JP2004024922A - Treatment method and treatment apparatus of infectious waste - Google Patents

Treatment method and treatment apparatus of infectious waste Download PDF

Info

Publication number
JP2004024922A
JP2004024922A JP2002149508A JP2002149508A JP2004024922A JP 2004024922 A JP2004024922 A JP 2004024922A JP 2002149508 A JP2002149508 A JP 2002149508A JP 2002149508 A JP2002149508 A JP 2002149508A JP 2004024922 A JP2004024922 A JP 2004024922A
Authority
JP
Japan
Prior art keywords
treatment
tank
waste water
waste
chlorine dioxide
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2002149508A
Other languages
Japanese (ja)
Other versions
JP3496094B1 (en
Inventor
Takao Ueda
上田 孝雄
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP2002149508A priority Critical patent/JP3496094B1/en
Publication of JP2004024922A publication Critical patent/JP2004024922A/en
Application granted granted Critical
Publication of JP3496094B1 publication Critical patent/JP3496094B1/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Filtration Of Liquid (AREA)
  • Agricultural Chemicals And Associated Chemicals (AREA)
  • Physical Water Treatments (AREA)
  • Removal Of Specific Substances (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a treatment method and treatment apparatus of infectious waste capable of efficiently treating the infectious waste without enlarging an ozonization apparatus. <P>SOLUTION: Waste water containing the infectious waste which is discarded of from medical facilities or else is pretreated by using chlorine dioxide and, thereafter, is ozonized. The treatment apparatus of infectious waste is provided with a first treatment tank 1, a second treatment tank 2, a chlorine dioxide injector 3 which injects chlorine dioxide C as a sterilizer into the first treatment tank 1, a waste water supply device 5 which supplies the waste water D containing the infectious waste to the first treatment tank 1, a circulation device 7 which circulates the waste water D between the first and second treatment tanks 1 and 2, an ozone supply device 8 which supplies ozone into the circulating waste water and a discharge device 9 discharging the treated waste water. <P>COPYRIGHT: (C)2004,JPO

