JP4874687B2 - Circulating flush toilet - Google Patents

Circulating flush toilet Download PDF

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JP4874687B2
JP4874687B2 JP2006089743A JP2006089743A JP4874687B2 JP 4874687 B2 JP4874687 B2 JP 4874687B2 JP 2006089743 A JP2006089743 A JP 2006089743A JP 2006089743 A JP2006089743 A JP 2006089743A JP 4874687 B2 JP4874687 B2 JP 4874687B2
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貴弘 藪下
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株式会社オリエント・エコロジー
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Description

本発明は、被処理水を移送する移送手段を備え便器の下方に配設された受水槽と、受水槽から移送された被処理水を浄化して排出する浄化装置と、受水槽より上方に配設され浄化装置から導入した被処理水を少なくとも使用時に受水槽に流下させる流下手段を備えた送水槽と、からなる循環水路が構成され、この循環水路内に被処理水を循環送水し浄化処理する循環式水洗トイレに関する。   The present invention includes a water receiving tank provided with a transfer means for transferring the water to be treated, disposed below the toilet bowl, a purification device for purifying and discharging the water to be treated transferred from the water receiving tank, and above the water receiving tank. A circulating water channel comprising a water supply tank provided with a flow-down means for flowing down the treated water introduced from the purification device to the water receiving tank at least in use is constituted, and the treated water is circulated and purified in this circulating water channel It relates to a circulating flush toilet.

被処理水としてのトイレ汚水を浄化処理する従来の循環式水洗トイレとして、例えば、公知の浄化装置と、オゾン処理手段とを組合せた循環水路を構成し、この循環水路に被処理水を循環送水し浄化処理する循環式水洗トイレがある(例えば、特許文献1参照)。   As a conventional circulating flush toilet that purifies toilet sewage as treated water, for example, a circulating water channel combining a known purification device and ozone treatment means is constructed, and the treated water is circulated and sent to this circulating water channel There is a circulating flush toilet that performs purification treatment (see, for example, Patent Document 1).

特開2005−60981号公報(第2頁、第2図)Japanese Patent Laying-Open No. 2005-60981 (page 2, FIG. 2)

しかしながら、特許文献1にあっては、被処理水が、浄化装置及びオゾン処理手段を含め、単一の循環水路を循環移送して常時浄化処理されるため、オゾン処理の要不要に関わらず、被処理水の全量についてオゾン処理手段の通過とともにオゾン処理を行っており、人体に悪影響を及ぼす虞のあるオゾンが常時発生し危険性を伴っていた。   However, in Patent Document 1, since the water to be treated is constantly purified by circulating and transporting a single circulation channel including the purification device and the ozone treatment means, regardless of whether ozone treatment is necessary or not, The entire amount of water to be treated was subjected to ozone treatment along with the passage of the ozone treatment means, and ozone that might adversely affect the human body was constantly generated and accompanied by danger.

本発明は、このような問題点に着目してなされたもので、人体に悪影響を及ぼす虞のあるオゾン処理を適宜使用して被処理水を安全に浄化処理できる循環式水洗トイレを提供することを目的とする。   The present invention has been made paying attention to such problems, and provides a circulating flush toilet that can safely purify treated water using ozone treatment that may adversely affect the human body as appropriate. With the goal.

上記課題を解決するために、本発明の請求項1に記載の循環式水洗トイレは、被処理水を移送する移送手段を備え便器の下方に配設された受水槽と、該受水槽から移送された被処理水を浄化して排出する浄化装置と、前記受水槽より上方に配設され前記浄化装置から導入した被処理水を少なくとも使用時に前記受水槽に流下させる流下手段を備えた送水槽と、からなる第1循環水路が構成され、該第1循環水路内に被処理水を循環送水し浄化処理する循環式水洗トイレであって、
前記第1循環水路の所定箇所に設けられ、少なくとも一部の被処理水を分岐可能とする分岐管と、該分岐管に接続され、被処理水をオゾン処理するオゾン処理手段と、該オゾン処理手段でオゾン処理された被処理水を前記第1循環水路に供給する供給管と、からなる第2循環水路が構成され、該第2循環水路の所定箇所に、前記第1循環水路内の被処理水を前記第2循環水路内に導入する導入手段が設けられており、
予め特定された特定時間帯内において、前記流下手段が被処理水を前記送水槽から前記受水槽に強制的に流下させるとともに、前記導入手段が前記第1循環水路内の被処理水を前記第2循環水路内に導入することを特徴としている。
この特徴によれば、浄化装置が構成された第1循環水路と、オゾン処理手段が構成された第2循環水路とを組合せ、第2循環水路に被処理水を循環送水可能とする導入手段が設けられていることにより、オゾン処理の要不要に応じて導入手段を起動停止し、人体に悪影響を及ぼす虞のあるオゾン処理を適宜使用して被処理水を安全に浄化処理できる。
また、特定時間帯内において、第1循環水路において被処理水を浄化処理するとともに、その被処理水を第2循環水路に導入しオゾン処理できるため、循環移送される被処理水の略全量をオゾン処理することが出来る。
In order to solve the above-mentioned problems, a circulating flush toilet according to claim 1 of the present invention includes a water receiving tank provided below the toilet bowl with transfer means for transferring the water to be treated, and a transfer from the water receiving tank. A purification tank that purifies and discharges the treated water, and a water supply tank provided with a flow-down means that is disposed above the water receiving tank and that causes the water to be treated introduced from the purification apparatus to flow down to the water receiving tank at least in use. A circulating water flush toilet that circulates water to be treated and purifies the treated water in the first circulating water channel,
A branch pipe which is provided at a predetermined location of the first circulation water channel and which can branch at least a part of the water to be treated; an ozone treatment means which is connected to the branch pipe and which treats the water to be treated; and the ozone treatment And a supply pipe for supplying the treated water ozone-treated by the means to the first circulating water channel, and a second circulating water channel is formed at a predetermined position of the second circulating water channel. Introducing means for introducing treated water into the second circulation channel ;
Within the specified time period specified in advance, the flow-down means forcibly causes the water to be treated to flow from the water tank to the water-receiving tank, and the introduction means removes the water to be treated in the first circulation channel. It is characterized by being introduced into two circulation channels .
According to this feature, the introduction means for combining the first circulation water channel in which the purification device is configured and the second circulation water channel in which the ozone treatment unit is configured to circulate and supply the water to be treated to the second circulation channel. By being provided, the introduction means can be started and stopped according to the necessity of ozone treatment, and the treated water can be safely purified using ozone treatment that may adversely affect the human body.
In addition, within the specific time zone, the treated water can be purified in the first circulating water channel, and the treated water can be introduced into the second circulating water channel and subjected to ozone treatment. It can be treated with ozone.

本発明の請求項に記載の循環式水洗トイレは、請求項に記載の循環式水洗トイレであって、被処理水を分岐可能とする前記分岐管が、前記送水槽に接続されていることを特徴としている。
この特徴によれば、第1循環水路において浄化装置より下流側の送水槽に分岐管が接続されており、浄化装置で一定程度浄化処理された後の被処理水を、第2循環水路に導入しオゾン処理できるため、オゾン処理に掛かる負荷を小さく抑えることが出来る。
The circulating flush toilet according to claim 2 of the present invention is the circulating flush toilet according to claim 1 , wherein the branch pipe that enables branching of the water to be treated is connected to the water tank. It is characterized by that.
According to this feature, the branch pipe is connected to the water tank downstream of the purification device in the first circulation channel, and the treated water after being purified to a certain extent by the purification device is introduced into the second circulation channel. Since the ozone treatment can be performed, the load applied to the ozone treatment can be reduced.

