JP2001137876A - Excrement treatment system - Google Patents

Excrement treatment system

Info

Publication number
JP2001137876A
JP2001137876A JP32219299A JP32219299A JP2001137876A JP 2001137876 A JP2001137876 A JP 2001137876A JP 32219299 A JP32219299 A JP 32219299A JP 32219299 A JP32219299 A JP 32219299A JP 2001137876 A JP2001137876 A JP 2001137876A
Authority
JP
Japan
Prior art keywords
tank
air
aeration
plate member
water
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP32219299A
Other languages
Japanese (ja)
Other versions
JP4283395B2 (en
Inventor
Masashi Arai
正志 荒井
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.)
Mazda Motor Corp
Original Assignee
Toyo Kogyo Co Ltd
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 Toyo Kogyo Co Ltd filed Critical Toyo Kogyo Co Ltd
Priority to JP32219299A priority Critical patent/JP4283395B2/en
Publication of JP2001137876A publication Critical patent/JP2001137876A/en
Application granted granted Critical
Publication of JP4283395B2 publication Critical patent/JP4283395B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/30Against vector-borne diseases, e.g. mosquito-borne, fly-borne, tick-borne or waterborne diseases whose impact is exacerbated by climate change
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Activated Sludge Processes (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Non-Flushing Toilets (AREA)
  • Sanitary Device For Flush Toilet (AREA)
  • Biological Treatment Of Waste Water (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an excrement treatment system for sufficiently ensuring the contact time of treatment liquid with bacteria and air, and for improving the decomposing performance of organic matters in excrement. SOLUTION: In an aeration tank 4a, a plate member 42a whose face to be brought into contact with air aerated from an aeration port 41a is arranged in a direction inclined from the ascending direction of the air is mounted at the ascending position of the air, and at least one or more plate members 43a whose faces to be brought into contact with the air are arranged in a direction inclined from the ascending direction of the air so as to be opposite to the direction of the plate member 42a or 43a formed just under it is mounted at the upper part of the plate member 42a so that this excrement treatment system can be constituted.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、処理水を便器の洗
浄水として再利用できる循環型のし尿処理装置に関する
ものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a circulating human waste treatment apparatus capable of reusing treated water as toilet flush water.

【0002】[0002]

【従来の技術】イベント会場、建築現場等に設置する水
洗式の仮設トイレは、洗浄水の確保や処理水の廃棄が困
難な場合が多いため、処理水を洗浄水として再利用でき
る循環型のし尿処理装置を利用するのが有効である。
2. Description of the Related Art It is often difficult to secure wash water and dispose of treated water at an event venue, a construction site, or the like. It is effective to use a human waste treatment device.

【0003】上記循環型のし尿処理装置は、処理水が人
目に触れる形で再利用されるので、処理水に不快な臭い
が残存するものは不適当である。よって、上記循環型の
し尿処理装置では、し尿中の有機物を分解除去する性能
は、一般に高度なものが求められる。
[0003] In the above-mentioned circulation type human waste treatment apparatus, since the treated water is reused so as to be visible to the public, it is not appropriate that the treated water has an unpleasant odor. Therefore, in the above-mentioned circulation type night soil treatment apparatus, a high performance is generally required for decomposing and removing organic substances in night soil.

【0004】しかし、イベント会場や建築現場等では、
設置スペースに制限のあることも多いので、上記し尿処
理装置は、大掛かりな構成のものは採用し難い。また、
イベント会場や建築現場等では、薬液化学処理を用いる
と、化学物質によって周辺環境を汚染するおそれがある
ので、微生物処理を用いたし尿処理装置を用いるのが一
般的である。
[0004] However, at event venues and construction sites,
Since the installation space is often limited, it is difficult to adopt a large-scale configuration of the human waste treatment apparatus. Also,
At an event site, a construction site, or the like, if chemical solution chemical treatment is used, the surrounding environment may be contaminated by a chemical substance. Therefore, it is common to use a urine treatment apparatus using microbial treatment.

【0005】そこで、従来、処理液を曝気して、処理液
中の有機物を好気性微生物の代謝作用によって分解する
曝気法と、濾材を充填した反応槽中に処理液を散水し、
生物学的処理によって有機物を分解する散水濾床法を組
み合わせ、各処理方法の利点を生かすように構成したし
尿処理装置が提案されている。以下、この従来のし尿処
理装置について簡単に説明する。
Therefore, conventionally, an aeration method in which a treatment liquid is aerated to decompose organic substances in the treatment liquid by the metabolic action of aerobic microorganisms, and a treatment liquid is sprayed into a reaction tank filled with a filter medium,
There has been proposed a human waste treatment apparatus configured to combine the sprinkling filter method for decomposing organic substances by biological treatment and to take advantage of each treatment method. Hereinafter, the conventional human waste processing apparatus will be briefly described.

【0006】図14は、上記従来のし尿処理装置の一例
を示す模式図である。従来のし尿処理装置101は、例
えば、水洗式の便器102と、この水洗式の便器102
よりし尿を導入し下方から曝気する曝気槽103と、こ
の曝気槽103からポンプ104の作用により処理液を
導入し生物学的処理を行う反応槽105と、この反応層
105を通過して得られる処理水をポンプ106の作用
により導入し貯溜しておく貯水槽107よりなり、この
貯水槽107に溜めておいた処理水を、ポンプ108の
作用により便器102の洗浄水を溜めておく水槽109
へと循環させるものである。
FIG. 14 is a schematic view showing an example of the above-mentioned conventional human waste processing apparatus. A conventional human waste treatment apparatus 101 includes, for example, a flush toilet 102 and this flush toilet 102
An aeration tank 103 for introducing excreta and aerating from below, a reaction tank 105 for introducing a treatment liquid from the aeration tank 103 by the action of a pump 104 and performing biological treatment, and a reaction tank 105 obtained through the reaction layer 105. A water tank 107 for introducing and storing the treated water by the action of the pump 106; and a water tank 109 for storing the treated water of the toilet 102 by the action of the pump 108.
Is to be circulated.

【0007】この従来のし尿処理装置101では、曝気
槽103の底部には、曝気装置103aが設けられてい
る。すなわち、曝気装置103aは、ブロアー103b
から空気を送り込むことにより、曝気槽103を下方か
ら曝気できるものである。この曝気装置103aより曝
気される空気とし尿が十分に接触することにより、曝気
槽103内は、好気性微生物が活発に活動できる環境と
なる。
In the conventional human waste treatment apparatus 101, an aeration apparatus 103a is provided at the bottom of the aeration tank 103. That is, the aeration device 103a is
The aeration tank 103 can be aerated from below by sending air from the inside. When the air aerated by the aeration device 103a and the urine sufficiently come into contact with each other, the inside of the aeration tank 103 becomes an environment in which aerobic microorganisms can be actively activated.

【0008】反応槽105の内部の上方には、ポンプ1
04の作用により処理液が導入される散水器105aが
取付けられている。この散水器105aには固定式のノ
ズル105bが複数取付けられていて、その長さ及び内
径は均一である。そして、散水器105aの下方には、
例えば合成樹脂製のチップ等で形成される濾材105c
が充填されている。この濾材105cには生物膜が付着
し、散水器105aより散水される処理液と接触して、
生物学的処理が行われるのである。
A pump 1 is provided above the inside of the reaction tank 105.
A sprinkler 105a into which the processing liquid is introduced by the action of the liquid supply unit 04 is attached. A plurality of fixed nozzles 105b are attached to the sprinkler 105a, and their length and inner diameter are uniform. And below the sprinkler 105a,
For example, a filter medium 105c formed of a synthetic resin chip or the like
Is filled. A biofilm adheres to the filter medium 105c and comes into contact with the treatment liquid sprinkled from the sprinkler 105a.
Biological processing takes place.

【0009】また、従来、曝気法と、嫌気性の微生物の
代謝作用により有機物を分解する嫌気性処理とを組み合
わせ、各処理方法の利点を生かすように構成したし尿処
理装置も開示されている。
[0009] Also, there has been disclosed a human waste treatment apparatus in which an aeration method and an anaerobic treatment for decomposing organic substances by the metabolic action of anaerobic microorganisms are combined to take advantage of each treatment method.

