JP2014040702A - Circulation type toilet - Google Patents

Circulation type toilet Download PDF

Info

Publication number
JP2014040702A
JP2014040702A JP2012182020A JP2012182020A JP2014040702A JP 2014040702 A JP2014040702 A JP 2014040702A JP 2012182020 A JP2012182020 A JP 2012182020A JP 2012182020 A JP2012182020 A JP 2012182020A JP 2014040702 A JP2014040702 A JP 2014040702A
Authority
JP
Japan
Prior art keywords
tank
treatment
chamber
aeration
sewage
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
Application number
JP2012182020A
Other languages
Japanese (ja)
Inventor
Kazuyoshi Udagawa
和義 宇田川
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BIO MICT KK
Original Assignee
BIO MICT KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by BIO MICT KK filed Critical BIO MICT KK
Priority to JP2012182020A priority Critical patent/JP2014040702A/en
Publication of JP2014040702A publication Critical patent/JP2014040702A/en
Pending legal-status Critical Current

Links

Images

Abstract

PROBLEM TO BE SOLVED: To provide a circulation type toilet of which the configuration is simplified and in which efficient aeration treatment can be performed, in the circulation type toilet including: a toilet room, a sewage water tank for storing sewage water from the toilet, a treatment tank for treating sewage water from the sewage water tank and a purification tank for purifying treatment water treated in the treatment tank being provided within an accommodation box; and an aeration treatment chamber being formed within the treatment tank.SOLUTION: An accommodation box is comprised of a cylindrical tank 1 having a horizontal shaft center S, and at least a part of inner wall surfaces of aeration treatment chambers 9a, 11a, 12a is formed from an arcuate inner circumferential surface of the tank 1 from a bottom face of the tank 1 to at least a height of the shaft center S of the tank 1. Therefore, a maximum water level in the aeration treatment chambers 9a, 11a, 12a is set to the height of the shaft center S of the tank 1 or more and sewage water is circulated along the arcuate inner wall surfaces.

Description

この発明は、水を再利用する循環式トイレに関する。   The present invention relates to a circulating toilet that reuses water.

便器が設置されたトイレ室と、トイレ室からの汚水を貯留する汚水槽と、汚水槽からの汚水を処理する処理槽と、処理槽で処理された処理水を浄化する浄化槽とを、単一の収容ボックス内に各別に設け、処理槽内に曝気処理を行う曝気処理室を形成し、浄化された浄化水がトイレ室内に還元される特許文献1に示す循環式トイレが公知になっている。   A toilet room in which a toilet is installed, a sewage tank for storing sewage from the toilet room, a treatment tank for treating sewage from the sewage tank, and a septic tank for purifying the treated water treated in the treatment tank, A circulation type toilet shown in Patent Document 1 is known in which an aeration treatment chamber is provided in each storage box to form an aeration treatment chamber for carrying out aeration treatment, and purified purified water is returned to the toilet chamber. .

実用新案登録第3173972号公報Utility Model Registration No. 3173972

上記文献の循環式トイレは、水を再利用できるので、節水できるとともに仮設トイレとしても利用可能である一方で、曝気処理室の形状によっては汚水がスムーズに対流せずに効率的な曝気処理を行うことができない場合がある他、収容ボックス内に別途、処理槽を設置しているため、装置の構成が複雑化する。   Since the circulation toilet in the above document can reuse water, it can save water and can be used as a temporary toilet. On the other hand, depending on the shape of the aeration treatment chamber, efficient aeration treatment can be performed without convection of sewage smoothly. In addition to being unable to do so, a separate processing tank is installed in the storage box, which complicates the configuration of the apparatus.

本発明は、トイレ室と、トイレ室からの汚水を貯留する汚水槽と、汚水槽からの汚水を処理する処理槽と、処理槽で処理された処理水を浄化する浄化槽とを収容ボックス内に設け、処理槽内に曝気処理室を形成した循環式トイレにおいて、構成が簡略化され、効率的な曝気処理を行うことが可能な循環式トイレを提供することを課題とする。   The present invention includes a toilet box, a sewage tank for storing sewage from the toilet room, a treatment tank for treating sewage from the sewage tank, and a purification tank for purifying the treated water treated in the treatment tank. An object of the present invention is to provide a circulation type toilet having a simplified structure and capable of performing an efficient aeration process in a circulation type toilet provided with an aeration treatment chamber in a treatment tank.

上記課題を解決するため、第1に、トイレ室6と、トイレ室6からの汚水を貯留する汚水槽21と、汚水槽21からの汚水を処理する処理槽9,11,12と、処理槽9,11,12で処理された処理水を浄化する浄化槽44とを、単一の収容ボックス内に各別に設け、処理槽9,11,12内に曝気処理を行う曝気処理室9a,11a,12aを形成し、浄化された浄化水がトイレ室6内に還元される循環式トイレにおいて、収容ボックスを、水平な軸心Sを有する円筒状のタンク1によって構成し、タンク1底面から少なくともタンク1軸心S高さに至る円弧状のタンク1内周面によって、前記曝気処理室9a,11a,12aの内壁面の少なくとも一部を形成することにより、曝気処理室9a,11a,12aの最大水位をタンク1軸心S高さ以上に設定し、曝気処理室9a,11a,12a内において上記円弧状の内壁面に沿って汚水を対流させることにより上記曝気処理を行うことを特徴とする。   In order to solve the above problems, first, the toilet room 6, the sewage tank 21 for storing the sewage from the toilet room 6, the treatment tanks 9, 11, and 12 for treating the sewage from the sewage tank 21, and the treatment tank A purification tank 44 for purifying the treated water treated in 9, 11, 12 is provided separately in a single storage box, and aeration treatment chambers 9a, 11a, for performing aeration treatment in the treatment tanks 9, 11, 12 In the circulating toilet in which 12a is formed and purified water purified is returned to the toilet room 6, the storage box is constituted by a cylindrical tank 1 having a horizontal axis S, and at least the tank from the bottom of the tank 1 By forming at least a part of the inner wall surface of the aeration treatment chamber 9a, 11a, 12a by the inner peripheral surface of the arc-shaped tank 1 reaching the height of the single axis S, the maximum of the aeration treatment chamber 9a, 11a, 12a is formed. Water level on tank 1 axis It is set more than S height, aeration chamber 9a, 11a, by convection wastewater along the arc-shaped inner wall surface in the 12a and performing the aeration treatment.

第2に、タンク1内周の全周によって円形断面の処理槽9,11,12を形成したことを特徴とする。   Second, the processing tanks 9, 11, and 12 having a circular cross section are formed by the entire inner periphery of the tank 1.

第3に、処理槽9,11,12の円形断面を複数に分割する仕切壁14A,14Bを形成し、該分割されたスペースの少なくとも1つを曝気処理室9a,11a,12aとしたことを特徴とする。   Third, the partition walls 14A and 14B that divide the circular sections of the treatment tanks 9, 11, and 12 into a plurality of portions are formed, and at least one of the divided spaces is defined as the aeration treatment chambers 9a, 11a, and 12a. Features.

第4に、前記仕切壁14Bの断面を上下方向に形成し、該仕切壁14Bによって分割される一方を曝気処理室11a,12aとするとともに、他方側を嫌気性処理を行う嫌気性処理室11b,12bとし、曝気処理室11a,12aと嫌気性処理室11b,12bとを連通させる連通口16をタンク1の底側に開口形成したことを特徴とする。   Fourth, the cross section of the partition wall 14B is formed in the vertical direction, and one side divided by the partition wall 14B is set as the aeration process chambers 11a and 12a, and the other side is subjected to the anaerobic process. 12b, and a communication port 16 for communicating the aeration processing chambers 11a, 12a and the anaerobic processing chambers 11b, 12b is formed on the bottom side of the tank 1.

第5に、曝気処理室11a,12a内の上記対流をガイドするガイド部33を前記仕切壁14Bに一体形成したことを特徴とする。   Fifth, a guide portion 33 for guiding the convection in the aeration processing chambers 11a and 12a is formed integrally with the partition wall 14B.

