JPH07313584A - Medical waste disposal facility - Google Patents
Medical waste disposal facilityInfo
- Publication number
- JPH07313584A JPH07313584A JP6108077A JP10807794A JPH07313584A JP H07313584 A JPH07313584 A JP H07313584A JP 6108077 A JP6108077 A JP 6108077A JP 10807794 A JP10807794 A JP 10807794A JP H07313584 A JPH07313584 A JP H07313584A
- Authority
- JP
- Japan
- Prior art keywords
- solid material
- tank
- waste
- dust collector
- absorbing liquid
- 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.)
- Pending
Links
Landscapes
- Gasification And Melting Of Waste (AREA)
- Apparatus For Disinfection Or Sterilisation (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】この発明は病院等の医療施設に付
帯した医療廃棄物の処理施設に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a medical waste treatment facility incidental to a medical facility such as a hospital.
【0002】[0002]
【発明が解決しようとする課題】従来、病院等で発生す
る医療廃棄物は外部の専門業者に任せて処理していた。Conventionally, medical waste generated in hospitals and the like has been handled by an external specialist.
【0003】しかし、医療廃棄物中には感染性のものが
含まれており、法規の改正により、発生源での処理が義
務づけられることとなる。[0003] However, medical waste contains infectious substances, and the amendment of laws and regulations requires treatment at the source.
【0004】医療廃棄物を焼却処理するには燃焼温度8
00℃以上に保ち、排煙、排水を完全に無公害化しなけ
ればならない。また、例えば廃棄物の発生量が2t/日
程度の規模の医療施設で、上記の条件を満足する処理施
設は広い処理スペースが必要となり、病院等の医療施設
を単位とする施設としては少なからぬ負担となる。Combustion temperature of 8 for incineration of medical waste
It is necessary to keep the temperature above 00 ° C and to completely eliminate smoke and wastewater pollution. In addition, for example, in a medical facility where the amount of waste generated is about 2 tons / day, a processing facility that satisfies the above conditions requires a large processing space, and is not a small number of medical facilities such as hospitals. It will be a burden.
【0005】この発明は上記問題点の解消を図ったもの
である。その目的は、比較的に狭い敷設に設置し、作業
能率よく運転でき、排煙、排水を完全に無公害化して焼
却処理できる医療施設に付帯した医療廃棄物の処理施設
を提案するにある。The present invention is intended to solve the above problems. The purpose is to propose a medical waste treatment facility attached to a medical facility which can be installed in a relatively narrow laying, can be operated efficiently, and can completely incinerate smoke and wastewater without incineration.
【0006】[0006]
【課題を解決するための手段】この医療廃棄物処理施設
は医療施設に付帯したものであって、廃棄物を焼却する
1次、2次燃焼室、気・液接触により燃焼ガスから分散
質を吸収除去する集塵機、吸収液から固形物を除去する
固形物除去装置および吸収液の曝気処理槽を含む排水処
理槽を順に設けてなることを特徴となる。[Means for Solving the Problems] This medical waste treatment facility is incidental to a medical facility. It is a primary combustion chamber for incinerating waste, a secondary combustion chamber, and dispersoids from combustion gas by gas-liquid contact. It is characterized in that a dust collector for absorbing and removing, a solid matter removing device for removing solid matter from the absorbing liquid, and a wastewater treatment tank including an aeration treatment tank for the absorbing liquid are sequentially provided.
【0007】[0007]
【実施例】以下、実施例の処理施設および処理プロセス
を図1に示すフローシートにより説明する。EXAMPLES The processing facilities and processing processes of the examples will be described below with reference to the flow sheet shown in FIG.
【0008】1,2は上下に連なった1次燃焼室および
2次燃焼室であり、それぞれバーナーを備え、800℃
まで昇温し感染性廃棄物の完全滅菌が可能となしてあ
る。1次燃焼室1の1側面に投入口3を設け、台車等の
投入装置4を用い廃棄物を投入し、燃焼室で発生する灰
は灰受台車5で受けて外部に搬出する。Reference numerals 1 and 2 are a primary combustion chamber and a secondary combustion chamber, which are vertically connected, each equipped with a burner, and 800 ° C.