【0010】例えば、特開平9−1171号公報では、
便器からのし尿を含んだ排水を生物学的に処理する一ま
たはそれ以上の生物学的分解手段と、該生物学的分解手
段によって処理された処理水を循環させて前記便器の洗
浄水として再利用する手段とを備えてなる循環浄化装置
であって、前記一またはそれ以上の生物学的分解手段に
おいて、好気性処理と嫌気性処理とが行われる排水循環
浄化装置が公開されている。
For example, in Japanese Patent Application Laid-Open No. Hei 9-1171,
One or more biological decomposition means for biologically treating wastewater containing human waste from a toilet bowl, and circulating the treated water treated by the biological decomposition means to recycle it as flush water for the toilet bowl There is disclosed a circulating purification apparatus comprising means for utilizing, wherein the one or more biological decomposition means performs an aerobic treatment and an anaerobic treatment in a wastewater circulating purification apparatus.

【0011】[0011]

【発明が解決しようとする課題】しかしながら、上記従
来のし尿処理装置101では、曝気槽において、曝気装
置103aより曝気された空気がし尿中をすぐに上昇し
てしまうので、空気と処理液の接触時間が短く、好気性
微生物の代謝作用による有機物の分解性能を十分に引き
出せないという問題があった。
However, in the above-mentioned conventional human waste processing apparatus 101, the air aerated from the aeration apparatus 103a immediately rises in the human waste in the aeration tank. There is a problem that the time is short and the ability to decompose organic substances by the metabolic action of aerobic microorganisms cannot be sufficiently brought out.

【0012】また、上記従来のし尿処理装置101で
は、反応槽105において、散水された処理液が、反応
槽105の内周面を伝って濾材105cと十分に接触せ
ずに下方に流出してしまうことがあるため、反応層10
5における生物学的処理の効率が悪いという問題もあっ
た。
Further, in the above-mentioned conventional human waste processing apparatus 101, in the reaction tank 105, the sprinkled processing liquid flows downward along the inner peripheral surface of the reaction tank 105 without sufficiently contacting the filter medium 105c. The reaction layer 10
There was also a problem that the biological treatment efficiency in No. 5 was poor.

【0013】さらに、反応槽105において、散水器1
05aのノズル105bの長さ及び内径が均一に構成さ
れているので、ノズル105bの先端から濾材105c
に散水される処理液の沁み込み範囲に重複が生じたり、
処理液が沁み込まない箇所が生じて、処理効率が悪いと
いう問題もあった。
Further, in the reaction tank 105, the sprinkler 1
Since the length and inner diameter of the nozzle 105b of the nozzle 105a are uniform, the filter medium 105c is inserted from the tip of the nozzle 105b.
Overlap of the infiltration range of the treatment liquid sprinkled on
There is also a problem that a portion where the processing liquid does not permeate is generated, and the processing efficiency is poor.

【0014】上記の問題点は、何れも処理液と微生物と
空気、あるいは処理液と微生物の接触時間を十分に確保
できないことに起因するものであり、微生物処理を用い
たし尿処理装置において、微生物が本来有している有機
物の分解性能を十分に引き出せていないという点で共通
する課題である。
[0014] The above problems are attributable to the inability to sufficiently secure the contact time between the treatment liquid and the microorganism or the air or between the treatment liquid and the microorganism. This is a common problem in that it does not sufficiently bring out the decomposition performance of organic substances originally possessed.

【0015】本発明は、上記した従来の問題点に鑑みて
なされたものであり、処理液と微生物と空気、あるいは
処理液と微生物の接触時間を十分に確保でき、し尿中の
有機物の分解性能を可及的に向上できるし尿処理装置を
提供することを目的としている。
The present invention has been made in view of the above-mentioned conventional problems, and can sufficiently secure the contact time between the processing solution and the microorganism and the air, or between the processing solution and the microorganism, and can degrade the organic matter in the night soil. It is an object of the present invention to provide a human waste treatment apparatus capable of improving as much as possible.

【0016】[0016]

【課題を解決するための手段】上記の目的を達成するた
め、本発明に係るし尿処理装置は、曝気槽において、曝
気口より曝気される空気が上昇する位置に、この空気と
接触する面が空気の上昇方向に対して斜め向きに配置さ
れた板部材を取付け、この板部材の上方には、空気と接
触する面が空気の上昇方向に対して直下の板部材とは逆
向きの斜め方向に配置された板部材を少なくとも一以上
取付けることとしている。そして、このようにすること
で、本発明に係るし尿処理装置では、処理液と微生物と
空気の接触時間を十分に確保できるので、有機物の分解
性能は可及的に向上する。
In order to achieve the above object, a human waste treatment apparatus according to the present invention has a surface in contact with the air at a position where air to be aerated from an aeration port rises in an aeration tank. Attach a plate member that is arranged obliquely to the rising direction of air. Above this plate member, the surface that comes into contact with air has an oblique direction that is opposite to the plate member that is directly below the rising direction of air. At least one or more of the plate members arranged in the above are attached. In this way, in the human waste treatment apparatus according to the present invention, the contact time between the treatment liquid, the microorganisms, and the air can be sufficiently ensured, so that the organic matter decomposition performance is improved as much as possible.

【0017】[0017]

【発明の実施の形態】本発明に係るし尿処理装置は、曝
気槽内において、曝気口より曝気される空気が上昇する
位置に、この空気と接触する面が空気の上昇方向に対し
て斜め向きに配置された板部材を取付け、この板部材の
上方には、空気と接触する面が空気の上昇方向に対して
直下の板部材とは逆向きの斜め方向に配置された板部材
を少なくとも一以上取付けた構成である。
BEST MODE FOR CARRYING OUT THE INVENTION A human waste treatment apparatus according to the present invention is arranged such that, in an aeration tank, a surface in contact with air is obliquely oriented with respect to a rising direction of air at a position where air to be aerated from an aeration port rises. And a plate member having a surface in contact with air disposed obliquely in a direction opposite to a plate member immediately below the rising direction of air above the plate member. This is the configuration attached above.

【0018】ここで、曝気槽内に取付ける板部材の形
状、取付け位置、取付け枚数は特に限定されない。但
し、板部材の形状は、曝気口より曝気される空気と接触
する面が空気の上昇方向に対して斜め向きに配置された
誘導部と、空気と接触する面が空気の上昇方向に対して
平行に配置された仕切部で構成し、両部材は、仕切部の
下端の位置が直下の板部材の誘導部の上端よりも曝気槽
の内周面寄りでかつ下方となるように配置することが望
ましい。上記のように構成し配置しておけば、直下の板
部材の誘導部の上端から上昇する空気を仕切部によって
確実に受けとめ、次の板部材に引き継ぐことができるか
らである。
Here, the shape, the mounting position, and the number of the plate members to be mounted in the aeration tank are not particularly limited. However, the shape of the plate member is such that the guiding portion is arranged such that the surface in contact with the air aerated from the aeration port is oblique to the rising direction of the air, and the surface in contact with the air is in the rising direction of the air. It is composed of partition parts arranged in parallel, and both members are arranged so that the lower end of the partition part is closer to the inner peripheral surface of the aeration tank and lower than the upper end of the guide part of the plate member immediately below. Is desirable. With the arrangement and arrangement as described above, the air rising from the upper end of the guide portion of the plate member immediately below can be reliably received by the partition portion and taken over to the next plate member.