第6に、ガイド部33を、仕切壁14Bの連通口16側端部に一体形成したことを特徴とする。   Sixth, the guide portion 33 is formed integrally with the end portion on the communication port 16 side of the partition wall 14B.

第7に、仕切壁14A,14Bをタンク1と共に一体形成したことを特徴とする。   Seventh, the partition walls 14 </ b> A and 14 </ b> B are integrally formed with the tank 1.

第8に、処理槽9,11,12を、互いに隣接させてタンク1の軸方向に複数配置し、隣接する処理槽9,11,12同士を仕切る隔壁4を設けたことを特徴とする。   Eighth, a plurality of processing tanks 9, 11, and 12 are arranged adjacent to each other in the axial direction of the tank 1, and a partition wall 4 that partitions the adjacent processing tanks 9, 11, and 12 is provided.

第9に、隔壁4をタンク1と共に一体形成したことを特徴とする。   Ninth, the partition 4 is integrally formed with the tank 1.

第10に、浄水を貯水する貯水槽8をタンク1内に形成し、該貯水槽8内に浄化槽44を配置したことを特徴とする。   Tenth, a water tank 8 for storing purified water is formed in the tank 1, and the water tank 8 is disposed in the water tank 8.

上記構成によれば、水平な軸心を有する円筒状のタンクの内周面によって、曝気処理室の内壁面の少なくとも一部を形成することにより、曝気処理室の最大水位がタンク軸心高さ以上に設定され、曝気処理室内において上記円弧状の内壁面に沿って汚水を対流させるため、汚水がよりスムーズに対流して効率的な曝気処理を行うことが可能であるとともに、タンク内周面によって前記曝気処理室の内壁面の少なくとも一部が形成されるため、部品点数を減少して構成が簡略化される。   According to the above configuration, by forming at least a part of the inner wall surface of the aeration processing chamber by the inner peripheral surface of the cylindrical tank having a horizontal axis, the maximum water level of the aeration processing chamber is set to the height of the tank axis. Since the sewage is convected along the arc-shaped inner wall surface in the aeration chamber set as described above, the sewage can be convected more smoothly and efficiently aerated. As a result, at least part of the inner wall surface of the aeration chamber is formed, so that the number of parts is reduced and the configuration is simplified.

また、タンク内周の全周によって円形断面の処理槽を形成したものによれば、タンク内周の全周を処理槽内で利用可能になるため、処理槽の曝気処理室での曝気処理をより効率的に行うことが可能であるとともに、タンク内周の全周によって処理槽の内壁面の大部分が形成されるため、構成がより簡略化される。   In addition, according to the processing tank having a circular cross section formed by the entire inner circumference of the tank, since the entire inner circumference of the tank can be used in the processing tank, aeration processing in the aeration processing chamber of the processing tank is performed. Since it is possible to perform more efficiently and most of the inner wall surface of the treatment tank is formed by the entire circumference of the inner circumference of the tank, the configuration is further simplified.

また、処理槽の円形断面を複数に分割する仕切壁を形成し、該分割されたスペースの少なくとも1つを曝気処理室としたものによれば、処理槽内に曝気処理室の他にも別の処理スペースを確保できるため、処理効率がさらに向上する。   In addition, according to the present invention, a partition wall that divides the circular cross section of the treatment tank into a plurality of parts and at least one of the divided spaces is used as an aeration treatment chamber. Therefore, the processing efficiency is further improved.

さらに、前記仕切壁の断面を上下方向に形成し、該仕切壁によって分割される一方を曝気処理室とするとともに、他方側を嫌気性処理を行う嫌気性処理室とし、曝気処理室と嫌気性処理室とを連通させる連通口をタンクの底側に開口形成したものによれば、曝気処理と、嫌気性処理とによって、より効率的に汚水を浄化処理できる。   Furthermore, the partition wall is formed in a vertical direction, and one side divided by the partition wall serves as an aerobic treatment chamber, and the other side serves as an anaerobic treatment chamber that performs anaerobic treatment. According to the structure in which the communication port for communicating with the processing chamber is formed on the bottom side of the tank, the sewage can be purified more efficiently by the aeration process and the anaerobic process.

なお、曝気処理室内の上記対流をガイドするガイド部を前記仕切壁に一体形成したものによれば、よりスムーズに汚水が曝気処理室内で対流するようになり、処理効率がさらに向上する。   In addition, according to what the guide part which guides the said convection in an aeration process chamber was integrally formed in the said partition wall, a sewage will convect more smoothly in an aeration process chamber, and processing efficiency will further improve.

ちなみに、ガイド部を、仕切壁の連通口側端部に一体形成したものによれば、曝気処理室内で対流している汚水が、その勢いでダイレクトに嫌気性処理室に流入することが抑制され、さらに効率的な曝気処理及び嫌気性処理を行うことが可能になる。   By the way, according to the guide part integrally formed at the end of the partition wall on the communication port side, the sewage convection in the aeration treatment chamber is prevented from flowing directly into the anaerobic treatment chamber. Further, more efficient aeration processing and anaerobic processing can be performed.

また、仕切壁をタンクと共に一体形成したものによれば、構成がさらに簡略化され、製造コストが低減する。   Moreover, according to what integrally formed the partition wall with the tank, a structure is further simplified and manufacturing cost reduces.

また、処理槽を、互いに隣接させてタンクの軸方向に複数配置し、隣接する処理槽同士を仕切る隔壁を設けたものによれば、複数の処理槽によって、より確実な曝気処理を行うことができる。   In addition, according to the method in which a plurality of processing tanks are arranged adjacent to each other in the axial direction of the tank and a partition wall is provided to partition adjacent processing tanks, a more reliable aeration process can be performed by the plurality of processing tanks. it can.

なお、隔壁をタンクと共に一体形成したものによれば、構成がさらに簡略化され、製造コストが低減する。   In addition, according to what formed the partition integrally with the tank, a structure is further simplified and manufacturing cost reduces.

また、浄水を貯水する貯水槽をタンク内に形成し、該貯水槽内に浄化槽を配置したものによれば、浄化槽を形成するスペースを、貯水槽と別に設ける必要がなく、省スペース化を図ることができる。   In addition, according to the water storage tank for storing the purified water formed in the tank and the purification tank disposed in the water storage tank, it is not necessary to provide a space for forming the purification tank separately from the water storage tank, thereby saving space. be able to.

本発明を適用した循環式トイレの正面図である。It is a front view of the circulation type toilet to which the present invention is applied. 図1の循環式トイレの構成を示す平断面図である。It is a plane sectional view which shows the structure of the circulation type toilet of FIG. 図2のA−A断面図である。It is AA sectional drawing of FIG. 図2のB−B断面図である。It is BB sectional drawing of FIG. 図2のC−C断面図である。It is CC sectional drawing of FIG. 図2のD−D断面図である。It is DD sectional drawing of FIG. 図2のE−E断面図である。It is EE sectional drawing of FIG.

図1は、本発明を適用した循環式トイレの正面図であり、図2は、図1の循環式トイレの構成を示す平断面図であり、図3は、図2のA−A断面図であり、図4は、図2のB−B断面図であり、図5は、図2のC−C断面図であり、図6は、図2のD−D断面図であり、図7は、図2のE−E断面図である。   1 is a front view of a circulating toilet to which the present invention is applied, FIG. 2 is a plan sectional view showing the configuration of the circulating toilet of FIG. 1, and FIG. 3 is a sectional view taken along line AA of FIG. 4 is a cross-sectional view taken along line BB in FIG. 2, FIG. 5 is a cross-sectional view taken along line CC in FIG. 2, and FIG. 6 is a cross-sectional view taken along line DD in FIG. These are EE sectional drawing of FIG.