It is possible to completely sterilize infectious waste by raising the temperature to. An input port 3 is provided on one side surface of the primary combustion chamber 1, waste is input using an input device 4 such as a trolley, and ash generated in the combustion chamber is received by an ash receiving trolley 5 and carried out to the outside.
【0009】2次燃焼室2から上方に伸びる排気管6内
を流れる燃焼ガスは熱交換機7において、水と熱交換し
降温した後、集塵機8に入る。集塵機8に薬液タンク群
9の苛性ソーダ液を給水槽10の水で濃度調整して霧状
に噴出して、燃焼ガスと気・液接触させてガス中の粉
塵、ミスト、溶解性成分等の分散質を吸収、除去する。The combustion gas flowing in the exhaust pipe 6 extending upward from the secondary combustion chamber 2 exchanges heat with water in the heat exchanger 7 to lower the temperature, and then enters the dust collector 8. The concentration of the caustic soda solution in the chemical solution tank group 9 is adjusted to the dust collector 8 with the water in the water supply tank 10 and ejected in a mist form to bring the gas and liquid into contact with the combustion gas to disperse dust, mist, soluble components, etc. Absorb and remove quality.
【0010】塩化ビニル系樹脂製の廃棄物が発生する塩
酸等はここで吸収液に吸収される。Hydrochloric acid or the like generated from waste made of vinyl chloride resin is absorbed by the absorbing liquid here.
【0011】集塵機8を出た燃焼ガスは排風機11を通
り、煙突12から大気中に放出する。分散質を吸収した
吸収液は中和槽13、流量調整槽14を経由して固形物
の除去装置に送り込まれる。The combustion gas leaving the dust collector 8 passes through the exhaust fan 11 and is discharged from the chimney 12 into the atmosphere. The absorbing liquid that has absorbed the dispersoid is sent to the solid substance removing device via the neutralization tank 13 and the flow rate adjusting tank 14.
【0012】除去装置は直列する第1、第2反応槽1
5,16、熟成槽17および加圧浮上槽18からなり、
薬液タンク群9から送られるポリ塩化アルミニウム溶液
(PAC)、苛性ソーダ溶液、高分子凝集剤等を添加し
て、固形物の凝集を図り、加圧浮上槽において圧気を噴
出させて加圧、浮上せしめ、レーキ19により捕集し、
汚泥貯留槽20に送り込む。固形物の汚泥は脱水機21
で脱水した後排出する。The removing device is a series of first and second reaction tanks 1.
5, 16, aging tank 17 and pressure floating tank 18,
Add polyaluminum chloride solution (PAC), caustic soda solution, polymer coagulant, etc. sent from the chemical tank group 9 to agglomerate solids and pressurize and float by ejecting pressured air in the pressure flotation tank. , Collected by rake 19,
It is sent to the sludge storage tank 20. Solid sludge is dehydrator 21
Drain after dehydration.
【0013】固形物を除去した吸収液は第1、第2曝気
槽22,23で曝気処理し、必要に応じ薬液タンク群9
から微生物繁殖用の栄養剤を添加して、BOD値の低下
を促進する。なお、図において24は送風機である。こ
の工程で発生する活性汚泥等の固形物を沈澱槽25で除
去し、処理水は濾過ポンプ槽26を経由して砂濾過器2
7で処理し、逆洗水槽28から系外に放出する。微量の
重金属類が残存する場合はキレート塔29で除去する。
生物処理装置内で沈澱槽25で発生した汚泥も汚泥貯留
槽20へ導かれる。The absorption liquid from which the solid matter has been removed is aerated in the first and second aeration tanks 22 and 23, and if necessary, the chemical liquid tank group 9
A nutrient for microbial propagation is added to promote the reduction of BOD value. In the figure, 24 is a blower. Solid matter such as activated sludge generated in this step is removed in the settling tank 25, and the treated water passes through the filtration pump tank 26 and the sand filter 2
It is treated with No. 7 and discharged from the backwash water tank 28 to the outside of the system. If a trace amount of heavy metals remains, they are removed by the chelate tower 29.
The sludge generated in the sedimentation tank 25 in the biological treatment device is also guided to the sludge storage tank 20.