【0019】[0019]

【実施例】以下、本発明を添付図面に示す一実施例に基
いて説明する。図1及び図4は、本実施例の嫌気性分解
槽及び曝気槽の部分断面図、図2は、図1を平面から見
た状態の説明図、図3は、図1を左側面から見た状態の
部分断面図、図5は、図4を左側面から見た状態の部分
断面図、図6は、本実施例の反応槽の部分断面図、図7
は、本実施例の反応槽及び散水器の断面図、図8は、本
実施例の散水器の説明図、図9は、本実施例を正面から
見た状態の断面図、図10は、本実施例を平面から見た
状態の断面図、図11は、本実施例を左側面から見た状
態の断面図、図12は、本実施例を右側面から見た状態
の断面図、図13は、本実施例の模式図である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below with reference to an embodiment shown in the accompanying drawings. 1 and 4 are partial cross-sectional views of the anaerobic decomposition tank and the aeration tank of the present embodiment, FIG. 2 is an explanatory view of FIG. 1 viewed from a plane, and FIG. 3 is a view of FIG. FIG. 5 is a partial cross-sectional view of FIG. 4 as viewed from the left side, FIG. 6 is a partial cross-sectional view of the reaction vessel of this embodiment, FIG.
Is a cross-sectional view of the reaction tank and the sprinkler of the present embodiment, FIG. 8 is an explanatory view of the sprinkler of the present embodiment, FIG. 9 is a cross-sectional view of the present embodiment as viewed from the front, FIG. FIG. 11 is a cross-sectional view of the present embodiment viewed from a plane, FIG. 11 is a cross-sectional view of the present embodiment viewed from a left side, and FIG. 12 is a cross-sectional view of the present embodiment viewed from a right side. FIG. 13 is a schematic diagram of the present embodiment.

【0020】最初に、本実施例の全体構成を図9〜12
を用いて説明する。本実施例のし尿処理装置Sは、トイ
レ部T及び分解処理部Bよりなり、トイレ部Tを収容す
る筐体7a内には水洗式の便器1と汚水槽2が、分解処
理部Bを収容する筐体7b内には嫌気性分解槽3a〜3
d、曝気槽4a〜4d、反応槽5、貯水槽6が設置され
ている。なお、11は、トイレ部Bの出入り口に設けた
ドアを示している。
First, the overall structure of this embodiment is shown in FIGS.
This will be described with reference to FIG. The human waste treatment apparatus S of the present embodiment includes a toilet section T and a disassembly processing section B, and a flush toilet 1 and a sewage tank 2 accommodate the disassembly processing section B in a housing 7a accommodating the toilet section T. Anaerobic decomposition tanks 3a to 3a
d, aeration tanks 4a to 4d, a reaction tank 5, and a water storage tank 6 are provided. Reference numeral 11 denotes a door provided at the entrance of the toilet section B.

【0021】汚水槽2は、便器1より導入されるし尿が
一時的に貯溜される槽であり、その底部には汚水ポンプ
8aへと繋がる流出口21が設けられている。図9〜1
1に示すように、汚水槽2は、し尿が流出口21の方向
に流れるように、流出口21に向けて勾配を有するよう
に形成されている。
The sewage tank 2 is a tank in which human waste introduced from the toilet bowl 1 is temporarily stored, and has an outlet 21 connected to the sewage pump 8a at the bottom thereof. 9 to 1
As shown in FIG. 1, the sewage tank 2 is formed so as to have a gradient toward the outlet 21 so that human waste flows in the direction of the outlet 21.

【0022】反応槽5は、円筒形の槽であり、図10に
示すように、分解処理部Bにおいて最も容積を占めてい
る。嫌気性分解槽3a〜3d及び曝気槽4a〜4dは、
反応槽5と筐体7bの四隅との間に設置されている。嫌
気性分解槽3a〜3d及び曝気槽4a〜4dは、図9及
び図12に示すような搭状の槽であって、この内3aと
4a、3bと4b、3cと4c、3dと4dは一側面が
接合しており一体に形成されている。貯水槽6は、図9
〜10及び図12に示すように、反応槽5の下部に設置
された方形の槽である。
The reaction tank 5 is a cylindrical tank, and occupies the largest volume in the decomposition processing section B as shown in FIG. The anaerobic decomposition tanks 3a to 3d and the aeration tanks 4a to 4d
It is installed between the reaction tank 5 and the four corners of the housing 7b. The anaerobic decomposition tanks 3a to 3d and the aeration tanks 4a to 4d are bed-like tanks as shown in FIGS. 9 and 12, and 3a and 4a, 3b and 4b, 3c and 4c, 3d and 4d One side is joined and formed integrally. The water storage tank 6 is shown in FIG.
As shown in FIGS. 10 to 10 and FIG. 12, a rectangular tank is provided below the reaction tank 5.

【0023】嫌気性分解槽3a〜3dは、曝気槽4a〜
4dよりも幅及び奥行きが小さい槽である。本実施例で
は、嫌気性分解槽3a〜3d及び曝気槽4a〜4dは、
図10に示すように、嫌気性分解槽3a〜3dが取付け
られている面を筐体7bの四隅の方向に向けるように配
置している。このような配置とした理由は、イベント会
場や建築現場等に設置される仮設トイレでは、設置スペ
ースに制限のあることも多いので、分解処理部Bのスペ
ースを有効に使うことにより、装置の小型化を図るため
である。
The anaerobic decomposition tanks 3a to 3d are provided with aeration tanks 4a to 4a.
This is a tank whose width and depth are smaller than 4d. In this embodiment, the anaerobic decomposition tanks 3a to 3d and the aeration tanks 4a to 4d
As shown in FIG. 10, the surface on which the anaerobic decomposition tanks 3a to 3d are attached is arranged so as to face the four corners of the housing 7b. The reason for this arrangement is that temporary toilets installed at event venues or construction sites are often limited in installation space, so by effectively using the space of the disassembly processing section B, the size of the device can be reduced. This is for the purpose of conversion.

【0024】各部の寸法を詳述すると、筐体7a及び7
bを合わせた全体の寸法は、幅260cm×高さ280
cm×奥行き130cmであり、この内、トイレ部Tの
筐体7aは幅110cmを、分解処理部Bの筐体7bは
幅150cmを占めている。また、曝気槽4a〜4dの
寸法は、幅30cm×奥行き20cm×高さ200c
m、嫌気性分解槽3a〜3dの幅及び奥行きは10cm
であり、貯水槽6の寸法は、幅85cm×奥行き100
cm×高さ40cmである。
The dimensions of each part will be described in detail.
The overall dimensions including b are 260 cm wide x 280 high
cm × 130 cm in depth, of which the housing 7a of the toilet section T occupies a width of 110 cm and the housing 7b of the disassembling section B occupies a width of 150 cm. The dimensions of the aeration tanks 4a to 4d are 30cm wide x 20cm deep x 200c high.
m, width and depth of the anaerobic decomposition tanks 3a to 3d are 10cm
And the dimensions of the water storage tank 6 are 85 cm in width × 100 in depth.
cm × 40 cm in height.

【0025】次に、本実施例におけるし尿処理の流れを
図13を用いて説明する。し尿は、水洗式の便器1より
汚水槽2に導入され、ここで一時的に貯溜される。汚水
槽2と嫌気性分解槽3aは連結管9aで繋がっており、
汚水槽2に貯溜されたし尿は連結管9aの途中に設けた
汚水ポンプ8aの作用によって嫌気性分解槽3aに導入
される。なお、10は、嫌気性分解槽3aが満杯の場合
に、し尿を汚水槽2の方へ戻すために設けた流量調整器
を示している。
Next, the flow of human waste processing in this embodiment will be described with reference to FIG. Night soil is introduced into the sewage tank 2 from the flush toilet 1 and temporarily stored therein. The sewage tank 2 and the anaerobic decomposition tank 3a are connected by a connecting pipe 9a.
Manure stored in the sewage tank 2 is introduced into the anaerobic decomposition tank 3a by the action of a sewage pump 8a provided in the middle of the connecting pipe 9a. Reference numeral 10 denotes a flow regulator provided to return human waste to the wastewater tank 2 when the anaerobic decomposition tank 3a is full.

