JP3026499U - Circulation type human waste treatment equipment - Google Patents

Circulation type human waste treatment equipment

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Publication number
JP3026499U
JP3026499U JP1995014621U JP1462195U JP3026499U JP 3026499 U JP3026499 U JP 3026499U JP 1995014621 U JP1995014621 U JP 1995014621U JP 1462195 U JP1462195 U JP 1462195U JP 3026499 U JP3026499 U JP 3026499U
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Japan
Prior art keywords
chamber
sewage
contact
water
toilet
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JP1995014621U
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Japanese (ja)
Inventor
弘三 大島
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オーシマシステム株式会社
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

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  • Biological Treatment Of Waste Water (AREA)
  • Water Treatment By Sorption (AREA)

Abstract

(57)【要約】 【課題】 汚水を低いランニングコストでもって中水道
として使用できる程BOD値を低くし且つ脱水脱臭し、
トイレ水として再使用できるようにした屎尿処理装置を
提供する。 【解決手段】 トイレ8の汚水を沈澱分離する沈澱分離
室3と、同沈澱分離室で沈澱分離された汚水の液体を流
入して多孔質の人工濾材13に接触させて嫌気的に分解
処理する嫌気ろ床室4と、同嫌気ろ床室で分解処理した
汚水を流入してかき殻を接触材17としてばっ気処理す
る接触ばっ気室5と、同接触ばっ気室でばっき処理され
た汚水を流入して吸着筒23中の活性炭の袋詰め24に
接触させて脱色・脱臭の高度浄化を行う仕上げ処理室6
と、同仕上げ処理室の浄化された水をトイレ8のタンク
に給水する給水管7とからなる。
(57) 【Abstract】 PROBLEM TO BE SOLVED: To lower the BOD value and to dehydrate and deodorize so that sewage can be used as tap water with a low running cost.
To provide a human waste treatment device that can be reused as toilet water. SOLUTION: A settling separation chamber 3 for settling and separating sewage in a toilet 8 and a liquid for sewage settling and separating in the settling separation chamber are introduced and brought into contact with a porous artificial filter medium 13 to anaerobically decompose. Anaerobic filter chamber 4, a contact aeration chamber 5 for injecting sewage decomposed in the anaerobic filter chamber and aerating it with a chaff as a contact material 17, and sewage aerated in the contact aeration chamber. Is introduced into the adsorption cylinder 23 and brought into contact with the activated carbon bag 24 in the adsorption cylinder 23 to perform advanced purification of decolorization and deodorization.
And a water supply pipe 7 for supplying purified water in the finishing treatment room to the tank of the toilet 8.

Description

【考案の詳細な説明】[Detailed description of the device]

【0001】[0001]

【考案の属する技術分野】[Technical field to which the device belongs]

本考案は、し尿、生活排水の汚水を浄化してその水分をトイレ水・消火用水・ 散水等の中水道のレベルの水として再使用するようにした循環式屎尿処理装置に 関する。家庭用の浄化槽、中小型の浄化槽、あるいは工事・イベントの臨時設置 用又は排水されない場所での浄化槽・公衆トイレでの使用に有用である。 The present invention relates to a circulating type human waste treatment device which purifies the wastewater of human waste and domestic wastewater and reuses the water as toilet water, water for fire extinguishing, water sprinkling and the like at the level of middle water. It is useful for household septic tanks, small and medium-sized septic tanks, temporary installation for construction / events, or septic tanks / public toilets in places where water is not drained.

【0002】[0002]

【従来の技術】[Prior art]