循環式トイレは、水平方向の軸心Sを有する円筒タンク(収容ボックス,タンク)1を備え、円筒タンク1の全長方向の一端面がフラットな前面壁2なるとともに、他端面が外側に凸曲面状に盛上った後面壁3になる。この円筒タンク1の円形断面の内部スペースは、軸心Sに対して垂直又は略垂直な複数の隔壁4によって複数の部屋6,7,8,9,11,12に区切られている。   The circulation toilet includes a cylindrical tank (container box, tank) 1 having a horizontal axis S, one end surface of the cylindrical tank 1 in the full length direction is a flat front wall 2, and the other end surface is a convex curved surface outward. The rear wall 3 swelled in a shape. The internal space of the circular cross section of the cylindrical tank 1 is partitioned into a plurality of rooms 6, 7, 8, 9, 11, and 12 by a plurality of partition walls 4 that are perpendicular or substantially perpendicular to the axis S.

言換えると、円筒タンク1の断面視円形リング状の周壁全周によって形成された円形断面の部屋6,7,8,9,11,12が、円筒タンク1の軸心Sの方向に複数配列され、この隣接する部屋6,7,8,9,11,12同士が隔壁4によって隔てられている。   In other words, a plurality of circular sections 6, 7, 8, 9, 11, and 12 formed by the entire circumference of the circular ring-shaped peripheral wall of the cylindrical tank 1 are arranged in the direction of the axis S of the cylindrical tank 1. The adjacent rooms 6, 7, 8, 9, 11, 12 are separated by the partition 4.

この複数の部屋6,7,8,9,11は、前面壁2から後面壁3に向かって順番に、トイレ室6、制御盤13等が設置された機械室7と、浄化された浄水が貯水される貯水槽8と、トイレ室6からの汚水を処理する第1処理槽(処理槽)9と、汚水を処理する第2処理槽(処理槽)11と、汚水を処理する第3処理槽(処理槽)12になる。   In the plurality of rooms 6, 7, 8, 9, and 11, in order from the front wall 2 to the rear wall 3, the machine room 7 in which the toilet room 6, the control panel 13 and the like are installed and the purified water are A water storage tank 8 for storing water, a first treatment tank (treatment tank) 9 for treating sewage from the toilet room 6, a second treatment tank (treatment tank) 11 for treating sewage, and a third treatment for treating sewage. It becomes a tank (processing tank) 12.

トイレ室6及び3つの処理槽9,11,12の各部屋には、自身の円形断面の空間を複数に分割する仕切壁14A,14Bが形成されている。仕切壁14A,14Bは、断面視で上下方向に形成され且つ軸心Sを通るように円筒タンク1の全長方向に延びている。   In each of the toilet room 6 and the three treatment tanks 9, 11, and 12, partition walls 14A and 14B that divide the space of the circular section of itself into a plurality are formed. The partition walls 14 </ b> A and 14 </ b> B are formed in the vertical direction in a cross-sectional view and extend in the full length direction of the cylindrical tank 1 so as to pass through the axis S.

トイレ室6及び第1処理槽9の仕切壁14Aは、円筒タンク1内の天井面から底面に至る全範囲に形成されて空間を完全に隔てる非連通用仕切壁になり、第2処理槽及び第3処理槽の仕切壁14Bは、円筒タンク1内の天井面から底面の手前に至る範囲に形成された連通用仕切壁になる。連通用仕切壁14Bの下端と円筒タンク1内の底面との間には、該仕切壁14Bによって分割された隣接スペース同士を連通させる連通口16が形成される。   The partition wall 14A of the toilet room 6 and the first treatment tank 9 is a non-communication partition wall that is formed in the entire range from the ceiling surface to the bottom surface in the cylindrical tank 1 and completely separates the space. The partition wall 14B of the third treatment tank is a communication partition wall formed in a range from the ceiling surface in the cylindrical tank 1 to the front of the bottom surface. A communication port 16 for communicating adjacent spaces divided by the partition wall 14B is formed between the lower end of the communication partition wall 14B and the bottom surface in the cylindrical tank 1.

なお、上述した円筒タンク1の周壁、前面壁2及び後面壁3は、隔壁4及び仕切壁14A,14Bと共にFRP等の硬化性合成樹脂によって一体形成される。   The peripheral wall, the front wall 2 and the rear wall 3 of the cylindrical tank 1 described above are integrally formed with a partition 4 and partition walls 14A and 14B by a curable synthetic resin such as FRP.

このように構成される2種類の仕切壁14A,14Bによって、トイレ室6及び3つの処理槽9,11,12は、それぞれ軸心Sを境に左右に等分に分割される。   By the two types of partition walls 14A and 14B configured as described above, the toilet room 6 and the three treatment tanks 9, 11, and 12 are each equally divided into left and right with the axis S as a boundary.

仕切壁14Aによって2分割されたトイレ室6の一方の空間は第1トイレルーム6aになり、他方の空間は第2トイレルーム6bとなる。この2つのトイレルーム6a,6bには、それぞれ1つの洋式の便器17が設置され、前記前面壁2には、トイレルーム6a,6b毎に出入口18が開口形成され、利用者がトイレルーム6a,6bを出入する際に用いる出入口18を開閉する開閉扉19が、出入口18毎に前面壁2側に設置されている。   One space of the toilet room 6 divided into two by the partition wall 14A becomes the first toilet room 6a, and the other space becomes the second toilet room 6b. Each of the two toilet rooms 6a and 6b is provided with one Western-style toilet bowl 17, and the front wall 2 is formed with an entrance 18 for each of the toilet rooms 6a and 6b. An opening / closing door 19 that opens and closes the entrance / exit 18 used when entering / exiting 6b is installed on the front wall 2 side for each entrance / exit 18.

また、仕切壁14Aによって2分割された第1処理槽9の一方の空間は導入室(曝気処理室)9aになるとともに、他方の空間は貯留室9bになる。第2処理槽11における仕切壁14Bによって、2分割された一方の空間は、該導入室9aと前後で隣接する第1好気性処理室(曝気処理室,好気性処理室)11aになるとともに、他方の空間は第1嫌気性処理室(嫌気性処理室)11bになる。仕切壁14Bによって2分割された第3処理槽12の一方の空間は、第1嫌気性処理室11bと隣接する第2好気性処理室(曝気処理室,好気性処理室)12aになるとともに、他方の空間は第2嫌気性処理室(嫌気性処理室)12bになる。   One space of the first processing tank 9 divided into two by the partition wall 14A is an introduction chamber (aeration processing chamber) 9a, and the other space is a storage chamber 9b. One space divided into two by the partition wall 14B in the second treatment tank 11 becomes a first aerobic treatment chamber (aeration treatment chamber, aerobic treatment chamber) 11a adjacent to the introduction chamber 9a in the front and rear, The other space becomes a first anaerobic processing chamber (anaerobic processing chamber) 11b. One space of the third treatment tank 12 divided into two by the partition wall 14B becomes a second aerobic treatment chamber (aeration treatment chamber, aerobic treatment chamber) 12a adjacent to the first anaerobic treatment chamber 11b, and The other space becomes a second anaerobic processing chamber (anaerobic processing chamber) 12b.

本循環式トイレは、以上のように形成される機械室7、貯水槽8及び3つの処理槽9,11,12によって、トレイ室6からの汚水を処理して浄化し、再度、トイレ室6の便器17の洗浄タンク17aに戻して利用する循環処理を行うものであり、以下、この循環処理の構成を詳述する。   This circulating toilet treats and purifies sewage from the tray chamber 6 by the machine room 7, the water storage tank 8 and the three treatment tanks 9, 11, and 12 formed as described above. The circulation process is performed by returning to the washing tank 17a of the toilet bowl 17, and the configuration of the circulation process will be described in detail below.

上記機械室7の床下には円筒タンク1の周壁等によって汚水槽21が形成され、この他、機械室7には、前記制御盤13と、トイレ室6の便器17と汚水槽21とを接続する汚水管22と、汚水槽21と導入室9aとを接続する導入管23と、貯水槽8と便器17(具体的には洗浄タンク17a)とを接続する洗浄管24と、外部の図示しない水道管と便器17の洗浄タンク17aとを接続する配水管26とが設けられている。   A sewage tank 21 is formed under the floor of the machine room 7 by the peripheral wall of the cylindrical tank 1, and the control panel 13, the toilet 17 of the toilet room 6, and the sewage tank 21 are connected to the machine room 7. The sewage pipe 22 to be connected, the introduction pipe 23 to connect the sewage tank 21 and the introduction chamber 9a, the washing pipe 24 to connect the water storage tank 8 and the toilet bowl 17 (specifically, the washing tank 17a), and an external not shown A water distribution pipe 26 that connects the water pipe and the cleaning tank 17a of the toilet bowl 17 is provided.