【0026】嫌気性分解槽3a〜3d及び曝気槽4a〜
4dには、それぞれ流入口又は流出口が設けられてお
り、図13に示すように、連結管9b〜9dにより勾配
を設けて連結されている。よって、嫌気性分解槽3aに
導入された処理液は、重力の作用によって各槽を順に通
過する。
Anaerobic decomposition tanks 3a-3d and aeration tanks 4a-
4d is provided with an inflow port or an outflow port, respectively, and as shown in FIG. 13, they are connected with a gradient by connecting pipes 9b to 9d. Therefore, the processing liquid introduced into the anaerobic decomposition tank 3a sequentially passes through each tank by the action of gravity.

【0027】嫌気性分解槽3a〜3dは、導入されたし
尿又は処理液が空気と接触しない密閉された構造であ
り、嫌気性微生物が活発に活動できる環境となってい
る。したがって、導入されたし尿又は処理液中の蛋白
質、脂肪、炭水化物等の有機物は、嫌気性微生物の代謝
作用により、低級脂肪酸、アルコール等の中間生成物に
分解される。
The anaerobic decomposition tanks 3a to 3d have a closed structure in which the introduced human waste or the processing liquid does not come into contact with the air, and provide an environment in which anaerobic microorganisms can be actively activated. Therefore, organic substances such as proteins, fats and carbohydrates in the introduced human waste or the processing solution are decomposed into intermediate products such as lower fatty acids and alcohols by metabolic action of anaerobic microorganisms.

【0028】曝気槽4a〜4dは、底部に曝気口41a
〜44dが設けられており、この曝気口41a〜44d
には、曝気ポンプ8bから空気が送り込まれる。すなわ
ち、曝気槽4a〜4dは、下方からの曝気により空気が
豊富に存在するので、好気性微生物が活発に活動できる
環境となっている。よって、導入された処理液中の蛋白
質、脂肪、炭水化物等の有機物は、好気性微生物の代謝
作用によって、低級脂肪酸、アルコール等の中間生成物
や、メタン、二酸化炭素等の生物ガス、水に分解され
る。
The aeration tanks 4a to 4d have an aeration port 41a at the bottom.
4444d are provided, and the aeration ports 41a44d
Is supplied with air from the aeration pump 8b. That is, the aeration tanks 4a to 4d have an abundance of air due to aeration from below, so that the aerobic microorganisms can be actively activated. Therefore, organic substances such as proteins, fats, and carbohydrates in the introduced processing solution are decomposed into intermediate products such as lower fatty acids and alcohols, biogases such as methane and carbon dioxide, and water by metabolism of aerobic microorganisms. Is done.

【0029】曝気槽4dの流出口は、連結管9eを介し
て、反応槽5の内部に取付けた散水器51と勾配を設け
て連結されている。よって、曝気槽4dの流出口より流
出される処理液は、重力の作用により散水器51へと導
入される。なお、52は、反応槽5の内部に充填された
濾材を示しており、本実施例では杉チップが用いられて
いる。
The outlet of the aeration tank 4d is connected to the sprinkler 51 mounted inside the reaction tank 5 with a gradient through a connecting pipe 9e. Therefore, the processing liquid flowing out from the outlet of the aeration tank 4d is introduced into the sprinkler 51 by the action of gravity. Reference numeral 52 denotes a filter medium filled in the reaction tank 5, and in this embodiment, cedar chips are used.

【0030】本発明では、濾材52の材質は、特に限定
するものではないが、本発明者が試験を行ったところに
よると、本実施例のように杉チップを用いるのが有効で
あることが判明している。これは、杉チップの場合、例
えば欅等の他の樹木のチップと比較すると多孔質であ
り、チップ表面に微細な孔が多数存在するので、生物膜
が付着し易いためと考えられている。
In the present invention, the material of the filter medium 52 is not particularly limited. However, according to a test conducted by the present inventors, it is effective to use cedar chips as in this embodiment. It is known. This is considered to be because cedar chips are more porous than chips of other trees such as zelkova, for example, and there are many fine pores on the chip surface, so that biofilms can be easily attached.

【0031】なお、本実施例のし尿処理装置Sでは、処
理水に不快な臭いが残存することはなく、洗浄水として
再利用することについて何ら支障はないが、処理水に杉
チップの色素が薄い褐色の色として付着することがあ
る。しかし、濾材52としてボイルされた杉チップを用
いた場合には、処理水に色が付着することはなくなり、
最も望ましいことが判明している。
In the human waste treatment apparatus S of this embodiment, no unpleasant odor remains in the treated water, and there is no problem in reusing it as washing water. May adhere as a light brown color. However, in the case of using the boiled cedar chips as the filter medium 52, the color does not adhere to the treated water,
It has proven most desirable.

【0032】散水器51から散水された処理液は、濾材
52の表面に付着した生物膜と接触しながら反応槽5内
を下降し、ここで生物学的処理がなされる。反応槽5を
通過した処理水は、貯水槽6に導入され一時的に貯溜さ
れる。この貯水槽6と便器1の洗浄水を溜めておく水槽
12は、連結管9fにより繋がっており、貯水槽6に貯
溜された処理水は、加圧ポンプ8cの作用によって水槽
12に送られて、洗浄水として再利用される。
The treatment liquid sprinkled from the sprinkler 51 descends in the reaction tank 5 while being in contact with the biofilm adhering to the surface of the filter medium 52, where biological treatment is performed. The treated water that has passed through the reaction tank 5 is introduced into a water storage tank 6 and is temporarily stored. The water tank 6 and the water tank 12 for storing the flush water of the toilet 1 are connected by a connecting pipe 9f, and the treated water stored in the water tank 6 is sent to the water tank 12 by the action of the pressurizing pump 8c. , Reused as washing water.

【0033】なお、反応槽5は生物学的処理がなされる
槽であるが、冬期になって気温が低下すると、微生物の
活動が低下するおそれがある。この問題点を回避するに
は、貯水槽6内の処理水をヒーターによって30〜35
℃の温度を保つように構成すると共に、反応槽5の周囲
に温水コイルを螺旋状に巻き付け、ポンプを用いて貯水
槽6内の温められた処理水を温水コイルに循環させ、反
応槽5の温度の低下を防ぐ方法が有効である。
The reaction tank 5 is a tank in which biological treatment is performed. However, if the temperature falls in winter, the activity of microorganisms may decrease. In order to avoid this problem, the treated water in the water storage tank 6 is heated by a heater to 30-35.
° C, and a hot water coil is spirally wound around the reaction tank 5, and the heated treated water in the water storage tank 6 is circulated through the hot water coil using a pump. A method of preventing the temperature from decreasing is effective.

【0034】次に、嫌気性分解槽3a及び曝気槽4aを
表した図1〜3を用いて、本発明の主要部である曝気槽
4aについて説明する。本実施例の曝気槽4aには、図
1に示すように、板部材42a及び43aが取付けられ
ている。板部材42aは、曝気口41aより曝気される
空気が上昇する位置に取付けられ、空気と接触する面が
空気の上昇方向に対して斜め向きになるように配置され
ている。また、この板部材42aの上方には、空気と接
触する面が空気の上昇方向に対して直下の板部材42a
又は43aとは逆向きの斜め方向に配置された板部材4
3aが、計5枚取付けられている。なお、44aは、外
部から処理液の水位を確認するために設けた水位確認器
を、45aは、連結管9bを介して曝気槽4bへと繋が
る曝気槽4aの流出口を示している。
Next, the aeration tank 4a which is a main part of the present invention will be described with reference to FIGS. 1 to 3 showing the anaerobic decomposition tank 3a and the aeration tank 4a. As shown in FIG. 1, plate members 42a and 43a are attached to the aeration tank 4a of this embodiment. The plate member 42a is attached to a position where the air to be aerated from the aeration port 41a rises, and the plate member 42a is arranged so that the surface that contacts the air is oblique to the rising direction of the air. Further, above the plate member 42a, a surface that comes into contact with air has a plate member 42a directly below the rising direction of air.
Or a plate member 4 arranged in an oblique direction opposite to 43a.
3a are mounted in total. Reference numeral 44a denotes a water level checker provided to check the water level of the processing liquid from the outside, and 45a denotes an outlet of the aeration tank 4a connected to the aeration tank 4b via the connecting pipe 9b.

