[go: up one dir, main page]

JP2009183819A - Excreta treating material and excreta treating device equipped with the same - Google Patents

Excreta treating material and excreta treating device equipped with the same Download PDF

Info

Publication number
JP2009183819A
JP2009183819A JP2008024300A JP2008024300A JP2009183819A JP 2009183819 A JP2009183819 A JP 2009183819A JP 2008024300 A JP2008024300 A JP 2008024300A JP 2008024300 A JP2008024300 A JP 2008024300A JP 2009183819 A JP2009183819 A JP 2009183819A
Authority
JP
Japan
Prior art keywords
manure
compost
treatment
stirring
toilet
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
JP2008024300A
Other languages
Japanese (ja)
Inventor
Hideji Yoshizawa
秀二 吉澤
Shinichi Gen
真一 巖
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.)
Tama TLO Co Ltd
Original Assignee
Tama TLO 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 Tama TLO Co Ltd filed Critical Tama TLO Co Ltd
Priority to JP2008024300A priority Critical patent/JP2009183819A/en
Publication of JP2009183819A publication Critical patent/JP2009183819A/en
Pending legal-status Critical Current

Links

Images

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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/20Sludge processing

Landscapes

  • Treatment Of Sludge (AREA)
  • Mixers With Rotating Receptacles And Mixers With Vibration Mechanisms (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide an excreta treating material for a bio-toilet which dispenses with replenishment and replacement and greatly improves an excreta biodegradation capacity, and a bio-toilet which is made to be further compact while maintaining the excreta biodegradation capacity. <P>SOLUTION: The excreta treating material adopts carbide instead of sawdust used as a microorganism carrier in the conventional bio-toilet 10 and adds aerobic microorganisms thereto. Carbide, unlike sawdust, is not biodegraded by microorganisms to semipermanently dispense with replacement, and has an excellent moisture conditioning effect and air permeability due to its microporous structure to realize an moisture condition and an aerobic condition suitable for promoting propagation of the aerobic microorganisms and their biodegradation reactions, thereby remarkably increasing the excreta biodegradation capacity per volume, comparing to when using sawdust. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、糞尿処理材に関し、より詳細には、炭化物の粉粒体材料を主成分とする糞尿処理材及び該糞尿処理材を備える糞尿処理装置に関する。   The present invention relates to an excrement disposal material, and more particularly, to an excrement disposal material mainly composed of a carbide powder material and an excrement disposal apparatus including the excrement disposal material.

現在、下水道区域内においてその設置が義務づけられている水洗トイレは、使用に際して膨大な量の水を消費するシステムであり、家庭用水使用量のうち、水洗トイレの使用量は、全体の20%以上を占めると言われている。加えて、水洗トイレに排泄された糞尿は、下水道を介して下水処理場に運ばれ、そこで処理水となって河川に放流されるが、この放流水に含まれる大量の窒素及びリンが河口付近の富栄養化を引き起こす原因になる等、既存の水洗トイレを前提としたシステムは、環境への負荷が大きい。   Currently, flush toilets that are required to be installed in the sewer area are systems that consume a huge amount of water when used, and out of household water use, flush toilets use more than 20% of the total. It is said to occupy. In addition, manure excreted in the flush toilet is transported to the sewage treatment plant via the sewer, where it is treated and discharged into the river. The large amount of nitrogen and phosphorus contained in this effluent is near the river mouth. The system that presupposes existing flush toilets has a heavy impact on the environment.

この点につき、排泄された糞尿を微生物の力によってその場で分解・処理する自律分散型のトイレ・システム、いわゆる「バイオ・トイレ」が注目されている。ここで、従来のバイオ・トイレの機構について以下、簡単に説明する。まず、排泄された糞尿は、逐次、おが屑が貯留された処理槽に導入され、おが屑とともに撹拌・混合される。その際、おが屑は、糞尿に含まれる水分を適宜、吸収・保持・蒸発させるとともに、糞便内に生息していた腸内細菌をはじめとする各種分解細菌の繁殖環境として機能し、当該繁殖した細菌によって糞尿が水と二酸化炭素に生分解される。このように、バイオ・トイレは、既存の水洗トイレ・システムに比較した場合、上下水道を必要としないため設置場所を選ばず、また、その場で糞尿を完全に生分解することができるため周囲環境への負荷がないという点で優れているということができる。特開平8−290988号公報は、上述したバイオ・トイレの一実施形態について開示する。   In this regard, an autonomous decentralized toilet system that decomposes and processes excreted excreta on the spot by the power of microorganisms, a so-called “bio-toilet”, has attracted attention. Here, the conventional bio-toilet mechanism will be briefly described below. First, excreted excreta is sequentially introduced into a treatment tank in which sawdust is stored, and is stirred and mixed together with sawdust. At that time, sawdust appropriately absorbs, retains, and evaporates the water contained in manure, and functions as a breeding environment for various degrading bacteria including intestinal bacteria that lived in feces. Manure is biodegraded into water and carbon dioxide. In this way, bio-toilet does not require water and sewage compared to existing flush toilet systems, so it can be installed anywhere, and manure can be completely biodegraded on the spot. It can be said that it is excellent in that there is no burden on the environment. JP-A-8-290988 discloses one embodiment of the biotoilet described above.

