank 41. To discharge. After draining the drained water after sterilization, the water-sealed vacuum pump 42 is evacuated again to perform sterilization as described above.

この排水滅菌システムにおいては、排水を直接高温高圧にするため、フィルタで除去できない、フィルタ孔径以下の汚染源も滅菌処理することができる。   In this wastewater sterilization system, since the wastewater is directly heated to a high temperature and high pressure, it is possible to sterilize a contamination source that cannot be removed by a filter and is smaller than the filter pore diameter.

特開2010−166830号公報JP 2010-166830 A 特開2008−200564号公報JP 2008-200244 A

しかしながら、密閉タンク41内をヒータ48で高温高圧にするため、その加熱のためのエネルギーが大きい。また真空引きの際には、60Lの密閉タンク41を真空引きし、水封式真空ポンプ42を10分間駆動するとした場合、その間に30Lの水道水を給水する必要がある。また、密閉タンク41内に導入する空気は、機械室内の空気であるが、機械室内の空気に汚染源が含まれている場合には、真空引きの際に、汚染源を含んだ空気が給水と共に排水ライン45に漏出してしまう問題がある。さらに滅菌処理後に密閉タンク41で121℃に加熱された排水を、一般排水系に流すためには、一般排水系の耐熱温度以下にする必要があり、10分かけて、例えば60℃以下に排水するとした場合には、冷水ライン49から、400Lもの多量の水道水を供給しなければならない問題がある。   However, since the inside of the sealed tank 41 is heated and heated by the heater 48, the energy for heating is large. Further, when evacuating, if the 60 L sealed tank 41 is evacuated and the water ring vacuum pump 42 is driven for 10 minutes, 30 L of tap water needs to be supplied during that time. The air introduced into the sealed tank 41 is air in the machine room, but when the air in the machine room contains a pollution source, the air containing the pollution source is drained together with the water supply during evacuation. There is a problem of leakage into the line 45. Further, in order to allow the waste water heated to 121 ° C. in the sealed tank 41 after sterilization to flow into the general drainage system, it is necessary to make the temperature lower than the heat resistance temperature of the general drainage system. In that case, there is a problem that a large amount of 400 L of tap water must be supplied from the cold water line 49.

そこで、本発明の目的は、上記課題を解決し、加熱エネルギーと使用水量を削減でき、しかも真空排気の際の空気中に含まれる汚染源の漏出を防止できる排水滅菌システムを提供することにある。   Accordingly, an object of the present invention is to provide a drainage sterilization system that can solve the above problems, reduce the heating energy and the amount of water used, and can prevent leakage of contamination sources contained in the air during vacuum exhaust.

上記目的を達成するために請求項1の発明は、排水タンク内の排水を、真空引きして密閉タンク内に導入した後、その密閉タンク内の排水を高温高圧に保って排水を滅菌する排水滅菌システムにおいて、前記密閉タンクに水封式真空ポンプを接続し、前記密閉タンクに、排水ラインを介して滅菌処理後の処理水を貯留する貯留タンクを接続し、前記排水ラインに滅菌処理後の処理水と前記排水タンク内の排水と熱交換する排水加熱用熱交換器を接続し、前記貯留タンクに、その貯留タンク内の前記処理水を、前記水封式真空ポンプに供給循環する処理水循環ラインを接続したことを特徴とする排水滅菌システムである。   In order to achieve the above object, the first aspect of the present invention provides a wastewater which is sterilized by keeping the wastewater in the sealed tank at a high temperature and high pressure after the wastewater in the drainage tank is evacuated and introduced into the sealed tank. In the sterilization system, a water-sealed vacuum pump is connected to the sealed tank, a storage tank for storing treated water after sterilization treatment is connected to the sealed tank via a drainage line, and the sterilization treatment is performed on the drainage line. Waste water heating heat exchanger that exchanges heat between the treated water and the waste water in the waste water tank, and the treated water circulation that supplies and circulates the treated water in the storage tank to the water-sealed vacuum pump. A drainage sterilization system characterized by connecting lines.