従来の浄化槽の処理は、沈殿分離し、その後人工ろ材を用いて接触ばっ気する 処理のものであった。これでは、充分なし尿の浄化ができず、浄化された水はB OD値も高く、PHも高い酸性であり、中水道レベルの水として利用できるもの ではなかった。 又、接触材としてかき殻を使用してばっ気処理を行い、浄化力を高くし且つ処 理水を中性に近づける浄化槽があるが、かき殻だけのばっ気処理では透明度・脱 色・脱臭が不充分であり、又かき殻を多数消耗するため、かき殻の補充回数が多 くなり、ランニングコストが高くなり、しかも浄化槽設置後の通常使用状態にな るまでの立ち上りに3カ月程度必要となるといった問題点があった。 Conventional septic tank treatment involves precipitation, separation, and then contact aeration using an artificial filter medium. In this case, the unpurified urine could not be sufficiently purified, and the purified water had a high BOD value and a high PH, and thus was not usable as water at the level of the water supply system. In addition, there is a septic tank that uses abacus as a contact material to perform aeration treatment to increase the purification power and bring the treated water closer to neutrality.However, aeration treatment using only a cask requires transparency, decolorization and deodorization. Is insufficient, and because many husks are exhausted, the number of times husks are replenished increases, running costs increase, and it takes about 3 months to start up before normal use after the septic tank is installed. There was a problem that became.

【0003】[0003]

【考案が解決しようとする課題】[Problems to be solved by the device]

本考案が解決しようとする課題は、従来のこれらの問題点を解消し、汚水処理 水のBOD値を低くし、処理水を中性化でき且つ処理水を脱色・脱臭して透明で 中水道として使用できる程度に高度に処理でき、又ランニングコストが廉価にで き、設置時の立ち上りが速く短日数で通常使用状態にでき、浄化槽の水を水洗ト イレの洗浄水として使用して水の循環使用を可能にした循環式屎尿処理装置を提 供することにある。 The problem to be solved by the present invention is to solve these conventional problems, to lower the BOD value of treated wastewater, to neutralize the treated water, and to decolorize and deodorize the treated water to make it transparent. It can be treated at a high level, can be used at a low cost, has a low running cost, can be quickly started up during installation, and can be put into normal use in a short period of time. The purpose is to provide a circulating type human waste treatment device that enables circulation.

【0004】[0004]

【課題を解決するための手段】[Means for Solving the Problems]

かかる課題を解決した本考案の構成は、 1) トイレ又は生活排水の汚水を沈澱分離する沈澱分離室と、同沈澱分離室で 沈澱分離された汚水の液体を流入して多孔質の人工濾材に接触させて嫌気的に分 解処理する嫌気ろ床室と、同嫌気ろ床室で分解処理した汚水を流入してかき殻を 接触材としてばっ気処理する接触ばっ気室と、同接触ばっ気室でばっき処理され た汚水を流入して活性炭に接触させて脱色・脱臭の高度浄化を行う仕上げ処理室 と、同仕上げ処理室の浄化された水をトイレのタンクに給水する給水路とからな る循環式屎尿処理装置 2) 嫌気ろ床室の多孔質の人工濾材として非晶質珪酸と結晶質珪酸とから多孔 質の粒状に成型された多孔質人工濾材を使用した前記1)記載の循環式屎尿処理 装置 にある。 本考案の多孔質の人工濾材としては、多孔性の汚物吸着力・浄化力のある粒状 ・塊状・板状の接触材を使用したタイプと、汚物浄化力・吸着力のある接触部材 を汚水の通過できる微細な間隙・通路を多数形成するように立体的に組み立て、 織り込み、網状体を多層化したタイプとがある。 The structure of the present invention which has solved such a problem is as follows: 1) A sedimentation chamber for precipitating and separating sewage from a toilet or domestic wastewater, and a sewage liquid that has been sedimented and separated in the sedimentation chamber to flow into a porous artificial filter medium. An anaerobic filter chamber that contacts and anaerobically disintegrates, a contact aeration chamber that injects sewage decomposed in the anaerobic filter chamber, and aerates with shavings as a contact material, and the same contact aeration It consists of a finishing treatment room where sewage treated in the room is made to flow in to contact activated carbon for advanced purification of decolorization and deodorization, and a water supply channel for supplying the purified water in the finishing treatment room to the toilet tank. Circulating type human waste treatment device 2) Circulation described in 1) above, wherein a porous artificial filter medium formed from amorphous silicic acid and crystalline silicic acid into a porous granular form is used as the porous artificial filter medium in the anaerobic filter bed chamber. It is located in the type of human waste treatment equipment. As the porous artificial filter material of the present invention, a type using a porous, granular, block-shaped or plate-like contact material having a filth adsorbing power / purifying power, and a contact member having a filth cleaning power / adsorbing power are used as sewage. There is a type in which three-dimensionally assembled, weaved, and meshed materials are multi-layered so as to form a large number of minute gaps and passages that can pass through.