しかしながら、従来のおが屑を細菌の繁殖媒体として用いるバイオ・トイレには以下に挙げる問題点があった。まず、通常の排泄量を処理するためには、大量のおが屑
が必要となるため、おが屑を貯留する処理槽の大型化が不可避であった。また、おが屑自体が細菌により生分解されることに伴って、徐々に塊状になり流動性を失うため、これを強制的に撹拌するための機構は大がかりなものとならざるを得なかった。さらに、おが屑自体の生分解に伴って、塊状内部は嫌気的になり、またその糞尿分解能力は経時的に低下し、これに伴って、アンモニア臭や発酵臭が発生することがあった。そのため、年に2〜3回は、おが屑を交換する必要があり、ランニング・コストがかかるという問題があった。
特開平8−290988号公報
However, conventional toilets that use sawdust as a bacterial propagation medium have the following problems. First, in order to process a normal amount of excretion, a large amount of sawdust is required. Therefore, it is inevitable to enlarge the processing tank for storing sawdust. In addition, as sawdust itself is biodegraded by bacteria, it gradually becomes lumpy and loses fluidity, so the mechanism for forcibly stirring it has to be large. Furthermore, with the biodegradation of sawdust itself, the inside of the lump becomes anaerobic, and its ability to decompose manure decreases with time, and ammonia odor and fermentation odor may be generated accordingly. Therefore, there has been a problem that it is necessary to replace sawdust twice or three times a year, which requires a running cost.
Japanese Patent Laid-Open No. 8-290988

本発明は、上記従来技術における課題に鑑みてなされたものであり、本発明は、補充・交換の必要が無く、糞尿の生分解能力が大幅に改善された新規なバイオ・トイレ用の糞尿処理材を提供することを目的とする。また、本発明は、糞尿の生分解性能を維持しつつよりコンパクト化された新規なバイオ・トイレを提供することを目的とする。   The present invention has been made in view of the above-mentioned problems in the prior art, and the present invention does not require replenishment / replacement, and is a novel biotoilet treatment for bio-toilet in which the biodegradability of manure is greatly improved. The purpose is to provide materials. Another object of the present invention is to provide a novel biotoilet that is more compact while maintaining the biodegradation performance of manure.

本発明者は、新規な糞尿処理材及び該糞尿処理材を備える新規な糞尿処理装置につき鋭意検討した結果、従来のバイオ・トイレにおいて微生物担体として用いられてきたおが屑に代わって、炭化物を採用し、さらに、好気性微生物を添加することによって、糞尿の生分解能力が大幅に改善されると同時に、当該糞尿処理材を用いることによって、糞尿処理装置の撹拌機構について新規な構成の採用が可能となり、もって、装置のコンパクト化が実現されることを見出し、本発明に至ったのである。   As a result of intensive studies on a novel manure treatment material and a novel manure treatment apparatus including the manure treatment material, the present inventor adopted carbide instead of sawdust which has been used as a microorganism carrier in conventional biotoilet. Furthermore, the biodegradability of manure is greatly improved by adding aerobic microorganisms, and at the same time, the use of the manure treatment material makes it possible to adopt a new configuration for the stirring mechanism of the manure treatment apparatus. Thus, the inventors have found that the apparatus can be made compact, and have reached the present invention.

すなわち、本発明によれば、好気性微生物と、該好気性微生物の担体としての炭化物の粉粒体材料とを主成分とする糞尿処理材が提供される。本発明において、前記炭化物は、木炭または竹炭とすることができ、炭化温度500℃〜1000℃で炭化したものを用いることが好ましい。また、前記好気性微生物を含有する物質としては、堆肥を用いることができる。前記堆肥は、落ち葉堆肥、家畜糞堆肥、生ゴミ堆肥、木質チップ堆肥からなる群より選択される少なくとも1種の堆肥とすることができ、前記堆肥は、完熟堆肥であることが好ましい。本発明においては、糞尿処理材は、さらにリン酸塩成分を含むことができる。   That is, according to the present invention, there is provided an excrement treatment material mainly composed of an aerobic microorganism and a carbide powder material as a carrier of the aerobic microorganism. In the present invention, the carbide may be charcoal or bamboo charcoal, and is preferably carbonized at a carbonization temperature of 500 ° C to 1000 ° C. Moreover, compost can be used as a substance containing the aerobic microorganism. The compost may be at least one compost selected from the group consisting of fallen leaf compost, livestock manure compost, garbage compost, and wood chip compost, and the compost is preferably a fully mature compost. In the present invention, the excrement disposal material can further contain a phosphate component.

また、本発明によれば、上述した糞尿処理材が充填された処理槽を備える糞尿処理装置であって、前記処理槽の内部に前記糞尿処理材を撹拌するための撹拌部材を備え、前記撹拌部材は、揺動運動によって前記糞尿処理材を撹拌する糞尿処理装置が提供される。前記処理槽は、前記糞尿処理材が充填される半円柱形状の空間を備え、前記撹拌部材は、前記半円柱形状と同心円の円弧の形状に合わせて湾曲して形成された底面部を備え、前記底面部は、前記空間の半円柱形状と同心円周上を揺動運動するものとすることができる。また、本発明においては、前記撹拌部材は、複数の撹拌子を備えることができ、前記底面部の外周面にブラシ状の部材を固設することができ、さらに、前記底面部に加温機構を備えることができる。   Further, according to the present invention, there is provided a manure processing apparatus including the processing tank filled with the above-described manure processing material, the stirring tank for stirring the manure processing material inside the processing tank, and the stirring The member is provided with a manure processing apparatus that stirs the manure processing material by a swinging motion. The treatment tank includes a semi-cylindrical space filled with the manure treatment material, and the stirring member includes a bottom surface portion that is formed to be curved according to the arc shape of the concentric circle with the semi-cylindrical shape, The bottom surface portion may swing on a circumference that is concentric with the semi-cylindrical shape of the space. In the present invention, the stirring member may include a plurality of stirring bars, a brush-like member may be fixed to the outer peripheral surface of the bottom surface portion, and a heating mechanism is provided on the bottom surface portion. Can be provided.

上述したように、本発明によれば、補充・交換の必要が無く、糞尿の生分解能力が大幅に改善された新規な糞尿処理材、及び該糞尿処理材を備え、糞尿の生分解性能を維持しつつ、よりコンパクト化された新規な糞尿処理装置が提供される。   As described above, according to the present invention, there is no need for replenishment / replacement, and there is provided a novel manure treatment material in which the biodegradability of manure is greatly improved, and the manure treatment material, and the biodegradation performance of manure is provided. A novel manure treatment apparatus that is more compact while being maintained is provided.