請求項2の発明は、前記貯留タンクは密閉型に形成され、前記密閉タンクに対して5〜10倍の容積に形成される請求項1記載の排水滅菌システムである。   The invention according to claim 2 is the drainage sterilization system according to claim 1, wherein the storage tank is formed in a closed type and has a volume 5 to 10 times that of the closed tank.

請求項3の発明は、前記貯留タンクには、上端が貯留タンク内の上部に開口すると共に貯留タンクの下部から外部に延びた放水ラインが接続され、その放水ラインの上端に形成される気相部と前記密閉タンクとが、空気給排ラインで接続される請求項2記載の排水滅菌システムである。   According to a third aspect of the present invention, the storage tank is connected to a water discharge line having an upper end opened at an upper portion in the storage tank and extended from a lower portion of the storage tank to the outside, and a gas phase formed at the upper end of the water discharge line. The drainage sterilization system according to claim 2, wherein the unit and the closed tank are connected by an air supply / discharge line.

請求項4の発明は、前記排水タンクは、前記密閉タンクに対して3〜6倍の容積に形成され、その排水タンクに、前記排水加熱用熱交換器に排水を供給循環する排水加熱用循環ラインが接続される請求項1〜3のいずれかに記載の排水滅菌システムである。   According to a fourth aspect of the present invention, the drainage tank is formed in a volume 3 to 6 times that of the sealed tank, and the drainage tank is provided with a drainage heating circulation for supplying and draining the drainage to the drainage heating heat exchanger. It is a wastewater sterilization system in any one of Claims 1-3 to which a line is connected.

請求項5の発明は、前記貯留タンクから前記水封式真空ポンプに至る処理水循環ラインと前記排水加熱用熱交換器の上流側の排水ライン間に、前記貯留タンク内の処理水を、前記排水ラインを介して前記排水加熱用熱交換器に供給循環する熱回収ラインが接続される請求項1〜4のいずれかに記載の排水滅菌システムである。   According to a fifth aspect of the present invention, the treated water in the storage tank is disposed between the treated tank circulation line extending from the storage tank to the water-sealed vacuum pump and the drainage line upstream of the wastewater heating heat exchanger. It is a wastewater sterilization system in any one of Claims 1-4 to which the heat recovery line which supplies and circulates to the said heat exchanger for wastewater heating through a line is connected.

請求項6の発明は、前記排水加熱用熱交換器の下流側の排水ラインには、培養液などの供給液を加温する加温用熱交換器が接続される請求項1〜5のいずれかに記載の排水滅菌システムである。   The invention according to claim 6 is the heating apparatus according to any one of claims 1 to 5, wherein a heating heat exchanger for heating a supply solution such as a culture solution is connected to a drainage line downstream of the wastewater heating heat exchanger. It is a wastewater sterilization system of crab.

本発明は、密閉タンク内を水封式真空ポンプで真空引きし、その密閉タンク内に排水を導入して高温高圧にして滅菌処理する際に、貯留タンクの処理水を水封式真空ポンプに供給循環することで、水道水等の給水量を削減できる。また密閉タンクから滅菌処理後の処理水を貯留タンクに排水する際に、処理前の排水タンク内の排水と熱交換してその熱を回収することで加熱エネルギーを削減できると共に、処理水を冷却するための水道水等の給水量を削減することができるという優れた効果を発揮する。   The present invention evacuates the inside of a sealed tank with a water-sealed vacuum pump and introduces waste water into the sealed tank to sterilize it at a high temperature and high pressure. By supplying and circulating, water supply such as tap water can be reduced. In addition, when draining the treated water after sterilization from the sealed tank to the storage tank, the heat energy can be reduced by exchanging heat with the wastewater in the wastewater tank before treatment to recover the heat and cooling the treated water. The outstanding effect that the amount of water supply, such as tap water for performing, can be reduced is exhibited.

本発明の一実施の形態を示す図である。It is a figure which shows one embodiment of this invention. 従来例を示す図である。It is a figure which shows a prior art example.

以下、本発明の好適な一実施の形態を添付図面に基づいて詳述する。   A preferred embodiment of the present invention will be described below in detail with reference to the accompanying drawings.