本発明の請求項に記載の循環式水洗トイレは、請求項に記載の循環式水洗トイレであって、前記送水槽の下部に前記分岐管が接続されるとともに、前記送水槽の上部に前記供給管が接続されており、前記流下手段と接続された流下管が、前記分岐管より上方で且つ前記供給管より下方において、前記送水槽に接続されていることを特徴としている。
この特徴によれば、送水槽内における略全量の被処理水をオゾン処理できるばかりか、オゾン処理された被処理水の一部を、第1循環水路におけるデッドエリアとしての流下管より下方領域に滞留水として貯留できため、特定時間帯以外において、第1循環水路を循環移送する被処理水に、オゾン処理された被処理水の脱臭・殺菌効果を長時間に亘って与えることが出来る。
The circulating flush toilet according to claim 3 of the present invention is the circulating flush toilet according to claim 2 , wherein the branch pipe is connected to the lower part of the water tank and the upper part of the water tank. The supply pipe is connected, and the downflow pipe connected to the downflow means is connected to the water tank above the branch pipe and below the supply pipe.
According to this feature, not only the entire amount of water to be treated in the water tank can be treated with ozone, but also a part of the treated water subjected to ozone treatment is placed in a region below the downstream pipe as a dead area in the first circulation channel. Since it can be stored as stagnant water, the deodorizing / sterilizing effect of the treated water that has been subjected to ozone treatment can be imparted over a long period of time to the treated water that is circulated and transferred through the first circulation channel except for the specific time period.

本発明の請求項に記載の循環式水洗トイレは、請求項1ないしのいずれかに記載の循環式水洗トイレであって、前記オゾン処理手段の上流側に色度検知手段が設けられており、該色度検知手段により検知された被処理水の色度に応じて、前記導入手段が起動停止可能となっていることを特徴としている。
この特徴によれば、色度検知手段により検知された被処理水の色度に応じて、被処理水をオゾン処理手段に導入するか否かを切替できるため、効率的なオゾン処理が可能となる。特に、請求項2を引用した発明においては、オゾン処理が、特定時間帯且つ被処理水の色度が所定値以上の場合に限定して行われるため、更に効率的となる。
A circulation flush toilet according to claim 4 of the present invention is the circulation flush toilet according to any one of claims 1 to 3 , wherein chromaticity detection means is provided upstream of the ozone treatment means. The introduction means can be started and stopped according to the chromaticity of the water to be treated detected by the chromaticity detection means.
According to this feature, according to the chromaticity of the water to be treated detected by the chromaticity detection means, it is possible to switch whether to introduce the water to be treated into the ozone treatment means, so that efficient ozone treatment is possible. Become. In particular, in the invention cited in claim 2, since the ozone treatment is performed only in a specific time zone and when the chromaticity of the water to be treated is a predetermined value or more, it is further efficient.

本発明の請求項に記載の循環式水洗トイレは、請求項1ないしのいずれかに記載の循環式水洗トイレであって、前記浄化装置は、少なくとも被処理水を固液分離し排出する固液分離槽を備えており、前記第1循環水路と別に、前記固液分離槽において被処理水を固液分離した後の濃縮物を搬出する搬出手段と、濃縮物を貯留する貯留槽が構成され、該貯留槽の所定高さ位置に、濃縮物を前記第2循環水路に導入可能とする導入管が設けられていることを特徴としている。
この特徴によれば、貯留槽に貯留した濃縮物を第2循環水路に導入し、オゾン処理した後に第1循環水路に戻すことにより、濃縮物として若しくは蒸発して失われていく第1循環水路内の被処理水の水量を、別段の水を供給することなく維持できる。
The circulating flush toilet according to claim 5 of the present invention is the circulating flush toilet according to any one of claims 1 to 4 , wherein the purification device separates and discharges at least water to be treated by solid-liquid separation. A solid-liquid separation tank is provided, and separately from the first circulation water channel, there are an unloading means for carrying out the concentrate after solid-liquid separation of the water to be treated in the solid-liquid separation tank, and a storage tank for storing the concentrate. It is comprised and the introduction pipe | tube which can introduce a concentrate into the said 2nd circulation water channel is provided in the predetermined height position of this storage tank, It is characterized by the above-mentioned.
According to this feature, the first circulating water channel that is lost as a concentrate or evaporated by introducing the concentrate stored in the storage tank into the second circulating water channel, returning it to the first circulating water channel after ozone treatment. The amount of water to be treated can be maintained without supplying extra water.

本発明の請求項に記載の循環式水洗トイレは、請求項に記載の循環式水洗トイレであって、前記貯留槽における所定水量を検知する水量検知手段と、前記貯留槽の所定高さ位置に設けられた前記導入管を開閉可能とする導入バルブと、が更に設けられており、前記導入手段が前記第1循環水路内の被処理水を前記第2循環水路内に導入しており、且つ前記水量検知手段が前記貯留槽の所定水量を検知したときに、前記導入バルブが開状態となることを特徴としている。
この特徴によれば、濃縮物を貯留槽の所定水量まで貯留できるとともに、被処理水をオゾン処理すると同時に濃縮物を第2循環水路内に導入してオゾン処理し、第1循環水路に戻すことができる。
The circulating flush toilet according to claim 6 of the present invention is the circulating flush toilet according to claim 5 , and includes a water amount detecting means for detecting a predetermined amount of water in the storage tank, and a predetermined height of the storage tank. An introduction valve capable of opening and closing the introduction pipe provided at a position, and the introduction means introduces the treated water in the first circulation channel into the second circulation channel. And when the said water quantity detection means detects the predetermined water quantity of the said storage tank, the said introduction valve will be in an open state.
According to this feature, the concentrate can be stored up to a predetermined amount of water in the storage tank, and the water to be treated is ozone-treated, and at the same time, the concentrate is introduced into the second circulation channel and ozone-treated, and returned to the first circulation channel. Can do.

本発明の請求項に記載の循環式水洗トイレは、請求項またはに記載の循環式水洗トイレであって、前記貯留槽に堆積した濃縮物をバイオ処理するバイオ処理手段が、更に設けられていることを特徴としている。
この特徴によれば、被処理水の濃縮物をバイオ処理手段によりバイオ処理することで、濃縮物の汲取り処理を大幅に軽減でき、長期的な循環式水洗トイレ単体による浄化処理が可能となる。
The circulating flush toilet according to claim 7 of the present invention is the circulating flush toilet according to claim 5 or 6 , further comprising a bio-processing means for bio-processing the concentrate deposited in the storage tank. It is characterized by being.
According to this feature, the concentrate of the water to be treated is bioprocessed by the bioprocessing means, so that the process of pumping the concentrate can be greatly reduced, and the purification process can be performed with a long-term circulating flush toilet alone. .

本発明の請求項に記載の循環式水洗トイレは、請求項ないしのいずれかに記載の循環式水洗トイレであって、前記受水槽には、被処理水の満水位を検知する満水位検知手段が設けられており、濃縮物を搬送する前記搬送手段が、前記満水位検知手段により起動することを特徴としている。
この特徴によれば、トイレの使用により被処理水が所定に増量した場合にのみ、濃縮物を搬送するため、固液分離槽において効率的に被処理水を濃縮できる。
The circulating flush toilet according to claim 8 of the present invention is the circulating flush toilet according to any of claims 5 to 7 , wherein the water receiving tank is filled with water to detect a full water level of the water to be treated. A position detecting means is provided, and the conveying means for conveying the concentrate is activated by the full water level detecting means.
According to this feature, since the concentrate is transported only when the amount of water to be treated is increased by using the toilet, the water to be treated can be efficiently concentrated in the solid-liquid separation tank.

本発明の請求項に記載の循環式水洗トイレは、請求項1ないしのいずれかに記載の循環式水洗トイレであって、前記送水槽に、被処理水の高水位を検知する第1水位検知手段と低水位を検知する第2水位検知手段とが設けられており、被処理水を移送する前記移送手段が、前記第2水位検知手段により起動し、前記第1水位検知手段により停止することを特徴としている。
この特徴によれば、被処理水を移送する移送手段が、送水槽の水位に応じて起動・停止する間欠運転を行うため、被処理水の循環送水に要する動力を省ける。
The circulating flush toilet according to claim 9 of the present invention is the circulating flush toilet according to any of claims 1 to 8 , wherein the first flushing toilet detects a high water level in the water tank. A water level detection means and a second water level detection means for detecting a low water level are provided, and the transfer means for transferring the water to be treated is activated by the second water level detection means and stopped by the first water level detection means It is characterized by doing.
According to this feature, since the transfer means for transferring the water to be treated performs an intermittent operation that starts and stops according to the water level of the water tank, power required for circulating water to be treated can be saved.