汚水槽21には、汚水管22によって、便器17からの排泄物を含んだ汚水が流入して貯留される。この汚水槽21内には導入ポンプ27が設けられ、この導入ポンプ27は、汚水槽21内の汚水を、前記導入管23を介して導入室9aに導入する。ちなみに、汚水槽21の導入ポンプ27側と、それ以外の部分とを仕切る仕切28を、該汚水槽21内に形成しており、この仕切28によって、汚水槽21内の汚水は、固形物がある程度分離された状態で、導入ポンプ27側に到達し、導入室9aに導入される。   In the sewage tank 21, sewage containing excrement from the toilet 17 flows in and is stored by the sewage pipe 22. An introduction pump 27 is provided in the sewage tank 21, and the introduction pump 27 introduces sewage in the sewage tank 21 into the introduction chamber 9 a through the introduction pipe 23. Incidentally, a partition 28 for separating the introduction pump 27 side of the sewage tank 21 from other parts is formed in the sewage tank 21, and the sewage in the sewage tank 21 is made of solid matter by the partition 28. In a state separated to some extent, it reaches the introduction pump 27 side and is introduced into the introduction chamber 9a.

上記導入室9aは、貯水槽8と第1処理槽9とを隔てる壁部4と、第1処理槽9と第2処理槽11を隔てる壁部4と、円筒タンク1の底面から天井面に至る断面視半径状の内周面(円弧面)と、仕切壁14Aとによって形成され、これらの部材によって導入室9aの内壁面が形成されるとともに、導入室9aの最大水位が円筒タンク1内の天井側に設定される。ちなみに、導入室9aの最大水位を、軸心Sの高さ以上に設定するため、円筒タンク1の底面から少なくとも軸心Sの高さに至る円弧状の円筒タンク1内周面によって、導入室9aの内壁面の少なくとも一部を形成する必要がある。   The introduction chamber 9a includes a wall 4 separating the water storage tank 8 and the first treatment tank 9, a wall 4 separating the first treatment tank 9 and the second treatment tank 11, and a bottom surface of the cylindrical tank 1 from the bottom surface to the ceiling surface. The inner circumferential surface (circular arc surface) having a radial shape in cross section and the partition wall 14A are formed, and the inner wall surface of the introduction chamber 9a is formed by these members, and the maximum water level of the introduction chamber 9a is within the cylindrical tank 1 It is set on the ceiling side. Incidentally, in order to set the maximum water level of the introduction chamber 9a to be equal to or higher than the height of the shaft center S, the introduction chamber is formed by the inner circumferential surface of the circular cylindrical tank 1 extending from the bottom surface of the cylindrical tank 1 to at least the height of the shaft center S. It is necessary to form at least a part of the inner wall surface of 9a.

この導入室9a内の底側にはブロア29が設置され、このブロア29には機械室7側からのエア配管31に接続され、該ブロア29は、上方に向かって高圧(具体的には、750[L/min])のエアを噴射するように構成されている。この上方に噴射されるエアによって、導入室9a内の汚水を、空気と混合しながら対流させる曝気処理を行う。この曝気処理は、酸素のある状態で育成されて増殖する微生物である好気性微生物によって、汚水を酸化させて浄化する好気性処理の一種である。しかも、ブロア29から噴射されるエアが高圧であるため、好気性処理がより促進されるとともに、汚水に含まれる固形物が細かく粉砕される。   A blower 29 is installed on the bottom side of the introduction chamber 9a. The blower 29 is connected to an air pipe 31 from the machine chamber 7 side, and the blower 29 has a high pressure (specifically, 750 [L / min]). By the air jetted upward, an aeration process is performed in which the sewage in the introduction chamber 9a is convected while being mixed with air. This aeration treatment is a kind of aerobic treatment in which sewage is oxidized and purified by an aerobic microorganism that is a microorganism that grows and proliferates in the presence of oxygen. Moreover, since the air jetted from the blower 29 is at a high pressure, the aerobic treatment is further promoted, and the solid matter contained in the sewage is finely pulverized.

このようにして、曝気処理された導入室9a内の汚水は、導入室9aと第1好気性処理室11aとを隔てる隔壁4の上部に穿設された導入孔4aによって、第1好気性処理室11aに導入される。すなわち、導入孔4aの下端の高さが、導入室9aの最大水位に設定される。   Thus, the sewage in the introduction chamber 9a subjected to the aeration treatment is subjected to the first aerobic treatment by the introduction hole 4a formed in the upper part of the partition wall 4 separating the introduction chamber 9a and the first aerobic treatment chamber 11a. It is introduced into the chamber 11a. That is, the height of the lower end of the introduction hole 4a is set to the maximum water level of the introduction chamber 9a.

上記第1好気性処理室11aは、第1処理槽9と第2処理槽11とを隔てる壁部4と、第2処理槽11と第3処理槽12を隔てる壁部4と、円筒タンク1の底面から天井面に至る断面視半径状の内周面(円弧面)と、仕切壁14Bとによって形成され、これらの部材によって第1好気性処理室11aの内壁面が形成されるとともに、第1好気性処理室11aの最大水位が軸心Sの高さ以上に設定される。ちなみに、第1好気性処理室11aの最大水位を軸心Sの高さ以上に設定するため、円筒タンク1の底面から少なくとも軸心Sの高さに至る円弧状の円筒タンク1内周面によって、第1好気性処理室11aの内壁面の少なくとも一部を形成する必要がある。   The first aerobic processing chamber 11a includes a wall 4 separating the first processing tank 9 and the second processing tank 11, a wall 4 separating the second processing tank 11 and the third processing tank 12, and the cylindrical tank 1. The inner peripheral surface (arc surface) having a radial cross section from the bottom surface to the ceiling surface and the partition wall 14B are formed by these members, and the inner wall surface of the first aerobic processing chamber 11a is formed by these members. The maximum water level of the one aerobic processing chamber 11a is set to be equal to or higher than the height of the axis S. Incidentally, in order to set the maximum water level of the first aerobic processing chamber 11a to be equal to or higher than the height of the axial center S, the inner circumferential surface of the circular cylindrical tank 1 extending from the bottom surface of the cylindrical tank 1 to at least the height of the axial center S. It is necessary to form at least a part of the inner wall surface of the first aerobic processing chamber 11a.

この第1好気性処理室11aの底側にはブロア32が設置され、このブロア32には機械室7側からの図示しないエア配管が接続され、該ブロア32は、上方に向かって通常圧(導入室9aのブロア29よりも低圧で、具体的には、80[L/min])のエアを噴射するように構成されている。この上方に噴射されるエアによって、第1好気性処理室11a内の汚水を、空気と混合しながら対流させる曝気処理を行う。ちなみに、この曝気処理は、導入室9aよりも低圧のエアで行われるため、処理効率は、導入室9aよりは低く設定される。   A blower 32 is installed on the bottom side of the first aerobic processing chamber 11a, and an air pipe (not shown) from the machine chamber 7 side is connected to the blower 32, and the blower 32 has a normal pressure (upward). The air is lower in pressure than the blower 29 in the introduction chamber 9a, specifically, 80 [L / min]). By the air jetted upward, aeration processing is performed in which sewage in the first aerobic processing chamber 11a is convected while being mixed with air. Incidentally, since this aeration process is performed with air having a pressure lower than that of the introduction chamber 9a, the processing efficiency is set lower than that of the introduction chamber 9a.