【0035】嫌気性分解槽3aは、図2に示すように、
曝気槽4aよりも幅及び奥行きが小さい槽であり、その
一側面は、図3に示すように、曝気槽4aに接着してお
り曝気槽4aと一体に構成されている。なお、31a
は、連結管9aを介して汚水槽2からし尿が導入される
嫌気性分解槽3aの流入口を、32aは、嫌気性分解槽
3aと曝気槽4aを繋ぐ接続口を示している。
The anaerobic decomposition tank 3a is, as shown in FIG.
The tank is smaller in width and depth than the aeration tank 4a, and one side surface thereof is adhered to the aeration tank 4a and integrally formed with the aeration tank 4a, as shown in FIG. In addition, 31a
Denotes an inflow port of the anaerobic decomposition tank 3a into which human waste is introduced from the sewage tank 2 via the connecting pipe 9a, and 32a denotes a connection port connecting the anaerobic decomposition tank 3a and the aeration tank 4a.

【0036】本実施例のし尿処理装置Sは、上記のよう
に構成した板部材42a及び43aを曝気槽4a内に取
付けることにより、曝気口41aから曝気される空気
が、板部材42a及び43aと接触しながら迂回して上
昇するので、空気が処理液と十分に接触せずに上昇して
しまうことはなくなる。よって、処理液と微生物と空気
の接触時間が十分に確保できるので、好気性微生物の代
謝作用による有機物の分解性能は可及的に向上する。
In the human waste processing apparatus S of this embodiment, the plate members 42a and 43a configured as described above are mounted in the aeration tank 4a, so that the air to be aerated from the aeration port 41a and the plate members 42a and 43a. Since the air rises by detouring while contacting, the air does not sufficiently come into contact with the processing liquid and does not rise. Therefore, a sufficient contact time between the treatment liquid, the microorganism, and the air can be ensured, and the performance of decomposing organic substances by the metabolic action of the aerobic microorganism is improved as much as possible.

【0037】本発明では、板部材42a及び43aの形
状や配置を特に限定するものではないが、本実施例で
は、板部材42aは、曝気口41aより曝気される空気
と接触する面がこの空気の上昇方向に対して斜め向きに
配置された誘導部42a1と、空気と接触する面が空気
の上昇方向に対して平行に配置された仕切部42a2で
形成している。また、板部材43aも板部材42aと同
様に、誘導部43a1と仕切部43a2で形成してい
る。
In the present invention, the shape and arrangement of the plate members 42a and 43a are not particularly limited. However, in the present embodiment, the surface of the plate member 42a which comes into contact with the air aerated from the aeration port 41a is this air. The guide portion 42a1 is disposed obliquely to the rising direction of the air, and the partitioning portion 42a2 is arranged so that the surface in contact with the air is disposed parallel to the rising direction of the air. Further, the plate member 43a is also formed by the guide portion 43a1 and the partition portion 43a2, similarly to the plate member 42a.

【0038】そして、板部材43aは、仕切部43a2
の下端の位置が、直下の板部材42aの誘導部42a
1、あるいは直下の板部材43aの誘導部43a1の上
端の位置よりも、曝気槽4の内周面寄りでかつ下方とな
るように配置している。
The plate member 43a is provided with a partition 43a2.
Is located at the lower end of the guide portion 42a of the plate member 42a immediately below.
1, or the plate member 43a is disposed so as to be closer to and below the inner peripheral surface of the aeration tank 4 than the upper end of the guide portion 43a1 of the plate member 43a immediately below.

【0039】板部材42a及び43aを上記のように構
成し配置した理由は、直下の板部材42aの誘導部42
a1、あるいは直下の板部材43aの誘導部43a1の
上端から上昇する空気を、板部材43aの仕切部43a
2によって確実に受けとめることができるからである。
すなわち、板部材42a及び43a間で空気を引き継ぐ
際に、空気が板部材42a及び43aから外れて上昇し
てしまうことを防ぐことができるので、板部材42a及
び板部材43aは、本実施例のように構成し配置するの
が望ましい。
The reason why the plate members 42a and 43a are constructed and arranged as described above is that the guide portion 42 of the plate member 42a immediately below is provided.
a1 or the air rising from the upper end of the guide portion 43a1 of the plate member 43a immediately below the partition member 43a of the plate member 43a.
This is because it can be reliably received by 2.
That is, when taking over the air between the plate members 42a and 43a, the air can be prevented from coming off from the plate members 42a and 43a and rising, so that the plate members 42a and 43a are It is desirable to arrange and arrange in such a manner.

【0040】なお、本実施例では、図1に示すように、
板状の部材をくの字状に形成して、誘導部42a1及び
43a1と、仕切部42a2及び43a2を一体に構成
したものを開示しているが、これらの部材は別体に構成
しても良い。
In this embodiment, as shown in FIG.
Although a plate-shaped member is formed in a U-shape and the guiding portions 42a1 and 43a1 and the partitioning portions 42a2 and 43a2 are integrally formed, these members may be formed separately. good.

【0041】本実施例では、板部材42a及び43aを
取付ける方法は、図3に示すように仕切部42a2及び
43a2を曝気槽4aの奥行き方向に延長し、曝気槽4
aの内周面に固定する方法を採用している。また、板部
材43aは、板部材42aの上方に計5枚取付ける例を
開示している。しかし、板部材42a及び43aの取付
け方法や、板部材43aの取付け枚数については、曝気
槽4aの形状や大きさ等にも応じて適宜決定すれば良
く、特に限定するものではない。
In this embodiment, the plate members 42a and 43a are attached by extending the partition portions 42a2 and 43a2 in the depth direction of the aeration tank 4a as shown in FIG.
The method of fixing to the inner peripheral surface of a is adopted. Also, an example is disclosed in which a total of five plate members 43a are mounted above the plate member 42a. However, the method of attaching the plate members 42a and 43a and the number of attached plate members 43a may be appropriately determined according to the shape and size of the aeration tank 4a, and are not particularly limited.

【0042】また、本実施例では、曝気槽4aにおい
て、曝気口41a付近の底部46aの形状は、曝気口4
1aを頂点とする逆向きの錘状としている。底部46a
をこのような形状とした理由は、例えばこの部分を柱状
に構成して、その底面に曝気口41aを設けると、曝気
口41aの周辺に、空気と処理液が十分に接触しない澱
みが生じてヘドロ化し、曝気処理の効率が低下するのを
回避するためである。本実施例のように底部46aを曝
気口41aを頂点とする逆向きの錘状に構成しておけ
ば、処理液は空気と十分に接触し、曝気槽4aにヘドロ
が溜まることはないので、曝気処理の効率は向上する。
In this embodiment, in the aeration tank 4a, the shape of the bottom 46a near the aeration port 41a is different from that of the aeration port 4a.
It is in the shape of an inverted cone with the vertex 1a. Bottom 46a
The reason for adopting such a shape is that, for example, when this portion is formed in a columnar shape and an aeration port 41a is provided on the bottom surface thereof, stagnation occurs in the vicinity of the aeration port 41a where the air and the processing liquid do not sufficiently contact each other. This is to avoid sludge and decrease the efficiency of the aeration treatment. If the bottom 46a is formed in the shape of an inverted cone with the aeration port 41a at the apex as in the present embodiment, the treatment liquid sufficiently contacts the air, and the sludge does not accumulate in the aeration tank 4a. The efficiency of the aeration process is improved.

【0043】次に、図4〜5を用いて嫌気性分解槽3b
及び曝気槽4bについて説明する。図4〜5において、
45bは、連結管9bを介して曝気槽4aから処理液が
導入される曝気槽4bの流入口を、31bは、連結管9
cを介して嫌気性分解槽3cへと繋がる嫌気性分解槽3
bの流出口である。図4〜5に示すように、流入口45
bを設ける位置は、流出口45aよりも低く、流出口3
1bよりも高い位置としている。
Next, the anaerobic decomposition tank 3b will be described with reference to FIGS.
And the aeration tank 4b will be described. 4 and 5,
45b is an inlet of the aeration tank 4b into which the processing liquid is introduced from the aeration tank 4a via the connection pipe 9b, and 31b is a connection pipe 9b.
Anaerobic decomposition tank 3 connected to anaerobic decomposition tank 3c via c
b. As shown in FIGS.
The position where b is provided is lower than the outlet 45a, and the outlet 3
1b.