本発明の請求項10に記載の循環式水洗トイレは、請求項1ないしのいずれかに記載の循環式水洗トイレであって、前記オゾン処理手段から前記浄化装置に向けてオゾンを導入するオゾン導入管が設けられていることを特徴としている。
この特徴によれば、オゾンの一部を浄化装置側に導入し、オゾン処理することで、浄化装置周辺が脱臭・殺菌処理されて衛生的となる。
A circulating flush toilet according to claim 10 of the present invention is the circulating flush toilet according to any one of claims 1 to 9 , wherein ozone is introduced from the ozone treatment means toward the purification device. An introduction pipe is provided.
According to this feature, by introducing a part of ozone to the purification device side and performing the ozone treatment, the periphery of the purification device is deodorized and sterilized to be sanitary.

本発明の請求項11に記載の可搬型循環式水洗トイレは、請求項1ないし10のいずれかに記載の循環式水洗トイレが、可搬型であることを特徴としている。
この特徴によれば、上水道若しくは下水道が設置されていない山間部や離島などにも設置できるばかりか、上水道若しくは下水道の故障により常設のトイレが使用不能となる災害時にあっても、任意の場所に循環式水洗トイレを設置できる。
The portable circulating flush toilet according to claim 11 of the present invention is characterized in that the circulating flush toilet according to any of claims 1 to 10 is portable.
According to this feature, it can be installed not only in mountainous areas or remote islands where water supply or sewerage is not installed, but also in any place even in the event of a disaster in which a permanent toilet becomes unusable due to failure of the water supply or sewerage Circulating flush toilets can be installed.

本発明の実施例を以下に説明する。   Examples of the present invention will be described below.

本発明の実施例を図面に基づいて説明すると、先ず図1は、循環式水洗トイレの特定時間帯における浄化処理を示す概略図である。図2は、特定時間帯を除いた時間帯における浄化処理を示す概略図である。図3は、送水槽における被処理水の流動状況を示す斜視図である。図1及び図2において、点線は圧縮空気若しくはオゾンガスの導管を示し、一点鎖線は信号線を示している。   DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described with reference to the drawings. First, FIG. 1 is a schematic view showing a purification process in a specific time zone of a circulating flush toilet. FIG. 2 is a schematic diagram showing the purification process in a time zone excluding a specific time zone. FIG. 3 is a perspective view showing a flow state of the water to be treated in the water tank. 1 and 2, the dotted line indicates a compressed air or ozone gas conduit, and the alternate long and short dash line indicates a signal line.

先ず図1に示されるように、本実施例における可搬型の循環式水洗トイレ1(以下、トイレ1と省略する)は、被処理水としてのトイレ汚水を、後述する浄化装置2及びオゾン処理手段としてのオゾン処理室7を循環移送することで浄化処理し、処理済水をトイレ洗浄水として再利用するものである。尚、被処理水とは、後述する浄化処理若しくはオゾン処理する前の水、処理中の水、処理済水を全て包含するものとする。   First, as shown in FIG. 1, a portable circulating flush toilet 1 (hereinafter abbreviated as “toilet 1”) in this embodiment is used to purify toilet sewage as treated water into a purifier 2 and ozone treatment means described later. The ozone treatment chamber 7 is circulated and transferred to purify it, and the treated water is reused as toilet wash water. Incidentally, the water to be treated includes all water before purification treatment or ozone treatment described later, water being treated, and treated water.

トイレ1の装置構成の概略について説明すると、被処理水を移送する移送手段としての第1ポンプ20を備え便器8の下方に配設された受水槽6と、受水槽6より上方に配設され、受水槽6から移送された被処理水を浄化して排出する浄化装置2と、同様に受水槽6より上方に配設され、浄化装置2から導入した被処理水を受水槽6に排出可能とする送水槽3と、送水槽3の略中間高さ位置から内部の被処理水を受水槽6に向かって流下可能とする流下管としての送水管12及び洗浄水管13と、からなる第1循環水路が構成されている(図示白抜矢印参照)。   The outline of the apparatus configuration of the toilet 1 will be described. A water receiving tank 6 provided with a first pump 20 as a transfer means for transferring water to be treated and disposed below the toilet bowl 8 and disposed above the water receiving tank 6. The purification device 2 that purifies and discharges the water to be treated transferred from the water receiving tank 6, and is similarly disposed above the water receiving tank 6, so that the water to be treated introduced from the purification device 2 can be discharged to the water receiving tank 6. A water supply tank 3 and a water supply pipe 12 and a wash water pipe 13 as a downflow pipe that allow the water to be treated to flow from the substantially intermediate height position of the water supply tank 3 toward the water receiving tank 6. A circulation channel is formed (see the white arrow in the figure).

また、送水槽3の最下部に設けられた分岐管10と、この分岐管10に接続され、被処理水をオゾン処理するオゾン処理室7と、オゾン処理室7でオゾン処理された被処理水を上述した第1循環水路に供給する供給管11と、からなる第2循環水路が構成されており、この第2循環水路に被処理水を循環送水可能とする導入手段としての第2ポンプ21が設けられている(図示黒塗矢印参照)。尚、オゾン処理室7は、図示しない区画壁により浄化装置2及び送水槽3と区画されている。   Further, a branch pipe 10 provided at the lowermost part of the water tank 3, an ozone treatment chamber 7 connected to the branch pipe 10 for ozone treatment of the water to be treated, and water to be treated which has been subjected to ozone treatment in the ozone treatment chamber 7. A second circulating water channel comprising a supply pipe 11 for supplying the first circulating water channel to the first circulating water channel described above is configured, and a second pump 21 serving as an introducing means that enables the water to be treated to be circulated and fed to the second circulating water channel. Is provided (see black arrow in the figure). The ozone treatment chamber 7 is partitioned from the purification device 2 and the water tank 3 by a partition wall (not shown).

更に、送水管12を開閉可能とする送水手段としての送水バルブ12aに、タイマTが接続されており、タイマTに予め特定された特定時間帯において、送水バルブ12aが開閉動作するようになっている。同期して、分岐管10を開閉可能とする分岐バルブ10a及び第2ポンプ21も、タイマTに予め特定された特定時間帯において、開閉動作するようになっている。   Furthermore, a timer T is connected to a water supply valve 12a as a water supply means that can open and close the water supply pipe 12, and the water supply valve 12a opens and closes in a specific time zone specified in advance by the timer T. Yes. The branch valve 10 a and the second pump 21 that can open and close the branch pipe 10 in synchronization with each other are also opened and closed during a specific time period specified in advance by the timer T.

次に、浄化装置2の構成について説明する。浄化装置2は、仕切壁25で区画され、堰部25aを介して互いに連通した固液分離槽4と微生物処理槽5とから構成されている。   Next, the configuration of the purification device 2 will be described. The purification device 2 is composed of a solid-liquid separation tank 4 and a microorganism treatment tank 5 which are partitioned by a partition wall 25 and communicate with each other via a weir 25a.

固液分離槽4は、堰部25aを被覆する様に設置され導入した被処理水を通過させるスクリーン4aと、スクリーン4aの面に沿って上昇する気泡を発生する散気孔23とを備え、被処理水を固液分離し排出するように成っている。   The solid-liquid separation tank 4 includes a screen 4a that is installed so as to cover the dam portion 25a and allows the treated water to be introduced therethrough, and a diffuser hole 23 that generates bubbles rising along the surface of the screen 4a. The treated water is separated into solid and liquid and discharged.