図1は、本発明の排水滅菌システムの一実施の形態を示す図である。   FIG. 1 is a diagram showing an embodiment of a wastewater sterilization system of the present invention.

図1において、10は、遺伝子組み換え植物工場や医療施設などハザード管理区域に設けられ、遺伝子組み換え植物工場などで使用された使用済の培養液、医療施設などで蒸気殺菌後のドレン水などの排水(被滅菌水)Wdを貯留する排水タンクであり、図では示していないが外周に断熱材が貼り付けられ高断熱性の排水タンク10とされる。排水タンク10には、ライン11から排水Wdが、連続的に或いは間欠的に供給され、これを貯留するようになっている。この排水Wdは、排水タンク10に貯留する際に、排水中に含まれる粒径100μm以上の大きな汚染源は、予めフィルタで取り除かれている。   In FIG. 1, reference numeral 10 is provided in a hazard management area such as a genetically modified plant factory or medical facility, and used culture fluid used in the genetically modified plant factory or the like, drainage water such as drain water after steam sterilization in a medical facility or the like. (Water to be sterilized) A drainage tank for storing Wd. Although not shown in the drawing, a heat insulating material is attached to the outer periphery to form a highly heat-insulating drainage tank 10. The drainage tank 10 is supplied with drainage Wd continuously or intermittently from the line 11 and stores it. When the drainage Wd is stored in the drainage tank 10, a large contamination source having a particle size of 100 μm or more contained in the drainage is removed in advance by a filter.

排水タンク10には、吸引ライン12が接続される。吸引ライン12の吸込口は、排水タンク10内の排水Wd内に位置するよう設けられ、排水タンク10が設けられた工場内などから、図示の二点線で囲ったハザード管理区域である機械室MRに延出されて密閉タンク13に接続される。なお排水タンク10は、植物工場などのハザード管理区域に設ける他に機械室MRに設けられてもよい。   A suction line 12 is connected to the drain tank 10. The suction port of the suction line 12 is provided so as to be located in the drainage Wd in the drainage tank 10, and from the inside of the factory where the drainage tank 10 is provided, the machine room MR which is a hazard management area surrounded by the two-dotted line shown in the figure And connected to the sealed tank 13. The drain tank 10 may be provided in the machine room MR in addition to being provided in a hazard management area such as a plant factory.

密閉タンク13は、排水ライン14を介して貯留タンク15に接続される。貯留タンク15は、排水タンク10と同様に断熱材が貼り付けられ高断熱性の貯留タンク15とされる。   The sealed tank 13 is connected to the storage tank 15 via the drain line 14. The storage tank 15 is a highly heat-insulating storage tank 15 to which a heat insulating material is attached in the same manner as the drainage tank 10.

吸引ライン12には入口側開閉弁16が接続され、排水ライン14には出口側開閉弁17が接続される。排水タンク10は、密閉タンク13に対して3〜6倍の容積に形成され、貯留タンク15は、密閉タンクに対して5〜10倍の容積に形成される。   An inlet side opening / closing valve 16 is connected to the suction line 12, and an outlet side opening / closing valve 17 is connected to the drainage line 14. The drain tank 10 is formed in a volume 3 to 6 times that of the sealed tank 13, and the storage tank 15 is formed in a volume 5 to 10 times that of the sealed tank 13.

密閉タンク13には、導入した排水Wdを121℃以上に加熱するヒータ18が設けられる。また密閉タンク13には密閉タンク13内を真空引きする水封式真空ポンプ20が吸入ライン19を介して接続される。水封式真空ポンプ20は、円型ケーシング20c内にインペラ20iを偏芯させて設けて構成される。   The sealed tank 13 is provided with a heater 18 for heating the introduced waste water Wd to 121 ° C. or higher. A water-sealed vacuum pump 20 that evacuates the sealed tank 13 is connected to the sealed tank 13 via a suction line 19. The water-sealed vacuum pump 20 is configured by providing an impeller 20i eccentric in a circular casing 20c.