以下、本発明を図面に示した実施の形態をもって説明するが、本発明は、図面に示した実施の形態に限定されるものではない。   Hereinafter, the present invention will be described with reference to embodiments shown in the drawings, but the present invention is not limited to the embodiments shown in the drawings.

本発明においては、従来のバイオ・トイレにおいて微生物担体として用いられてきたおが屑に代わって、炭化物を主成分とする材料を採用することを特徴とする。炭化温度500℃〜1000℃で炭化した炭化物は、おが屑のように微生物によって自身が生分解されることがないため、半永久的に交換が不要であるということに加え、使用が進むに従って塊状になるというようなことがなく、常に、その流動性が保持されるため、好気条件が確保され、また撹拌における負荷を低減しうるという利点を有する。また、炭化物は、その微細多孔構造による優れた調湿作用および通気性を備えており、好気性微生物の繁殖およびその生分解反応を促進するのに好適な水分条件および好気条件を実現することができるため、おが屑を用いた場合に比べて、微生物の存在量に対応したアデノシン三リン酸(ATP)濃度が数倍から数十倍高く、体積あたりの糞尿の生分解能力が格段に増大する。よって、本発明においては、嫌気性の腐敗菌による生分解に伴う腐敗臭の発生が抑制されるとともに、より少ない量の媒体でおが屑と同等の効果が得られるため、処理槽を小型化することが可能となる。さらに、炭化物は、その優れた吸着作用によってアンモニア臭などの悪臭を消臭するという効果を奏する。   In the present invention, instead of sawdust which has been used as a microbial carrier in conventional bio-toilet, a material mainly composed of carbide is employed. Carbonized carbonized at a carbonization temperature of 500 ° C. to 1000 ° C. does not biodegrade itself by microorganisms like sawdust, and in addition to being semipermanently replaced, it becomes a lump as use progresses. Since the fluidity is always maintained, there is an advantage that the aerobic condition is secured and the load in stirring can be reduced. Carbide has excellent moisture conditioning and air permeability due to its microporous structure, and realizes moisture and aerobic conditions suitable for promoting the growth of aerobic microorganisms and their biodegradation reactions. Therefore, compared with sawdust, adenosine triphosphate (ATP) concentration corresponding to the amount of microorganisms is several to several tens of times higher, and the biodegradability of manure per volume is significantly increased. . Therefore, in the present invention, the generation of spoilage odor accompanying biodegradation by anaerobic spoilage bacteria is suppressed, and an effect equivalent to sawdust is obtained with a smaller amount of medium, so the processing tank can be downsized. Is possible. Further, the carbide has an effect of deodorizing malodors such as ammonia odor due to its excellent adsorption action.

本発明における炭化物は、木炭または竹炭などを用いることができ、これらを粉粒体としたものを微生物担体として用いることが好ましい。また、本発明における炭化物は、炭化温度500℃〜1000℃で炭化したものを用いることが好ましい。高温で炭化された炭化物は、無機化された炭素が多くなり、微生物により炭化物自身が生分解されることがないためである。   As the carbide in the present invention, charcoal or bamboo charcoal can be used, and it is preferable to use a powder of these as a microorganism carrier. Moreover, it is preferable to use the carbide | carbonized_material in this invention carbonized by carbonization temperature 500 to 1000 degreeC. This is because the carbonized carbonized at a high temperature contains a large amount of mineralized carbon, and the carbide itself is not biodegraded by microorganisms.

さらに本発明においては、糞尿の生分解能力を増強するため、微生物担体である炭化物に対して好気性微生物を別途添加することが好ましい。本発明において添加する好気性微生物は、糞尿の生分解能力を備えるものであれば特に限定するものではない。本発明においては、上述した好気性微生物の添加を、該好気性微生物を含有する物質の添加によって行なうことができ、例えば、落ち葉堆肥、家畜糞堆肥、生ゴミ堆肥、木質チップ堆肥などに代表される堆肥を炭化物に対して配合することによって行なうことができる。なお、配合する堆肥としては、処理槽内でさらなる生分解が進行することのない完熟堆肥を用いることが好ましい。   Furthermore, in the present invention, in order to enhance the biodegradability of manure, it is preferable to add aerobic microorganisms separately to the carbide that is the microorganism carrier. The aerobic microorganism added in the present invention is not particularly limited as long as it has the ability to biodegrade manure. In the present invention, the above-mentioned aerobic microorganisms can be added by adding a substance containing the aerobic microorganisms, for example, fallen leaf compost, livestock manure compost, garbage compost, and wood chip compost. This can be done by adding compost to the carbide. In addition, as compost | mixed to mix | blend, it is preferable to use the fully matured compost | cure which does not advance further biodegradation within a processing tank.

さらに加えて、本発明においては、糞尿の生分解能力をより増強するため、微生物担体である炭化物に対して、K3PO4、Ca3(PO4)2、MgPO4
などのリン酸塩を添加することが好ましい。以上、本発明の糞尿処理材について説明してきたが、次に、本発明の糞尿処理材を採用した新規なバイオ・トイレについて、以下説明する。
In addition, in the present invention, K 3 PO 4 , Ca 3 (PO 4 ) 2 , MgPO 4 is used as a microorganism carrier to further enhance the biodegradability of manure.
It is preferable to add a phosphate such as. The manure treatment material of the present invention has been described above. Next, a novel bio-toilet employing the manure treatment material of the present invention will be described below.