【0044】すなわち、嫌気性分解槽3b及び曝気槽4
bでは、曝気処理と嫌気性微生物による分解処理の順番
を逆転している点が、嫌気性分解槽3a及び曝気槽4a
とは異なっている。なお、41bは曝気口を、42bは
誘導部42b1と仕切部42b2で形成される板部材
を、43bは誘導部43b1と仕切部43b2で形成さ
れる板部材を、44bは水位確認器を、46bは曝気槽
4bの底部を、32bは嫌気性分解槽3bと曝気槽4b
を繋ぐ接続口を示しているが、これらの構成について
は、既に説明した図1〜3における構成と特に変るとこ
ろはない。
That is, the anaerobic decomposition tank 3b and the aeration tank 4
b, the point that the order of the aeration treatment and the decomposition treatment by the anaerobic microorganism is reversed is that the anaerobic decomposition tank 3a and the aeration tank 4a
Is different from In addition, 41b is an aeration port, 42b is a plate member formed by the guide part 42b1 and the partition part 42b2, 43b is a plate member formed by the guide part 43b1 and the partition part 43b2, 44b is a water level checker, 46b Is the bottom of the aeration tank 4b, and 32b is the anaerobic decomposition tank 3b and the aeration tank 4b.
Are shown, but these configurations are not particularly different from the configurations in FIGS. 1 to 3 already described.

【0045】次に、図6〜8を用いて、反応槽5及び散
水器51について説明する。本実施例の反応槽5は、図
6に示すように、上面の中央には、連結管9eを介して
曝気槽4dから処理水が導入される流入口53を有し、
この流入口53の下部には散水器51を取付け、反応槽
5の内周面には、斜め下方向に突出した水切りガイド5
4を計4箇所周設した構成である。なお、52は、反応
槽5内に充填された濾材を示している。
Next, the reaction tank 5 and the sprinkler 51 will be described with reference to FIGS. As shown in FIG. 6, the reaction tank 5 of the present embodiment has an inflow port 53 at the center of the upper surface into which treated water is introduced from the aeration tank 4d via the connection pipe 9e.
A sprinkler 51 is attached to a lower portion of the inlet 53, and a drain guide 5 projecting obliquely downward is provided on the inner peripheral surface of the reaction tank 5.
4 are provided around a total of four places. Reference numeral 52 denotes a filter medium filled in the reaction tank 5.

【0046】本実施例のし尿処理装置Sでは、上記のよ
うに構成した反応槽5を採用したので、散水器51より
散水された処理液が反応槽5の内周面を伝って落下する
ことがあるとしても、水切りガイド54の作用によっ
て、処理液を反応槽5の中心方向に誘導することができ
る。よって、処理液が反応槽5の内周面を伝って、濾材
52と十分接触することなく貯水槽6に流出してしまう
ことはなくなり、反応槽5における生物学的処理の処理
効率を可及的に向上することができる。
In the human waste processing apparatus S of this embodiment, the reaction tank 5 configured as described above is employed, so that the processing liquid sprinkled from the water sprayer 51 falls along the inner peripheral surface of the reaction tank 5. Even if there is, the treatment liquid can be guided toward the center of the reaction tank 5 by the action of the draining guide 54. Therefore, the treatment liquid does not flow along the inner peripheral surface of the reaction tank 5 and flows out to the water storage tank 6 without making sufficient contact with the filter medium 52, and the treatment efficiency of the biological treatment in the reaction tank 5 is increased. Can be improved.

【0047】なお、本実施例では、図6に示す位置に水
切りガイド54を計4箇所周設した例を開示している
が、水切りガイド54を設ける数及び位置は、反応槽5
の形状及び大きさ等にも応じて適宜決定すれば良く、特
に限定するものではない。
Although the present embodiment discloses an example in which four draining guides 54 are provided at the positions shown in FIG. 6, the number and positions of the draining guides 54 are different from those in the reaction tank 5.
May be appropriately determined according to the shape and size of the device, and are not particularly limited.

【0048】本実施例の散水器51は、図7〜8に示す
ように、分配部57の底面の周縁付近に大内径ノズル5
5と小内径ノズル56を各4本ずつ、交互かつ放射状に
取付けた構成である。分配部57は、図8に示すような
円筒状の部材であり、その底面には、図7に示すよう
に、大内径ノズル55に繋がる流出口57aと、小内径
ノズル56に繋がる流出口が57bが開口している。
As shown in FIGS. 7 and 8, the sprinkler 51 of the present embodiment has a large-diameter nozzle 5 near the periphery of the bottom surface of the distribution unit 57.
5 and four small-diameter nozzles 56 are alternately and radially attached to each other. The distribution section 57 is a cylindrical member as shown in FIG. 8, and has an outlet 57 a connected to the large-diameter nozzle 55 and an outlet connected to the small-diameter nozzle 56 on the bottom surface, as shown in FIG. 7. 57b is open.

【0049】大内径ノズル55のノズルの長さは、図7
に示すように、反応槽5の中心と反応槽5の内周面の中
間付近から反応槽5の内周面寄りの位置に散水し得る長
さである。また、本実施例では、内径100cmの反応
槽5に対して、大内径ノズル55の内径は2cmとして
いる。
The nozzle length of the large-diameter nozzle 55 is shown in FIG.
As shown in (2), the length is such that water can be sprayed from a position near the center of the reaction tank 5 and the inner peripheral surface of the reaction tank 5 to a position near the inner peripheral surface of the reaction tank 5. In the present embodiment, the inner diameter of the large inner diameter nozzle 55 is set to 2 cm with respect to the reaction tank 5 having the inner diameter of 100 cm.

【0050】大内径ノズル55の内径を2cmとした理
由は、上記の条件の場合には、大内径ノズル55より散
水される処理液が濾材52中に沁み込む範囲は、概ね図
7の55aに示す範囲となり、流出口57aから反応槽
5の内周面までの距離を直径とする略円形となるからで
ある。但し、大内径ノズル55の内径の最適値は、反応
槽5の内径との比率により変るので、大内径ノズル55
の内径に応じて最適なものを選択する必要がある。
The reason why the inner diameter of the large-diameter nozzle 55 is set to 2 cm is that, under the above-described conditions, the range in which the treatment liquid sprinkled from the large-diameter nozzle 55 penetrates into the filter medium 52 is approximately 55a in FIG. This is because the diameter becomes a substantially circular shape having a diameter from the outlet 57a to the inner peripheral surface of the reaction tank 5. However, the optimum value of the inner diameter of the large-diameter nozzle 55 varies depending on the ratio to the inner diameter of the reaction tank 5.
It is necessary to select the most suitable one according to the inner diameter of.

【0051】そして、本実施例では、小内径ノズル56
の内径は1.5cmとし、そのノズルの長さは、図7に
示すように、大内径ノズル55の散水位置よりもさらに
反応槽の内周面寄りの位置に散水し得る長さとしてい
る。
In this embodiment, the small inner diameter nozzle 56
The inner diameter of the nozzle is 1.5 cm, and the length of the nozzle is such that water can be sprayed to a position closer to the inner peripheral surface of the reaction tank than the watering position of the large inner diameter nozzle 55 as shown in FIG.