また、微生物処理槽5は、仕切壁26で送水槽3と区画され、導入した被処理水を通過させる微生物固定化担体5aと、微生物固定化担体5aに向かって気泡を発生する曝気孔24と、上部孔27aと下部孔27bとが内部で連通し上下方向に設置されたダクト27とを備え、被処理水を微生物処理し排出するように成っている。   The microorganism treatment tank 5 is partitioned from the water supply tank 3 by a partition wall 26, and a microorganism-immobilized carrier 5a that allows the introduced treated water to pass through, and an aeration hole 24 that generates bubbles toward the microorganism-immobilized carrier 5a. The upper hole 27a and the lower hole 27b communicate with each other inside and are provided with a duct 27 installed in the vertical direction. The treated water is treated with microorganisms and discharged.

次に、特定時間帯としての夜間(例えば、18:00〜6:00の12時間)におけるトイレ1の浄化処理フローについて、図1に基づいて説明する。夜間においては後述する昼間と比較してトイレ1使用は頻繁でなく、昼間にトイレ1使用で発生した被処理水としてのトイレ汚水は、第1循環水路及び第2循環水路を循環移送されるとともに浄化処理される。   Next, the purification process flow of the toilet 1 at night as a specific time zone (for example, 12 hours from 18:00 to 6:00) will be described with reference to FIG. At night, the toilet 1 is used less frequently than in the daytime, which will be described later, and toilet sewage as treated water generated by using the toilet 1 in the daytime is circulated and transferred through the first circulation channel and the second circulation channel. Purified.

予めタイマTに特定された特定時間帯(18:00〜6:00)において、タイマTに接続された導入手段としての第2ポンプ21が起動し分岐バルブ10aが開状態となるとともに、同期して送水槽3の送水バルブ12aが開状態となる。この動作により被処理水が、夜間において定常的に第1循環水路及び第2循環水路を循環移送される。   In a specific time zone (18: 00 to 6:00) specified in advance by the timer T, the second pump 21 serving as the introducing means connected to the timer T is activated and the branch valve 10a is opened and synchronized. Thus, the water supply valve 12a of the water supply tank 3 is opened. By this operation, the water to be treated is circulated and transferred through the first circulation channel and the second circulation channel constantly at night.

先ず、第1循環水路における被処理水の循環移送について説明すると、送水槽3において被処理水は、水頭圧により強制的に送水管12を介して下方に設置された受水槽6に向かって自然流下する。被処理水の流下により送水槽3の水位が下降し、所定の低水位となると、第2水位検知手段28bにより検知された低水位信号により第1ポンプ20が起動し、被処理水が固液分離槽4に移送される。   First, the circulating transfer of the water to be treated in the first circulation channel will be described. The water to be treated in the water feeding tank 3 is naturally forced toward the water receiving tank 6 installed below via the water feeding pipe 12 by the head pressure. Flow down. When the water level in the water tank 3 is lowered by the flow of the water to be treated and reaches a predetermined low water level, the first pump 20 is activated by the low water level signal detected by the second water level detection means 28b, and the water to be treated is solid liquid. It is transferred to the separation tank 4.

この移送により送水槽3の水位が上昇し、所定の高水位となると、第1水位検知手段28aにより検知された高水位信号により第1ポンプ20が停止する。以降、第1ポンプ20は送水槽3の水位に応じて上述のように、起動・停止を繰り返す間欠運転をするように成っている。   When the water level of the water tank 3 rises by this transfer and reaches a predetermined high water level, the first pump 20 is stopped by the high water level signal detected by the first water level detecting means 28a. Thereafter, the first pump 20 is configured to perform intermittent operation that repeats starting and stopping according to the water level of the water tank 3 as described above.

このように、被処理水を移送する第1ポンプ20が、送水槽3の水位に応じて起動・停止する間欠運転を行うため、被処理水の循環送水に要する動力を省ける。   Thus, since the 1st pump 20 which transfers to-be-processed water performs the intermittent driving | operation which starts and stops according to the water level of the water-feeding tank 3, the power required for the circulating water-supply of to-be-processed water can be saved.

固液分離槽4において、被処理水は、堰部25aの周囲に配設された細目多孔のスクリーン4aを通過するとともに、固液分離されてスクリーン4aを通過した被処理水が、後述する微生物処理槽5に移動し、固形分はスクリーン4aに捕捉される。   In the solid-liquid separation tank 4, the water to be treated passes through the fine porous screen 4a disposed around the dam portion 25a, and the water to be treated which has been solid-liquid separated and passed through the screen 4a is a microorganism which will be described later. It moves to the processing tank 5, and solid content is capture | acquired by the screen 4a.

スクリーン4aに捕捉された固形分は、ブロア22により散気孔23を介して散気されスクリーン4aの面に沿って上昇する気泡により剥離し、固液分離槽4内部に生じた対流とともに、その重量により下方に沈降し、経時的に濃縮して後述する濃縮物を生成する。   The solid content trapped in the screen 4a is diffused by the blower 22 through the air diffusion holes 23 and peeled off by the bubbles rising along the surface of the screen 4a, and the convection generated in the solid-liquid separation tank 4 and its weight To settle downward and concentrate over time to produce a concentrate as described below.

次に、固液分離槽4を通過した被処理水は、仕切壁25の堰部25aを通過し、微生物処理槽5内に導入される。   Next, the water to be treated that has passed through the solid-liquid separation tank 4 passes through the weir 25 a of the partition wall 25 and is introduced into the microorganism treatment tank 5.

微生物処理槽5において、被処理水は、微生物処理槽5内に充填された多数個の微生物固定化担体5aを通過するとともに、上方から下方に向かって流動する。この流動により微生物固定化担体5aに固定付着した微生物が、被処理水に含有された有機分を捕捉し、有機分解処理する。同時に、ブロア22により曝気孔24を介して微生物固定化担体5aに向かって曝気されることで、微生物が活性化し、微生物処理能力が向上できる。   In the microbial treatment tank 5, the water to be treated passes through a large number of microbial immobilization carriers 5 a filled in the microbial treatment tank 5 and flows downward from above. The microorganisms fixed and attached to the microorganism-immobilized carrier 5a by this flow capture the organic component contained in the water to be treated, and organically decompose it. At the same time, the microorganisms are activated by the aeration by the blower 22 through the aeration holes 24 toward the microorganism-immobilized carrier 5a, so that the microorganism processing ability can be improved.

このように、微生物処理槽5において、上方から下方に向かって流動した被処理水は、上下方向に設けられたダクト27の下部孔27bからダクト27内部に流入し、上部孔27aを介して送水槽3内に導入される。   Thus, in the microorganism treatment tank 5, the water to be treated that has flowed from the upper side to the lower side flows into the duct 27 from the lower hole 27b of the duct 27 provided in the vertical direction, and is sent through the upper hole 27a. It is introduced into the water tank 3.

そして上述したように、送水槽3において被処理水は、水頭圧により強制的に送水バルブ12aを介して下方に設置された受水槽6に向かって自然流下し、第1循環水路を形成する。   As described above, the water to be treated in the water supply tank 3 naturally flows down toward the water receiving tank 6 installed below through the water supply valve 12a due to the water head pressure, thereby forming a first circulation water channel.

次に、第2循環水路における被処理水の循環移送について説明すると、タイマTと接続された第2ポンプ21の起動により、送水槽3内の被処理水は、送水槽3の最下部において接続された分岐管10を介してオゾン処理室7に供給され、オゾン発生装置17にて発生するオゾンガスによりオゾン処理される。オゾン処理された被処理水は、送水槽3の上部に接続された供給管11を介して第1循環水路を構成する送水槽3内に供給される。   Next, the circulating transfer of the water to be treated in the second circulating water channel will be described. By the activation of the second pump 21 connected to the timer T, the water to be treated in the water tank 3 is connected at the bottom of the water tank 3. The ozone is supplied to the ozone processing chamber 7 through the branched pipe 10 and is ozone-treated with ozone gas generated by the ozone generator 17. The treated water that has been subjected to the ozone treatment is supplied into the water tank 3 that constitutes the first circulation channel through the supply pipe 11 connected to the upper part of the water tank 3.