従来の糞尿処理材としておが屑を用いるバイオ・トイレにおいては、処理槽内部に、その長手方向に貫き、羽根状(または、スクリュー状)の突起部材が配設されたシャフトを備えており、当該シャフトを回転させることによって、おが屑を撹拌していた。当該構成は、自身の生分解によって経時的に塊状化することが避けられないおが屑を強制的に撹拌するための構成としては一定の理があったが、一方で、突起部材と処理槽の内壁の間に必然的に隙間が生じ、当該隙間の部分に滞留するおが屑が撹拌されないまま固化してしまうという問題や、処理槽内部を貫いてシャフトが定置的に存在することに伴って、糞便がシャフトに定常的に付着したまま生分解されないことにより、シャフトの腐食・破損を引き起こすという問題、さらには、おが屑の合間からスクリュー状の突起物が回転している様子が使用者に見えてしまうことによって、使用者が心理的圧迫感を覚えるという問題があった。   A conventional biotoilet that uses sawdust as a manure treatment material has a shaft that penetrates in the longitudinal direction inside the treatment tank and is provided with a blade-like (or screw-like) protruding member. The sawdust was stirred by rotating the. The structure had a certain reason for forcibly stirring sawdust that was unavoidably agglomerated over time due to its own biodegradation, but on the other hand, the protruding member and the inner wall of the treatment tank A gap is inevitably generated between the two, and the problem that the sawdust staying in the gap is solidified without stirring, and the presence of the shaft through the inside of the treatment tank, The problem of causing corrosion and breakage of the shaft due to the fact that it is not biodegraded while constantly attached to the shaft, and that the screw-like protrusions are rotating from the gap between sawdust is visible to the user. As a result, there was a problem that the user felt psychological pressure.

この点につき、本発明のバイオ・トイレは、流動性の高い炭化物の粉粒体材料を主成分とする糞尿処理材を採用したことによって、その撹拌機構について新規な構成を採用しうるに至ったのである。以下、本発明のバイオ・トイレにおける新規な撹拌機構について、図1〜図3を参照しながら以下説明する。   In this regard, the biotoilet of the present invention can adopt a novel structure for its stirring mechanism by adopting a manure treatment material mainly composed of a carbide material with high fluidity. It is. Hereinafter, the novel stirring mechanism in the biotoilet of the present invention will be described below with reference to FIGS.

図1は、本発明のバイオ・トイレおよびその撹拌機構について示す。図1(a)は、本発明のバイオ・トイレ10の外観を示す。本発明のバイオ・トイレ10においては、長方体形状の筐体部12の上面に直付式の便座14が配置されて構成され、便座14の両脇には使用時の安定を考慮して手すり16が配設されている。筐体部12の内部には、破線で示す処理槽18が収納されており、筐体部12の側面側には後述する撹拌部材を駆動するための電気モータなどの動力源20が設けられている。なお、上述した、筐体部12、便座14、および手すり16の構成は、既存のバイオ・トイレに採用されている構成を適用したものであって、本発明の技術思想はこれらの構成によって限定されるものでなく、備え付ける便器の具体的な形状・種類、筐体部の形状などは適宜選択することができ、また、処理槽18内部に負圧を生じさせるための排気機構などを適宜設けることができる。   FIG. 1 shows the bio-toilet of the present invention and its stirring mechanism. Fig.1 (a) shows the external appearance of the biotoilet 10 of this invention. In the biotoilet 10 of the present invention, a direct-attached toilet seat 14 is arranged on the upper surface of a rectangular parallelepiped casing 12, and in consideration of stability during use on both sides of the toilet seat 14. A handrail 16 is provided. A processing tank 18 indicated by a broken line is accommodated inside the casing 12, and a power source 20 such as an electric motor for driving a stirring member described later is provided on the side of the casing 12. Yes. In addition, the structure of the housing | casing part 12, the toilet seat 14, and the handrail 16 mentioned above applies the structure employ | adopted for the existing bio-toilet, Comprising: The technical thought of this invention is limited by these structures. The specific shape and type of the toilet bowl to be provided, the shape of the casing, and the like can be selected as appropriate, and an exhaust mechanism for generating a negative pressure in the processing tank 18 is appropriately provided. be able to.

図1(b)は、処理槽18のみを抜き出して示す。処理槽18は、略半円柱形状とされており、その上面18aには、便座14に対応する位置に開口22が形成され、この開口22から糞尿が処理槽18の内部に導入されるように構成されている。また、処理槽18の側面の動力源20に対応する位置には、後述する撹拌部材に動力を伝達するための回転軸24が突出している。さらに、図1(c)は、説明の便宜のため、処理槽18の内部を切り欠いて示す。図1(c)に示すように、処理槽18の下側は、半円柱形状の収容空間を備えており、当該収容空間に本発明の糞尿処理材が充填される。また。処理槽18の内壁側面18s,18sには、撹拌部材26が回転軸24を中心に図中の矢印方向に揺動自在に固定されている。   FIG. 1B shows only the processing tank 18 extracted. The treatment tank 18 has a substantially semi-cylindrical shape, and an opening 22 is formed on the upper surface 18 a thereof at a position corresponding to the toilet seat 14 so that feces and urine can be introduced into the treatment tank 18 from the opening 22. It is configured. Further, a rotary shaft 24 for transmitting power to a stirring member described later protrudes at a position corresponding to the power source 20 on the side surface of the processing tank 18. Further, FIG. 1C shows the interior of the processing tank 18 by cutting it out for convenience of explanation. As shown in FIG.1 (c), the lower side of the processing tank 18 is equipped with the semi-cylindrical storage space, and the said storage space is filled with the excrement processing material of this invention. Also. On the inner wall side surfaces 18 s and 18 s of the processing tank 18, a stirring member 26 is fixed so as to be swingable in the direction of the arrow in the drawing with the rotating shaft 24 as the center.