【0052】上記の条件の場合には、小内径ノズル56
より散水される処理液が、濾材52中に沁み込む範囲
は、概ね図7の56aに示す範囲となり、大内径ノズル
55の沁み込み範囲55aと重複することはない。ま
た、大内径ノズル55では処理液を沁み込ませることが
出来ない反応槽5の内周面寄りの箇所に、効率的に処理
液を染み込ませることができる。このような最適な沁み
込み範囲55a及び56aを得るためには、小内径ノズ
ル56の内径は、大内径ノズルの30〜80%の範囲と
する必要がある。
Under the above conditions, the small inner diameter nozzle 56
The range in which the treatment liquid to be more sprinkled permeates the filter medium 52 is substantially the range indicated by 56a in FIG. 7, and does not overlap the permeation range 55a of the large-diameter nozzle 55. Further, the processing liquid can be efficiently impregnated into a portion near the inner peripheral surface of the reaction tank 5 where the large-diameter nozzle 55 cannot impregnate the processing liquid. In order to obtain such optimal permeation ranges 55a and 56a, the inner diameter of the small inner diameter nozzle 56 needs to be in the range of 30 to 80% of the large inner diameter nozzle.

【0053】本実施例のし尿処理装置Sでは、分配部5
7の底面の周縁付近に上記のように構成した大内径ノズ
ル55と小内径ノズル56を各4本ずつ、交互かつ放射
状に取付けた散水器51を採用したので、濾材52に散
水される処理液の沁み込み範囲55a及び56aに重複
が生じることはなくなり、処理液が浸透しない箇所の面
積も減らせるので、反応槽5における生物学的処理の処
理効率を可及的に向上することができる。
In the human waste processing apparatus S of this embodiment, the dispensing section 5
7 employs a sprinkler 51 in which four large-diameter nozzles 55 and four small-diameter nozzles 56 each configured as described above are alternately and radially mounted near the periphery of the bottom surface of the processing liquid 7. No overlap occurs in the infiltration ranges 55a and 56a, and the area of the portion where the treatment liquid does not penetrate can be reduced, so that the treatment efficiency of the biological treatment in the reaction tank 5 can be improved as much as possible.

【0054】[0054]

【発明の効果】以上説明したように、本発明に係るし尿
処理装置は、曝気槽において、曝気口より曝気される空
気が上昇する位置に、この空気と接触する面が空気の上
昇方向に対して斜め向きに配置された板部材を取付け、
この板部材の上方には、空気と接触する面が空気の上昇
方向に対して直下の板部材とは逆向きの斜め方向に配置
された板部材を少なくとも一以上取付けるように構成し
たので、処理液と微生物と空気の接触時間が十分に確保
でき、有機物の分解性能を可及的に向上することができ
るという効果を有する。
As described above, in the night soil treatment apparatus according to the present invention, the surface in contact with the air in the aeration tank is located at the position where the air to be aerated from the aeration port rises. Attach the plate members arranged diagonally,
Above this plate member, at least one plate member whose surface in contact with air is arranged in an oblique direction opposite to the plate member immediately below the rising direction of air is configured to be attached. This has the effect that the contact time between the liquid, the microorganism and the air can be sufficiently ensured, and the decomposition performance of organic substances can be improved as much as possible.

【0055】また、反応槽の内周面に水切りガイドを周
設したし尿処理装置を用いた場合には、反応槽中に散水
された処理液が、反応槽の内周面を伝って、濾材と十分
接触することなく貯水槽に流出してしまうことはなくな
る。さらに、散水器のノズルを、大内径ノズルと小内径
ノズルで構成したし尿処理装置を用いた場合には、濾材
に散水される処理液の沁み込み範囲に重複が生じること
はなくなり、処理液が浸透しない箇所の面積も減らせる
ので、有機物の分解性能をさらに向上することができる
という効果を有する。
In the case of using a human waste treatment apparatus in which a drainage guide is provided around the inner peripheral surface of the reaction tank, the treatment liquid sprinkled into the reaction tank travels along the inner peripheral surface of the reaction tank to form a filter medium. It will not flow out into the water tank without making sufficient contact. Furthermore, in the case of using a human waste treatment apparatus in which the nozzle of the sprinkler is constituted by a large-diameter nozzle and a small-diameter nozzle, there is no longer any overlap in the permeation range of the processing liquid sprinkled on the filter medium, and the processing liquid is not Since the area of the portion that does not penetrate can also be reduced, there is an effect that the decomposition performance of organic substances can be further improved.

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

【図1】本実施例の嫌気性分解槽及び曝気槽の部分断面
図である。
FIG. 1 is a partial sectional view of an anaerobic decomposition tank and an aeration tank of the present embodiment.

【図2】図1を上面から見た状態の説明図である。FIG. 2 is an explanatory diagram of FIG. 1 viewed from above.

【図3】図1を左側面から見た状態の部分断面図であ
る。
FIG. 3 is a partial cross-sectional view of FIG. 1 as viewed from a left side surface.

【図4】本実施例の曝気槽及び嫌気性分解槽の部分断面
図である。
FIG. 4 is a partial cross-sectional view of an aeration tank and an anaerobic decomposition tank of the present embodiment.

【図5】図4を左側面から見た状態の部分断面図であ
る。
FIG. 5 is a partial cross-sectional view of FIG. 4 as viewed from a left side surface.

【図6】本実施例の反応槽の部分断面図である。FIG. 6 is a partial cross-sectional view of a reaction tank of the present embodiment.

【図7】本実施例の反応槽及び散水器の断面図である。FIG. 7 is a sectional view of a reaction tank and a sprinkler of the present embodiment.

【図8】本実施例の散水器の説明図である。FIG. 8 is an explanatory diagram of a sprinkler according to the present embodiment.

【図9】本実施例を正面から見た状態の断面図である。FIG. 9 is a sectional view of the embodiment when viewed from the front.

【図10】本実施例を平面から見た状態の断面図であ
る。
FIG. 10 is a cross-sectional view of the present embodiment viewed from a plane.

【図11】本実施例を左側面から見た状態の断面図であ
る。
FIG. 11 is a cross-sectional view of the embodiment when viewed from the left side.

【図12】本実施例を右側面から見た状態の断面図であ
る。
FIG. 12 is a cross-sectional view of the embodiment when viewed from the right side.

【図13】本実施例の模式図である。FIG. 13 is a schematic diagram of the present embodiment.

【図14】従来のし尿処理装置の模式図である。FIG. 14 is a schematic view of a conventional human waste treatment apparatus.

【符号の説明】[Explanation of symbols]

S し尿処理装置 1 便器 2 汚水槽 3a、3b、3c、3d 嫌気性分解槽 4a、4b、4c、4d 曝気槽 41a、41b 曝気口 42a、42b、43a、43b 板部材 42a1、43a1 誘導部 42a2、43a2 仕切部 5 反応槽 51 散水器 52 濾材 54 水切りガイド 55 大内径ノズル 56 小内径ノズル 57 分配部 6 貯水槽 S Human waste treatment apparatus 1 Toilet bowl 2 Sewage tank 3a, 3b, 3c, 3d Anaerobic decomposition tank 4a, 4b, 4c, 4d Aeration tank 41a, 41b Aeration port 42a, 42b, 43a, 43b Plate member 42a1, 43a1 Induction part 42a2, 43a2 Partitioning part 5 Reaction tank 51 Sprinkler 52 Filter medium 54 Drainage guide 55 Large internal diameter nozzle 56 Small internal diameter nozzle 57 Distributing section 6 Water tank

フロントページの続き Fターム(参考) 2D036 CB05 2D039 AC09 4D003 AA02 AB01 BA02 BA03 CA07 DA03 DA18 DA19 DA28 DA29 EA11 EA19 EA21 FA05 FA10 4D028 AA03 AA07 AB00 BB02 BB07 BC01 BC12 BC22 BC24 BC26 4D040 BB65 Continued on the front page F term (reference) 2D036 CB05 2D039 AC09 4D003 AA02 AB01 BA02 BA03 CA07 DA03 DA18 DA19 DA28 DA29 EA11 EA19 EA21 FA05 FA10 4D028 AA03 AA07 AB00 BB02 BB07 BC01 BC12 BC22 BC24 BC26 4D040 BB65