この水封式真空ポンプ20には、貯留タンク15内の滅菌後の処理水Wtを供給循環する処理水循環ライン21が接続される。処理水循環ライン21は、貯留タンク15と水封式真空ポンプ20を結ぶ上流側循環ライン21aと水封式真空ポンプ20と排水ライン14に接続された下流側循環ライン21bとからなり、上流側循環ライン21aに処理水循環ポンプ22が接続され、下流側循環ライン21bにポンプ用開閉弁23が接続される。   The water-sealed vacuum pump 20 is connected to a treated water circulation line 21 for supplying and circulating treated water Wt after sterilization in the storage tank 15. The treated water circulation line 21 includes an upstream circulation line 21 a connecting the storage tank 15 and the water ring vacuum pump 20, and a downstream circulation line 21 b connected to the water ring vacuum pump 20 and the drain line 14. A treated water circulation pump 22 is connected to the line 21a, and a pump opening / closing valve 23 is connected to the downstream circulation line 21b.

出口側開閉弁17の下流側の排水ライン14には、排水タンク10内の排水Wdを加熱する排水加熱用熱交換器24が接続されると共に培養液を加温する加温用熱交換器25が接続される。   A drainage heating heat exchanger 24 for heating the drainage Wd in the drainage tank 10 is connected to the drainage line 14 on the downstream side of the outlet side opening / closing valve 17 and a heating heat exchanger 25 for heating the culture solution. Is connected.

排水タンク10と排水加熱用熱交換器24とは、排水タンク10内の排水Wdを、排水加熱用熱交換器24に供給循環する排水循環ポンプ26を有する排水循環ライン27が接続される。また培養液タンク28と加温用熱交換器25とは、培養液タンク28内の培養液を加温用熱交換器25に供給循環する培養液循環ポンプ29を有する培養液循環ライン30が接続される。   A drainage circulation line 27 having a drainage circulation pump 26 that supplies and circulates the wastewater Wd in the drainage tank 10 to the wastewater heating heat exchanger 24 is connected to the drainage tank 10 and the wastewater heating heat exchanger 24. The culture medium tank 28 and the heating heat exchanger 25 are connected to a culture medium circulation line 30 having a culture medium circulation pump 29 for supplying and circulating the culture medium in the culture medium tank 28 to the heating heat exchanger 25. Is done.

貯留タンク15は、密閉型に形成され、排水ライン14の下端14aは、貯留タンク15内の処理水Wt内に浸るように設けられる。貯留タンク15には、上端31aが貯留タンク15内の上部に開口すると共に貯留タンク15の下部から延出されると共に機械室MRから外部に延出された放水ライン31が接続される。放水ライン31の上端31aの上部に形成される気相部15gと密閉タンク13とが、空気給排ライン32で接続され、その空気給排ライン32に給排用開閉弁33が接続される。また、放水ライン31には、気相部15内の空気が、放水ライン31を通して排出されないようにU字状に形成された水封部31sが形成される。   The storage tank 15 is formed in a sealed type, and the lower end 14 a of the drain line 14 is provided so as to be immersed in the treated water Wt in the storage tank 15. The storage tank 15 is connected to a water discharge line 31 that has an upper end 31a that opens to an upper portion in the storage tank 15 and that extends from the lower portion of the storage tank 15 and extends from the machine room MR to the outside. A gas phase portion 15 g formed at the upper part of the upper end 31 a of the water discharge line 31 and the closed tank 13 are connected by an air supply / discharge line 32, and a supply / discharge on / off valve 33 is connected to the air supply / discharge line 32. Further, the water discharge line 31 is formed with a water sealing portion 31 s formed in a U shape so that air in the gas phase portion 15 is not discharged through the water discharge line 31.

加温用熱交換器25の下流側排水ライン14には、貯留タンク15内に水道水等を給水する給水ライン34が接続され、その給水ライン34に給水弁35が接続される。   A water supply line 34 for supplying tap water or the like into the storage tank 15 is connected to the downstream drain line 14 of the heating heat exchanger 25, and a water supply valve 35 is connected to the water supply line 34.