図2は、本発明のバイオ・トイレにおいて採用される撹拌部材26を示す。撹拌部材26は、略扇状の側面部26s,26sと、側面部26s,26sの円弧の形状に合わせて形成された湾曲した底面部26tを含んで構成されており、側面部26s,26sの円弧側に、湾曲した底面部26tが固着されてなる基本構造に対して、複数の棒状部材からなる撹拌子28が配設されている。図2に示す実施形態においては、側面部26s,26sの間に架設する形で格子状の撹拌子28aが設けられ、さらに、複数の棒状の撹拌子28bが底面部26tに対して略垂直方向に突設されている。本実施形態においては、撹拌部材26が図中の矢印方向に揺動運動することに伴って、処理槽に充填された糞尿処理材が撹拌子28a,28bによって撹拌される。なお、本発明においては、撹拌子を図2に示す構成に限定するものではなく、種々の設計変更が可能である。   FIG. 2 shows the stirring member 26 employed in the biotoilet of the present invention. The agitating member 26 includes substantially fan-shaped side surface portions 26s and 26s and a curved bottom surface portion 26t formed in accordance with the arc shape of the side surface portions 26s and 26s, and the arcs of the side surface portions 26s and 26s. On the side, a stirrer 28 made up of a plurality of rod-like members is disposed with respect to a basic structure in which a curved bottom surface portion 26t is fixed. In the embodiment shown in FIG. 2, a lattice-like stirrer 28a is provided so as to be installed between the side surface parts 26s, 26s, and a plurality of rod-like stirrer 28b are substantially perpendicular to the bottom surface part 26t. Projected to In the present embodiment, as the stirring member 26 swings in the direction of the arrow in the figure, the excrement disposal material filled in the processing tank is stirred by the stirring bars 28a and 28b. In the present invention, the stirrer is not limited to the configuration shown in FIG. 2, and various design changes can be made.

なお、細菌による糞尿の生分解反応は、50〜60℃の温度条件下で促進されるため、処理槽内部を所定温度に保持するための加温機構を備えることが好ましい。本発明のバイオ・トイレにおいては、上述した撹拌部材26に加温機構を設けることができる。図2(b)は、加温機構を備える撹拌部材26を示す。なお、図2(b)においては、説明の便宜のため、撹拌子を除外して示している。図2(b)に示す実施形態においては、撹拌部材26の底面部26tに加温機構30が埋設されている。本発明においては、加温機構30を電熱線などの電気抵抗を含むヒーターなどによって実現することができる。なお、図2(b)に示す実施形態においては、加温機構30は、回転軸24、側面部26sなどを介して配線された電線32によって電力を供給されるように構成されている。   In addition, since the biodegradation reaction of manure by bacteria is accelerated | stimulated on the temperature conditions of 50-60 degreeC, it is preferable to provide the heating mechanism for maintaining the inside of a processing tank at predetermined temperature. In the biotoilet of the present invention, the above-described stirring member 26 can be provided with a heating mechanism. FIG.2 (b) shows the stirring member 26 provided with a heating mechanism. In FIG. 2B, the stirrer is omitted for convenience of explanation. In the embodiment shown in FIG. 2B, the heating mechanism 30 is embedded in the bottom surface portion 26 t of the stirring member 26. In the present invention, the heating mechanism 30 can be realized by a heater including an electric resistance such as a heating wire. In the embodiment shown in FIG. 2B, the heating mechanism 30 is configured to be supplied with electric power by an electric wire 32 wired via the rotating shaft 24, the side surface portion 26s, and the like.

図3は、本発明のバイオ・トイレの処理槽18に充填された糞尿処理材34が撹拌部材26の揺動運動によって撹拌される態様を示す。図3においては、説明の便宜のため、処理槽18を側面から透視して示す。図3(a)に示されるように、側面部26sの円弧は、処理槽18の下側の収容空間の半円柱形状と同心円の円弧として形成されており、底面部26tは、側面部26sの円弧の形状に合わせて湾曲して形成されているため、撹拌部材26は、処理槽18の内壁面に接触することなく揺動運動することができる。なお、図3(a)において、破線の囲んだ部分の拡大図を紙面右側に実線で囲んで示す。図3(a)右側に実線で囲んで示すように、本実施形態においては、底面部26tの外周面に可撓性の材質からなるブラシ状の部材36を固着することができる。このように構成することによって、処理槽18の内壁面と底面部26tの外周面の間に形成された隙間gに入り込んだ糞尿処理材34は、ブラシ状の部材36によって掻き出されるので、糞尿処理材34が隙間gに滞留することが防止される。   FIG. 3 shows an aspect in which the excrement disposal material 34 filled in the treatment tank 18 of the biotoilet of the present invention is agitated by the swinging motion of the agitating member 26. In FIG. 3, for convenience of explanation, the treatment tank 18 is seen through from the side. As shown in FIG. 3 (a), the arc of the side surface portion 26s is formed as a circular arc concentric with the semi-cylindrical shape of the accommodation space below the processing tank 18, and the bottom surface portion 26t is formed of the side surface portion 26s. Since it is curved and formed in accordance with the shape of the arc, the stirring member 26 can swing without contacting the inner wall surface of the processing bath 18. In FIG. 3A, an enlarged view of a portion surrounded by a broken line is shown surrounded by a solid line on the right side of the drawing. As shown by a solid line on the right side of FIG. 3A, in the present embodiment, a brush-like member 36 made of a flexible material can be fixed to the outer peripheral surface of the bottom surface portion 26t. With this configuration, the manure treatment material 34 that has entered the gap g formed between the inner wall surface of the treatment tank 18 and the outer peripheral surface of the bottom surface portion 26t is scraped out by the brush-like member 36. The treatment material 34 is prevented from staying in the gap g.

図3(a)〜(c)に示されるように、撹拌部材26が図中の矢印方向に揺動することによって、糞尿処理材34はまんべんなく撹拌される。このような揺動運動のみで充分な撹拌効果を得るためには、糞尿処理材が高い流動性を備えていることが前提となるが、すでに上述したように、本発明の糞尿処理材34は、流動性の高い炭化物の粉粒体材料を主成分とし、また、含水等によって塊状化することがないため、本機構によって、細菌の生分解反応を維持するために必要十分な撹拌が好適に実現される。また、本機構によれば、揺動運動によって撹拌を行なうため、従来のスクリュー撹拌に比較して撹拌ムラがないことに加え、使用者に心理的な圧迫感を与えることが無く、また、稼働部の高さ方向の稼働範囲Hが低減されるため、処理槽18をコンパクト化することが可能となる。   As shown in FIGS. 3 (a) to 3 (c), when the stirring member 26 swings in the direction of the arrow in the drawing, the excreta treating material 34 is uniformly stirred. In order to obtain a sufficient stirring effect only by such a rocking motion, it is premised that the excrement disposal material has high fluidity. However, as already described above, the excrement disposal material 34 of the present invention is Because of its high fluidity, carbide powder and granule material as the main component, and because it does not agglomerate due to water content, etc., this mechanism is suitable for sufficient agitation to maintain the biodegradation reaction of bacteria. Realized. Further, according to this mechanism, since the agitation is performed by the swinging motion, there is no unevenness of stirring compared to the conventional screw agitation, and there is no psychological pressure on the user, and the operation is not performed. Since the operating range H in the height direction of the section is reduced, the processing tank 18 can be made compact.