【0005】[0005]

【考案の実施の形態】[Embodiment of device]

本考案では、トイレから排出されるし尿汚水又は台所等からの排出される生活 排水の汚水は、沈殿分離室に流入し、汚水の中の固形分・プラスチック・ゴム製 物品・金属片等は室床面に沈殿し、一部は液面に浮上し、汚水の成分は固液分離 される。固液分離された汚水の液体は嫌気ろ床室へ流入し、多孔質の人工濾材を 接触材として汚水は微生物によって嫌気的に分解処理される。嫌気ろ床室で嫌気 的に分解処理された汚水は、接触ばっ気室に流入し、かき殻を接触材として好気 的に分解処理される。 接触ばっ気室では、かき殻を接触材としてばっ気処理され、かき殻によって汚 水をアルカリ化して中性に近くし、しかもかき殻の多孔の表面で効率的に好気的 なばっ気処理で汚水をよく分解浄化する。 接触ばっ気室で分解浄化された汚水の水はBOD値を5PPM以下程度まで浄 化され、又PH7の近くまで中性化する。 その後接触ばっ気室の水は仕上げ処理室へ流入し、活性炭と接触し、水の脱色 ・脱臭を行い、透明で中性でBOD値5〜1PPM程度になり、トレイのタンク へ給水路を介して送られ、トイレ水として再使用される。 本考案では、かき殻を使うことで、高い分解浄化力と、中性化を得ることがで きるが、浄化を全部かき殻を使わないことで、かき殻の使用量を減らすことがで き、かき殻の消費を減らして補充の回数を減らす。又嫌気的なろ床浄化を加える ことで、分解浄化の質を高め、好気ばっ気では分解処理しにくいものも充分に分 解できるようにしている。 According to the present invention, wastewater discharged from the toilet or domestic wastewater discharged from the kitchen, etc. flows into the sedimentation separation chamber, and solids, plastics, rubber articles, metal pieces, etc. in the wastewater are stored in the room. It settles on the floor surface, part of which floats on the liquid surface, and the components of wastewater are solid-liquid separated. The liquid of the sewage that has been solid-liquid separated flows into the anaerobic filter chamber, and the sewage is anaerobically decomposed by microorganisms using the porous artificial filter medium as a contact material. The sewage that has been anaerobically decomposed in the anaerobic filter chamber flows into the contact aeration chamber and is aerobically decomposed using the chaff as a contact material. In the contact aeration chamber, the aeration process is performed by using the oyster shell as a contact material, and the sewage is alkalized by the oyster shell to make it close to neutral, and the aeration process is efficiently performed aerobically on the porous surface of the oyster shell. Well decomposes and purifies sewage. The wastewater that has been decomposed and purified in the contact aeration chamber is purified to a BOD value of 5 PPM or less, and is neutralized to near PH7. After that, the water in the contact aeration chamber flows into the finishing treatment chamber, comes into contact with the activated carbon, decolorizes and deodorizes the water, and becomes transparent and neutral with a BOD value of about 5 to 1 PPM, and passes through the water supply channel to the tank of the tray. Sent for reuse as toilet water. In the present invention, by using oyster shells, high decomposition and purification power and neutralization can be obtained, but by not using all oyster shells for purification, the usage amount of oyster shells can be reduced. , Reduce the consumption of husks and reduce the number of refills. Also, by adding anaerobic filter purification, the quality of decomposition and purification is improved so that even those that are difficult to decompose by aerobic aeration can be sufficiently decomposed.