また、この第1好気性処理室11aと第1嫌気性処理室11bとを仕切る連通用仕切壁14Bの下端部(連通口16側端部)には、下方に向かって第1好気性処理室11a側に湾曲形成されたガイド部33が一体形成され、このガイド部33によって、対流している汚水が第1嫌気性処理室11bに流入することを抑制するとともに、第1好気性処理質11a内で、汚水をよりスムーズに対流させ、好気性処理を促進する。このようにして、曝気処理された第1好気性処理室11a内の汚水は、上記連通口16によって、第1嫌気性処理室11b内に流入する。   In addition, a first aerobic processing chamber is directed downward at a lower end portion (end portion on the side of the communication port 16) of the communication partition wall 14B that partitions the first aerobic processing chamber 11a and the first anaerobic processing chamber 11b. A guide portion 33 that is curved on the 11a side is integrally formed, and the guide portion 33 suppresses inflow of convective sewage into the first anaerobic treatment chamber 11b and also the first aerobic treatment quality 11a. Inside, sewage is convected more smoothly and aerobic treatment is promoted. In this way, the sewage in the first aerobic processing chamber 11a subjected to the aeration process flows into the first anaerobic processing chamber 11b through the communication port 16.

上記第1嫌気性処理室11bは、第1処理槽9と第2処理槽11とを隔てる壁部4と、第2処理槽11と第3処理槽12を隔てる壁部4と、円筒タンク1の底面から天井面に至る断面視半径状の内周面(円弧面)と、仕切壁14Bとによって形成され、これらの部材によって第1嫌気性処理室11bの内壁面が形成されるとともに、第1嫌気性処理室11bの最大水位が軸心Sの高さ以上に設定される。ちなみに、第1嫌気性処理室11bの最大水位が軸心Sの高さ以上に設定するため、円筒タンク1の底面から少なくとも軸心Sの高さに至る円弧状の円筒タンク1内周面によって、第1嫌気性処理室11bの内壁面の少なくとも一部を形成する必要がある。   The first anaerobic treatment chamber 11b includes a wall 4 separating the first treatment tank 9 and the second treatment tank 11, a wall 4 separating the second treatment tank 11 and the third treatment tank 12, and the cylindrical tank 1. The inner circumferential surface (arc surface) having a radial cross section from the bottom surface to the ceiling surface and the partition wall 14B are formed by these members, and the inner wall surface of the first anaerobic treatment chamber 11b is formed by these members. The maximum water level of the one anaerobic treatment chamber 11b is set to be equal to or higher than the height of the axis S. Incidentally, since the maximum water level of the first anaerobic treatment chamber 11b is set to be equal to or higher than the height of the axial center S, the inner circumferential surface of the circular arc-shaped cylindrical tank 1 extending from the bottom surface of the cylindrical tank 1 to at least the height of the axial center S. It is necessary to form at least a part of the inner wall surface of the first anaerobic treatment chamber 11b.

この第1嫌気性処理室11b内では、汚水を対流させず空気が混合しない状態とする。これによって、汚水中の酸素濃度を低下させ、酸素が無い状態で育成されて増殖する微生物である嫌気性微生物が育成及び増殖し、この嫌気性微生物によって、汚水を還元分解させて浄化する嫌気性処理が行われる。   In the first anaerobic treatment chamber 11b, sewage is not convected and air is not mixed. This reduces the oxygen concentration in the sewage, and anaerobic microorganisms that grow and proliferate in the absence of oxygen grow and proliferate, and the anaerobic microorganisms reduce and purify the sewage by reductive decomposition. Processing is performed.

このようにして、嫌気性処理された第1嫌気性処理室11b内の汚水は、第1嫌気性処理室11bと第2好気性処理室12aとを隔てる隔壁4の上部に穿設された導入孔4aによって、第2好気性処理室12aに導入される。すなわち、この導入孔4aの下端の高さが、第2処理槽11(第1好気性処理室11a及び第1嫌気性処理室11b)の最大水位に設定され、この最大水位は導入室9aよりも低くなる。   In this way, the sewage in the first anaerobic treatment chamber 11b subjected to the anaerobic treatment is introduced in the upper part of the partition wall 4 separating the first anaerobic treatment chamber 11b and the second aerobic treatment chamber 12a. It introduce | transduces into the 2nd aerobic processing chamber 12a by the hole 4a. That is, the height of the lower end of the introduction hole 4a is set to the maximum water level of the second treatment tank 11 (the first aerobic treatment chamber 11a and the first anaerobic treatment chamber 11b), and this maximum water level is higher than that of the introduction chamber 9a. Also lower.

上記第2好気性処理室12aは、第2処理槽11と第3処理槽12とを隔てる壁部4と、後面壁3と、円筒タンク1の底面から天井面に至る断面視半径状の内周面(円弧面)と、仕切壁14Bとによって形成され、これらの部材によって第2好気性処理室12aの内壁面が形成されるとともに、第2好気性処理室12aの最大水位が軸心Sの高さ以上に設定される。ちなみに、第2好気性処理室12aの最大水位を軸心Sの高さ以上に設定するため、円筒タンク1の底面から少なくとも軸心Sの高さに至る円弧状の円筒タンク1内周面によって、第2好気性処理室12aの内壁面の少なくとも一部を形成する必要がある。   The second aerobic processing chamber 12a includes a wall portion 4 that separates the second processing tank 11 and the third processing tank 12, a rear surface wall 3, and a radial inner section from the bottom surface of the cylindrical tank 1 to the ceiling surface. These members are formed by the peripheral surface (arc surface) and the partition wall 14B, and the inner wall surface of the second aerobic processing chamber 12a is formed by these members, and the maximum water level of the second aerobic processing chamber 12a is the axis S. It is set to a height higher than. Incidentally, in order to set the maximum water level of the second aerobic processing chamber 12a to be equal to or higher than the height of the axial center S, the inner circumferential surface of the circular cylindrical tank 1 extending from the bottom surface of the cylindrical tank 1 to at least the height of the axial center S. It is necessary to form at least a part of the inner wall surface of the second aerobic processing chamber 12a.

この第2好気性処理室12aの底側にはブロア34が設置され、このブロア34には機械室7側からの図示しないエア配管に接続され、該ブロア34は、上方に向かって通常圧(導入室9aのブロア29よりも低圧で、具体的には、第1好気性処理室11aのブロア32の圧力と同一の80[L/min])のエアを噴射するように構成されている。この上方に噴射されるエアによって、第2好気性処理室12a内の汚水を、空気と混合しながら対流させる曝気処理を行う。   A blower 34 is installed on the bottom side of the second aerobic processing chamber 12a, and this blower 34 is connected to an air pipe (not shown) from the machine chamber 7 side. More specifically, the air is injected at a pressure lower than that of the blower 29 in the introduction chamber 9a, specifically, 80 [L / min], which is the same as the pressure of the blower 32 in the first aerobic processing chamber 11a. By the air jetted upward, aeration processing is performed in which sewage in the second aerobic processing chamber 12a is convected while being mixed with air.

また、この第2好気性処理室12aと第2嫌気性処理室12bとの仕切る連通用仕切壁14Bの下端部(連通口16側端部)には、下方に向かって第2好気性処理室12a側に湾曲形成されたガイド部33が一体形成され、このガイド部33によって、対流している汚水が第2嫌気性処理室12bに流入することを抑制するとともに、汚水をよりスムーズに対流させ、好気性処理を促進する。   Further, the second aerobic processing chamber is directed downward at the lower end portion (end portion on the side of the communication port 16) of the communication partition wall 14B that partitions the second aerobic processing chamber 12a and the second anaerobic processing chamber 12b. The guide part 33 curvedly formed on the 12a side is integrally formed, and the guide part 33 prevents the convective sewage from flowing into the second anaerobic treatment chamber 12b and convects the sewage more smoothly. Promote aerobic treatment.

このようにして、曝気処理された第2好気性処理室12a内の汚水は、上記ガイド部33と、円筒タンク1の底面との間に形成された上記連通口16によって、第2嫌気性処理室12b内に流入する。   In this way, the sewage in the second aerobic processing chamber 12a subjected to the aeration process is subjected to the second anaerobic process by the communication port 16 formed between the guide portion 33 and the bottom surface of the cylindrical tank 1. It flows into the chamber 12b.