以下、本発明のバイオ・トイレについて、実施例を用いてより具体的に説明を行なうが、本発明は、後述する実施例に限定されるものではない。   Hereinafter, the biotoilet of the present invention will be described more specifically with reference to examples, but the present invention is not limited to the examples described later.

(実施例1)
本発明の糞尿処理材が処理槽に充填されたバイオ・トイレを、一日あたり数名から数十名の利用が見込まれる環境に10ヶ月にわたって設置した。バイオ・トイレの100リットルの処理槽に50kgの粉炭を投入した。用いた粉炭は、炭化温度600℃〜700℃の竹炭であり、その粒径は100μm〜数mmであった。さらに、この処理槽内の粉炭に対し、完熟した落葉堆肥5kgを添加した。なお、実験期間中、処理槽内の温度を50−60℃に保持し、処理槽内の内容物の含水率が50−60%になるように調整した。また、処理槽内の好気性条件を保持すべく、処理槽内部が、トイレ使用直後に撹拌され、また使用の有無にかかわらず所定時間おきに定期的に撹拌されるように構成した。
Example 1
The bio-toilet in which the treatment tank of the present invention is filled in the treatment tank was installed for 10 months in an environment where several to several tens of people are expected to be used per day. 50 kg of pulverized coal was put into a 100 liter treatment tank of a biotoilet. The used pulverized coal was bamboo charcoal having a carbonization temperature of 600 ° C. to 700 ° C., and the particle size thereof was 100 μm to several mm. Furthermore, 5 kg of fully ripe deciduous compost was added to the pulverized coal in the treatment tank. During the experiment, the temperature in the treatment tank was maintained at 50-60 ° C., and the water content of the contents in the treatment tank was adjusted to 50-60%. Further, in order to maintain the aerobic condition in the treatment tank, the inside of the treatment tank is stirred immediately after the use of the toilet and is periodically stirred every predetermined time regardless of whether or not it is used.

10ヶ月にわたる実験期間において、トイレに排泄された糞尿は、完全に生分解していることが認められた。また、粉炭を主成分とする媒体は、最後までさらさらの状態を保っており、交換・補充の必要がなかった。また、定期的にトイレの排気中のアンモニア濃度を検知管により測定した結果、測定されたアンモニア濃度は、0−数ppmであった。   It was found that the manure excreted in the toilet was completely biodegraded during the 10-month experimental period. In addition, the medium containing pulverized coal as a main component was kept in a smooth state until the end, and there was no need for replacement or replenishment. Moreover, as a result of periodically measuring the ammonia concentration in the exhaust of the toilet with a detector tube, the measured ammonia concentration was 0 to several ppm.

(実施例2)
処理槽内の粉炭に対し、さらに、K3PO4を1kg添加した以外は、実施例1について上述したのと同様の条件で実験を行なった。10ヶ月にわたる実験期間において、排泄された糞尿が完全に生分解していることが認められ、粉炭を主成分とする媒体は、実施例1と同様に、最後までさらさらの状態を保っており、交換・補充の必要がなかった。また、定期的にトイレの排気中のアンモニア濃度を検知管により測定した結果、測定されたアンモニア濃度は、0−1ppmであり、アンモニア濃度が若干低減したことが認められた。
(Example 2)
The experiment was performed under the same conditions as described above for Example 1 except that 1 kg of K 3 PO 4 was further added to the pulverized coal in the treatment tank. In the experimental period of 10 months, it was found that excreted excreta was completely biodegraded, and the medium based on pulverized coal remained in a free-flowing state until the end, as in Example 1. There was no need for replacement or replenishment. As a result of periodically measuring the ammonia concentration in the exhaust of the toilet with a detector tube, the measured ammonia concentration was 0-1 ppm, and it was confirmed that the ammonia concentration was slightly reduced.

(比較例)
従来のおが屑が処理槽に充填されたバイオ・トイレを、一日あたり数名から数十名の利用が見込まれる環境に10ヶ月にわたって設置した。バイオ・トイレの100リットルの処理槽に50kgのおが屑を投入した。実験中、処理槽内の温度を50−60℃に保持し、処理槽内の内容物の含水率が50−60%になるように調整した。また、処理槽内の好気性条件を保持すべく、処理槽内部が、トイレ使用直後に撹拌され、また使用の有無にかかわらず所定時間おきに定期的に撹拌されるように構成した。
(Comparative example)
A conventional biotoilet filled with sawdust in a treatment tank was installed for 10 months in an environment where several to several tens of people are expected to be used per day. 50kg sawdust was put into the 100 liter treatment tank of the biotoilet. During the experiment, the temperature in the treatment tank was maintained at 50-60 ° C., and the water content of the contents in the treatment tank was adjusted to 50-60%. Further, in order to maintain the aerobic condition in the treatment tank, the inside of the treatment tank is stirred immediately after the use of the toilet and is periodically stirred every predetermined time regardless of whether or not it is used.