貯留タンク15には、処理水Wtの温度を検出する温度計36が設けられる。処理水循環ライン21の上流側循環ライン21aには、その上流側循環ライン21aから分岐し、処理水を排水加熱用熱交換器24に供給循環する熱回収ライン37が接続され、その熱回収ライン37に熱回収用開閉弁38が接続される。この熱回収用開閉弁38は、温度計36の検出値で開閉制御されると共に、温度計36の検出値で排水循環ポンプ26と培養液循環ポンプ29とが駆動制御されるようになっている。   The storage tank 15 is provided with a thermometer 36 that detects the temperature of the treated water Wt. A heat recovery line 37 that branches from the upstream circulation line 21 a and supplies and circulates the treated water to the waste water heating heat exchanger 24 is connected to the upstream circulation line 21 a of the treated water circulation line 21. A heat recovery on-off valve 38 is connected to the stub. The heat recovery on-off valve 38 is controlled to open and close by the detection value of the thermometer 36, and the drain circulation pump 26 and the culture medium circulation pump 29 are driven and controlled by the detection value of the thermometer 36. .

次に、排水Wdの滅菌処理を説明する。   Next, the sterilization process of the waste water Wd will be described.

先ず、入口側開閉弁16と出口側開閉弁17が閉じられた状態で、密閉タンク13内が、水封式真空ポンプ20により真空引きされる。   First, the closed tank 13 is evacuated by the water ring vacuum pump 20 with the inlet side opening / closing valve 16 and the outlet side opening / closing valve 17 closed.

水封式真空ポンプ20による真空引きは、円型ケーシング20c内のインペラ20iが回転駆動されることで、貯留タンク15内の処理水Wtが上流側循環ライン21aを介して円型ケーシング20c内に導入され、その処理水がインペラ20iで回転され、円型ケーシング20c内で遠心力により円環状となり、インペラ20iの円型ケーシング20cの側壁に形成した吸気口から吸入ライン19を介して密閉タンク13内の空気が吸引され、排気口から吸引した空気を処理水Wtと共に下流側循環ライン21bを介して貯留タンク15に排出される。貯留タンク15内では処理水Wtと空気が分離され、空気が気相部15g内に溜まる。   The vacuuming by the water-sealed vacuum pump 20 is performed by rotating the impeller 20i in the circular casing 20c so that the treated water Wt in the storage tank 15 enters the circular casing 20c via the upstream circulation line 21a. Then, the treated water is rotated by the impeller 20i, becomes annular due to centrifugal force in the circular casing 20c, and enters the sealed tank 13 via the suction line 19 from the intake port formed in the side wall of the circular casing 20c of the impeller 20i. The air inside is sucked and the air sucked from the exhaust port is discharged together with the treated water Wt to the storage tank 15 via the downstream circulation line 21b. In the storage tank 15, the treated water Wt and air are separated, and the air is stored in the gas phase portion 15g.

この真空引きは、10分程度行い、処理水量は、30Lとなるが、貯留タンク15内の処理水Wtを循環して用いるため、水道水等を多量に消費することを防止できる。   This evacuation is performed for about 10 minutes, and the amount of treated water is 30 L. However, since the treated water Wt in the storage tank 15 is circulated and used, it is possible to prevent consumption of tap water and the like in large quantities.

密閉タンク13内を真空引きした後は、水封式真空ポンプ20と処理水循環ポンプ22を停止し、入口側開閉弁16を開く。これにより排水タンク10内の排水Wdが吸引ライン12を介して密閉タンク13内に導入される。   After evacuating the sealed tank 13, the water-sealed vacuum pump 20 and the treated water circulation pump 22 are stopped, and the inlet side opening / closing valve 16 is opened. As a result, the waste water Wd in the drain tank 10 is introduced into the sealed tank 13 through the suction line 12.