上記第2嫌気性処理室12bは、第2処理槽11と第3処理槽12とを隔てる壁部14と、後面壁3と、円筒タンク1の底面から天井面に至る断面視半径状の内周面(円弧面)と、仕切壁14Bとによって形成され、これらの部材によって第2嫌気性処理室12bの内壁面が形成されるとともに、第2嫌気性処理室12bの最大水位が軸心Sの高さ以上に設定される。ちなみに、第2嫌気性処理室12bの最大水位を軸心Sの高さ以上に設定するため、円筒タンク1の底面から少なくとも軸心Sの高さに至る円弧状の円筒タンク1内周面によって、第2嫌気性処理室12bの内壁面の少なくとも一部を形成する必要がある。   The second anaerobic processing chamber 12b has a wall portion 14 that separates the second processing tank 11 and the third processing tank 12, the rear wall 3, and a radial inner section from the bottom surface of the cylindrical tank 1 to the ceiling surface. The inner wall surface of the second anaerobic treatment chamber 12b is formed by the peripheral surface (arc surface) and the partition wall 14B, and the maximum water level of the second anaerobic treatment chamber 12b is the axis S. It is set to a height higher than. Incidentally, in order to set the maximum water level of the second anaerobic treatment chamber 12b to be equal to or higher than the height of the axial center S, the inner circumferential surface of the arc-shaped cylindrical tank 1 extending from the bottom surface of the cylindrical tank 1 to at least the height of the axial center S. It is necessary to form at least a part of the inner wall surface of the second anaerobic treatment chamber 12b.

この第2嫌気性処理室12b内では、汚水を対流させず空気が混合しない状態とする。これによって、上述した嫌気性処理が行われる。第2嫌気性処理室12bの上部から貯留室9bの第2処理槽寄り部分に至る範囲には処理水管36が配管され、該処理水管36の一端側(図示する例では、貯留室9b側端部)には、嫌気性処理された第2嫌気性処理室12b内の汚水を処理水として貯留室9bに送出す貯留ポンプ37が設置されている。   In the second anaerobic treatment chamber 12b, sewage is not convected and air is not mixed. Thereby, the anaerobic process described above is performed. A treated water pipe 36 is provided in a range from the upper part of the second anaerobic treatment chamber 12b to a portion near the second treatment tank of the storage chamber 9b, and one end side of the treated water pipe 36 (in the illustrated example, the end of the storage chamber 9b side). Part) is provided with a storage pump 37 for sending the sewage in the second anaerobic processing chamber 12b subjected to anaerobic processing to the storage chamber 9b as treated water.

上記貯留室9bと、第1好気性処理室11aとは還元管38によって接続されるとともに、この貯留室9bと、貯水槽8とは浄水管39によって接続される。貯留室9b内に設置された還元ポンプ41によって送出される処理水は、還元管38を介して、汚水として第1好気処理室11aに還元される。また、貯留室9b内の上部且つ貯水槽8寄り箇所に設置された浄水ポンプ42によって送出される処理水は、浄水管39を介して、貯水槽8に導入される。   The storage chamber 9b and the first aerobic treatment chamber 11a are connected by a reduction pipe 38, and the storage chamber 9b and the water storage tank 8 are connected by a water purification pipe 39. The treated water sent out by the reduction pump 41 installed in the storage chamber 9b is returned to the first aerobic treatment chamber 11a as sewage through the reduction pipe 38. Further, the treated water sent out by the water purification pump 42 installed in the upper part of the storage chamber 9 b and near the water storage tank 8 is introduced into the water storage tank 8 through the water purification pipe 39.

貯留室9bを、貯水槽8寄り空間と、第2処理槽11寄りの空間との分割する分割壁43が設けられ、この分割壁43の下端と、円筒タンク1内の底面との間は、開口しており、第2嫌気性処理室12bから貯留室9bに送られてくる処理水が、上記開口した部分を介して、浄水ポンプ42側に至り、浄水管39を介して、貯水槽8内に送られる。一方、貯留室9bの処理水の水質が所定以下の場合には、還元ポンプ41によって、還元管38から、第1好気性処理室11aに戻される。   A dividing wall 43 that divides the storage chamber 9b into a space close to the water storage tank 8 and a space close to the second processing tank 11 is provided, and the space between the lower end of the dividing wall 43 and the bottom surface in the cylindrical tank 1 is The treated water that is open and sent from the second anaerobic treatment chamber 12b to the storage chamber 9b reaches the purified water pump 42 side through the opened portion, and passes through the purified water pipe 39 to the water storage tank 8. Sent in. On the other hand, when the quality of the treated water in the storage chamber 9b is below a predetermined level, the reduction pump 41 returns the water from the reduction pipe 38 to the first aerobic treatment chamber 11a.

上記貯水槽8には、上下方向に延びる円筒状の浄化槽44が、平面視で、上記軸心Sに対して交差(直交)する方向に複数(図示する例では2つ)並列配置されている。貯水槽8における浄化槽44が占める以外のスペースは、浄化槽44によって浄化された浄化水が貯水される貯水スペース8aになる。   In the water storage tank 8, a plurality of (two in the illustrated example) parallel-arranged cylindrical purification tanks 44 extending in the vertical direction are arranged in a direction intersecting (orthogonal) with the axis S in plan view. . The space other than that occupied by the septic tank 44 in the water storage tank 8 is a water storage space 8a in which the purified water purified by the septic tank 44 is stored.

各浄化槽44は、上下方向に延びる円筒状の浄化筒46と、浄化筒46の直下に配置された下部タンク47とを備えている。浄化筒46内の上部には、平面視で浄化筒46の円形断面に内側から沿う円形リング状の散水パイプ48が設置され、浄化筒46内の散水パイプ48の直下には、木材チップが充填された処理層49が形成されている。木材チップは、広い表面積を有し、好気性微生物と嫌気性微生物の両方が棲息している。そして、散水パイプ48から下方に円形状に散水された処理水は、チップ層49を下方に流動する過程で、好気性処理及び嫌気性処理の両方が行われて浄化され、下部タンク47に漏下して貯水される。   Each purification tank 44 includes a cylindrical purification cylinder 46 extending in the vertical direction, and a lower tank 47 disposed immediately below the purification cylinder 46. In the upper part of the purification cylinder 46, a circular ring-shaped water sprinkling pipe 48 is installed along the circular cross section of the purification cylinder 46 in plan view from the inside, and wood chips are filled immediately below the water spraying pipe 48 in the purification cylinder 46. The treated layer 49 is formed. Wood chips have a large surface area and are inhabited by both aerobic and anaerobic microorganisms. Then, the treated water sprayed in a circular shape downward from the sprinkling pipe 48 is purified through both aerobic treatment and anaerobic treatment in the process of flowing down the tip layer 49 and leaks into the lower tank 47. Is stored.

隣接する浄化槽44,44同士は、接続管51によって接続されている。具体的には、一方の浄化槽44の下部タンク47と、他方の浄化槽44の散水パイプ48とが接続管51によって接続され、該一方の浄化槽44の下部タンク47側に設置された散水ポンプ52によって、該下部タンク47内の処理水が、上記他方の浄化槽44の散水パイプ48に送られ、該浄化槽44の上部で前記散水が行われる。   Adjacent septic tanks 44, 44 are connected by a connecting pipe 51. Specifically, a lower tank 47 of one septic tank 44 and a watering pipe 48 of the other septic tank 44 are connected by a connecting pipe 51, and a watering pump 52 installed on the lower tank 47 side of the one septic tank 44 is used. The treated water in the lower tank 47 is sent to the watering pipe 48 of the other septic tank 44, and the watering is performed on the upper part of the septic tank 44.