このように、第1循環水路において浄化装置2より下流側の送水槽3に分岐管10が接続されていることで、浄化装置2を構成する固液分離槽4にて固液分離されるとともに微生物処理槽5にて微生物処理されることにより一定程度浄化処理された後の被処理水を、第2循環水路に導入しオゾン処理室7でオゾン処理できるため、オゾン処理に掛かる負荷を小さく抑えることが出来る。   As described above, the branch pipe 10 is connected to the water supply tank 3 on the downstream side of the purification device 2 in the first circulation channel, so that the solid-liquid separation is performed in the solid-liquid separation tank 4 constituting the purification device 2. Water to be treated that has been purified to a certain extent by being subjected to microbial treatment in the microbial treatment tank 5 can be introduced into the second circulating water channel and ozonized in the ozone treatment chamber 7, so that the load on the ozone treatment is kept small. I can do it.

また、このようにすることで、送水槽3内における略全量の被処理水をオゾン処理できる。また、上述した第1循環水路を循環移送する浄化処理された被処理水と、第2循環水路を循環移送するオゾン処理された被処理水とが、送水槽3内において流動撹拌することで混合し、浄化効率が高まる。   Moreover, by doing in this way, substantially the whole amount of water to be treated in the water tank 3 can be treated with ozone. In addition, the purified water to be treated that circulates and transports the first circulating water channel and the ozone treated water that circulates and transports the second circulating water channel are mixed by flowing and stirring in the water tank 3. And purification efficiency is increased.

送水槽3内に供給された被処理水は、供給管11より下方において送水槽3と接続された送水管12より、上述したように、受水槽6に自然流下し、第1循環水路を循環移送される。   As described above, the water to be treated supplied into the water tank 3 naturally flows down to the water receiving tank 6 from the water pipe 12 connected to the water tank 3 below the supply pipe 11 and circulates in the first circulation channel. Be transported.

このように、オゾン処理前の被処理水と比較して比重の大きいオゾン処理後の被処理水を、送水管より上方に設けられた供給管より第1循環水路に環流させることで、送水槽内においてオゾン処理された被処理水が効率よく対流し、第1循環水路において循環送水される。   As described above, the water to be treated after the ozone treatment having a larger specific gravity than the water to be treated before the ozone treatment is circulated from the supply pipe provided above the water feeding pipe to the first circulation water channel, thereby supplying the water tank. The to-be-treated water that has been subjected to ozone treatment convects efficiently and is circulated and sent in the first circulation channel.

また、浄化装置2が構成された第1循環水路と、オゾン処理室7が構成された第2循環水路とを組合せ、第2循環水路に被処理水を循環送水可能とする導入手段としての第2ポンプ21が設けられていることにより、オゾン処理の要不要に応じて第2ポンプ21を起動・停止し、人体に悪影響を及ぼす虞のあるオゾン処理を適宜使用して被処理水を安全に浄化処理できる。   Further, the first circulating water channel in which the purification device 2 is configured and the second circulating water channel in which the ozone treatment chamber 7 is configured are combined, and the first circulating unit as the introduction means that enables the treated water to be circulated and sent to the second circulating channel. By providing two pumps 21, the second pump 21 is started and stopped according to the necessity of ozone treatment, and ozone treatment that may adversely affect the human body is used as appropriate to safely treat the water to be treated. It can be purified.

更に、第1循環水路において被処理水を浄化処理するとともに、その被処理水を第2循環水路に導入しオゾン処理できるため、循環移送される被処理水の略全量をオゾン処理することが出来る。特に、人体に悪影響を及ぼす虞のあるオゾン処理を、タイマTにより予め任意に特定した特定時間帯内に限定して行うことが出来、特定時間以外である昼間においてはオゾン処理を除いた浄化処理が出来るため、安全性が向上する。   Furthermore, since the water to be treated is purified in the first circulation water channel and the water to be treated can be introduced into the second circulation water channel and subjected to ozone treatment, substantially the entire amount of water to be circulated can be treated with ozone. . In particular, ozone treatment that may adversely affect the human body can be performed only within a specific time zone that is arbitrarily specified in advance by a timer T, and purification treatment that excludes ozone treatment during the daytime other than the specific time. Can improve safety.

更に、分岐管10に接続された色度検知手段としての色度センサ29により検知された被処理水の色度に応じて、第2ポンプ21が起動・停止可能となっている。即ち、被処理水が比較的清浄であることにより色度が所定の設定値より小さい場合には、第2ポンプ21が停止し、第2循環水路における被処理水の流動は止まる。また、被処理水が比較的汚濁していることにより色度が所定の設定値より大きい場合には、第2ポンプ21が起動し、第2循環水路における被処理水の流動は再び始まる。   Furthermore, the second pump 21 can be started and stopped in accordance with the chromaticity of the water to be treated detected by the chromaticity sensor 29 serving as the chromaticity detecting means connected to the branch pipe 10. That is, when the water to be treated is relatively clean and the chromaticity is smaller than the predetermined set value, the second pump 21 is stopped and the flow of the water to be treated in the second circulating water channel is stopped. In addition, when the chromaticity is larger than a predetermined set value due to the relatively untreated water, the second pump 21 is activated and the flow of the treated water in the second circulation channel starts again.

このようにすることで、色度センサ29により検知された被処理水の色度に応じて、被処理水をオゾン処理室7に導入するか否かを切替できるため、効率的なオゾン処理が可能となる。特に、本実施例のように、夜間の特定時間帯においてオゾン処理が行われ、特定時間帯且つ被処理水の色度が所定値以上の場合に限定して行われるため、更に効率的となる。   By doing in this way, according to the chromaticity of the to-be-processed water detected by the chromaticity sensor 29, it can switch whether to introduce the to-be-processed water into the ozone treatment chamber 7, Therefore An efficient ozone treatment is carried out. It becomes possible. In particular, as in this embodiment, ozone treatment is performed in a specific time zone at night, and is performed only when the chromaticity of the water to be treated and the specific time zone is greater than or equal to a predetermined value. .

また、オゾン処理室7から浄化装置2側に向けてオゾンを導入するオゾン導入管15が設けられており、このようにすることで、オゾンガスの一部を浄化装置2側に導入し、オゾン処理することで、浄化装置2周辺が脱臭・殺菌処理されて衛生的となる。   Further, an ozone introduction pipe 15 for introducing ozone from the ozone treatment chamber 7 toward the purification device 2 side is provided. By doing so, a part of the ozone gas is introduced to the purification device 2 side, and the ozone treatment is performed. By doing so, the periphery of the purification apparatus 2 is deodorized and sterilized to be sanitary.

次に、図2に示されるように、上述した特定時間帯を除いた時間帯としての昼間(例えば、6:00〜18:00の12時間)におけるトイレ1の浄化処理フローについて説明する。昼間においては後述のように、被処理水は、第1循環水路を循環移送されるとともに浄化処理され、第2循環水路には循環移送されない。   Next, as shown in FIG. 2, a cleaning process flow of the toilet 1 in the daytime (for example, 12 hours from 6:00 to 18:00) as a time zone excluding the specific time zone described above will be described. During the daytime, as will be described later, the water to be treated is circulated and transferred through the first circulation channel and purified, and is not circulated and transferred to the second circulation channel.

使用者のトイレ1使用により、被処理水としてのトイレ汚水が、便器8下方の受水槽6に貯留されるとともに、使用者の洗浄水スイッチSの操作により、流下手段としての洗浄水バルブ13aが開状態となり、便器8の洗浄水として上述のように浄化処理した処理済の被処理水が、水頭圧により送水槽3から便器8を介して受水槽6に向かって自然流下し、受水槽6に貯留される。   By using the toilet 1 of the user, toilet sewage as treated water is stored in the water receiving tank 6 below the toilet bowl 8, and a washing water valve 13a as a downflow means is provided by operating the washing water switch S of the user. The treated water that has been treated and purified as described above as flush water for the toilet bowl 8 naturally flows down from the water supply tank 3 through the toilet bowl 8 toward the water receiving tank 6 by the water head pressure. It is stored in.