10ヶ月にわたる実験期間において、定期的にトイレの排気中のアンモニア濃度を検知管により測定した結果、測定されたアンモニア濃度は、数−数十ppmと比較的高い値を示した。さらに、実験期間の途中、処理槽内でおが屑が塊状になり、撹拌に支障を来たした。また、実験期間中、おが屑の量が経時的に減少したため、3〜4ヶ月に1回の頻度でおが屑を20kg程度補充する必要があった。   As a result of periodically measuring the ammonia concentration in the exhaust of the toilet with a detector tube during the experiment period of 10 months, the measured ammonia concentration showed a relatively high value of several to several tens of ppm. Furthermore, sawdust became agglomerated in the treatment tank during the experiment period, which hindered stirring. In addition, since the amount of sawdust decreased with time during the experiment, it was necessary to replenish about 20 kg of sawdust once every 3 to 4 months.

以上、説明したように、本発明によれば、補充・交換の必要が無く、糞尿の生分解能力が大幅に改善された新規な糞尿処理材、及び該糞尿処理材を備え、糞尿の生分解性能を維持しつつ、よりコンパクト化された新規な糞尿処理装置が提供される。本発明は、観光地、キャンプ場、イベント会場、工事現場、または介護現場などに設置される仮設トイレとしての応用展開が期待される。また、微生物の担体としての炭化物の粉粒体は、基本的には劣化することがないため、長期の保存性が良い。そのため、災害時の簡易トイレとしての用途も期待される。   As described above, according to the present invention, there is no need for replenishment / replacement, and a novel excrement treatment material in which the biodegradation ability of excrement has been greatly improved, and the excrement biotreatment of manure are provided. A novel manure treatment apparatus that is more compact while maintaining performance is provided. The application of the present invention is expected to be applied as a temporary toilet installed in a sightseeing spot, a campsite, an event venue, a construction site, or a nursing care site. In addition, carbide particles as a carrier for microorganisms are basically not deteriorated and thus have long-term storage stability. Therefore, the use as a simple toilet at the time of disaster is also expected.

本発明のバイオ・トイレおよびその撹拌機構について示す図。The figure shown about the bio-toilet of this invention, and its stirring mechanism. 本発明のバイオ・トイレにおいて採用される撹拌部材を示す図。The figure which shows the stirring member employ | adopted in the bio-toilet of this invention. 本発明のバイオ・トイレにおいて、糞尿処理材が撹拌部材の揺動運動によって撹拌される態様を示す図。The figure which shows the aspect in which the manure processing material is stirred by the rocking | fluctuation motion of a stirring member in the biotoilet of this invention.

符号の説明Explanation of symbols

10…バイオ・トイレ、12…筐体部、14…便座、16…手すり、18…処理槽、20…動力源、22…開口、24…回転軸、26…撹拌部材、28…撹拌子、30…加温機構、32…電線、34…糞尿処理材、36…ブラシ状の部材 DESCRIPTION OF SYMBOLS 10 ... Bio toilet, 12 ... Housing part, 14 ... Toilet seat, 16 ... Handrail, 18 ... Processing tank, 20 ... Power source, 22 ... Opening, 24 ... Rotating shaft, 26 ... Stirring member, 28 ... Stirring bar, 30 ... Warming mechanism, 32 ... electric wire, 34 ... manure treatment material, 36 ... brush-like member

Claims (12)

好気性微生物を含有する物質と、該好気性微生物の担体としての炭化物の粉粒体材料とを主成分とする糞尿処理材。   An excrement treatment material comprising as a main component a substance containing an aerobic microorganism and a carbide particulate material as a carrier for the aerobic microorganism. 前記炭化物は、木炭または竹炭である、請求項1に記載の糞尿処理材。   The manure treatment material according to claim 1, wherein the carbide is charcoal or bamboo charcoal. 前記炭化物は、炭化温度500℃〜1000℃で炭化したものである、請求項1または2に記載の糞尿処理材。   The manure treatment material according to claim 1 or 2, wherein the carbide is carbonized at a carbonization temperature of 500C to 1000C. 前記好気性微生物を含有する物質は、堆肥である、請求項1〜3のいずれか1項に記載の糞尿処理材。   The manure processing material according to any one of claims 1 to 3, wherein the substance containing the aerobic microorganism is compost. 前記堆肥は、落ち葉堆肥、家畜糞堆肥、生ゴミ堆肥、木質チップ堆肥からなる群より選択される少なくとも1種の堆肥である、請求項1〜4のいずれか1項に記載の糞尿処理材。   The manure processing material according to any one of claims 1 to 4, wherein the compost is at least one compost selected from the group consisting of fallen leaf compost, livestock manure compost, garbage compost, and wood chip compost. 前記堆肥は、完熟堆肥である、請求項5に記載の糞尿処理材。   The manure processing material according to claim 5, wherein the compost is fully matured compost. さらにリン酸塩成分を含む、請求項1〜6のいずれか1項に記載の糞尿処理材。   Furthermore, the excrement processing material of any one of Claims 1-6 containing a phosphate component. 請求項1〜7のいずれか1項に記載の糞尿処理材が充填された処理槽を備える糞尿処理装置であって、
前記処理槽の内部に前記糞尿処理材を撹拌するための撹拌部材を備え、
前記撹拌部材は、揺動運動によって前記糞尿処理材を撹拌する、
糞尿処理装置。
It is a manure processing apparatus provided with the processing tank with which the manure processing material of any one of Claims 1-7 was filled,
A stirring member for stirring the manure treatment material inside the processing tank,
The stirring member stirs the manure treatment material by a swinging motion,
Manure processing equipment.
前記処理槽は、前記糞尿処理材が充填される半円柱形状の空間を備え、前記撹拌部材は、前記半円柱形状と同心円の円弧の形状に合わせて湾曲して形成された底面部を備え、前記底面部は、前記空間の半円柱形状と同心円周上を揺動運動する、請求項8に記載の糞尿処理装置。   The treatment tank includes a semi-cylindrical space filled with the manure treatment material, and the stirring member includes a bottom surface portion that is formed to be curved according to the arc shape of the concentric circle with the semi-cylindrical shape, The feces and urine treatment apparatus according to claim 8, wherein the bottom portion swings on a circumference concentric with the semi-cylindrical shape of the space. 前記撹拌部材は、複数の撹拌子を備える、請求項8または9に記載の糞尿処理装置。   The manure processing apparatus according to claim 8 or 9, wherein the stirring member includes a plurality of stirring bars. 前記撹拌部材は、前記底面部の外周面にブラシ状の部材が固設された、請求項8〜10のいずれか1項に記載の糞尿処理装置。   The manure treatment apparatus according to any one of claims 8 to 10, wherein the stirring member has a brush-like member fixed to an outer peripheral surface of the bottom surface portion. 前記撹拌部材は、前記底面部に加温機構を備える、請求項8〜11のいずれか1項に記載の糞尿処理装置。
The feces and urine treatment apparatus according to claim 8, wherein the stirring member includes a heating mechanism on the bottom surface portion.
JP2008024300A 2008-02-04 2008-02-04 Excreta treating material and excreta treating device equipped with the same Pending JP2009183819A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2008024300A JP2009183819A (en) 2008-02-04 2008-02-04 Excreta treating material and excreta treating device equipped with the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2008024300A JP2009183819A (en) 2008-02-04 2008-02-04 Excreta treating material and excreta treating device equipped with the same