密閉タンク13内に排水Wdを導入した後、再度入口側開閉弁16を閉じ、ヒータ18にて排水Wdを121℃に加熱する。加熱により密閉タンク13は、飽和水蒸気圧(約0.2MPa)まで上昇し、この高温高圧状態を20分程度維持することで、排水中の植物片や細胞などの汚染源が不活化されて滅菌される。   After introducing the waste water Wd into the sealed tank 13, the inlet side on-off valve 16 is closed again, and the waste water Wd is heated to 121 ° C. by the heater 18. By heating, the closed tank 13 rises to a saturated water vapor pressure (about 0.2 MPa), and by maintaining this high temperature and high pressure state for about 20 minutes, contaminant sources such as plant fragments and cells in the wastewater are inactivated and sterilized. The

滅菌後、出口側開閉弁17を開くことで、密閉タンク13内の圧力により、排水ライン14を介して貯留タンク15に排水する。この際、排水循環ポンプ26を駆動し、排水循環ライン27にて排水タンク10内の排水Wdを排水加熱用熱交換器24に流すことで、排水ライン14を流れる滅菌処理後の処理水Wtと熱交換し、その熱が高断熱性の排水タンク10内に回収される。   After the sterilization, the outlet side opening / closing valve 17 is opened, and the water is discharged to the storage tank 15 through the drain line 14 by the pressure in the sealed tank 13. At this time, the drainage circulation pump 26 is driven, and the wastewater Wd in the drainage tank 10 is caused to flow through the drainage circulation line 27 to the wastewater heating heat exchanger 24, whereby the sterilized treated water Wt flowing through the drainage line 14 and The heat is exchanged, and the heat is recovered in the highly heat-insulating drain tank 10.

密閉タンク13内の滅菌処理後の処理水Wtが貯留タンク15内に全て排出された後は、出口側開閉弁17を閉じ、密閉タンク13内を、水封式真空ポンプ20により再度真空引きする。   After all the sterilized treated water Wt in the sealed tank 13 has been discharged into the storage tank 15, the outlet side open / close valve 17 is closed and the sealed tank 13 is evacuated again by the water-sealed vacuum pump 20. .

この際、貯留タンク15の処理水Wtの温度が温度計36にて検出され、貯留タンク15内の処理水Wtの温度が高い場合には、水封式真空ポンプ20で真空引きする前に、或いは真空引きと同時に処理水循環ポンプ22を駆動し、熱回収用開閉弁38を開として、上流側循環ライン21aから熱回収ライン37を介して排水ライン14に処理水Wtを流すことで、排水加熱用熱交換器24で、排水タンク10の排水Wdを加熱して、さらに熱回収することができる。   At this time, when the temperature of the treated water Wt in the storage tank 15 is detected by the thermometer 36 and the temperature of the treated water Wt in the storage tank 15 is high, before evacuating with the water-sealed vacuum pump 20, Alternatively, the waste water heating is performed by driving the treated water circulation pump 22 simultaneously with evacuation, opening the heat recovery on-off valve 38, and flowing the treated water Wt from the upstream circulation line 21a to the drain line 14 via the heat recovery line 37. The waste heat Wd in the drain tank 10 can be heated by the heat exchanger 24 for heat recovery.

このように密閉タンク13から排出される高温の処理水の熱を、処理前の排水に熱回収することで、密閉タンク13に導入される排水温度を常温より十分高く(60〜80℃程度)できるため、ヒータ18での加熱エネルギーを削減することができる。   Thus, by recovering the heat of the high-temperature treated water discharged from the sealed tank 13 to the waste water before treatment, the temperature of the drained water introduced into the sealed tank 13 is sufficiently higher than room temperature (about 60 to 80 ° C.). Therefore, the heating energy in the heater 18 can be reduced.

また上述したように密閉タンク13を真空引きした後、密閉タンク13内に導入された排水Wdをヒータ18で高温高圧で処理している間に、培養液循環ポンプ29を駆動し、培養液循環ライン30にて培養液を加温用熱交換器25に供給循環することで、培養液を加温することで、さらなる熱回収が行える。   Further, as described above, after the sealed tank 13 is evacuated, while the waste water Wd introduced into the sealed tank 13 is treated at high temperature and high pressure by the heater 18, the culture solution circulation pump 29 is driven to circulate the culture solution. By supplying and circulating the culture solution to the heating heat exchanger 25 in the line 30, further heat recovery can be performed by heating the culture solution.