Description

【0001】
【発明の属する技術分野】
本発明は、たとえば医療機関における廃水の処理方法および処理装置に関し、特に手術や解剖時に出る感染性廃棄物の廃水処理方法および処理装置に関する。
【0002】
【従来の技術】
手術や解剖時に出る廃棄物の廃水には、血液が混じっており、病原菌に汚染されている可能性が高く、下水道や河川に放流する場合には、消毒しておく必要があり、法令によっても適正処理が定められている。
従来の推奨される処理方法は、廃水を80℃に加熱して加熱殺菌する方法であるが、処理量に対して大規模で高価な処理設備が必要となり、コスト的に合わず、一部の大規模医療機関を除き、大部分の医療機関では一般の雑廃水と一緒に処理され、十分な殺菌処理がなされずに下水や河川に放流されているのが現状である。
【0003】
【発明が解決しようとする課題】
感染性処理設備が普及しない理由は高コストにあり、低コストで処理できる処理設備が社会的な要請となっている。
低コストの処理方法としては、広く普及しているオゾン処理が有望であるが、小型のオゾン処理装置では処理量が追いつかず、処理設備を大型化しなければならない。
また、各種殺菌分解剤による処理も考えられるが、確実に殺菌するためには殺菌分解剤の濃度を高める必要がある。そうすると処理後の廃水中の殺菌分解剤の残留濃度が高くなり、そのまま外部へ放流すると環境への影響が大きい。殺菌分解剤の濃度によっては二次汚染のおそれがある。したがって、処理後に他の薬剤によって殺菌分解剤の残留分を中和処理をする必要があり、結局、処理設備が余分に必要となる結果となる。
【0004】
本発明は上記した社会的要請に応じてなされたもので、その目的とするところは、処理設備を大型化することなく、低コストで効率的に感染性破棄物を処理できる感染性廃棄物の処理方法および処理装置を提供することにある。
【0005】
【課題を解決するための手段】
上記目的を達成するために、本発明に係る感染性廃棄物の処理方法は、医療機関等から廃棄される感染性廃棄物を含む廃水を殺菌消毒剤で前処理をし、その後、オゾン処理をすることを特徴とする。
殺菌消毒剤としては二酸化塩素が好適である。
殺菌消毒剤による前処理は、殺菌消毒剤を注入した後一定時間攪拌することを特徴とする。
【0006】
オゾン処理は、第1および第2処理槽間を循環する廃水中にオゾンを供給して処理する方法であり、殺菌消毒剤による前処理は一方の第1処理槽で行い、その後循環させて所定時間オゾン処理を行うことを特徴とする。
第1処理槽の前に廃水を随時受け付ける一時貯留槽を設け、該一時貯留槽から一定量だけ第1処理槽に移して処理することが好ましい。
【0007】
また、本発明の感染性廃棄物の処理装置は、第1処理槽と、第2処理槽と、第1処理槽に殺菌消毒剤を注入する殺菌消毒剤注入手段と、前記第1処理槽に感染性廃棄物を含む廃水を供給する廃水供給手段と、廃水を第1処理槽と第2処理槽間を循環させる循環手段と、循環する廃水中にオゾンを供給するオゾン供給手段と、処理した廃水を放出する放出手段とを備えていることを特徴とする。
前記殺菌消毒剤は二酸化塩素であることが好ましい。
【0008】
殺菌消毒剤が注入された第1処理槽内の廃水を攪拌する攪拌手段を備えているのが効果的である。
廃水供給手段に設けられる異物除去手段と、前記殺菌消毒剤注入手段から分岐して殺菌消毒剤の一部を前記異物除去手段に対して注入する分岐通路とを備えていることが好適である。
第1処理槽の前に設けられ感染性廃棄物の廃水を随時受け付ける一時貯留槽と、該一時貯留槽から廃水を所定量第1処理槽へ供給する供給手段とを備えていることが好ましい。
また、一時貯留槽の前に設けられる廃水を受けるための受水槽と、該受水槽から前記一時貯留槽に廃水を供給する供給手段とを備えていてもよい。
さらに、殺菌分解剤の前処理工程で二酸化塩素の水溶液にたとえば紫外線を照射して二酸化塩素を活性化するようにしてもよく、その場合には、殺菌分解剤による処理系に紫外線照射手段等の活性化手段を配置する。活性化させる方法としては、紫外線照射の他に酢酸等の酸を加えてもよい。
【0009】
【発明の実施の形態】
以下に本発明を図示の実施の形態に基づいて説明する。
実施の形態1
図1は本発明の実施の形態1に係る感染性廃棄物の処理装置を示している。
すなわち、この処理装置10は、第1処理槽1と、第2処理槽2と、第1処理槽1に殺菌消毒剤としての二酸化塩素Cを注入する二酸化塩素注入手段としての二酸化塩素注入装置3と、感染性廃棄物を含む廃水Dを第1処理槽1に供給する廃水供給手段としての廃水供給装置5と、廃水Dを第1処理槽1と第2処理槽2との間を循環させる循環装置7と、循環する廃水中にオゾンを供給するオゾン供給装置8と、処理した廃水を放出するための放出手段としての放出装置9と、を備えている。
【0010】
ここで、感染性廃棄物とは、廃棄物処理法にれば、解剖・手術等に伴って発生する病理廃棄物(臓器、組織等)と、解剖・手術等に伴って発生する血液、血清、血漿、体液(精液を含む)を含む感染性産業廃棄物に分類されているが、本発明が対象としている感染性廃棄物は、主として感染性産業廃棄物が該当する。もちろん、法令の定義に限定されるものではなく、殺菌の必要のある医療廃棄物全般に適用可能である。
二酸化塩素としては水溶液の形態で、特に二酸化塩素をアルカリ溶液中にとかして安定化させた安定化二酸化塩素を用いることが好適である。
【0011】
図示例では、第1処理槽1と第2処理槽2は地下の設備室100内に配置されているが、設備室100は地上にあってもよい。設備室100には、設備室100の空気の入れ換えをするための給気ファン等の吸気設備101、排気ファン等の排気設備102が設けられ、また、清掃時や水漏れ等が生じた場合に水を排水するための排水ポンプ103が設けられている。この廃水は外部に放流することなく、再び第1処理槽1に戻される。
第1処理槽1は密閉された容器で、第1処理槽1内部に貯まるガスを排気するための排気パイプ11と、液面スイッチ12とが設けられている。
排気パイプ11は第1処理槽1上部に設けられ、パイプ途中に脱臭器13が設けられている。
【0012】
第2処理槽2は圧力容器で、上部には減圧弁21と、内部のガスを排気するための排気通路22が設けられている。排気通路22には排オゾン吸着器23が設けられている。また、第2処理槽2内の内圧を計測する圧力計24が設けられている。
二酸化塩素注入装置3は、二酸化塩素を貯留するタンク31と、このタンク31と第1処理槽1間を接続する注入路6と、タンク31内の二酸化塩素を第1処理槽1に送り出すポンプ33とを備えている。また、図示しないが、給水路120のラインを分岐させてタンク内に給水可能とし、二酸化塩素濃度を調整可能としてもよい。その場合には、タンク31内の二酸化塩素を撹拌する攪拌器、タンク31内の液面を検出する液面計,タンク内に水位が所定量に達すると給水を停止するリミットスイッチ等が適宜設けられる。
【0013】
また、第1処理槽1の上部には洗浄用の散水器14が配置され、この散水器11に給水パイプ120が接続されている。
廃水供給装置5は、解剖室等の廃棄物発生部署からの廃水を流す排水路51と、排水路51からの廃水を受けて異物を除去する異物除去具としての排水桝52と、排水桝52と第1処理槽1間を連通する供給路53と、を備えている。排水桝52の位置は第1処理槽1より高く、廃水は排水桝52から第1処理槽1に重力によって流入する。
廃水供給装置5は、解剖室等からの廃棄物発生部署から直接第1処理槽1に供給される場合だけでなく、別にピット等の一時貯留槽を設け、一時的に貯留槽に貯留するようにしてもよい。
【0014】
また、二酸化塩素注入流路6はタンク31と第1処理槽1とを直接結んでいるが、途中に排水桝52に至る分岐通路61が設けられ、二酸化塩素Cを一部排水桝52に注入している。排水桝52に供給された二酸化塩素は排水桝52を消毒し、供給路53を通じて供給路53を消毒しながら第1処理槽1に送られる。したがって、二酸化塩素Cは、設備タンク31から直接注入される経路と、排水桝52を介して注入される経路の2経路を通じて注入されることになり、分岐通路61,排水桝52および供給路53も殺菌消毒剤である二酸化塩素の注入手段として機能する。
【0015】
循環装置7は、第1処理槽1と第2処理槽2を結ぶ循環路70と、循環路70に設けられ廃水を第1,第2処理槽1,2間を循環させる循環ポンプ73とを備えた構成となっている。循環路70は第1処理槽1の底部と第2処理槽2の上部とを接続する輸送通路71と、第2処理槽の底部と第1処理槽1の上部とを接続する戻し通路72とを備えている。循環ポンプ73は輸送通路71に2つ並列に設けられ、一つが予備となっている。輸送通路71の循環ポンプ73の上流側にはストレーナ74、さらに、通路を開閉する電動の開閉弁75が設けられている。
オゾン供給装置8は、オゾン発生装置80と、輸送通路71の第2処理槽2近傍に設けられるエゼクタ81と、オゾン発生装置8とエゼクタ81間を接続するオゾン供給路82と、を備えており、エゼクタ81を通じて循環する廃水中に供給される。
【0016】
また、処理した廃水を放流する放流装置9は、一端が電動の第1切換バルブ93を介して循環路70に接続され他端が解放された放出路91と、放出路91に設けられる放流ポンプ92とを備えている。この放流ポンプ92によって、第1,第2処理槽内の廃水を循環路70を介して放流する。
第1処理槽1の底部には戻し通路72に設けられた電動の第2切換バルブ95に接続される抜き取り通路94が設けられており、第1処理槽1からの放流は、この抜き取り通路94,戻し通路72および放出路91に至る経路と、第1処理槽1から輸送路71および第2処理槽2および放出路91を通る経路の2経路を通じて放流される。第2処理槽1からの放流経路は、戻し流路72および第1放出流路91を通じて放流される。戻し通路72を経由させずに、輸送通路71のみから放流するようにしてもよいし、場合によっては、抜き取り通路94および戻し通路72のみから放流するようにしてもよい。
また、戻し通路72の第2切換バルブ95の下流側には、廃水を取り出してサンプリングするためのサンプリング通路130が設けられ、水質を検査するようになっている。
【0017】
上記構成の廃棄物処理装置は、次のように作動する。
まず、解剖室等の廃棄物発生部署から排水路51を通じて流された廃水は排水桝52を経て廃水供給流路52に流入し、廃水供給流路52を通じて第1処理槽1に供給される。
一方、廃水が第1処理槽1に流入すると同時に、二酸化塩素注入装置3のポンプ33を駆動して注入路6を通じて二酸化塩素を一定量注入する。二酸化塩素の大部分は注入路6を通じて直接第1処理槽1内に注入され、一部は注入路6から分岐通路61を経てを排水桝52に供給され、排水桝52から供給路53を経由して第1処理槽1に流入する。排水桝52から供給路53を流れていく途中廃水が二酸化塩素に接触し、殺菌されつつ第1処理槽1に流入するので、薬液が廃水によく混じり合い、殺菌を促進することができる。
この二酸化塩素の注入は、排水桝52を経由させずに、第1処理槽1のみに注入するようにしてもよいし、第1処理槽1に直接注入せず、全量排水桝52を経由させて注入するようにしてもよい。
【0018】
第1処理槽1に供給される廃水の量が所定量に達すると廃水の供給を停止する。第1処理槽1における二酸化塩素の濃度が所定範囲となるようになるように、注入する二酸化塩素Cの量が決定される。濃度があまり濃いと、殺菌効果は高いが処理後の二酸化塩素の残留濃度が高くなってしまう。これは後工程のオゾン処理とのバランスにもよるが、5ppm程度の濃度でよい結果が得られた。
【0019】
廃水の充填が終了すると、輸送路71の開閉バルブ75を開くと共に循環ポンプ74を回転駆動して廃水を輸送通路71および戻し通路72を通じて第1,第2処理槽1,2間を循環させる。廃水がエゼクタ81を通過する際に、オゾンが輸送通路71内に自動的に吸引され、オゾンが廃水に供給されながら第2処理槽2に流入する。循環している間、エゼクタ81を通じて廃水に常時オゾンが供給され続け、廃水はオゾンに曝されながら循環することになり、殺菌、浄化が進行する。
所定時間運転後、サンプリング通路130から廃水を取水し、水質を検査し、検査基準内に収まっていれば、循環ポンプ73およびオゾン発生装置8を停止する。
【0020】
放流は、第1,第2切換バルブ93,95を切り換えると共に、放流ポンプ93を駆動する。第2処理槽2内に残留している廃水は第2放出流路92を通じて放流される。第1処理槽1内に残留している廃水は、輸送通路71および第2処理槽2を通じて放流される分と、第1放出流路91と戻し通路72を通じて抜かれる分の2系統の通路を通じて放流される。
上記した各バルブ類の切換およびポンプ類の制御は、電気室104内に設けられた不図示の制御盤によって自動制御される。
【0021】
本発明によれば、前処理工程で二酸化塩素で殺菌することにより、オゾン処理によって効率的に廃水を処理できた。
オゾン処理単独で達成しようとすると、処理に時間がかかり、時間を短縮しようとすれば、大型のオゾン発生器80が必要となり、コストが高くなる。これに対し、本発明によれば、容量の小さいオゾン発生器80で、基準内の水質を達成することができた。
また、二酸化塩素単独で処理する場合には、20〜30ppm程度の濃度が必要とされており、後の中和処理が必要となるが、本発明の場合には、濃度が低くても後工程のオゾン処理によって殺菌をし、有機物を分解することができる。
さらに、前処理で残留した二酸化塩素はオゾン処理工程で分解され、二酸化塩素の残留濃度を適正に押さえることができた。
なお、二酸化塩素Cによる前処理工程で紫外線を照射するようにしてもよく、その場合には二酸化塩素Cによる処理系に不図示の二酸化塩素を活性化させる活性化手段としての紫外線照射装置を配置する。
紫外線の照射は二酸化塩素を活性化させる作用が認められており、紫外線照射装置は、二酸化塩素注入路6、第1処理槽1、分岐通路61および廃液供給路53等、前処理工程で二酸化塩素Cが存在する箇所に配置される。一箇所だけに設けてもよいし、複数箇所に設けてもよい。この場合、処理水が濁っている場合には活性化の効果が薄いと考えられるので、二酸化塩素注入路6,分岐通路61といった処理水と混ざる前に配置することが好ましい。
また、活性化手段としては、酢酸等の酸を二酸化塩素の水溶液中に注入するようにしてもよい。注入量については処理の進行具合によって適宜調整する。
配管系に配置する紫外線照射装置としては、たとえば、配管に接続される一対の流出入ポートを備えた装置本体と、注入ポートから装置本体内部に流入した処理対象液に紫外線を照射する紫外線ランプとを備えた構成であればよい。
【0022】
次に本発明の他の実施の形態について説明する。
以下の説明では、上記実施の形態と異なる点についてのみ説明するものとし、同一の構成部分については同一の符号を付してその説明は省略する。
実施の形態2
図2は本発明の実施の形態2に係る感染性廃棄物廃水処理装置を示している。
この実施の形態2では、第1処理槽1に攪拌手段としての攪拌器15を設け、前処理工程で第1処理槽1内の廃水を所定時間攪拌するようにしたものである。攪拌器15は、第1処理槽内に挿入される撹拌羽15aと、攪拌羽15aを回転駆動するモータ15bとを備えている。
【0023】
そして、第1処理槽1への廃水の充填が終了した時点で、攪拌器15を所定時間回転駆動し、攪拌器15を停止した後、循環ポンプ74を駆動して廃水を循環させ、廃水にオゾン発生装置80からオゾンを供給し、オゾンにて殺菌処理をする。
このように、二酸化塩素による前処理工程で所定時間攪拌処理すれば、上記した実施の形態1に比べて殺菌消毒が効率的に進行し、後処理でのオゾン処理時間を短縮化できる。
【0024】
実施の形態3
図3には本発明の実施の形態3に係る感染性廃棄物の処理装置を示している。
この実施の形態は、第1処理槽1に廃水を供給する廃水供給系が異なる。
すなわち、この実施の形態2では、感染性廃棄物としては、解剖室からの廃水の他に、手術部門、隔離病室、透析部門からの各廃水を処理するもので、量が多くなる場合もあり、第1処理槽1の前に一時貯留槽300を設け、各廃棄物発生部署から廃水を一時貯留しておき、汲み上げポンプ301によって第1処理槽1内に所定量ずつ汲み上げて処理するようにしたものである。もちろん、廃水が出る部署が一つだけの場合についても適用可能である。
【0025】
また、この実施の形態では、二酸化塩素注入装置3は、給水路120からの第1分岐ライン121を通じてタンク31内に給水可能とし、二酸化塩素濃度を調整可能としたものである。タンク31には、タンク31内の二酸化塩素を撹拌する攪拌器32と、タンク31内の液面を検出する液面計34と,タンク31内に水位が所定量に達すると給水を停止するリミットスイッチ35が設けられている。
給水路120の第1分岐ライン121の分岐部で分岐した第2分岐ライン122は二酸化塩素注入路6に接続され、第1処理槽1への給水は二酸化塩素注入路6を通じて行うようになっている。そして、タンク31への給水は第1分岐ライン121に設けられた電動の第1開閉バルブ121aによって制御され、第1処理槽1への給水は第2分岐ライン122に設けられた電動の第2開閉バルブ122aによって制御され、二酸化塩素の注入路6は電動の第3開閉バルブ6aによって制御される。
各部署からの廃水は排水通路を通して一時貯留槽300に送られる。排水通路には排水桝やバスケットスクリーン等のゴミや異物を除去する異物除去具352が設けられている。異物除去具352に二酸化塩素注入通路6からの分岐通路61を通じて二酸化塩素が供給される。分岐通路61は各固分除去具に対して3つに分岐している。
一時貯留槽300には、汲み上げポンプ301が予備のために2つ設けられ、この汲み上げポンプ301から汲み上げ通路302を通じて第1処理槽1に供給される。
一時貯留槽300が接地される床には、清掃用あるいは一時貯留槽300から溢れた廃水を汲み上げるポンプ303が設定され、このポンプ303によって汲み上げられた廃水は一時処理槽300に戻されるようになっている。
【0026】
この実施の形態2に係る感染性廃棄物処理装置は、各部署からの廃水は随時一時貯留室300に貯留され、所定量貯まるとポンプ301が駆動して貯留された廃水が第1処理槽1に汲み上げられる。同時に殺菌消毒剤注入装置3のポンプ33が駆動し、二酸化塩素が所定量第1処理槽1に注入される。
二酸化塩素の一部は、分岐通路61を経由して各部署の排水出口に置かれた異物除去具352に注入される。この分岐通路61への注入量は、各分岐通路61に設けられた切換バルブ61aを開閉することによって調節可能である。
この分岐通路61を経由して注入された二酸化塩素によって異物除去具352は殺菌消毒され、さらに、一時貯留槽300に流入して、一時貯留槽300に貯留されている廃水についても殺菌消毒する。この二酸化塩素の濃度は随時流入する廃水によって希釈化されて薄い濃度であるが、第1処理槽1の前段階である程度殺菌処理が進む。
【0027】
第1処理槽1に汲み上げられた廃水に注入設備3から注入される所定量の二酸化塩素が注入されるので、少なくとも一定濃度以上の二酸化塩素濃度が確保される。
第1処理槽1内に排水量が所定量に達すると、汲み上げポンプ301および注入ポンプ33が停止され、撹拌器15が駆動を開始し一定時間撹拌する。
一定時間経過後、撹拌器15が停止し、オゾン処理に移行する。
オゾン処理については上記実施の形態1と全く同一である。
なお、二酸化塩素に紫外線を照射する場合、あるいは酢酸等の酸を加えて二酸化塩素を活性化させる場合には、紫外線照射装置等の活性化手段は、二酸化塩素注入路6、第1処理槽1、分岐通路61および一時貯留槽300と第1処理槽1間の供給路のいずれか、あるいは複数箇所に設ければよい。
【0028】
実施の形態4
図4は本発明の実施の形態4に係る感染性廃棄物の処理装置を示している。
この処理装置は、廃棄物発生部署からの廃水の取水口に個別の受水槽400を設け、この個別貯留槽400から一時貯留槽300にポンプ401で汲み上げるようにしたものである。この受水槽400が一時貯留槽より低い位置にある場合に有効である。
この場合、配管系が複雑になる場合には、図5に示すように、二酸化塩素の分岐通路は無くし、異物除去具352の消毒は二酸化塩素の散布を手作業で行うようにすればよい。