Publications (1)

Publication Number Publication Date
JP2009183819A true JP2009183819A (en) 2009-08-20

Family

ID=41067653

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2008024300A Pending JP2009183819A (en) 2008-02-04 2008-02-04 Excreta treating material and excreta treating device equipped with the same

Country Status (1)

Country Link
JP (1) JP2009183819A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101878423B1 (en) * 2017-08-01 2018-07-13 (주)일광비티 Composition for promoting treatment of livestock wastewater and method of removing bubbles or reducing bad smell using the same in aeration tank for promoting treatment of livestock sludge
WO2021149811A1 (en) * 2020-01-24 2021-07-29 株式会社日本環境科学研究所 Organic matter decomposer and use therefor

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5776835U (en) * 1980-10-27 1982-05-12
JPH09313401A (en) * 1996-05-31 1997-12-09 Toyoda Gosei Co Ltd Portable toilet
JPH11197635A (en) * 1998-01-12 1999-07-27 Shinichi Sakai Method for decomposing organic waste, and method for producing plant soil by decomposing organic waste
JPH11300395A (en) * 1998-04-17 1999-11-02 Motoda Electronics Co Ltd Belt conveyor-type sludge treating method and sludge treating system
JP2003026492A (en) * 2001-07-16 2003-01-29 Ryokusan Co Ltd Seed mixed compost composition and method of manufacturing the same
JP2003221288A (en) * 2002-01-30 2003-08-05 Kiyoshi Kitagawa Production method of compost from organic material
JP2004149336A (en) * 2002-10-29 2004-05-27 Someya:Kk Alkaline bark, alkaline composition, and method of manufacturing alkaline microorganism-supporting alkaline bark

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5776835U (en) * 1980-10-27 1982-05-12
JPH09313401A (en) * 1996-05-31 1997-12-09 Toyoda Gosei Co Ltd Portable toilet
JPH11197635A (en) * 1998-01-12 1999-07-27 Shinichi Sakai Method for decomposing organic waste, and method for producing plant soil by decomposing organic waste
JPH11300395A (en) * 1998-04-17 1999-11-02 Motoda Electronics Co Ltd Belt conveyor-type sludge treating method and sludge treating system
JP2003026492A (en) * 2001-07-16 2003-01-29 Ryokusan Co Ltd Seed mixed compost composition and method of manufacturing the same
JP2003221288A (en) * 2002-01-30 2003-08-05 Kiyoshi Kitagawa Production method of compost from organic material
JP2004149336A (en) * 2002-10-29 2004-05-27 Someya:Kk Alkaline bark, alkaline composition, and method of manufacturing alkaline microorganism-supporting alkaline bark

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101878423B1 (en) * 2017-08-01 2018-07-13 (주)일광비티 Composition for promoting treatment of livestock wastewater and method of removing bubbles or reducing bad smell using the same in aeration tank for promoting treatment of livestock sludge
WO2021149811A1 (en) * 2020-01-24 2021-07-29 株式会社日本環境科学研究所 Organic matter decomposer and use therefor

Similar Documents

Publication Publication Date Title
US3884804A (en) Method of deodorizing animal wastes
CN101786727A (en) Moving-bed biofilm oxidation ditch
CN104829050A (en) Fully automatic control hospital sewage treatment method and device
JP2009183819A (en) Excreta treating material and excreta treating device equipped with the same
JP3786656B2 (en) Toilet equipment
JP4863179B2 (en) Non-discharge type water circulation type simple flush toilet and method of purifying sewage in no discharge type water circulation type simple flush toilet
CN211005018U (en) Efficient culture sewage treatment system
CN103537189A (en) Deodorant filler and preparation method thereof
JP3696218B2 (en) Feces and urine decomposition treatment agent and method for degradation of manure by activating microorganisms
JPS6174527A (en) Granular product for feeding animal
CN114604930A (en) Excrement and urine diversity type quick harmless reduction toilet system for excrement
JP2010247094A (en) Livestock wastewater treatment method including livestock waste and livestock wastewater treatment equipment used therefor
JP4471216B2 (en) Microbial carrier with nitrohumate
JP2007308325A (en) Earthworm dung carbide and adsorbent
JP2006116421A (en) Deodorizing material, manufacturing method therefor and deodorizing method
JP2008049251A (en) Apparatus for removing nitrogen
JP2002219497A (en) Waste and sludge treatment method, carbonized product obtained by the method, and ordinary fertilizer using carbonized product
WO1997021647A1 (en) Method of stabilizing odors in manure
JP3192408B2 (en) Garbage processing equipment
JP2001334236A (en) Organic waste treatment method and apparatus
WO2000045689A1 (en) Toilet paper
JP4628089B2 (en) Small animal deodorization cage
JPH0523553Y2 (en)
AU1729701A (en) A method and system for treatment of animal waste
JP2004209362A (en) Sewage treatment apparatus

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20110202

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20111117

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20111213

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20120417