この熱回収において排水タンク10の容積は、密閉タンク13の容積に対して3〜6倍の容積に形成されており、密閉タンク13内で121℃に加熱された処理水Wtの熱を、排水タンク10内の排水Wdで回収しても、排水Wdの温度は、60〜80℃程度であり過度に上昇することはない。   In this heat recovery, the volume of the drainage tank 10 is 3 to 6 times the volume of the closed tank 13, and the heat of the treated water Wt heated to 121 ° C. in the closed tank 13 is drained. Even if the waste water Wd in the tank 10 is recovered, the temperature of the waste water Wd is about 60 to 80 ° C. and does not rise excessively.

また、貯留タンク15では、水封式真空ポンプ20で真空引き時に密閉タンク13内の空気が、気相部15gに溜まるが、貯留タンク15は密閉タンク13の容積に対して5〜10倍にされ、気相部15gの容積も密閉タンク13の容積の約2倍程度あるため、真空引きが支障なく行える。   In the storage tank 15, the air in the sealed tank 13 is accumulated in the gas phase portion 15 g when the water-sealed vacuum pump 20 is evacuated, but the storage tank 15 is 5 to 10 times the volume of the sealed tank 13. Since the volume of the gas phase portion 15g is about twice the volume of the sealed tank 13, evacuation can be performed without any trouble.

高温高圧で滅菌処理後の処理水Wtは、密閉タンク13の圧力で、貯留タンク15に排出されるが、密閉タンク13内の圧力が排出とともに下がり、貯留タンク15の気相部15gの圧力と同じとなった後は、空気給排ライン32の給排用開閉弁33を開くことで、密閉タンク13内の処理水Wtは、重力で貯留タンク15に流下し、同時に気相部15gの空気が空気給排ライン32を介して密閉タンク13内に導入される。密閉タンク13と貯留タンク15とは共に密閉型であり、空気は、密閉タンク13と貯留タンク15を移動するだけであり、機械室MRから取り込んだ空気中に汚染源が含まれていても外部に漏出することはない。   The treated water Wt after sterilization at high temperature and pressure is discharged to the storage tank 15 by the pressure of the sealed tank 13, but the pressure in the sealed tank 13 decreases with the discharge, and the pressure of the gas phase portion 15g of the storage tank 15 After the same, by opening the supply / discharge on / off valve 33 of the air supply / discharge line 32, the treated water Wt in the sealed tank 13 flows down to the storage tank 15 by gravity, and at the same time, air in the gas phase section 15g. Is introduced into the sealed tank 13 through the air supply / discharge line 32. Both the sealed tank 13 and the storage tank 15 are sealed, and the air only moves between the sealed tank 13 and the storage tank 15, and even if a contamination source is included in the air taken in from the machine room MR, the air remains outside. There is no leakage.

貯留タンク15内の処理水Wtの液面が、放水ライン31の上端31aより上昇した際には、処理水Wtは、機械室MRから放水ライン31より外部に排出される。   When the liquid level of the treated water Wt in the storage tank 15 rises from the upper end 31a of the water discharge line 31, the treated water Wt is discharged from the machine room MR to the outside through the water discharge line 31.

なお、滅菌処理前は、貯留タンク15内は空であるため、給水ライン34から水道水等を給水しておく。また貯留タンク15から放水ライン31を介して処理水Wtを外部に排出する際に、その処理水Wtの温度が、過度に高い場合には、温度計36でこれを検出して貯留タンク15に適宜給水を行う。   Before the sterilization process, since the storage tank 15 is empty, tap water or the like is supplied from the water supply line 34. When the treated water Wt is discharged from the storage tank 15 through the water discharge line 31 to the outside, if the temperature of the treated water Wt is excessively high, the temperature is detected by the thermometer 36 and stored in the storage tank 15. Supply water appropriately.