【0006】[0006]

【実施例】【Example】

以下、本考案の実施例を図面に基づいて説明する。 図1〜3に示す実施例は、家庭用、公衆便所用の循環式屎尿処理装置の例であ る。 図1は実施例の横断面図、図2は図1のA−A断面図、図3は図1のB−B断 面図である。 図中、1は装置ケーシング、2はトイレからの屎尿の流入管、3は沈殿分離室 、4は嫌気ろ床室、5は接触ばっ気室、6は仕上げ処理室、7は同仕上げ処理室 の浄化された水をトレイ8のタンク9へ給水する給水路となる給水管、8はトイ レ、9は同トイレのタンク、10は沈殿分離室3と嫌気ろ床室4との区画壁、1 1は同区画壁の汚水溢流部、12は同汚水溢流部へ汚水を誘導し、浮遊物の流出 を防止するためのガイド、13非晶質珪酸と結晶質珪酸とを特殊加工した多孔質 の粒状物(商品名 日鉄鉱クリスバール)を使用した多孔質の人工濾材、14は 接触ばっ気質5の室下部に設けた散気管、15は同散気管へ空気を送る送気管、 16は同送気管に空気を圧送するブロワー、17はかき殻を多数袋詰めし、接触 ばっ気室5の中段に左右一対設けた接触材、18は嫌気ろ床室4と接触ばっ気室 5とを区画する区画壁、18は同区画壁の上端の低くなった溢流部、20は溢流 部19へ汚水をガイドし、浮遊物が流出しないようにするガイドプレート、21 は接触ばっ気室5と仕上げ処理室6との区画壁、22は同区画壁の溢流部、23 は仕上げ処理6の内部に立設した吸着筒、24は同吸着筒内に封入された活性炭 の袋詰め、25は吸着筒23に仕上げ処理室6の浄化された汚水を送り込むパイ プ、26は同パイプに仕上げ処理室6の水を汲み上げて送る循環ポンプ、27は 同循環ポンプ26の吸水管、28は仕上げ処理室6の浄化された水を汲み上げて トイレ8のタンク9へ給水する送水ポンプ、29は放流用に排水するための水中 ポンプ、30は同水中ポンプ29で汲み上げられて排水する放流管、31は基礎 、32は地盤である。 Hereinafter, embodiments of the present invention will be described with reference to the drawings. The embodiment shown in FIGS. 1 to 3 is an example of a circulating type human waste treatment apparatus for home and public toilets. 1 is a cross sectional view of the embodiment, FIG. 2 is a cross sectional view taken along the line AA of FIG. 1, and FIG. 3 is a cross sectional view taken along the line BB of FIG. In the figure, 1 is a device casing, 2 is an inflow pipe for human waste from a toilet, 3 is a sedimentation separation chamber, 4 is an anaerobic filtration chamber, 5 is a contact aeration chamber, 6 is a finishing treatment chamber, and 7 is a finishing treatment chamber. A water pipe serving as a water supply channel for supplying the purified water of the above to the tank 9 of the tray 8, 8 is a toilet, 9 is a tank of the toilet, 10 is a partition wall between the sedimentation separation chamber 3 and the anaerobic filter bed chamber 4, 11 sewage overflow part of the same partition wall, 12 guide sewage to the sewage overflow part to prevent outflow of suspended solids, 13 special processing of amorphous silicic acid and crystalline silicic acid Porous artificial filter medium using porous granular material (trade name: Nittite Krisvar), 14 is an air diffuser provided at the lower part of the chamber of contact aeration 5, 5 is an air supply pipe for sending air to the air diffuser, 16 Is a blower for sending air to the air supply tube, 17 is a bag of a large number of shaves, and the middle stage of the contact aeration chamber 5 A pair of left and right contact members, 18 is a partition wall for partitioning the anaerobic filter chamber 4 and the contact aeration chamber 5, 18 is a lower overflow portion of the upper end of the partition wall, and 20 is an overflow portion 19. A guide plate that guides sewage and prevents floating substances from flowing out, 21 is a partition wall between the contact aeration chamber 5 and the finishing treatment chamber 6, 22 is an overflow portion of the same partition wall, and 23 is an inside of the finishing treatment 6. Adsorption cylinder standing upright, 24 is a bag of activated carbon sealed in the adsorption cylinder, 25 is a pipe for feeding the purified waste water of the finishing treatment chamber 6 to the adsorption cylinder 23, and 26 is a pipe for finishing treatment chamber 6 is a circulation pump for pumping and sending water, 27 is a water suction pipe of the same circulation pump 26, 28 is a water pump for pumping purified water in the finishing treatment chamber 6 and supplying it to the tank 9 of the toilet 8, 29 is for discharge Submersible pump for draining, 30 is submersible pump 2 Discharge tube for draining pumped up, the 31 foundation 32 is ground.