また、最初にチップ層49により浄化処理を行う浄化槽44の散水パイプ48には、上述した浄水管39が接続され、前記浄水ポンプ42によって送出される処理水が、該散水パイプ48から散水される。   Further, the water purification pipe 39 of the purification tank 44 that performs the purification process first by the tip layer 49 is connected to the water purification pipe 39 described above, and the treated water sent out by the water purification pump 42 is sprinkled from the watering pipe 48. .

一方、最後にチップ層49により浄化処理を行う浄化槽44の下部タンク47側には、貯水ポンプ53が設置され、該下部タンク47と貯水スペース8aとの間には貯水管54が配管され、この浄化槽44の下部タンク47内の処理水が、浄水として貯水スペース8aに送られて貯水される。このようにして、貯水スペース8aに貯水された浄水は、洗浄管24によって、便器17の洗浄タンク17aに戻され、洗浄水として再利用される。   On the other hand, a water storage pump 53 is installed on the side of the lower tank 47 of the purification tank 44 that finally performs the purification treatment with the chip layer 49, and a water storage pipe 54 is provided between the lower tank 47 and the water storage space 8a. The treated water in the lower tank 47 of the septic tank 44 is sent to the water storage space 8a as purified water and stored. Thus, the purified water stored in the water storage space 8a is returned to the cleaning tank 17a of the toilet 17 by the cleaning pipe 24 and reused as cleaning water.

以上のように構成される循環式トレイでは、便器17→汚水槽21→導入室9a→第1好気性処理室11a→第1嫌気性処理室11b→第2好気性処理室12a→第2嫌気性処理室12b→貯留室9b→浄化槽44→浄化槽44→浄水スペース8a→便器17→・・・と続く水の循環によって、洗浄水が再利用される。   In the circulation tray configured as described above, the toilet bowl 17 → the sewage tank 21 → the introduction chamber 9a → the first aerobic processing chamber 11a → the first anaerobic processing chamber 11b → the second aerobic processing chamber 12a → the second anaerobic. Washing water is reused by the circulation of water, such as the treatment chamber 12b → the storage chamber 9b → the purification tank 44 → the purification tank 44 → the purified water space 8a → the toilet 17 →.

導入室9aから第1好気性処理室11aへの汚水の移動と、第1嫌気性処理室11bから第2好気性処理室12aへの汚水の移動は、最大水位を順次低く設定した導入孔4aを介して行い、ポンプ等が不要であるため、構成が簡略化される。   The movement of the sewage from the introduction chamber 9a to the first aerobic treatment chamber 11a and the movement of the sewage from the first anaerobic treatment chamber 11b to the second aerobic treatment chamber 12a are the introduction holes 4a in which the maximum water level is sequentially set lower. The configuration is simplified because no pump or the like is required.

また、第1好気性処理室11aから第1嫌気性処理室11bへの汚水の移動と、第2好気性処理室12aから第2嫌気性処理室12bへの汚水の移動も、連通口16を介して行われるため、動力が不要で、構成が簡略化される。   In addition, the movement of sewage from the first aerobic treatment chamber 11a to the first anaerobic treatment chamber 11b and the movement of sewage from the second aerobic treatment chamber 12a to the second anaerobic treatment chamber 12b are also performed through the communication port 16. Therefore, no power is required and the configuration is simplified.

また、導入室9a、第1好気性処理室11a及び第2好気性処理室12aでは、円筒タンク1の円形断面によって形成された円弧面状の内壁面に沿って、汚水を円滑に対流させるため、好気性処理が円滑に行われる。しかも、導入室9aは、高圧のブロアによって、汚水を対流させると共に、汚水の含まれた固形物が粉砕される。   Further, in the introduction chamber 9a, the first aerobic processing chamber 11a, and the second aerobic processing chamber 12a, the sewage is smoothly convected along the arcuate inner wall surface formed by the circular cross section of the cylindrical tank 1. The aerobic process is smoothly performed. Moreover, in the introduction chamber 9a, the sewage is convected by the high-pressure blower and the solid matter containing the sewage is pulverized.

さらに、円筒タンク1の円弧状の底面によって、汚水のスムーズな流動が促進されるため、3つの処理槽9,11,12の底側にヘドロ等の汚物が溜まることも効率的に防止される。   Furthermore, since the smooth flow of sewage is promoted by the arc-shaped bottom surface of the cylindrical tank 1, the accumulation of filth such as sludge on the bottom side of the three treatment tanks 9, 11, and 12 is efficiently prevented. .

なお、上記水の循環システムにおいて、浄化の度合が低ければ、貯留室9bから第1好気性処理室11aに汚水を戻すことが可能であるため、水質の悪い浄水が便器17の洗浄タンク17aに還元されることも防止される。この他、洗浄タンク17aは、配水管26によって、水道管からの市販の水も利用可能であるため、利便性が高い。   In the above water circulation system, if the degree of purification is low, the sewage can be returned from the storage chamber 9b to the first aerobic treatment chamber 11a. Reduction is also prevented. In addition, the washing tank 17a is highly convenient because the water distribution pipe 26 can also use commercially available water from the water pipe.

また、円筒タンク1の周壁を用いて、各部屋を形成し、空間を有効活用できるため、全体をよりコンパクトに成形可能である。   Moreover, since each room can be formed using the surrounding wall of the cylindrical tank 1 and the space can be effectively used, the whole can be formed more compactly.

ちなみに、この循環式トイレでは、上述した制御盤13によって、ポンプ27,37,42,52,53の駆動及びブロア29,32,34等の駆動を自動制御し、各部の水位や水質を最適制御する。   Incidentally, in this circulating toilet, the control panel 13 described above automatically controls the drive of the pumps 27, 37, 42, 52, 53 and the blowers 29, 32, 34, etc., and optimally controls the water level and water quality of each part. To do.

1 円筒タンク(タンク)
4 隔壁
6 トイレ室
8 貯水槽
9 第1処理槽(処理槽)
9a 導入室(曝気処理室)
11 第2処理槽(処理槽)
11a 第2好気性処理室(曝気処理室,好気性処理室)
12 第3処理槽(処理槽)
12a 第3好気性処理室(曝気処理室,好気性処理室)
14A 非連通用仕切壁(仕切壁)
14B 連通用仕切壁(仕切壁)
16 連通口
21 汚水槽
33 ガイド部
44 浄化槽
S 軸心
1 Cylindrical tank (tank)
4 Bulkhead 6 Toilet room 8 Reservoir 9 First treatment tank (treatment tank)
9a Introduction room (aeration treatment room)
11 Second treatment tank (treatment tank)
11a Second aerobic processing chamber (aeration processing chamber, aerobic processing chamber)
12 3rd processing tank (processing tank)
12a Third aerobic processing chamber (aeration processing chamber, aerobic processing chamber)
14A Non-communication partition wall (partition wall)
14B Communication partition wall (partition wall)
16 Communication port 21 Sewage tank 33 Guide part 44 Septic tank S Shaft center

Claims (10)