【0014】図2に上記施設の建屋内の配置を示す。3
階建ての建物の2階部分に1次、2次燃焼室1,2、3
階に熱交換器7、および集塵機8、1階に流量調整槽1
4および曝気槽22等の排水処理槽が施設してある。廃
棄物は投入口3から投入し、焼却後の灰は灰受台車5で
受け、灰出コンテナで系外に搬出する。FIG. 2 shows the layout of the inside of the facility. Three
Primary and secondary combustion chambers 1, 2 and 3 on the second floor of a one-story building
Heat exchanger 7 and dust collector 8 on the first floor, flow rate adjustment tank 1 on the first floor
4 and the aeration tank 22 are installed as wastewater treatment tanks. The waste is put in through the inlet 3, the ash after incineration is received by the ash carrier 5 and is carried out of the system by the ash container.
【0015】[0015]
【作用】この発明は以上の構成からなる。この施設は 1次、2次燃焼室を備え、容易に焼却温度を800
℃以上となし、感染性廃棄物の完全滅菌処理ができる。The present invention is constructed as described above. This facility is equipped with primary and secondary combustion chambers and can easily incinerate at a temperature of 800.
It can be completely sterilized from infectious waste by keeping the temperature above ℃.
【0016】 燃焼ガスは集塵機において気・液接触
により粉塵、ミスト、溶解性成分等を吸収、除去するこ
とにより、規制値以下に浄化して放出できる。The combustion gas can be purified and released below a regulated value by absorbing and removing dust, mist, soluble components and the like by contacting gas and liquid in a dust collector.
【0017】 吸収液は固形物除去装置および曝気処
理槽等の排水処理槽で、化学的、生物化学的、物理化学
的に排水処理し、規制値以下に浄化して排出できる。The absorbing liquid can be chemically, biochemically or physicochemically treated with wastewater in a wastewater treatment tank such as a solid matter removing device and an aeration treatment tank, and purified to a regulated value or less and discharged.
【0018】この処理施設を、1次、2次燃焼室を設置
した階を中心にしてその上階に集塵機、その下階に固形
物除去装置および吸収液の排水処理槽を配置すると、広
い敷地を占有することなく施設を立体的に構築ができ、
また、最も人力を要する廃棄物の投入および灰の搬出作
業を、排気および排水処理工程の階と異なる階で行なう
ので、他の工程に制約されず作業の能率化を図ることが
できる。If a dust collector is arranged on the upper floor of the treatment facility and a solid substance removing device and a waste water treatment tank for absorbing liquid are arranged on the lower floor of the floor with the primary and secondary combustion chambers installed, it is a large site. The facility can be constructed three-dimensionally without occupying
Further, since the most labor-intensive work of inputting waste and carrying out ash is performed on a floor different from the floor of the exhaust and wastewater treatment steps, the efficiency of the work can be improved without being restricted by other steps.
【0019】[0019]
【発明の効果】この処理施設は以上の通りであり、広い
面積を占有することなく、病院等の医療施設に付帯して
建設でき、作業能率よく廃棄物を焼却処理し、排気、排
水を規制値以下に浄化して排出することが可能となる。EFFECTS OF THE INVENTION This treatment facility is as described above, and it can be attached to a medical facility such as a hospital without occupying a large area, can incinerate waste with good work efficiency, and can regulate exhaust and drainage. It becomes possible to purify the gas below the specified value and discharge it.
【図1】実施例の処理施設の工程図である。FIG. 1 is a process diagram of a processing facility according to an embodiment.
【図2】3階建ての建屋に設置した処理施設の一部断面
で示す側面図である。FIG. 2 is a side view showing a partial cross section of a treatment facility installed in a three-story building.