【0007】 この実施例では、トイレ8から排出される屎尿及び洗い水は流入管2から沈澱 分離室3へ流入し、屎尿の中の固体部分・ゴム製品・プラスチック製品等は沈降 し、下部に集積し、一部は液面に浮遊する。又汚水の一部は微生物で分解し始め る。沈殿分離室3で固液分離した汚水の液分は、ガイド12の内側に移動し、浮 遊した固体部分が入らないようにして区画壁10の上端の低くなった汚水溢流部 11から嫌気ろ床室4へ移流する。嫌気ろ床室4に流入した汚水は非晶質珪酸と 結晶質珪酸とを特殊加工した多孔質の粒状物である日鉄クリスバール(商標名) に接触し、同日鉄クリスバールに繁殖した嫌気性菌によって効果的によく分解さ れる。 よく嫌気的に分解された汚水は、区画壁18の溢流部19から接触ばっ気室5 へ流入する。接触ばっ気室5では下方の散気管14から空気が気泡状に送り込ま れ、接触ばっ気室5内に汚水の対流を生起するとともに、汚水を空気と接触材1 7のかき殻の好気性菌と接触させ、微生物的な分解と空気による分散攪拌によっ て更によく分解させる。これによって大略5BOD程度まで汚水は浄化されると ともにかき殻によってアルカリ化され、略PH7の中性の状態になる。 かなり浄化された接触ばっ気室5内の汚水は、区画壁21の溢流部22から仕 上げ処理室6へ流入する。 仕上げ処理室6に流入した汚水は、循環ポンプ26によって吸水管27から吸 引され、パイプ23を介して吸着筒23の下方へ強制的に送り込まれる。吸着筒 23内に送り込まれた水はその内部に袋詰め24された活性炭によって、脱色・ 脱臭・除粒されてその上部から仕上げ処理室6内へ戻され、再び吸水管27に吸 引されて活性炭を通過する。これをくり返すことで仕上げ処理室6内の水は更に 脱臭・脱色されBOD値5以下にされ、高く浄化されたものとされる。中水道と して使用できる程度浄化された仕上げ処理室6の水は、送水ポンプ28によって 汲み上げられて、給水管7を介してトイレ8のタンク9へ送られ、トイレ水とし て使用される。更に、仕上げ処理室6の水は、水中ポンプ29によって汲み上げ られ、庭水・消火用水にも使用され、水が多くなれば河川・下水へ放流できるよ うにしている。又、かき殻を接触材17として使用することで屎尿処理の開始の 浄化力の立ち上りが早期になされ、設置時の立ち上りが短日数でできる。又かき 殻と人工濾材の二種の接触材を使用することで、かき殻の消費量を少なくし、ラ ンニングコストを廉価にできるようにした。更に、浄化した水は、トイレ8のタ ンク9へ戻されて中水道として最利用できるのでトイレの水の外部からの給水量 をかなり少なくでき、水の消費も少なくできる。更に給水設備、排水設備のない 所、例えば土木建設現場、公園、農地、山奥地でも容易に設置できるものとした 。In this embodiment, the human waste and the wash water discharged from the toilet 8 flow into the sedimentation separation chamber 3 through the inflow pipe 2, and the solid parts, rubber products, plastic products, etc. in the human waste settle down to the lower part. Accumulate, and a part floats on the liquid surface. Also, part of the wastewater begins to decompose by microorganisms. The sewage liquid that has undergone solid-liquid separation in the settling separation chamber 3 moves to the inside of the guide 12 and prevents the floating solids from entering the sewage overflow part 11 at the upper end of the partition wall 10 which is anaerobic. Transfer to filter bed room 4. The sewage flowing into the anaerobic filter chamber 4 comes into contact with Nittetsu Krisvar (trademark), which is a porous granular material obtained by specially processing amorphous silicic acid and crystalline silicic acid, and the anaerobic breeding on the same day iron krisvar. It is effectively and well decomposed by sex bacteria. The well-anaerobically decomposed sewage flows into the contact aeration chamber 5 from the overflow portion 19 of the partition wall 18. In the contact aeration chamber 5, air is blown into the contact aeration chamber 5 in the form of bubbles from the lower air diffuser 14 to cause convection of sewage in the contact aeration chamber 5, and the sewage is aerated with the aerobic bacteria of the cask of the contact material 17. To further decompose by microbial decomposition and dispersion stirring with air. As a result, the sewage is purified to about 5 BOD, and at the same time, it is alkalized by the chaff and becomes approximately PH7 neutral. The wastewater in the contact aeration chamber 5 which has been considerably purified flows into the finishing treatment chamber 6 through the overflow portion 22 of the partition wall 21. The sewage that has flowed into the finishing treatment chamber 6 is sucked from the water suction pipe 27 by the circulation pump 26, and is forcibly sent below the adsorption cylinder 23 via the pipe 23. The water sent into the adsorption cylinder 23 is decolorized, deodorized, and grain-removed by the activated carbon packed in the inside of the adsorption cylinder 23, returned to the inside of the finishing treatment chamber 6 from the upper portion, and again sucked by the water absorption pipe 27. Pass through activated carbon. By repeating this, the water in the finishing treatment chamber 6 is further deodorized and decolorized to a BOD value of 5 or less, and is highly purified. The water in the finishing treatment chamber 6 that has been purified to the extent that it can be used as tap water is pumped up by the water supply pump 28, sent to the tank 9 of the toilet 8 via the water supply pipe 7, and used as toilet water. Further, the water in the finishing treatment room 6 is pumped up by the submersible pump 29 and is also used for garden water and fire extinguishing water so that when the water becomes large, it can be discharged to rivers and sewers. In addition, by using the oyster shell as the contact material 17, the purification power at the start of human waste treatment can be quickly raised, and the startup at the time of installation can be done in a short number of days. In addition, by using two types of contact materials, the oyster shell and the artificial filter medium, the consumption of the oyster shell can be reduced and the running cost can be reduced. Further, since the purified water is returned to the tank 9 of the toilet 8 and can be reused as the tap water, the amount of water supplied from the outside of the toilet water can be considerably reduced and the water consumption can be reduced. In addition, it can be easily installed in places without water supply and drainage facilities, such as civil engineering construction sites, parks, farmland, and mountainous areas.