10 排水タンク
13 密閉タンク
14 排水ライン
15 貯留タンク
20 水封式真空ポンプ
21 処理水循環ライン
24 排水加熱用熱交換器
DESCRIPTION OF SYMBOLS 10 Drain tank 13 Sealed tank 14 Drain line 15 Storage tank 20 Water-sealed vacuum pump 21 Treated water circulation line 24 Heat exchanger for drainage heating

Claims (6)

排水タンク内の排水を、真空引きして密閉タンク内に導入した後、その密閉タンク内の排水を高温高圧に保って排水を滅菌する排水滅菌システムにおいて、前記密閉タンクに水封式真空ポンプを接続し、前記密閉タンクに、排水ラインを介して滅菌処理後の処理水を貯留する貯留タンクを接続し、前記排水ラインに滅菌処理後の処理水と前記排水タンク内の排水と熱交換する排水加熱用熱交換器を接続し、前記貯留タンクに、その貯留タンク内の前記処理水を、前記水封式真空ポンプに供給循環する処理水循環ラインを接続したことを特徴とする排水滅菌システム。   In a drainage sterilization system that evacuates the drainage water in the drainage tank and introduces it into the sealed tank, and then sterilizes the drainage by keeping the drainage in the sealed tank at high temperature and high pressure, a water-sealed vacuum pump is installed in the sealed tank. A drainage tank connected to a storage tank for storing treated water after sterilization treatment through the drainage line, and exchanging heat between the treated water after sterilization treatment and the wastewater in the drainage tank. A drainage sterilization system, wherein a heat exchanger for heating is connected, and a treated water circulation line for supplying and circulating the treated water in the storage tank to the water-sealed vacuum pump is connected to the storage tank. 前記貯留タンクは密閉型に形成され、前記密閉タンクに対して5〜10倍の容積に形成される請求項1記載の排水滅菌システム。   The drainage sterilization system according to claim 1, wherein the storage tank is formed in a closed type and has a volume 5 to 10 times that of the closed tank. 前記貯留タンクには、上端が貯留タンク内の上部に開口すると共に貯留タンクの下部から外部に延びた放水ラインが接続され、その放水ラインの上端に形成される気相部と前記密閉タンクとが、空気給排ラインで接続される請求項2記載の排水滅菌システム。   The storage tank is connected to a water discharge line having an upper end opened at an upper portion in the storage tank and extended from the lower portion of the storage tank to the outside, and a gas phase portion formed at the upper end of the water discharge line and the sealed tank The drainage sterilization system according to claim 2 connected by an air supply / discharge line. 前記排水タンクは、前記密閉タンクに対して3〜6倍の容積に形成され、その排水タンクに、前記排水加熱用熱交換器に排水を供給循環する排水加熱用循環ラインが接続される請求項1〜3のいずれかに記載の排水滅菌システム。   The drainage tank is formed to have a volume 3 to 6 times that of the sealed tank, and a drainage heating circulation line for supplying and circulating drainage to the drainage heating heat exchanger is connected to the drainage tank. The wastewater sterilization system in any one of 1-3. 前記貯留タンクから前記水封式真空ポンプに至る処理水循環ラインと前記排水加熱用熱交換器の上流側の排水ライン間に、前記貯留タンク内の処理水を、前記排水ラインを介して前記排水加熱用熱交換器に供給循環する熱回収ラインが接続される請求項1〜4のいずれかに記載の排水滅菌システム。   Between the treated water circulation line extending from the storage tank to the water-sealed vacuum pump and the drainage line upstream of the wastewater heating heat exchanger, the treated water in the storage tank is heated via the drainage line. The drainage sterilization system according to any one of claims 1 to 4, wherein a heat recovery line that is supplied and circulated to the heat exchanger is connected. 前記排水加熱用熱交換器の下流側の排水ラインには、培養液などの供給液を加温する加温用熱交換器が接続される請求項1〜5のいずれかに記載の排水滅菌システム。   The drainage sterilization system according to any one of claims 1 to 5, wherein a heating heat exchanger for heating a supply liquid such as a culture solution is connected to a drainage line on the downstream side of the wastewater heating heat exchanger. .
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CN114517846A (en) * 2020-11-20 2022-05-20 中国石油化工股份有限公司 Water seal system for acid gas and flare combustion system

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