トイレ室(6)と、トイレ室(6)からの汚水を貯留する汚水槽(21)と、汚水槽(21)からの汚水を処理する処理槽(9,11,12)と、処理槽(9,11,12)で処理された処理水を浄化する浄化槽(44)とを、単一の収容ボックス内に各別に設け、処理槽(9,11,12)内に曝気処理を行う曝気処理室(9a,11a,12a)を形成し、浄化された浄化水がトイレ室(6)内に還元される循環式トイレにおいて、収容ボックスを、水平な軸心(S)を有する円筒状のタンク(1)によって構成し、タンク(1)底面から少なくともタンク(1)軸心(S)高さに至る円弧状のタンク(1)内周面によって、前記曝気処理室(9a,11a,12a)の内壁面の少なくとも一部を形成することにより、曝気処理室(9a,11a,12a)の最大水位をタンク(1)軸心(S)高さ以上に設定し、曝気処理室(9a,11a,12a)内において上記円弧状の内壁面に沿って汚水を対流させることにより上記曝気処理を行う循環式トイレ。   Toilet room (6), sewage tank (21) for storing sewage from toilet room (6), treatment tank (9, 11, 12) for treating sewage from sewage tank (21), treatment tank ( A purification tank (44) for purifying the treated water treated in 9, 11, 12) is provided in each single storage box, and aeration treatment is performed in the treatment tank (9, 11, 12). In a circulating toilet in which chambers (9a, 11a, 12a) are formed and purified purified water is returned to the toilet chamber (6), the storage box is a cylindrical tank having a horizontal axis (S) The aeration chamber (9a, 11a, 12a) is constituted by an arcuate tank (1) inner peripheral surface which is configured by (1) and extends from the bottom of the tank (1) to at least the height of the tank (1) axis (S). By forming at least a part of the inner wall surface of the aeration treatment chamber (9a The maximum water level of 11a, 12a) is set higher than the height of the tank (1) axis (S), and sewage is convected along the arcuate inner wall in the aeration chamber (9a, 11a, 12a). A circulating toilet that performs the above aeration process. タンク(1)内周の全周によって円形断面の処理槽(9,11,12)を形成した請求項1に記載の循環式トイレ。   The circulation type toilet according to claim 1, wherein a treatment tank (9, 11, 12) having a circular cross section is formed by the entire inner circumference of the tank (1). 処理槽(9,11,12)の円形断面を複数に分割する仕切壁(14A,14B)を形成し、該分割されたスペースの少なくとも1つを曝気処理室(9a,11a,12a)とした請求項2に記載の循環式トイレ。   A partition wall (14A, 14B) that divides the circular cross section of the treatment tank (9, 11, 12) into a plurality of portions is formed, and at least one of the divided spaces is defined as an aeration treatment chamber (9a, 11a, 12a). The circulation type toilet according to claim 2. 前記仕切壁(14B)の断面を上下方向に形成し、該仕切壁(14B)によって分割される一方を曝気処理室(11a,12a)とするとともに、他方側を嫌気性処理を行う嫌気性処理室(11b,12b)とし、曝気処理室(11a,12a)と嫌気性処理室(11b,12b)とを連通させる連通口(16)をタンク(1)の底側に開口形成した請求項3に記載の循環式トイレ。   An anaerobic treatment in which a section of the partition wall (14B) is formed in the vertical direction, one side divided by the partition wall (14B) is used as an aeration treatment chamber (11a, 12a), and the other side is subjected to anaerobic treatment. The chamber (11b, 12b) is provided, and a communication port (16) for communicating the aeration processing chamber (11a, 12a) and the anaerobic processing chamber (11b, 12b) is formed at the bottom side of the tank (1). The circulation type toilet described in 1. 曝気処理室(11a,12a)内の上記対流をガイドするガイド部(33)を前記仕切壁(14B)に一体形成した請求項4に記載の循環式トイレ。   The circulating toilet according to claim 4, wherein a guide portion (33) for guiding the convection in the aeration processing chamber (11a, 12a) is integrally formed with the partition wall (14B). ガイド部(33)を、仕切壁(14B)の連通口(16)側端部に一体形成した請求項5に記載の循環式トイレ。   The circulation type toilet according to claim 5, wherein the guide portion (33) is integrally formed at the end of the partition wall (14B) on the side of the communication port (16). 仕切壁(14A,14B)をタンク(1)と共に一体形成した請求項3乃至6の何れかに記載の循環式トイレ。   The circulating toilet according to any one of claims 3 to 6, wherein the partition walls (14A, 14B) are integrally formed with the tank (1). 処理槽(9,11,12)を、互いに隣接させてタンク(1)の軸方向に複数配置し、隣接する処理槽(9,11,12)同士を仕切る隔壁(4)を設けた請求項1乃至7の何れかに記載の循環式トイレ。   A plurality of treatment tanks (9, 11, 12) are arranged adjacent to each other in the axial direction of the tank (1), and a partition wall (4) for partitioning the adjacent treatment tanks (9, 11, 12) is provided. The circulating toilet according to any one of 1 to 7. 隔壁(4)をタンク(1)と共に一体形成した請求項8に記載の循環式トイレ。   The circulating toilet according to claim 8, wherein the partition wall (4) is integrally formed with the tank (1). 浄水を貯水する貯水槽(8)をタンク(1)内に形成し、該貯水槽(8)内に浄化槽(44)を配置した請求項1乃至9の何れかに記載の循環式トイレ。   The circulating toilet according to any one of claims 1 to 9, wherein a water tank (8) for storing purified water is formed in the tank (1), and a water tank (44) is disposed in the water tank (8).
JP2012182020A 2012-08-21 2012-08-21 Circulation type toilet Pending JP2014040702A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2012182020A JP2014040702A (en) 2012-08-21 2012-08-21 Circulation type toilet

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2012182020A JP2014040702A (en) 2012-08-21 2012-08-21 Circulation type toilet

Publications (1)

Publication Number Publication Date
JP2014040702A true JP2014040702A (en) 2014-03-06

Family

ID=50393152

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2012182020A Pending JP2014040702A (en) 2012-08-21 2012-08-21 Circulation type toilet

Country Status (1)

Country Link
JP (1) JP2014040702A (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS607995A (en) * 1983-06-24 1985-01-16 Takenaka Komuten Co Ltd Aeration tank in filthy water treating process using activated sludge
JPH02222775A (en) * 1989-02-25 1990-09-05 Toto Ltd Septic tank having upward anaerobic filter bed
JPH07124578A (en) * 1993-11-01 1995-05-16 Kirin Brewery Co Ltd Biomembrane filter tank
JPH1121972A (en) * 1997-07-03 1999-01-26 Chuo Setsubi Kogyo Kk Movable toilet

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS607995A (en) * 1983-06-24 1985-01-16 Takenaka Komuten Co Ltd Aeration tank in filthy water treating process using activated sludge
JPH02222775A (en) * 1989-02-25 1990-09-05 Toto Ltd Septic tank having upward anaerobic filter bed
JPH07124578A (en) * 1993-11-01 1995-05-16 Kirin Brewery Co Ltd Biomembrane filter tank
JPH1121972A (en) * 1997-07-03 1999-01-26 Chuo Setsubi Kogyo Kk Movable toilet

Similar Documents

Publication Publication Date Title
CN104528932B (en) A kind of advanced treatment of wastewater denitrification bio-filter apparatus system and process technique
KR101256956B1 (en) Portable toilets can circulate slender recycling of sewage purification processing device
CN103466787A (en) Combined aeration moving bed bio-membrane reactor
UA92375C2 (en) Plant for the treatment of waste water
CN103613229A (en) Reinforced electrochemical coupling catalytic oxidation device and technology
CN104891748B (en) Purification tank
CN106865745B (en) Biological contact oxidation pond
JP4440826B2 (en) Membrane separation oxidation ditch
CN203668118U (en) Integrated reclaimed water treatment equipment adopting compound circulating biochemical membrane
JP2014040702A (en) Circulation type toilet
CN208995355U (en) A kind of buried sewage treatment equipment
KR101421179B1 (en) Bio-oxdation tank for sludge treatment
CN203498149U (en) Combined type aeration moving bed bio-membrane reactor
KR20120108585A (en) Purification system of seawater for cistern
CN101891300B (en) Photocatalytic-bioreactor for sewage treatment
KR101501615B1 (en) Waste water purifing apparatus using microorganism
KR100957825B1 (en) Water Purification System using Exterior Circulative Membrane Module
CN207792983U (en) A kind of buried AO techniques denitrification processing device
TW202035304A (en) Wastewater regulating pool and cooling structure thereof
CN203683327U (en) Contact oxidation and completely-mixed activated sludge process combined sewage treatment equipment
CN203440190U (en) Multivariant microelectrolysis combined binary catalytic oxidation device
KR200439298Y1 (en) microbe reactor
KR101334273B1 (en) Processing apparatus for organic waste water by aerobic and anaerobic microbes using micro-air bubble and ciculation
KR101803041B1 (en) Gas and bubble removal type liquid fertilizer producting device
CN211497071U (en) Contact disinfection pond

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20140901

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20150806

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20150825

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20151026

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20160216

RD04 Notification of resignation of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7424

Effective date: 20160324

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20160823