【0008】[0008]

【考案の効果】[Effect of device]

以上の様に、本考案によれば、多孔質の人工濾材による嫌気ろ床による分解と 、かき殻による接触ばっ気と、活性炭を用いた高度処理とを組み合せることによ って、汚水を中水道として使用できるまで浄化でき、しかもこれをトイレの水と して再利用することで、トイレ水の消費を少なくでき節水効果があるとともに、 放流することなく処理できることとなり、河川の汚染・屎尿汲み取りの量を大巾 に減らすことができる。更に、排水できない場所、又は大量の給水を受けること ができにくい場所、例えば工事現場、公園、イベント会場、山奥地等でも使用で きるものとしている。 As described above, according to the present invention, by combining the decomposition by the anaerobic filter bed with the porous artificial filter medium, the contact aeration by the chaff, and the advanced treatment with the activated carbon, the wastewater is removed. By purifying it until it can be used as tap water, and by reusing it as toilet water, it can reduce the consumption of toilet water, have a water-saving effect, and treat it without discharging it, resulting in river pollution and human waste. The amount of pumping can be greatly reduced. In addition, it can be used in places where it is not possible to drain water or where it is difficult to receive a large amount of water, such as construction sites, parks, event venues, and mountainous areas.

【図面の簡単な説明】[Brief description of drawings]

【図1】実施例の横断面図である。FIG. 1 is a cross-sectional view of an example.

【図2】図1のA−A断面図である。FIG. 2 is a sectional view taken along line AA of FIG.