上記実施の形態では、殺菌消毒剤として二酸化塩素を用いた例を示したが、二酸化塩素に限られず、他の殺菌消毒剤を用いることができる。その場合、それ自身安全でトリハロメタンのような二次汚染の問題がなく、しかも殺菌力が高く、かつ後処理のオゾン処理となじみのよい殺菌消毒剤であることが好適である。
【0029】
【発明の効果】
本発明は以上の構成及び作用を有するもので、医療機関等から廃棄される感染性廃棄物を含む廃水を殺菌消毒剤で前処理をし、その後、オゾン処理をするようにしたので、殺菌消毒剤で大半の病原菌は死滅あるいは弱り、比較的小型のオゾン処理設備で処理することができる。また、固形分についても分解処理することができる。
また、オゾン処理によって前処理工程で使用した殺菌消毒剤が分解されるので、特に中和処理等の後処理を必要せず、殺菌消毒剤の残留濃度を適正範囲に押さえることができる。
特に、請求項2に記載のように、殺菌消毒剤として二酸化塩素を用いれば、安定で殺菌効果が高く、また、他の塩素系の殺菌消毒剤のようにトリハロメタンが発生せず、環境に対する影響が小さい。また、排出されるホルマリンなどの薬品についても分解することができる。
【0030】
請求項3に記載のように、殺菌消毒剤による前処理を一定時間攪拌すれば、殺菌消毒が効率的に進行し、オゾン処理時間の短縮化を図ることができる。
また、請求項4に記載のように、オゾン処理は第1および第2処理槽間を循環する廃水中にオゾンを供給して処理する方法であり、殺菌消毒剤による前処理は一方の第1処理槽で行い、その後循環させて所定時間オゾン処理を行うようにすれば、連続して処理することができる。
さらに、請求項5に記載のように、第1処理槽の前に廃水を随時受け付ける一時貯留槽を設け、一時貯留槽から一定量だけ第1処理槽に移して処理するようにすれば、排水量が多くなっても、処理を安定して行うことができる。
【0031】
本発明の感染性廃棄物の処理装置は、請求項6に記載のように、第1処理槽と、第2処理槽と、第1処理槽に殺菌消毒剤を注入する殺菌消毒剤注入手段と、前記第1処理槽に感染性廃棄物を含む廃水を供給する廃水供給手段と、廃水を第1処理槽と第2処理槽間を循環させる循環手段と、循環する廃水中にオゾンを供給するオゾン供給手段と、処理した廃水を放出する放出手段とを備えた構成としたので、第1処理槽が殺菌消毒剤による処理とオゾン処理に共用することができ、装置構成がコンパクト化される。
請求項8に記載のように、殺菌消毒剤が注入された第1処理槽内の廃水を攪拌する攪拌手段を備えることにより、殺菌消毒を効率的に処理できる。
【0032】
また、請求項9に記載のように、廃水供給手段に設けられる異物除去手段と、前記殺菌消毒剤注入手段から分岐して殺菌消毒剤の一部を前記異物除去手段に対して注入する分岐通路とを備えることにより、排水桝などの異物除去手段の殺菌,消毒を行うことができる。
請求項10に記載の発明によれば、第1処理槽の前に設けられ感染性廃棄物の廃水を随時受け付ける一時貯留槽と、一時貯留槽から廃水を所定量第1処理槽へ供給する供給手段とを備えた構成としたので、排水量に関わらず適正に処理することができる。
請求項11に記載の発明によれば、一時貯留槽の上流側に設けられる受水槽と、受水槽から前記一時貯留槽に廃水を供給する供給手段とを備えた構成としたので、感染廃棄物の廃水が発生する部署のフロアが一時貯留槽より低い位置にある場合に有効である。
請求項12,13に記載の発明によれば、二酸化塩素の前処理工程で紫外線の照射等によって二酸化塩素を活性化させるようにしたので、二酸化塩素が低濃度でも殺菌効果が高くなる。
【図面の簡単な説明】
【図1】図1は本発明の実施の形態1に係る感染性廃棄物の処理装置の構成図である。
【図2】図2は本発明の実施の形態2に係る感染性廃棄物の処理装置の構成図である。
【図3】図3は本発明の実施の形態3に係る感染性廃棄物の処理装置の構成図である。
【図4】図4は本発明の実施の形態4に係る感染性廃棄物の処理装置の構成図である。
【図5】図5は本発明の実施の形態4の変形例を示す図である。
【符号の説明】
10 処理装置
1 第1処理槽、2  第2処理槽
3  二酸化塩素注入装置
31 タンク、32 ポンプ、6 注入路
5 廃棄物供給装置
52 排水桝、53 供給路
7 循環装置
70 循環路、71 輸送通路、72 戻し通路、73 循環ポンプ、75 バルブ
8 オゾン供給装置
80 オゾン発生器、81 エゼクタ、82 オゾン供給路
9 放流装置。
91 放出路、92 放流ポンプ、93 第1放流バルブ、94 抜き取り通路、95 第2放流バルブ
130 サンプリング通路
15 攪拌器
300 一時貯留槽
301 ポンプ
303 ポンプ
352 異物除去具
400 受水槽
401 ポンプ
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to, for example, a wastewater treatment method and treatment apparatus in a medical institution, and more particularly, to a wastewater treatment method and treatment apparatus for infectious waste that occurs during surgery or dissection.
[0002]
[Prior art]
Waste water generated during surgery and dissection contains blood and is likely to be contaminated with pathogens. When discharged into sewers and rivers, it must be disinfected. Appropriate treatment is defined.
The conventional recommended treatment method is a method in which wastewater is heated to 80 ° C. and sterilized by heating. However, a large-scale and expensive treatment facility is required for the treatment amount, and this is not suitable for cost. Except for large-scale medical institutions, most medical institutions are treated together with general wastewater and discharged into sewage and rivers without being fully sterilized.
[0003]
[Problems to be solved by the invention]
The reason why infectious treatment equipment is not widespread is the high cost, and a treatment equipment capable of processing at low cost is a social demand.
As a low-cost treatment method, widely used ozone treatment is promising, but a small ozone treatment apparatus cannot catch up with the treatment amount, and the treatment equipment must be enlarged.
Although treatment with various sterilizing / decomposing agents can be considered, it is necessary to increase the concentration of the sterilizing / decomposing agent in order to reliably sterilize. If it does so, the residual density | concentration of the bactericidal decomposition agent in the wastewater after a process will become high, and if it discharges to the outside as it is, the influence on an environment will be large. Depending on the concentration of the disinfectant, there is a risk of secondary contamination. Therefore, after treatment, it is necessary to neutralize the residue of the bactericidal decomposition agent with other chemicals, and as a result, extra processing equipment is required.
[0004]
The present invention has been made in response to the above-mentioned social demands. The purpose of the present invention is to provide an infectious waste that can be efficiently processed at low cost without increasing the size of the processing equipment. The object is to provide a processing method and a processing apparatus.
[0005]
[Means for Solving the Problems]
In order to achieve the above object, the infectious waste treatment method according to the present invention pretreats waste water containing infectious waste discarded from a medical institution or the like with a disinfectant and then performs ozone treatment. It is characterized by doing.
Chlorine dioxide is preferred as the disinfectant.
The pretreatment with the disinfectant is characterized by stirring for a certain time after injecting the disinfectant.
[0006]
The ozone treatment is a method in which ozone is supplied to the waste water circulating between the first and second treatment tanks, and the pretreatment with the disinfectant is performed in one of the first treatment tanks and then circulated to a predetermined level. It is characterized by performing time ozone treatment.
It is preferable to provide a temporary storage tank that accepts wastewater as needed before the first treatment tank, and transfer the fixed amount from the temporary storage tank to the first treatment tank for processing.
[0007]
The infectious waste processing apparatus of the present invention includes a first processing tank, a second processing tank, a sterilizing / disinfecting agent injection means for injecting a sterilizing / disinfecting agent into the first processing tank, and the first processing tank. Waste water supply means for supplying waste water containing infectious waste, circulation means for circulating waste water between the first treatment tank and the second treatment tank, and ozone supply means for supplying ozone into the circulating waste water And a discharge means for discharging waste water.
The disinfectant is preferably chlorine dioxide.
[0008]
It is effective to provide a stirring means for stirring the waste water in the first treatment tank into which the sterilizing / disinfecting agent is injected.
It is preferable to include a foreign matter removing means provided in the waste water supply means and a branch passage that branches from the sterilizing / disinfecting agent injecting means and injects part of the sterilizing / disinfecting agent into the foreign matter removing means.
It is preferable to include a temporary storage tank that is provided in front of the first treatment tank and receives waste water of infectious waste as needed, and a supply unit that supplies a predetermined amount of waste water from the temporary storage tank to the first treatment tank.
Moreover, you may provide the water receiving tank for receiving the wastewater provided in front of a temporary storage tank, and the supply means which supplies wastewater from this water receiving tank to the said temporary storage tank.
Furthermore, the chlorine dioxide aqueous solution may be activated by irradiating the aqueous solution of chlorine dioxide with, for example, ultraviolet rays in the pretreatment step of the sterilizing / decomposing agent. An activation means is arranged. As a method for activation, an acid such as acetic acid may be added in addition to ultraviolet irradiation.
[0009]
DETAILED DESCRIPTION OF THE INVENTION
The present invention will be described below based on the illustrated embodiments.
Embodiment 1
FIG. 1 shows an infectious waste treatment apparatus according to Embodiment 1 of the present invention.
That is, this processing apparatus 10 includes a first processing tank 1, a second processing tank 2, and a chlorine dioxide injection device 3 as chlorine dioxide injection means for injecting chlorine dioxide C as a disinfectant into the first processing tank 1. And a waste water supply device 5 as waste water supply means for supplying waste water D containing infectious waste to the first treatment tank 1, and circulating the waste water D between the first treatment tank 1 and the second treatment tank 2. A circulation device 7, an ozone supply device 8 for supplying ozone into the circulating wastewater, and a discharge device 9 as a discharge means for discharging the treated wastewater are provided.
[0010]
Here, infectious waste refers to pathological waste (organs, tissues, etc.) that accompanies anatomy / surgery and blood and serum that accompanies dissection / surgery, etc. Infectious industrial wastes including plasma and body fluid (including semen) are classified into infectious industrial wastes, and infectious industrial wastes targeted by the present invention mainly correspond to infectious industrial wastes. Of course, it is not limited to the definition of laws and regulations, and can be applied to all medical wastes that need to be sterilized.