昼間においては頻繁にトイレ1使用がされるため、洗浄水の使用により、送水槽3の水位が下降し、第2水位検知手段28bにより検知された低水位信号により第1ポンプ20が起動し、被処理水が移送管16を介して固液分離槽4に移送される。この移送により送水槽3の水位が上昇し、第1水位検知手段28aにより検知された高水位信号により第1ポンプ20が停止する。そして、上述と同様に、被処理水は、固液分離槽4と微生物処理槽5とからなる浄化装置2を通過するとともに浄化処理され、送水槽3の上部に設けられたダクト27の上部孔27aを介して、送水槽3内に落下して導入される。   Since the toilet 1 is frequently used in the daytime, the water level of the water tank 3 is lowered by using the washing water, and the first pump 20 is activated by the low water level signal detected by the second water level detection means 28b. The water to be treated is transferred to the solid-liquid separation tank 4 through the transfer pipe 16. By this transfer, the water level in the water tank 3 rises, and the first pump 20 is stopped by the high water level signal detected by the first water level detection means 28a. And as above-mentioned, to-be-processed water passes through the purification apparatus 2 which consists of the solid-liquid separation tank 4 and the microorganism treatment tank 5, is purified, and is the upper hole of the duct 27 provided in the upper part of the water tank 3. It falls and introduce | transduces in the water tank 3 via 27a.

次に、図3に示されるように、送水槽3内部の被処理水の流動について説明すると、昼間においては、第2循環水路における被処理水の流動が無く、送水槽3の略中央高さ位置に設けられた送水管12よりも下方の下方領域Dはデッドエリアとなるため(図示斜線部参照)、この下方領域Dにおける被処理水は、上述のように夜間においてオゾン処理された被処理水が滞留している。そこへ送水槽3に導入される被処理水の流動により、送水槽3内部に対流が生じ、この対流により、送水槽3に導入される被処理水と、下方領域に滞留していたオゾン処理された被処理水とが、混合された後、洗浄水管13を介して流下するようになる。   Next, as shown in FIG. 3, the flow of the water to be treated inside the water tank 3 will be described. In the daytime, there is no flow of the water to be treated in the second circulation water channel, and the height of the center of the water tank 3 is approximately the same. Since the lower area D below the water pipe 12 provided at the position is a dead area (see the shaded area in the figure), the water to be treated in the lower area D is treated with ozone at night as described above. Water is stagnating. Due to the flow of the water to be treated introduced into the water tank 3, convection is generated inside the water tank 3, and the water to be treated introduced into the water tank 3 by this convection and the ozone treatment remaining in the lower region. After the treated water is mixed, it flows down through the washing water pipe 13.

もし、オゾン処理された被処理水の全部を第1循環水路に循環移送すれば、オゾン処理の効果の持続時間は限られたものとなるが、本実施例のように、オゾン処理された被処理水の一部を、被処理水の第1循環水路におけるデッドエリアとしての送水管12より下方領域Dに滞留水として貯留できるため、特定時間帯以外であるトイレ1の使用頻度が高い昼間において、第1循環水路を循環移送する被処理水に、オゾン処理された被処理水の脱臭・殺菌効果を長時間に亘って与えることが出来る。   If all the ozone-treated water to be treated is circulated and transferred to the first circulation channel, the duration of the effect of the ozone treatment will be limited. However, as in this embodiment, the ozone-treated water to be treated is limited. Since part of the treated water can be stored as stagnant water in the region D below the water pipe 12 as a dead area in the first circulation channel of the water to be treated, in the daytime when the use frequency of the toilet 1 other than the specific time zone is high In addition, the deodorizing / sterilizing effect of the ozone-treated water can be given to the treated water circulating and transported through the first circulation channel for a long time.

特に、送水槽3内における被処理水の対流とともに、下方領域Dにおける滞留水と、送水管12よりも上方の上方領域Bにおける被処理水とを混合でき、上述した被処理水の脱臭・殺菌効果がより効率的となる。   In particular, with the convection of the water to be treated in the water tank 3, the stagnant water in the lower region D and the water to be treated in the upper region B above the water pipe 12 can be mixed. The effect becomes more efficient.

次に、昼間におけるトイレ1使用により、第1循環水路を流動する被処理水の全水量が増加し、この増加量分は受水槽6に蓄積されるようになる。受水槽6に設けられた満水位検知手段30が、所定の満水位を検知すると、エアバルブ31が開放するとともに、固液分離槽4の下層に蓄積された濃縮物としての被処理水の固形分が、エア管19内に搬出手段としてのブロア22により供給される圧縮空気が流動することによりエアリフト効果で、固液分離槽4から貯留槽9に向かって搬出され、第1循環水路とは別に設けられた貯留槽9内に貯留される。図示しないタイマにより設定した所定時間後、エアバルブ31は閉じて濃縮物の搬出は終了する。このエアリフトによる濃縮物の搬出は、受水槽6の水位に応じて間欠運転するようになっている。   Next, due to the use of the toilet 1 in the daytime, the total amount of water to be treated flowing in the first circulation channel increases, and this increased amount is accumulated in the water receiving tank 6. When the full water level detection means 30 provided in the water receiving tank 6 detects a predetermined full water level, the air valve 31 is opened and the solid content of the water to be treated as a concentrate accumulated in the lower layer of the solid-liquid separation tank 4 However, the compressed air supplied by the blower 22 serving as the unloading means flows into the air pipe 19 and is unloaded from the solid-liquid separation tank 4 toward the storage tank 9 due to the air lift effect, separately from the first circulation water channel. It is stored in the provided storage tank 9. After a predetermined time set by a timer (not shown), the air valve 31 is closed, and the carry-out of the concentrate ends. The carry-out of the concentrate by the air lift is intermittently operated according to the water level of the water receiving tank 6.

このようにすることで、トイレ1の使用により被処理水が所定に増量した場合にのみ、濃縮物を搬送するため、固液分離槽4において効率的に被処理水を濃縮できる。   By doing in this way, since the concentrate is conveyed only when the amount of treated water is increased by a predetermined amount due to the use of the toilet 1, the treated water can be efficiently concentrated in the solid-liquid separation tank 4.

貯留槽9においては、搬出された固形分が経時的に蓄積されるとともに、貯留槽9の下層には濃縮固形分が堆積し、トイレ汚水が含有する物性により、上層にはいわゆるスカム層が発生して、中間層にはいわゆる嫌気層が介在し、全体の層を生成するようになる。この嫌気層には、上述した微生物処理槽5における微生物処理(好気性処理)を経た後の、嫌気性を有する物質が多く介在し、下層と比較して固形分濃度は薄い。   In the storage tank 9, the transported solids are accumulated over time, concentrated solids accumulate in the lower layer of the storage tank 9, and so-called scum layer is generated in the upper layer due to the physical properties contained in the toilet sewage. Thus, a so-called anaerobic layer is interposed in the intermediate layer, and the entire layer is generated. This anaerobic layer contains a large amount of anaerobic substances after the microbial treatment (aerobic treatment) in the microbial treatment tank 5 described above, and the solid content concentration is lower than that of the lower layer.

上述した夜間におけるオゾン処理を行っているときであって、且つ貯留槽9内に濃縮固形分が蓄積し貯留槽9に設けられた水量検知手段33が所定水量を検知すると、導入バルブ14aが開状態となる。   When the above-described ozone treatment is performed at night, and when the concentrated solid content is accumulated in the storage tank 9 and the water amount detection means 33 provided in the storage tank 9 detects a predetermined amount of water, the introduction valve 14a is opened. It becomes a state.

このようにすることで、濃縮物を貯留槽9の所定水量まで貯留できるとともに、被処理水をオゾン処理すると同時に、濃縮物を第2循環水路内に導入してオゾン処理し、第1循環水路に戻すことができる。   In this way, the concentrate can be stored up to a predetermined amount of water in the storage tank 9, and the water to be treated is ozone-treated, and at the same time, the concentrate is introduced into the second circulation channel and subjected to ozone treatment, and the first circulation channel Can be returned to.