1,2…第1、第2次燃焼室、3…投入口、4…投入装
置、5…灰受台車、6…排気管、7…熱交換機、8…集
塵機、9…薬液タンク群、10…給水槽、11…排風
機、12…煙突、13…流量調整槽、14…固形物除去
装置、15,16…第1、第2反応槽、17…熟成槽、
18…加圧浮上槽、19…レーキ、20…汚泥貯留槽、
21…脱水機、22,23…第1、第2曝気槽、24…
送風機、25…沈澱槽、26…濾過ポンプ槽、27…砂
濾過器、28…逆洗水槽、29…キレート塔。1, 2 ... First and second combustion chambers, 3 ... Charging port, 4 ... Charging device, 5 ... Ash carrier, 6 ... Exhaust pipe, 7 ... Heat exchanger, 8 ... Dust collector, 9 ... Chemical liquid tank group, 10 ... water supply tank, 11 ... blower, 12 ... chimney, 13 ... flow rate adjusting tank, 14 ... solids removing device, 15,16 ... first and second reaction tanks, 17 ... aging tank,
18 ... Pressurized floating tank, 19 ... Rake, 20 ... Sludge storage tank,
21 ... Dehydrator, 22, 23 ... First and second aeration tanks, 24 ...
Blower, 25 ... Settling tank, 26 ... Filtration pump tank, 27 ... Sand filter, 28 ... Backwash water tank, 29 ... Chelate tower.
フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 F23G 7/00 ZAB A (72)発明者 高山 善治 愛知県名古屋市新栄町2丁目14番地 鹿島 建設株式会社名古屋支店内 (72)発明者 浅村 和夫 愛知県名古屋市新栄町2丁目14番地 鹿島 建設株式会社名古屋支店内 (72)発明者 川田 一士 愛知県名古屋市新栄町2丁目14番地 鹿島 建設株式会社名古屋支店内 (72)発明者 藤田 啓介 愛知県豊明市栄町南館12番地の1Continuation of front page (51) Int.Cl. 6 Identification number Office reference number FI Technical display location F23G 7/00 ZAB A (72) Inventor Zenji Takayama 2-14 Shineicho, Aichi Prefecture Nagoya Kashima Construction Co., Ltd. Nagoya In branch (72) Inventor Kazuo Asamura 2-14 Shineicho, Nagoya, Aichi Kashima Construction Co., Ltd.In Nagoya branch (72) Inventor Kazushi Kawada 2-14 Shineicho, Nagoya, Aichi Kashima Construction Co., Ltd.Nagoya branch (72) Inventor Keisuke Fujita 1 of 12 Sakaemachi South Building, Toyoake City, Aichi Prefecture
Claims (2)
であって、廃棄物を焼却する1次、2次燃焼室、気・液
接触により燃焼ガスから分散質を吸収除去する集塵機、
吸収液から固形物を除去する固形物除去装置および吸収
液の曝気処理槽を含む排水処理槽を順に設けてなること
を特徴とする医療廃棄物処理施設。1. A medical waste treatment facility incidental to a medical facility, in which primary and secondary combustion chambers for incinerating waste, a dust collector for absorbing and removing dispersoids from combustion gas by gas / liquid contact,
A medical waste treatment facility comprising a solid matter removing device for removing solid matter from an absorbent and a wastewater treatment tank including an aeration treatment tank for the absorbent in order.
し、その上階に集塵機、その下階に固形物除去装置およ
び吸収液の排水処理槽を配してなることを特徴とする請
求項1記載の医療廃棄物処理施設。2. A center of a floor where primary and secondary combustion chambers are installed, a dust collector is arranged on an upper floor thereof, and a solid substance removing device and a waste water treatment tank for absorbing liquid are arranged on a lower floor thereof. The medical waste treatment facility according to claim 1.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6108077A JPH07313584A (en) | 1994-05-23 | 1994-05-23 | Medical waste disposal facility |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6108077A JPH07313584A (en) | 1994-05-23 | 1994-05-23 | Medical waste disposal facility |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH07313584A true JPH07313584A (en) | 1995-12-05 |
Family
ID=14475297
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6108077A Pending JPH07313584A (en) | 1994-05-23 | 1994-05-23 | Medical waste disposal facility |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07313584A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7361263B2 (en) | 2002-12-03 | 2008-04-22 | Sanyo Electric Co., Ltd. | Water treatment apparatus and method |
-
1994
- 1994-05-23 JP JP6108077A patent/JPH07313584A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7361263B2 (en) | 2002-12-03 | 2008-04-22 | Sanyo Electric Co., Ltd. | Water treatment apparatus and method |
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Legal Events
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