Chlorine dioxide is preferably used in the form of an aqueous solution, and in particular, stabilized chlorine dioxide obtained by stabilizing chlorine dioxide in an alkaline solution.
[0011]
In the illustrated example, the first treatment tank 1 and the second treatment tank 2 are disposed in the underground facility room 100, but the facility room 100 may be on the ground. The facility room 100 is provided with an intake facility 101 such as an air supply fan for exchanging air in the facility room 100, and an exhaust facility 102 such as an exhaust fan, and when cleaning or water leakage occurs. A drainage pump 103 is provided for draining water. This waste water is returned to the first treatment tank 1 again without being discharged outside.
The first treatment tank 1 is a sealed container, and is provided with an exhaust pipe 11 for exhausting gas stored in the first treatment tank 1 and a liquid level switch 12.
The exhaust pipe 11 is provided in the upper part of the 1st processing tank 1, and the deodorizer 13 is provided in the middle of the pipe.
[0012]
The second treatment tank 2 is a pressure vessel, and is provided with a pressure reducing valve 21 and an exhaust passage 22 for exhausting internal gas. An exhaust ozone adsorber 23 is provided in the exhaust passage 22. In addition, a pressure gauge 24 for measuring the internal pressure in the second treatment tank 2 is provided.
The chlorine dioxide injection device 3 includes a tank 31 that stores chlorine dioxide, an injection path 6 that connects the tank 31 and the first processing tank 1, and a pump 33 that sends chlorine dioxide in the tank 31 to the first processing tank 1. And. Although not shown, the line of the water supply channel 120 may be branched so that water can be supplied into the tank and the chlorine dioxide concentration can be adjusted. In that case, a stirrer that stirs chlorine dioxide in the tank 31, a liquid level meter that detects the liquid level in the tank 31, a limit switch that stops water supply when the water level reaches a predetermined amount in the tank, and the like are provided as appropriate. It is done.
[0013]
In addition, a sprinkler 14 for cleaning is disposed on the upper portion of the first treatment tank 1, and a water supply pipe 120 is connected to the sprinkler 11.
The wastewater supply device 5 includes a drainage channel 51 through which wastewater from a waste generation department such as an autopsy room flows, a drainage basin 52 as a foreign matter removing tool that receives wastewater from the drainage channel 51 and removes foreign matter, and a drainage basin 52 And a supply path 53 that communicates between the first treatment tanks 1. The position of the drainage basin 52 is higher than that of the first treatment tank 1, and the wastewater flows from the drainage basin 52 into the first treatment tank 1 by gravity.
The waste water supply device 5 is provided not only when it is directly supplied from the waste generation department from the dissection room or the like to the first treatment tank 1 but also separately provided with a temporary storage tank such as a pit so that it is temporarily stored in the storage tank. It may be.
[0014]
Further, the chlorine dioxide injection channel 6 directly connects the tank 31 and the first treatment tank 1, but a branch passage 61 is provided on the way to the drainage tank 52, and chlorine dioxide C is partially injected into the drainage tank 52. doing. Chlorine dioxide supplied to the drainage tank 52 disinfects the drainage tank 52 and is sent to the first treatment tank 1 through the supply path 53 while disinfecting the supply path 53. Therefore, the chlorine dioxide C is injected through two routes, a route directly injected from the equipment tank 31 and a route injected via the drainage basin 52, and the branch passage 61, the drainage basin 52 and the supply passage 53 are injected. Also functions as a means for injecting chlorine dioxide, which is a disinfectant.
[0015]
The circulation device 7 includes a circulation path 70 that connects the first treatment tank 1 and the second treatment tank 2, and a circulation pump 73 that is provided in the circulation path 70 and circulates waste water between the first and second treatment tanks 1 and 2. It has a configuration with. The circulation path 70 includes a transport passage 71 that connects the bottom of the first treatment tank 1 and the top of the second treatment tank 2, and a return passage 72 that connects the bottom of the second treatment tank and the top of the first treatment tank 1. It has. Two circulation pumps 73 are provided in parallel in the transport passage 71, and one is reserved. A strainer 74 and an electric on-off valve 75 for opening and closing the passage are provided on the upstream side of the circulation pump 73 in the transport passage 71.
The ozone supply device 8 includes an ozone generation device 80, an ejector 81 provided in the vicinity of the second treatment tank 2 in the transport passage 71, and an ozone supply path 82 that connects between the ozone generation device 8 and the ejector 81. The wastewater is circulated through the ejector 81.
[0016]
Further, the discharge device 9 for discharging the treated wastewater has a discharge path 91 having one end connected to the circulation path 70 via the electric first switching valve 93 and the other end released, and a discharge pump provided in the discharge path 91. 92. The discharge pump 92 discharges the waste water in the first and second treatment tanks via the circulation path 70.
An extraction passage 94 connected to an electric second switching valve 95 provided in the return passage 72 is provided at the bottom of the first treatment tank 1, and discharge from the first treatment tank 1 is performed in the extraction passage 94. , The path to the return path 72 and the discharge path 91 and the path from the first processing tank 1 through the transport path 71, the second processing tank 2 and the discharge path 91. The discharge path from the second treatment tank 1 is discharged through the return flow path 72 and the first discharge flow path 91. It may be discharged only from the transport passage 71 without going through the return passage 72, or may be discharged only from the extraction passage 94 and the return passage 72 in some cases.
A sampling passage 130 for taking out and sampling waste water is provided on the downstream side of the second switching valve 95 in the return passage 72 so as to inspect the water quality.
[0017]
The waste disposal apparatus having the above-described configuration operates as follows.
First, wastewater that has flowed from a waste generation department such as an autopsy room through a drainage channel 51 flows into a wastewater supply channel 52 through a drainage basin 52 and is supplied to the first treatment tank 1 through the wastewater supply channel 52.
On the other hand, at the same time as the wastewater flows into the first treatment tank 1, the pump 33 of the chlorine dioxide injection device 3 is driven to inject a certain amount of chlorine dioxide through the injection path 6. Most of the chlorine dioxide is directly injected into the first treatment tank 1 through the injection path 6, and a part of the chlorine dioxide is supplied from the injection path 6 through the branch passage 61 to the drainage basin 52 and from the drainage basin 52 via the supply path 53. And flows into the first treatment tank 1. Since the waste water is in contact with chlorine dioxide and flows into the first treatment tank 1 while being sterilized, the chemical liquid is well mixed with the waste water and promotes sterilization.
The chlorine dioxide may be injected only into the first treatment tank 1 without going through the drainage basin 52, or directly into the first treatment tank 1 and through the whole drainage basin 52. May be injected.
[0018]
When the amount of waste water supplied to the first treatment tank 1 reaches a predetermined amount, the supply of waste water is stopped. The amount of chlorine dioxide C to be injected is determined so that the concentration of chlorine dioxide in the first treatment tank 1 falls within a predetermined range. If the concentration is too high, the sterilizing effect is high, but the residual concentration of chlorine dioxide after treatment becomes high. Although this depends on the balance with the subsequent ozone treatment, good results were obtained with a concentration of about 5 ppm.
[0019]