図示しないタイマにより設定した所定時間後、導入バルブ14aは閉状態となり、オゾン処理室7への導入は終了する。この被処理水のオゾン処理室7への導入は、再び貯留槽9の所定水量に達した場合に間欠運転するようになっている。   After a predetermined time set by a timer (not shown), the introduction valve 14a is closed, and the introduction into the ozone treatment chamber 7 is completed. The introduction of the water to be treated into the ozone treatment chamber 7 is intermittently operated when the predetermined amount of water in the storage tank 9 is reached again.

このようにすることで、貯留槽9に貯留した濃縮物を第2循環水路に導入し、オゾン処理した後に第1循環水路に戻すことにより、第1循環水路から濃縮物として若しくは蒸発して失われていく被処理水の水量を、別段の水を供給することなく維持できる。   In this way, the concentrate stored in the storage tank 9 is introduced into the second circulation channel, and after ozone treatment, the concentrate is returned to the first circulation channel to be lost as a concentrate or evaporated from the first circulation channel. The amount of water to be treated can be maintained without supplying extra water.

尚、貯留槽9に設けられる導入管14は、必ずしも貯留槽9の略中間高さに設けられている必要はなく、被処理水の物性に応じて、所定高さに設けられていればよい。   In addition, the introduction pipe 14 provided in the storage tank 9 does not necessarily need to be provided at a substantially intermediate height of the storage tank 9, and may be provided at a predetermined height according to the physical properties of the water to be treated. .

更に、貯留槽9の最下部に、貯留槽9の下層を形成する濃縮固形分を排出する排出管18と、排出管18を開閉可能とする排出バルブ18aとが設けられており、排出した濃縮固形分は、図示しないバイオ処理手段によりバイオ処理するようになっている。バイオ処理の一例として、おが屑を利用した処理が挙げられる。おが屑を利用した処理とは、おが屑に含まれている微生物の働きで、濃縮固形分が水と二酸化炭素に分解処理するものである。   Furthermore, a discharge pipe 18 that discharges the concentrated solid content that forms the lower layer of the storage tank 9 and a discharge valve 18a that can open and close the discharge pipe 18 are provided at the bottom of the storage tank 9, and the discharged concentration The solid content is bioprocessed by bioprocessing means (not shown). An example of bioprocessing is processing using sawdust. The process using sawdust is a process in which concentrated solids are decomposed into water and carbon dioxide by the action of microorganisms contained in sawdust.

このように、濃縮固形分をバイオ処理することで、濃縮物の汲取り処理を大幅に軽減でき、長期的な循環式水洗トイレ1単体による浄化処理が可能となる。尚、バイオ処理とは、必ずしも上記おが屑を利用した処理に限られず、濃縮固形分を生物学的に処理するものであればよい。   In this way, the concentrated solid content is bioprocessed, so that the process of drawing the concentrate can be greatly reduced, and a long-term purification process using the circulating flush toilet 1 can be performed. The biotreatment is not necessarily limited to the treatment using the sawdust, and any biotreatment of the concentrated solid content may be used.

また、上述した循環式水洗トイレ1は、ユニット全体として可搬型の循環式水洗トイレであってもよい。このようにすることで、上水道若しくは下水道が設置されていない山間部や離島などにも設置できるばかりか、上水道若しくは下水道の故障により常設のトイレが使用不能となる災害時にあっても、任意の場所に循環式水洗トイレ1を設置できる。   Moreover, the circulating flush toilet 1 described above may be a portable circulating flush toilet as a whole unit. By doing in this way, it can be installed not only in mountains or remote islands where water supply or sewerage is not installed, but also in any place even when a permanent toilet becomes unusable due to failure of water supply or sewerage Circulating flush toilet 1 can be installed in

以上、本発明の実施例を図面により説明してきたが、具体的な構成はこれら実施例に限られるものではなく、本発明の要旨を逸脱しない範囲における変更や追加があっても本発明に含まれる。   Although the embodiments of the present invention have been described with reference to the drawings, the specific configuration is not limited to these embodiments, and modifications and additions within the scope of the present invention are included in the present invention. It is.

例えば、上記実施例では、特定時間帯としての夜間において、被処理水のオゾン処理を行っているが、オゾン処理は特定時間帯に限らず、被処理水を第2循環水路に人の操作により任意に流動可能としてもよい。   For example, in the above embodiment, the ozone treatment of the water to be treated is performed at night as the specific time zone, but the ozone treatment is not limited to the specific time zone, and the water to be treated is manually operated in the second circulation channel. It may be arbitrarily flowable.

また、上記実施例では、オゾン処理を行う特定時間帯として夜間を設定しているが、トイレ1を頻繁に使用する時間帯を避ければ、特定時間とは夜間でなくてもよく、例えば深夜若しくは早朝であっても構わない。更に、特定時間帯とは、上述のように1日(24時間)単位において特定した時間帯に限られず、例えば、1月(30日)単位において予め特定した日の時間帯であってもよいし、1年(365日)単位において予め特定した時期の時間帯であってもよい。   Moreover, in the said Example, although the night is set as the specific time slot | zone which performs ozone treatment, if the time slot | zone which uses the toilet 1 frequently is avoided, the specific time may not be night time, for example, midnight or It can be early in the morning. Furthermore, the specific time zone is not limited to the time zone specified in units of one day (24 hours) as described above, and may be, for example, the time zone of days specified in advance in units of January (30 days). In addition, it may be a time zone specified in advance in one year (365 days).

また、上記実施例では、固液分離槽と微生物処理槽とからなる浄化装置により、被処理水を浄化処理しているが、浄化装置は、他の公知の浄化技術を利用した浄化槽からなる装置であってもよい。   Moreover, in the said Example, although the to-be-processed water is purified by the purification apparatus which consists of a solid-liquid separation tank and a microorganisms processing tank, a purification apparatus is an apparatus which consists of a purification tank using another well-known purification technique. It may be.

循環式水洗トイレの特定時間帯における浄化処理を示す概略図である。It is the schematic which shows the purification process in the specific time slot | zone of a circulation type flush toilet. 特定時間帯を除いた時間帯における浄化処理を示す概略図である。It is the schematic which shows the purification process in the time slot | zone except the specific time slot | zone. 送水槽における被処理水の流動状況を示す斜視図である。It is a perspective view which shows the flow condition of the to-be-processed water in a water tank.

符号の説明Explanation of symbols

1 循環式水洗トイレ
2 浄化装置
3 送水槽
4 固液分離槽
4a スクリーン
5 微生物処理槽
5a 微生物固定化担体
6 受水槽
7 オゾン処理室(オゾン処理手段)
8 便器
9 貯留槽
10 分岐管
10a 分岐バルブ
11 供給管
12 送水管(流下管)
12a 送水バルブ(流下手段)
13 洗浄水管(流下管)
13a 洗浄水バルブ(流下手段)
14 導入管
14a 導入バルブ
15 オゾン導入管
16 移送管
17 オゾン発生装置
18 排出管
18a 排出バルブ
19 エア管
20 第1ポンプ(移送手段)
21 第2ポンプ(導入手段)
22 ブロア(搬出手段)
23 散気孔
24 曝気孔
25 仕切壁
25a 堰部
26 仕切壁
27 ダクト
27a 上部孔
27b 下部孔
28a 第1水位検知手段
28b 第2水位検知手段
29 色度センサ(色度検知手段)
30 満水位検知手段
31 エアバルブ
33 水量検知手段
B 上方領域
D 下方領域
S 洗浄水スイッチ
T タイマ
DESCRIPTION OF SYMBOLS 1 Circulating flush toilet 2 Purification apparatus 3 Water tank 4 Solid-liquid separation tank 4a Screen 5 Microbial processing tank 5a Microorganism immobilization support 6 Water receiving tank 7 Ozone processing chamber (ozone processing means)
8 Toilet bowl 9 Storage tank 10 Branch pipe 10a Branch valve 11 Supply pipe 12 Water supply pipe (downflow pipe)
12a Water supply valve (flowing means)
13 Washing water pipe (downflow pipe)
13a Washing water valve (flowing means)
14 introduction pipe 14a introduction valve 15 ozone introduction pipe 16 transfer pipe 17 ozone generator 18 discharge pipe 18a discharge valve 19 air pipe 20 first pump (transfer means)
21 Second pump (introduction means)
22 Blower (unloading means)
23 Aeration hole 24 Aeration hole 25 Partition wall 25a Weir portion 26 Partition wall 27 Duct 27a Upper hole 27b Lower hole 28a First water level detection means 28b Second water level detection means 29 Chromaticity sensor (chromaticity detection means)
30 Water level detection means 31 Air valve 33 Water amount detection means B Upper area D Lower area S Washing water switch T Timer