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 処理水を便器の洗浄水として再利用でき
る循環型のし尿処理装置であって、水洗式の便器と、し
尿を一時的に貯溜する汚水槽と、この汚水槽から導入さ
れるし尿中の有機物を嫌気性微生物の代謝作用により分
解する嫌気性分解槽と、この嫌気性分解槽で処理された
処理液を導入し下方から曝気して好気性微生物の代謝作
用により分解する曝気槽と、この曝気槽で処理された処
理液を導入し散水する散水器と、内部には濾材が充填さ
れており前記散水器により上方から散水される処理液と
前記濾材とを接触させて生物学的処理を行う反応槽と、
この反応槽で処理されて得られる処理水を貯溜しておく
貯水槽からなり、前記曝気槽内には、曝気口より曝気さ
れる空気が上昇する位置に、この空気と接触する面が前
記空気の上昇方向に対して斜め向きに配置された板部材
を取付け、この板部材の上方には、前記空気と接触する
面が前記空気の上昇方向に対して直下の板部材とは逆向
きの斜め方向に配置された板部材を少なくとも一以上取
付けたことを特徴とするし尿処理装置。
1. A circulation type human waste treatment apparatus capable of reusing treated water as flush water for a toilet, comprising a flush toilet, a waste water tank for temporarily storing human waste, and a waste water introduced from the waste water tank. An anaerobic decomposition tank that decomposes organic matter in human waste by the metabolic action of anaerobic microorganisms, and an aeration tank that introduces the processing solution treated in this anaerobic decomposition tank and aerates from below to decompose by the metabolic action of aerobic microorganisms And a sprinkler for introducing and sprinkling the treatment liquid treated in the aeration tank, and contacting the treatment liquid with the filter medium, which is filled with a filter medium and sprinkled from above by the sprinkler, to form a biological sample. A reaction tank for performing a chemical treatment,
The aeration tank comprises a water storage tank for storing treated water obtained by the treatment in the reaction tank, and a surface in contact with the air is provided at a position where air to be aerated from the aeration port rises. A plate member arranged obliquely to the rising direction of the air is attached. Above this plate member, the surface that comes into contact with the air has an oblique direction opposite to the plate member immediately below the rising direction of the air. A human waste treatment apparatus, wherein at least one or more plate members arranged in the direction are attached.
【請求項2】 板部材は、曝気口より曝気される空気と
接触する面が前記空気の上昇方向に対して斜め向きに配
置された誘導部と、前記空気と接触する面が前記空気の
上昇方向に対して平行に配置された仕切部からなり、こ
の仕切部の下端の位置は、直下の板部材の誘導部の上端
よりも曝気槽の内周面寄りでかつ下方となるように配置
したことを特徴とする請求項1記載のし尿処理装置。
2. A plate member, wherein a guide portion having a surface contacting air aerated from an aeration port is arranged obliquely to a rising direction of the air, and a plate contacting the air has a surface rising the air. It consists of a partition arranged in parallel to the direction, and the position of the lower end of this partition is arranged closer to the inner peripheral surface of the aeration tank and lower than the upper end of the guide portion of the plate member immediately below. The human waste treatment apparatus according to claim 1, wherein
【請求項3】 反応層の内周面に、斜め下方向に突出し
た水切りガイドを周設したことを特徴とする請求項1又
は2記載のし尿処理装置。
3. The human waste treatment apparatus according to claim 1, wherein a draining guide projecting obliquely downward is provided on the inner peripheral surface of the reaction layer.
【請求項4】 散水器のノズルは、反応槽の中心と反応
槽の内周面の中間付近から反応槽の内周面寄りの位置に
散水し得る大内径ノズルと、ノズルの内径を前記大内径
ノズルの内径の30〜80%の範囲とし、前記大内径ノ
ズルの散水位置よりもさらに反応槽の内周面寄りの位置
に散水し得る小内径ノズルからなり、この小内径ノズル
と前記大内径ノズルを分配部に交互かつ放射状に取付け
たことを特徴とする請求項1〜3の何れかに記載のし尿
処理装置。
4. A nozzle having a large inner diameter capable of spraying water from a position between the center of the reaction tank and the inner peripheral surface of the reaction tank to a position closer to the inner peripheral surface of the reaction tank. A small-diameter nozzle which is capable of spraying water to a position closer to the inner peripheral surface of the reaction tank than the water-spraying position of the large-diameter nozzle, in a range of 30 to 80% of the inner diameter of the inner-diameter nozzle; The human waste treatment apparatus according to any one of claims 1 to 3, wherein the nozzles are alternately and radially attached to the distribution unit.
JP32219299A 1999-11-12 1999-11-12 Human waste treatment equipment Expired - Lifetime JP4283395B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP32219299A JP4283395B2 (en) 1999-11-12 1999-11-12 Human waste treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP32219299A JP4283395B2 (en) 1999-11-12 1999-11-12 Human waste treatment equipment

Publications (2)

Publication Number Publication Date
JP2001137876A true JP2001137876A (en) 2001-05-22
JP4283395B2 JP4283395B2 (en) 2009-06-24

Family

ID=18140983

Family Applications (1)

Application Number Title Priority Date Filing Date
JP32219299A Expired - Lifetime JP4283395B2 (en) 1999-11-12 1999-11-12 Human waste treatment equipment

Country Status (1)

Country Link
JP (1) JP4283395B2 (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002119988A (en) * 2000-10-12 2002-04-23 Toyo Kogyo Co Ltd Evaporative reaction tank for excretion treatment apparatus
JP2004050127A (en) * 2002-07-23 2004-02-19 Kawanabe Kogyo Kk Cleaning treatment apparatus for high concentration organic wastewater
JP2004243181A (en) * 2003-02-12 2004-09-02 Furukawa Netsugaku Engineering Kk Human waste treatment device provided with stream diffusion plate
JP2006288564A (en) * 2005-04-07 2006-10-26 Daio Densetsu Kogyo Kk Bio-toilet
JP2007160280A (en) * 2005-12-16 2007-06-28 National Agriculture & Food Research Organization Movable lid type sewage sprinkler equipped with stream disperser and automatic cleaning mechanism
JP2011252293A (en) * 2010-06-01 2011-12-15 Aqua Project Inc Circulation type simple toilet
JP2018167194A (en) * 2017-03-30 2018-11-01 三機工業株式会社 Sprinkler and sprinkler type cleaner
CN110156270A (en) * 2019-06-11 2019-08-23 中铁第一勘察设计院集团有限公司 Source-separated urine recovery of nitrogen and phosphorus and water reclaiming system and its operation method

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002119988A (en) * 2000-10-12 2002-04-23 Toyo Kogyo Co Ltd Evaporative reaction tank for excretion treatment apparatus
JP2004050127A (en) * 2002-07-23 2004-02-19 Kawanabe Kogyo Kk Cleaning treatment apparatus for high concentration organic wastewater
JP2004243181A (en) * 2003-02-12 2004-09-02 Furukawa Netsugaku Engineering Kk Human waste treatment device provided with stream diffusion plate
JP2006288564A (en) * 2005-04-07 2006-10-26 Daio Densetsu Kogyo Kk Bio-toilet
JP4671407B2 (en) * 2005-04-07 2011-04-20 大央電設工業株式会社 Bio toilet
JP2007160280A (en) * 2005-12-16 2007-06-28 National Agriculture & Food Research Organization Movable lid type sewage sprinkler equipped with stream disperser and automatic cleaning mechanism
JP2011252293A (en) * 2010-06-01 2011-12-15 Aqua Project Inc Circulation type simple toilet
JP2018167194A (en) * 2017-03-30 2018-11-01 三機工業株式会社 Sprinkler and sprinkler type cleaner
CN110156270A (en) * 2019-06-11 2019-08-23 中铁第一勘察设计院集团有限公司 Source-separated urine recovery of nitrogen and phosphorus and water reclaiming system and its operation method
CN110156270B (en) * 2019-06-11 2023-08-08 中铁第一勘察设计院集团有限公司 Source separation urine liquid nitrogen and phosphorus recovery and water recycling system and operation method thereof

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