When the filling of the waste water is completed, the opening / closing valve 75 of the transport path 71 is opened and the circulation pump 74 is rotationally driven to circulate the waste water between the first and second treatment tanks 1 and 2 through the transport path 71 and the return path 72. When the wastewater passes through the ejector 81, ozone is automatically sucked into the transport passage 71 and flows into the second treatment tank 2 while being supplied to the wastewater. During circulation, ozone is continuously supplied to the wastewater through the ejector 81, and the wastewater is circulated while being exposed to ozone, and sterilization and purification proceed.
After the operation for a predetermined time, waste water is taken from the sampling passage 130, the water quality is inspected, and if it falls within the inspection standard, the circulation pump 73 and the ozone generator 8 are stopped.
[0020]
In the discharge, the first and second switching valves 93 and 95 are switched and the discharge pump 93 is driven. Waste water remaining in the second treatment tank 2 is discharged through the second discharge channel 92. Waste water remaining in the first treatment tank 1 passes through two passages that are discharged through the transport passage 71 and the second treatment tank 2 and discharged through the first discharge passage 91 and the return passage 72. It is released.
The switching of the valves and the control of the pumps are automatically controlled by a control panel (not shown) provided in the electric chamber 104.
[0021]
According to the present invention, waste water can be efficiently treated by ozone treatment by sterilizing with chlorine dioxide in the pretreatment step.
If it is attempted to achieve the ozone treatment alone, it takes time for the treatment, and if it is intended to shorten the time, a large ozone generator 80 is required, resulting in an increase in cost. On the other hand, according to the present invention, the water quality within the standard could be achieved with the ozone generator 80 having a small capacity.
In addition, in the case of treating with chlorine dioxide alone, a concentration of about 20 to 30 ppm is required, and a subsequent neutralization treatment is required. It can be sterilized by ozone treatment to decompose organic matter.
Furthermore, the chlorine dioxide remaining in the pretreatment was decomposed in the ozone treatment process, and the residual concentration of chlorine dioxide could be appropriately suppressed.
In addition, you may make it irradiate with an ultraviolet-ray in the pre-processing process by chlorine dioxide C, and arrange | position the ultraviolet irradiation device as an activation means which activates the chlorine dioxide not shown in the processing system by chlorine dioxide C in that case To do.
Irradiation of ultraviolet rays has been recognized to activate chlorine dioxide, and the ultraviolet irradiation device is chlorine dioxide in the pretreatment process such as the chlorine dioxide injection path 6, the first treatment tank 1, the branch path 61 and the waste liquid supply path 53. Arranged where C exists. You may provide in one place and may provide in several places. In this case, since the effect of activation is considered to be small when the treated water is cloudy, it is preferably arranged before being mixed with the treated water such as the chlorine dioxide injection path 6 and the branch path 61.
Further, as an activating means, an acid such as acetic acid may be injected into an aqueous solution of chlorine dioxide. The injection amount is appropriately adjusted depending on the progress of the treatment.
Examples of the ultraviolet irradiation device disposed in the piping system include, for example, an apparatus main body provided with a pair of inflow / outflow ports connected to the pipe, and an ultraviolet lamp that irradiates the processing target liquid flowing into the apparatus main body from the injection port with ultraviolet rays. As long as the configuration is provided.
[0022]
Next, another embodiment of the present invention will be described.
In the following description, only different points from the above embodiment will be described, and the same components are denoted by the same reference numerals and the description thereof will be omitted.
Embodiment 2
FIG. 2 shows an infectious wastewater treatment apparatus according to Embodiment 2 of the present invention.
In this Embodiment 2, the stirrer 15 as a stirring means is provided in the 1st processing tank 1, and the waste water in the 1st processing tank 1 is stirred for the predetermined time by the pre-processing process. The stirrer 15 includes a stirring blade 15a inserted into the first processing tank, and a motor 15b that rotationally drives the stirring blade 15a.
[0023]
Then, when the filling of the waste water into the first treatment tank 1 is completed, the stirrer 15 is driven to rotate for a predetermined time, and after the stirrer 15 is stopped, the circulation pump 74 is driven to circulate the waste water. Ozone is supplied from the ozone generator 80 and sterilized with ozone.
As described above, if the agitation treatment is performed for a predetermined time in the pretreatment step using chlorine dioxide, sterilization and disinfection proceed more efficiently than in the first embodiment, and the ozone treatment time in the post-treatment can be shortened.
[0024]
Embodiment 3
FIG. 3 shows an infectious waste treatment apparatus according to Embodiment 3 of the present invention.
This embodiment is different in a waste water supply system for supplying waste water to the first treatment tank 1.
That is, in the second embodiment, infectious waste is treated with waste water from the surgical department, isolation room, and dialysis department in addition to the waste water from the dissection room. In addition, a temporary storage tank 300 is provided in front of the first treatment tank 1, waste water is temporarily stored from each waste generation department, and a predetermined amount is pumped into the first treatment tank 1 by the pumping pump 301 for processing. It is a thing. Of course, this is also applicable to cases where there is only one department that produces wastewater.
[0025]
Further, in this embodiment, the chlorine dioxide injecting device 3 can supply water into the tank 31 through the first branch line 121 from the water supply channel 120 and adjust the chlorine dioxide concentration. The tank 31 includes a stirrer 32 for stirring the chlorine dioxide in the tank 31, a liquid level gauge 34 for detecting the liquid level in the tank 31, and a limit for stopping water supply when the water level reaches a predetermined amount in the tank 31. A switch 35 is provided.
The second branch line 122 branched at the branch portion of the first branch line 121 of the water supply path 120 is connected to the chlorine dioxide injection path 6, and water supply to the first treatment tank 1 is performed through the chlorine dioxide injection path 6. Yes. The water supply to the tank 31 is controlled by an electric first opening / closing valve 121 a provided in the first branch line 121, and the water supply to the first treatment tank 1 is an electric second supplied to the second branch line 122. The chlorine dioxide injection path 6 is controlled by an electric third on-off valve 6a.
Waste water from each department is sent to the temporary storage tank 300 through the drainage passage. The drainage passage is provided with a foreign matter removing tool 352 for removing dust and foreign matters such as a drainage basin and a basket screen. Chlorine dioxide is supplied to the foreign matter removing tool 352 through the branch passage 61 from the chlorine dioxide injection passage 6. The branch passage 61 branches into three for each solid content removal tool.
The temporary storage tank 300 is provided with two pumping pumps 301 for backup, and is supplied from the pumping pump 301 to the first processing tank 1 through the pumping path 302.
On the floor to which the temporary storage tank 300 is grounded, a pump 303 for pumping up the waste water for cleaning or overflowing from the temporary storage tank 300 is set, and the waste water pumped up by the pump 303 is returned to the temporary treatment tank 300. ing.
[0026]
In the infectious waste treatment apparatus according to the second embodiment, waste water from each department is stored in the temporary storage chamber 300 as needed, and when a predetermined amount is accumulated, the waste water stored by driving the pump 301 is stored in the first treatment tank 1. Pumped up. At the same time, the pump 33 of the sterilizing / disinfecting agent injecting device 3 is driven to inject a predetermined amount of chlorine dioxide into the first treatment tank 1.