Claims (11)

被処理水を移送する移送手段を備え便器の下方に配設された受水槽と、該受水槽から移送された被処理水を浄化して排出する浄化装置と、前記受水槽より上方に配設され前記浄化装置から導入した被処理水を少なくとも使用時に前記受水槽に流下させる流下手段を備えた送水槽と、からなる第1循環水路が構成され、該第1循環水路内に被処理水を循環送水し浄化処理する循環式水洗トイレであって、
前記第1循環水路の所定箇所に設けられ、少なくとも一部の被処理水を分岐可能とする分岐管と、該分岐管に接続され、被処理水をオゾン処理するオゾン処理手段と、該オゾン処理手段でオゾン処理された被処理水を前記第1循環水路に供給する供給管と、からなる第2循環水路が構成され、該第2循環水路の所定箇所に、前記第1循環水路内の被処理水を前記第2循環水路内に導入する導入手段が設けられており、
予め特定された特定時間帯内において、前記流下手段が被処理水を前記送水槽から前記受水槽に強制的に流下させるとともに、前記導入手段が前記第1循環水路内の被処理水を前記第2循環水路内に導入することを特徴とする循環式水洗トイレ。
A water receiving tank provided with a transfer means for transferring the water to be treated, disposed below the toilet bowl, a purification device for purifying and discharging the water to be treated transferred from the water receiving tank, and disposed above the water receiving tank. A water supply tank having a flow-down means for flowing down the treated water introduced from the purification device to at least the water receiving tank at the time of use, and a first circulating water channel is configured, and the treated water is placed in the first circulating water channel A circulating flush toilet that circulates water and purifies it,
A branch pipe which is provided at a predetermined location of the first circulation water channel and which can branch at least a part of the water to be treated; an ozone treatment means which is connected to the branch pipe and which treats the water to be treated; and the ozone treatment And a supply pipe for supplying the treated water ozone-treated by the means to the first circulating water channel, and a second circulating water channel is formed at a predetermined position of the second circulating water channel. Introducing means for introducing treated water into the second circulation channel ;
Within the specified time period specified in advance, the flow-down means forcibly causes the water to be treated to flow from the water tank to the water-receiving tank, and the introduction means removes the water to be treated in the first circulation channel. 2 Circulating flush toilet , which is introduced into the circulation channel .
被処理水を分岐可能とする前記分岐管が、前記送水槽に接続されていることを特徴とする請求項に記載の循環式水洗トイレ。 The circulating flush toilet according to claim 1 , wherein the branch pipe capable of branching water to be treated is connected to the water tank. 前記送水槽の下部に前記分岐管が接続されるとともに、前記送水槽の上部に前記供給管が接続されており、前記流下手段と接続された流下管が、前記分岐管より上方で且つ前記供給管より下方において、前記送水槽に接続されていることを特徴とする請求項に記載の循環式水洗トイレ。 The branch pipe is connected to the lower part of the water tank, the supply pipe is connected to the upper part of the water tank, and the flow pipe connected to the flow means is above the branch pipe and the supply The circulating flush toilet according to claim 2 , wherein the circulating flush toilet is connected to the water tank below the pipe. 前記オゾン処理手段の上流側に色度検知手段が設けられており、該色度検知手段により検知された被処理水の色度に応じて、前記導入手段が起動停止可能となっていることを特徴とする請求項1ないしのいずれかに記載の循環式水洗トイレ。 A chromaticity detection means is provided upstream of the ozone treatment means, and the introduction means can be started and stopped according to the chromaticity of the water to be treated detected by the chromaticity detection means. The circulating flush toilet according to any one of claims 1 to 3 . 前記浄化装置は、少なくとも被処理水を固液分離し排出する固液分離槽を備えており、前記第1循環水路と別に、前記固液分離槽において被処理水を固液分離した後の濃縮物を搬出する搬出手段と、濃縮物を貯留する貯留槽が構成され、該貯留槽の所定高さ位置に、濃縮物を前記第2循環水路に導入可能とする導入管が設けられていることを特徴とする請求項1ないしのいずれかに記載の循環式水洗トイレ。 The purification device includes a solid-liquid separation tank that separates and discharges at least water to be treated in a solid-liquid manner, and separates the water to be treated in the solid-liquid separation tank and concentrates the solid-liquid separation in the solid-liquid separation tank. An unloading means for unloading the material and a storage tank for storing the concentrate are configured, and an introduction pipe capable of introducing the concentrate into the second circulation channel is provided at a predetermined height position of the storage tank. The circulating flush toilet according to any one of claims 1 to 4 . 前記貯留槽における所定水量を検知する水量検知手段と、前記貯留槽の所定高さ位置に設けられた前記導入管を開閉可能とする導入バルブと、が更に設けられており、前記導入手段が前記第1循環水路内の被処理水を前記第2循環水路内に導入しており、且つ前記水量検知手段が前記貯留槽の所定水量を検知したときに、前記導入バルブが開状態となることを特徴とする請求項に記載の循環式水洗トイレ。 Water amount detecting means for detecting a predetermined amount of water in the storage tank, and an introduction valve capable of opening and closing the introduction pipe provided at a predetermined height position of the storage tank are further provided, and the introduction means is the When the treated water in the first circulation channel is introduced into the second circulation channel, and the water amount detection means detects the predetermined water amount in the storage tank, the introduction valve is opened. The circulating flush toilet according to claim 5 , wherein 前記貯留槽に堆積した濃縮物をバイオ処理するバイオ処理手段が、更に設けられていることを特徴とする請求項またはに記載の循環式水洗トイレ。 The circulating flush toilet according to claim 5 or 6 , further comprising bioprocessing means for bioprocessing the concentrate deposited in the storage tank. 前記受水槽には、被処理水の満水位を検知する満水位検知手段が設けられており、濃縮物を搬送する前記搬送手段が、前記満水位検知手段により起動することを特徴とする請求項ないしのいずれかに記載の循環式水洗トイレ。 The full water level detection means for detecting the full water level of the water to be treated is provided in the water receiving tank, and the transport means for transporting the concentrate is activated by the full water level detection means. The circulating flush toilet according to any one of 5 to 7 . 前記送水槽に、被処理水の高水位を検知する第1水位検知手段と低水位を検知する第2水位検知手段とが設けられており、被処理水を移送する前記移送手段が、前記第2水位検知手段により起動し、前記第1水位検知手段により停止することを特徴とする請求項1ないしのいずれかに記載の循環式水洗トイレ。 The water tank is provided with a first water level detecting means for detecting a high water level of the treated water and a second water level detecting means for detecting a low water level, and the transferring means for transferring the treated water comprises the first water level detecting means. The circulating flush toilet according to any one of claims 1 to 8 , wherein the circulating flush toilet is started by two water level detection means and stopped by the first water level detection means. 前記オゾン処理手段から前記浄化装置に向けてオゾンを導入するオゾン導入管が設けられていることを特徴とする請求項1ないしのいずれかに記載の循環式水洗トイレ。 The circulating flush toilet according to any one of claims 1 to 9 , further comprising an ozone introduction pipe for introducing ozone from the ozone treatment means toward the purification device. 請求項1ないし10のいずれかに記載の循環式水洗トイレが、可搬型であることを特徴とする可搬型循環式水洗トイレ。 The circulating flush toilet according to any one of claims 1 to 10 , wherein the circulating flush toilet is portable.
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