【図3】図1のB−B断面図である。FIG. 3 is a sectional view taken along line BB of FIG. 1;

【符号の説明】[Explanation of symbols]

1 装置ケーシング 2 流入管 3 沈殿分離室 4 嫌気ろ床室 5 接触ばっ気室 6 仕上げ処理室 7 給水管 8 トイレ 9 タンク 10 区画壁 11 汚水溢流部 12 ガイド 13 人工濾材 14 散気管 15 送気管 16 ブロワー 17 接触材 18 区画壁 19 溢流部 20 ガイドプレート 21 区画壁 22 溢流部 23 吸着筒 24 袋詰め 25 パイプ 26 循環ポンプ 27 吸水管 28 送水ポンプ 29 水中ポンプ 30 放流管 31 基礎 32 地盤 1 Equipment casing 2 Inflow pipe 3 Precipitation separation chamber 4 Anaerobic floor chamber 5 Contact aeration chamber 6 Finishing treatment chamber 7 Water supply pipe 8 Toilet 9 Tank 10 Partition wall 11 Sewage overflow 12 Guide 13 Artificial filter 14 Air diffuser 15 Air pipe 16 Blower 17 Contact material 18 Partition wall 19 Overflow part 20 Guide plate 21 Partition wall 22 Overflow part 23 Adsorption cylinder 24 Bag packing 25 Pipe 26 Circulation pump 27 Water absorption pipe 28 Water pump 29 Underwater pump 30 Discharge pipe 31 Foundation 32 Ground

Claims (2)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 トイレ又は生活排水の汚水を沈澱分離す
る沈澱分離室と、同沈澱分離室で沈澱分離された汚水の
液体を流入して多孔質の人工濾材に接触させて嫌気的に
分解処理する嫌気ろ床室と、同嫌気ろ床室で分解処理し
た汚水を流入してかき殻を接触材としてばっ気処理する
接触ばっ気室と、同接触ばっ気室でばっき処理された汚
水を流入して活性炭に接触させて脱色・脱臭の高度浄化
を行う仕上げ処理室と、同仕上げ処理室の浄化された水
をトイレのタンクに給水する給水路とからなる循環式屎
尿処理装置。
1. A settling separation chamber for settling and separating sewage from toilets or domestic wastewater, and a sewage liquid that has been settled and separated in the settling separation chamber is introduced and brought into contact with a porous artificial filter medium to anaerobically decompose it. The anaerobic filter chamber, the contact aeration chamber that injects the sewage decomposed in the anaerobic filter chamber to perform aeration using the chaff as a contact material, and the sewage that has been treated in the contact aeration chamber flows in. A circulating type human waste treatment system consisting of a finishing treatment room that performs high-level purification of decolorization and deodorization by contacting with activated carbon, and a water supply channel that supplies purified water in the finishing treatment room to the tank of the toilet.
【請求項2】 嫌気ろ床室の多孔質の人工濾材として非
晶質珪酸と結晶質珪酸とから多孔質の粒状に成型された
多孔質人工濾材を使用した請求項1記載の循環式屎尿処
理装置。
2. The circulating human waste treatment according to claim 1, wherein the porous artificial filter medium in the anaerobic filter chamber is a porous artificial filter medium formed of amorphous silicic acid and crystalline silicic acid into a porous granular form. apparatus.
JP1995014621U 1995-12-29 1995-12-29 Circulation type human waste treatment equipment Expired - Lifetime JP3026499U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1995014621U JP3026499U (en) 1995-12-29 1995-12-29 Circulation type human waste treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1995014621U JP3026499U (en) 1995-12-29 1995-12-29 Circulation type human waste treatment equipment

Publications (1)

Publication Number Publication Date
JP3026499U true JP3026499U (en) 1996-07-12

Family

ID=43161655

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1995014621U Expired - Lifetime JP3026499U (en) 1995-12-29 1995-12-29 Circulation type human waste treatment equipment

Country Status (1)

Country Link
JP (1) JP3026499U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3438172B2 (en) 2000-01-20 2003-08-18 宮澤鋼業株式会社 Toilet sewage purification circulation method and apparatus
JPWO2006057287A1 (en) * 2004-11-25 2008-06-05 楠 敏明 Activated sludge production inhibitor

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3438172B2 (en) 2000-01-20 2003-08-18 宮澤鋼業株式会社 Toilet sewage purification circulation method and apparatus
JPWO2006057287A1 (en) * 2004-11-25 2008-06-05 楠 敏明 Activated sludge production inhibitor

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