Part of the chlorine dioxide is injected into the foreign matter removing tool 352 placed at the drain outlet of each department via the branch passage 61. The injection amount into the branch passage 61 can be adjusted by opening and closing the switching valve 61 a provided in each branch passage 61.
The foreign matter removing tool 352 is sterilized and sterilized by chlorine dioxide injected through the branch passage 61, and further flows into the temporary storage tank 300 to sterilize and disinfect the waste water stored in the temporary storage tank 300. The concentration of this chlorine dioxide is diluted by the waste water that flows in as needed, and is a thin concentration, but the sterilization process proceeds to some extent in the previous stage of the first treatment tank 1.
[0027]
Since a predetermined amount of chlorine dioxide injected from the injection facility 3 is injected into the waste water pumped into the first treatment tank 1, a chlorine dioxide concentration of at least a certain concentration is ensured.
When the amount of drainage reaches a predetermined amount in the first treatment tank 1, the pumping pump 301 and the injection pump 33 are stopped, and the stirrer 15 starts to drive and stirs for a certain time.
After a certain period of time, the stirrer 15 is stopped and the process proceeds to ozone treatment.
The ozone treatment is exactly the same as in the first embodiment.
In addition, when irradiating chlorine dioxide with ultraviolet rays or activating chlorine dioxide by adding an acid such as acetic acid, the activating means such as an ultraviolet irradiation device is the chlorine dioxide injection path 6, the first treatment tank 1. In addition, the branch passage 61 and the supply path between the temporary storage tank 300 and the first treatment tank 1 may be provided at a plurality of locations.
[0028]
Embodiment 4
FIG. 4 shows an infectious waste treatment apparatus according to Embodiment 4 of the present invention.
In this processing apparatus, an individual water receiving tank 400 is provided at the intake of waste water from the waste generation department, and the individual storage tank 400 is pumped up to the temporary storage tank 300 by a pump 401. This is effective when the water receiving tank 400 is located lower than the temporary storage tank.
In this case, when the piping system becomes complicated, as shown in FIG. 5, the branch passage of chlorine dioxide is eliminated, and the foreign matter removing tool 352 may be disinfected by manually spraying chlorine dioxide.
In the said embodiment, although the example which used chlorine dioxide as a disinfection disinfectant was shown, it is not restricted to chlorine dioxide, Another disinfectant disinfectant can be used. In that case, it is preferable that the disinfectant is safe and free from problems of secondary contamination such as trihalomethane, has a high sterilizing power, and is familiar with the post-treatment ozone treatment.
[0029]
【The invention's effect】
The present invention has the above-described configuration and action, and the waste water containing infectious waste discarded from medical institutions is pretreated with a disinfectant and then treated with ozone. Most pathogens are killed or weakened by chemicals and can be treated with relatively small ozone treatment equipment. Moreover, it can decompose also about solid content.
Moreover, since the disinfectant used in the pretreatment process is decomposed by the ozone treatment, a post-treatment such as a neutralization treatment is not particularly required, and the residual concentration of the disinfectant can be kept within an appropriate range.
In particular, if chlorine dioxide is used as a disinfectant as described in claim 2, it is stable and highly effective in disinfecting, and trihalomethane is not generated unlike other chlorine-based disinfectants. Is small. In addition, chemicals such as formalin discharged can be decomposed.
[0030]
As described in claim 3, if the pretreatment with the sterilizing / disinfecting agent is stirred for a certain period of time, the sterilizing / disinfecting efficiently proceeds and the ozone treatment time can be shortened.
Further, as described in claim 4, the ozone treatment is a method of supplying ozone to waste water circulating between the first and second treatment tanks, and the pretreatment with the disinfectant is one of the first treatments. If it is performed in a treatment tank and then circulated and subjected to ozone treatment for a predetermined time, it can be treated continuously.
Furthermore, if the temporary storage tank which receives wastewater at any time is provided in front of the first treatment tank as described in claim 5 and a certain amount is transferred from the temporary storage tank to the first treatment tank for processing, Even if there is an increase, the processing can be performed stably.
[0031]
The infectious waste processing apparatus according to the present invention includes a first processing tank, a second processing tank, and a sterilizing / disinfecting agent injecting unit that injects a sterilizing / disinfecting agent into the first processing tank, as described in claim 6. , Waste water supply means for supplying waste water containing infectious waste to the first treatment tank, circulation means for circulating the waste water between the first treatment tank and the second treatment tank, and supplying ozone to the circulating waste water Since the configuration includes the ozone supply means and the discharge means for discharging the treated wastewater, the first treatment tank can be used for both the treatment with the sterilizer and the ozone treatment, and the apparatus configuration is made compact.
As described in claim 8, sterilization and disinfection can be efficiently processed by providing a stirring means for stirring the waste water in the first processing tank into which the sterilizing and disinfecting agent is injected.
[0032]
Further, as described in claim 9, foreign matter removing means provided in the waste water supply means, and a branch passage branching from the sterilizing / disinfecting agent injecting part and injecting a part of the sterilizing / disinfecting agent into the foreign matter removing means. The sterilization and disinfection of foreign matter removing means such as a drainage can be performed.
According to the invention described in claim 10, a temporary storage tank provided before the first treatment tank and receiving waste water of infectious waste as needed, and a supply for supplying a predetermined amount of waste water from the temporary storage tank to the first treatment tank Therefore, it is possible to treat appropriately regardless of the amount of drainage.
According to invention of Claim 11, since it was set as the structure provided with the water receiving tank provided in the upstream of a temporary storage tank, and the supply means which supplies wastewater from a water receiving tank to the said temporary storage tank, infectious waste This is effective when the floor of the department where the wastewater is generated is located lower than the temporary storage tank.
According to the invention described in claims 12 and 13, since chlorine dioxide is activated by irradiation of ultraviolet rays or the like in the chlorine dioxide pretreatment step, the bactericidal effect is enhanced even if the concentration of chlorine dioxide is low.
[Brief description of the drawings]
FIG. 1 is a configuration diagram of an infectious waste treatment apparatus according to Embodiment 1 of the present invention.
FIG. 2 is a configuration diagram of an infectious waste treatment apparatus according to Embodiment 2 of the present invention.
FIG. 3 is a configuration diagram of an infectious waste treatment apparatus according to Embodiment 3 of the present invention.
FIG. 4 is a configuration diagram of an infectious waste treatment apparatus according to Embodiment 4 of the present invention.
FIG. 5 is a diagram showing a modification of the fourth embodiment of the present invention.
[Explanation of symbols]
10 Processing device
1 1st processing tank, 2nd processing tank
3 Chlorine dioxide injector
31 tanks, 32 pumps, 6 injection channels
5 Waste supply equipment
52 drainage basin, 53 supply channel
7 Circulator
70 Circulation path, 71 Transport path, 72 Return path, 73 Circulation pump, 75 Valve
8 Ozone supply device
80 Ozone generator, 81 Ejector, 82 Ozone supply path
9 Discharge device.
91 discharge passage, 92 discharge pump, 93 first discharge valve, 94 extraction passage, 95 second discharge valve
130 Sampling passage
15 Stirrer
300 Temporary storage tank
301 pump
303 pump
352 Foreign object removal tool
400 water tank
401 pump

Claims (13)

感染性廃棄物を含む廃水を殺菌分解剤で前処理をし、その後、オゾン処理をすることを特徴とする感染性廃棄物の処理方法。A method for treating infectious waste, characterized in that waste water containing infectious waste is pretreated with a disinfectant and then treated with ozone. 前記殺菌消毒剤は二酸化塩素である請求項1に記載の感染性廃棄物の処理方法。The method for treating infectious waste according to claim 1, wherein the disinfectant is chlorine dioxide. 前記殺菌消毒剤による前処理は、殺菌消毒剤を注入した後一定時間攪拌することを特徴とする請求項1または2に記載の感染性廃棄物の処理方法。The method for treating infectious waste according to claim 1 or 2, wherein the pretreatment with the disinfectant is agitated for a certain time after the disinfectant is injected. オゾン処理は、第1および第2処理槽間を循環する廃水中にオゾンを供給して処理する方法であり、殺菌消毒剤による前処理は一方の第1処理槽で行い、その後循環させて所定時間オゾン処理を行うことを特徴とする請求項1乃至3のいずれかの項に記載の感染性廃棄物の処理方法。The ozone treatment is a method in which ozone is supplied to the waste water circulating between the first and second treatment tanks, and the pretreatment with the disinfectant is performed in one of the first treatment tanks and then circulated to a predetermined level. The method for treating infectious waste according to any one of claims 1 to 3, wherein a time ozone treatment is performed. 第1処理槽の前に廃水を随時受け付ける一時貯留槽を設け、該一時貯留槽から一定量だけ第1処理槽に移して処理することを特徴とする請求項1乃至4のいずかの項に記載の感染性廃棄物の処理方法。The temporary storage tank which receives wastewater at any time is provided in front of the first treatment tank, and a certain amount is transferred from the temporary storage tank to the first treatment tank for processing. A method for treating infectious waste as described in 1. 第1処理槽と、第2処理槽と、第1処理槽に殺菌消毒剤を注入する殺菌消毒剤注入手段と、前記第1処理槽に感染性廃棄物を含む廃水を供給する廃水供給手段と、廃水を第1処理槽と第2処理槽間を循環させる循環手段と、循環する廃水中にオゾンを供給するオゾン供給手段と、処理した廃水を放出する放出手段とを備えていることを特徴とする感染性廃棄物の処理装置。A first treatment tank, a second treatment tank, a sterilizing / disinfecting agent injection means for injecting a sterilizing / disinfecting agent into the first treatment tank, and a waste water supply means for supplying waste water containing infectious waste to the first treatment tank. And a circulation means for circulating the waste water between the first treatment tank and the second treatment tank, an ozone supply means for supplying ozone into the circulating waste water, and a discharge means for releasing the treated waste water. Infectious waste treatment equipment. 前記殺菌消毒剤は二酸化塩素である請求項6に記載の感染性廃棄物の処理装置。The infectious waste treatment apparatus according to claim 6, wherein the disinfectant is chlorine dioxide. 殺菌消毒剤が注入された第1処理槽内の廃水を攪拌する攪拌手段を備えている請求項6または7に記載の感染性廃棄物の処理装置。The infectious waste processing apparatus according to claim 6 or 7, further comprising stirring means for stirring the waste water in the first processing tank into which the sterilizing and disinfecting agent is injected. 廃水供給手段に設けられる異物除去手段と、前記殺菌消毒剤注入手段から分岐して殺菌消毒剤の一部を前記異物除去手段に対して注入する分岐通路とを備えている請求項6乃至8のいずれかの項に記載の感染性廃棄物の処理装置。The foreign matter removing means provided in the waste water supply means, and a branch passage branched from the sterilizing / disinfecting agent injecting means and injecting a part of the sterilizing disinfectant into the foreign matter removing means The infectious waste disposal apparatus according to any one of the items. 第1処理槽の前に設けられ感染性廃棄物の廃水を随時受け付ける一時貯留槽と、該一時貯留槽から廃水を所定量第1処理槽へ供給する供給手段とを備えている請求項6乃至9のいずれかの項に記載の感染性廃棄物の処理装置。A temporary storage tank provided in front of the first treatment tank and receiving waste water of infectious waste as needed, and a supply means for supplying a predetermined amount of waste water from the temporary storage tank to the first treatment tank. The infectious waste disposal apparatus according to any one of items 9 to 9. 一時貯留槽の前に廃水を受けるために設けられる受水槽と、該受水槽から前記一時貯留槽に廃水を供給する供給手段とを備えている請求項10に記載の感染性廃棄物の処理装置。The infectious waste treatment apparatus according to claim 10, further comprising: a water receiving tank provided to receive waste water before the temporary storage tank; and a supply unit that supplies waste water from the water receiving tank to the temporary storage tank. . 殺菌分解剤の前処理工程で二酸化塩素を活性化させる請求項2乃至5のいずれかの項に記載の感染性廃棄物の処理方法。The method for treating infectious waste according to any one of claims 2 to 5, wherein chlorine dioxide is activated in a pretreatment step of a sterilizing and decomposing agent. 殺菌分解剤による処理系に二酸化塩素を活性化させる活性化手段を配置した請求項7乃至11のいずれかの項に記載の感染性廃棄物の処理装置。The infectious waste treatment apparatus according to any one of claims 7 to 11, wherein an activating means for activating chlorine dioxide is disposed in a treatment system using a bactericidal decomposition agent.
JP2002149508A 2002-05-23 2002-05-23 Method and apparatus for treating infectious waste Expired - Fee Related JP3496094B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002149508A JP3496094B1 (en) 2002-05-23 2002-05-23 Method and apparatus for treating infectious waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002149508A JP3496094B1 (en) 2002-05-23 2002-05-23 Method and apparatus for treating infectious waste

Publications (2)

Publication Number Publication Date
JP2004024922A true JP2004024922A (en) 2004-01-29
JP3496094B1 JP3496094B1 (en) 2004-02-09

Family

ID=31170866

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2002149508A Expired - Fee Related JP3496094B1 (en) 2002-05-23 2002-05-23 Method and apparatus for treating infectious waste

Country Status (1)

Country Link
JP (1) JP3496094B1 (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1318319C (en) * 2005-07-01 2007-05-30 哈尔滨工业大学 Water treatment method capable of killing midge larva by ozone
KR101053132B1 (en) 2010-08-13 2011-08-02 해룡화학(주) Sewage water treatment and hvac system for hospital
JP2012161785A (en) * 2011-01-19 2012-08-30 Air Water Safety Service Inc Inactivation method of pathogenic microorganism
JP2012161786A (en) * 2011-01-19 2012-08-30 Air Water Safety Service Inc Apparatus for treating infectious waste liquid
CN111533354A (en) * 2020-05-12 2020-08-14 广德华东电子电路发展有限公司 Recovery process for electroplating wastewater
JP2021037502A (en) * 2019-08-27 2021-03-11 上田 孝雄 Treatment method and apparatus for infectious waste
WO2021251444A1 (en) * 2020-06-09 2021-12-16 株式会社エム・イー・エス Infectious drainage treatment system

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1318319C (en) * 2005-07-01 2007-05-30 哈尔滨工业大学 Water treatment method capable of killing midge larva by ozone
KR101053132B1 (en) 2010-08-13 2011-08-02 해룡화학(주) Sewage water treatment and hvac system for hospital
JP2012161785A (en) * 2011-01-19 2012-08-30 Air Water Safety Service Inc Inactivation method of pathogenic microorganism
JP2012161786A (en) * 2011-01-19 2012-08-30 Air Water Safety Service Inc Apparatus for treating infectious waste liquid
JP2016190237A (en) * 2011-01-19 2016-11-10 エア・ウォーター防災株式会社 Method for inactivation of pathogenic microorganisms
WO2013099333A1 (en) * 2011-12-27 2013-07-04 エア・ウォーター防災株式会社 Processing device for liquid infectious waste
WO2013099332A1 (en) * 2011-12-27 2013-07-04 エア・ウォーター防災株式会社 Method for inactivating pathogenic microorganism
JP2021037502A (en) * 2019-08-27 2021-03-11 上田 孝雄 Treatment method and apparatus for infectious waste
JP7093564B2 (en) 2019-08-27 2022-06-30 株式会社エム・イー・エス Infectious waste treatment equipment
CN111533354A (en) * 2020-05-12 2020-08-14 广德华东电子电路发展有限公司 Recovery process for electroplating wastewater
WO2021251444A1 (en) * 2020-06-09 2021-12-16 株式会社エム・イー・エス Infectious drainage treatment system

Also Published As

Publication number Publication date
JP3496094B1 (en) 2004-02-09

Similar Documents

Publication Publication Date Title
US5932171A (en) Sterilization apparatus utilizing catholyte and anolyte solutions produced by electrolysis of water
CN107921162B (en) Decontamination apparatus and method of decontaminating a load in a decontamination apparatus
US8025807B2 (en) Method for treating rinse water in decontamination devices
JP7093564B2 (en) Infectious waste treatment equipment
JP3496094B1 (en) Method and apparatus for treating infectious waste
KR100957757B1 (en) Suction system for dental clinic
JP4229363B2 (en) Water treatment equipment
US7351329B2 (en) Potable water station sanitizing system and method
CA2683061C (en) Method and apparatus for pathogenic and chemical reduction in fluid waste
JP2008036061A (en) Treatment method and apparatus of emission matter such as waste liquid in dead body treatment process
JP2011130783A (en) Sterilization washing apparatus
JP4472857B2 (en) Ultra high molecular mineral magnetic ionized water supply device
JP4249642B2 (en) Wastewater treatment method for water system of dialysis facility
JP2018202292A (en) Method of preventing proliferation of viable bacteria in pure water tank, and apparatus of producing pure water
JP3270509B2 (en) Bathtub hot water sterilization and purification equipment
US20230271859A1 (en) Infectious drainage treatment system
RU25845U1 (en) DEVICE FOR DISINFECTING LIQUID WASTE OF TREATMENT AND PREVENTIVE INSTITUTIONS
JPH10309309A (en) Method and device for sterilization while using ozone water
CN216303534U (en) Micro-acid disinfection system of purified water machine for preparation
JP2709717B2 (en) Flow path terminal contamination prevention device
JPH07256280A (en) Ozone sterilizing apparatus
KR20210020769A (en) Apparatus for circulating working fluid
JP2001149469A (en) Method of sterilizing and cleaning hemodialyzer and sterilizing and cleaning system
JP3405780B2 (en) Wastewater trap equipment
KR20010035309A (en) grain remnant agricultural drug and bacteria removing device and method

Legal Events

Date Code Title Description
TRDD Decision of grant or rejection written
R150 Certificate of patent or registration of utility model

Ref document number: 3496094

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20081128

Year of fee payment: 5

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20081128

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20091128

Year of fee payment: 6

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20101128

Year of fee payment: 7

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20101128

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20111128

Year of fee payment: 8

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20111128

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20121128

Year of fee payment: 9

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20131128

Year of fee payment: 10

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees