JPS5846356B2 - Human waste solubilization “filtration” overdecomposition tank - Google Patents

Human waste solubilization “filtration” overdecomposition tank

Info

Publication number
JPS5846356B2
JPS5846356B2 JP56075990A JP7599081A JPS5846356B2 JP S5846356 B2 JPS5846356 B2 JP S5846356B2 JP 56075990 A JP56075990 A JP 56075990A JP 7599081 A JP7599081 A JP 7599081A JP S5846356 B2 JPS5846356 B2 JP S5846356B2
Authority
JP
Japan
Prior art keywords
chamber
tank
filtration
human waste
solubilization
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.)
Expired
Application number
JP56075990A
Other languages
Japanese (ja)
Other versions
JPS57190624A (en
Inventor
義男 鵜瀬
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.)
TSUCHIMI KOZABURO
Original Assignee
TSUCHIMI KOZABURO
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 TSUCHIMI KOZABURO filed Critical TSUCHIMI KOZABURO
Priority to JP56075990A priority Critical patent/JPS5846356B2/en
Publication of JPS57190624A publication Critical patent/JPS57190624A/en
Publication of JPS5846356B2 publication Critical patent/JPS5846356B2/en
Expired 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
    • 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

  • Biological Treatment Of Waste Water (AREA)
  • Treatment Of Biological Wastes In General (AREA)
  • Filtration Of Liquid (AREA)

Description

【発明の詳細な説明】 この発明は、生し尿を可溶化に成し、生物学的涙過分解
作用を、より有効に行なわれるようにした、し尿の可溶
化分解槽に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a solubilization and decomposition tank for human waste, which solubilizes human waste and enables the biological tear hyperdecomposition effect to be carried out more effectively.

し尿及び附随汚物を直接、p退店(活性土壌と称してい
る)に***または投棄して処理を行なう従来の堆肥式ト
イレ或は、乾式トイレと称されるものに於いて生糞、附
随汚物など、特にトイレットペーパーによる目詰まりが
甚しく濾過作用を阻害し、且つ濾過床面の通気が妨たげ
られている。
Raw excrement and associated filth are removed in conventional composting toilets or dry toilets, where human waste and associated filth are disposed of by being directly excreted or dumped into p-stores (referred to as activated soil). In particular, clogging caused by toilet paper seriously impedes the filtration action and prevents ventilation of the filtration floor surface.

従ってこれらのものは沢退店に於ける好気性微生物の分
解能力が衰え浄化作用が低下し、糞及び附随汚物が極度
に堆積して嫌気発酵による悪臭を放つ状態を呈し、たと
え沢退店の可橋を掻き均すに至っても附随汚物による濾
過機能障害を除去することはできない構成になっている
Therefore, the decomposition ability of aerobic microorganisms in the store deteriorates, and the purification effect decreases, and feces and associated filth accumulate to an extreme extent, giving off a bad odor due to anaerobic fermentation. The structure is such that even if the bridge is leveled, it is not possible to remove the filtration dysfunction caused by the accompanying dirt.

尚、障害に起因して沢退店局部より稀薄水分が滲透して
沢退店底面より多量に流滴する状態に於いて1材の保水
能力と水分の蒸発とのバランス保持ができていないなど
、機能的に欠点を見出すものである。
In addition, due to a failure, diluted water seeps from the local part of the store and drips in large quantities from the bottom of the store, making it impossible to maintain a balance between the water retention capacity of one material and the evaporation of water. , we find functional deficiencies.

この発明は、し尿、附随汚物など特にトイレットペーパ
ーによる濾過機能低下、及び高頻度の***使用に耐え、
且つ機能麻痺など発生することなく濾過作用を円滑にし
て、微生物による浄化作用を容易に安定して行はせるこ
とを目的としている。
This invention can withstand the deterioration of the filtration function of toilet paper, such as human waste and accompanying filth, and the high frequency of excretion use.
In addition, the purpose is to facilitate the filtration action without causing functional paralysis, and to easily and stably carry out the purification action by microorganisms.

この発明を図面にもとづいて説明すると、第1図に図示
するし原種1に破砕機2及び温風発生器3を内蔵したし
原種。
The present invention will be explained based on the drawings. As shown in FIG. 1, there is shown in FIG.

恒温槽上部7に電動機4、減速伝動機構(第11図、3
2〜47)を介して掻寄せ羽根5及び撒布盤6を固着し
た撒布装置を装着して、沢過槽9〜1103重函を収納
された恒温槽8を第8図に示す接手31.31’にゴム
バッキングを挾んで接続固着して、し尿の可溶化濾過分
解槽を構成する。
An electric motor 4 and a reduction transmission mechanism (Fig. 11, 3
2 to 47) to which a spreading device with raking blades 5 and a spreading plate 6 fixed is attached, and a constant temperature bath 8 containing overflow tanks 9 to 1103 and heavy boxes is connected to a joint 31.31 shown in FIG. A rubber backing is sandwiched between the two and fixed to form a human waste solubilization, filtration and decomposition tank.

以下、部分を説明すると、 し原種1の内部は第4図に示す通気口24を穿孔した仕
切板19及び仕切板19を貫通せるトラフ20を設け、
し尿沈殿室、破砕混合室、可溶化室、温風発生室など4
つの室に区分し、トラフ20内に破砕機2を挿入して固
着する。
To explain the parts below, the inside of the original species 1 is provided with a partition plate 19 with a ventilation hole 24 shown in FIG. 4 and a trough 20 that can pass through the partition plate 19.
Human waste sedimentation chamber, crushing mixing chamber, solubilization chamber, hot air generation chamber, etc. 4
The crusher 2 is inserted into the trough 20 and fixed therein.

トラフ20には対流口21を設げ接手25付壁面にし尿
S液面に位置して越流堰22を設け、更に樋23を取付
けている。
A convection opening 21 is provided in the trough 20, an overflow weir 22 is provided on the wall surface with a joint 25 located at the human urine S liquid level, and a gutter 23 is further attached.

し原種のし尿沈殿室は片楔型とし、その底部の空間に温
風発生器3を収納して外壁面にて固着させ温風吹出側を
吹出室1′に嵌め込まれる。
The excreta sedimentation chamber for night soil is wedge-shaped, and a hot air generator 3 is housed in the space at the bottom thereof and fixed to the outer wall surface, and the hot air blowing side is fitted into the blowing chamber 1'.

し原種***口は便座18或は他の形状の便器類を装着さ
せることも可能な形状にしている恒温槽は第8図に示す
接手25’、25〃、3131′を設けた2面間口の画
状とした恒温槽上部7下部8を組合せていつ体に形成さ
れる、恒温槽上部に排気口15吸び電動機4を介する減
速伝導機構(第11図32〜47)を収納する伝動室2
6が設げられている。
The original species excretion port has a shape that allows the installation of a toilet seat 18 or other shaped toilet bowls.The thermostatic chamber has a two-sided opening provided with joints 25', 25〃, and 3131' as shown in Figure 8. A power transmission chamber 2 that houses a deceleration transmission mechanism (FIG. 11, 32 to 47) through an exhaust port 15 and a suction motor 4 is formed in the upper part of the constant temperature chamber by combining an upper part 7 and a lower part 8 of the constant temperature chamber in the shape of a picture.
6 is provided.

恒温槽下部8は鎖線図示9゜10.11の濾過槽を積み
重ねて収容される内部構造とし、縦横の仕切に於ける送
風室27を形成して横仕切は開口部28を設けた補強枠
を形成しこれに沢過槽を設置する。
The lower part 8 of the constant temperature chamber has an internal structure in which filtration tanks of 9° 10.11 shown in chain lines are stacked and housed, and ventilation chambers 27 are formed in the vertical and horizontal partitions, and the horizontal partitions have a reinforcing frame with openings 28. A sewage tank is installed in this area.

縦仕切は内壁面に平行に仕切られ接手31′の延長に於
いて掩被され、第9図に示す送風口29を上下に設けて
おり送風室27に第8図に示す如く取出し口30を設け
、外壁より盲蓋15で塞がれる。
The vertical partition is partitioned parallel to the inner wall surface and covered by the extension of the joint 31', and has ventilation ports 29 shown in FIG. 9 above and below, and an outlet 30 in the ventilation chamber 27 as shown in FIG. It is closed off with a blind cover 15 from the outer wall.

接手25“側聞口部には案内板を第10図に示す如く中
央部に於いて鎖線図示9,10.11の沢過槽を導入し
得る形状に設けている。
A guide plate is provided at the side opening of the joint 25, as shown in FIG. 10, in a shape that allows introduction of a sump tank indicated by chain lines 9, 10, and 11 at the center.

撒布装置は第11図に示す如(、電動機4を介して減速
ギヤー32〜35を回転軸37に固着して軸受36上下
2個を挿入して取付板44〜46に取付げる。
The spraying device is constructed as shown in FIG. 11 (reduction gears 32 to 35 are fixed to a rotating shaft 37 via an electric motor 4, two upper and lower bearings 36 are inserted, and mounted to mounting plates 44 to 46.

軸受38に軸受47上下2個及び減速ギヤー43を取付
けて挿通して取付板46に固着される。
Two upper and lower bearings 47 and a reduction gear 43 are attached to the bearing 38 and fixed to the mounting plate 46 by inserting them.

撒布軸40に減速ギヤー41を固着して掻寄せ軸42に
挿通して取付板44に軸受39を介して固着される。
A reduction gear 41 is fixed to the spreading shaft 40, inserted through the scraping shaft 42, and fixed to the mounting plate 44 via a bearing 39.

掻寄せ羽根5は8枚の羽根を放射状に等分して各羽根に
ゴムヘラ49を固定板48で挾んで固定される。
The scraping blade 5 has eight blades divided radially into equal parts and fixed to each blade by sandwiching a rubber spatula 49 between fixing plates 48.

撒布盤6は円形皿状に形成し中央凸部を設は盤面には撒
布口54を設けた回転盤と成し、その撒布口54の位置
する裏面の25°回転方向寄りに中心を軸とした線上に
振り分けて2枚の掻均し板51を固着してVノツチ状の
均しゴム52を固定板50で挾んで固定される。
The spreading plate 6 is formed into a circular dish shape, has a central convex portion, and is a rotary plate with a spreading port 54 on the plate surface, and the center is located near the 25° rotation direction of the back surface where the spreading port 54 is located. Two leveling plates 51 are fixed on the line, and a V-notch leveling rubber 52 is sandwiched between the fixing plates 50 and fixed.

掻寄せ羽根5を掻寄せ軸42に挿通して締附はナツト5
3に於いて固定され、撒布盤6も中央凸部に於いて撒布
軸40に挿通され掻寄せ羽根5に設けられたゴムヘラ4
9が稍々湾曲する程に撒布盤6を抑圧気味にして撒布軸
40に固定される。
Insert the scraping blade 5 into the scraping shaft 42 and tighten with the nut 5.
3, the spreading plate 6 is also inserted into the spreading shaft 40 at the central convex portion, and the rubber spatula 4 is attached to the scraping blade 5.
The spreader 6 is fixed to the spreader shaft 40 in such a way that the spreader 9 is slightly curved.

これら電動機4及び減速伝動機構(部品記号32〜47
)は鎖線図示恒温槽上部7の第9図に示す伝導室26に
収納され第1図に示すカバー17で掩被させ、掻寄せ羽
根5及び撒布盤6は第11図、鎖線図に示すように恒温
槽上部7の内部に装着されるとともに、樋23の下側に
位置し、且つ濾過槽9内に位置されている。
These electric motors 4 and reduction transmission mechanisms (part symbols 32 to 47
) is housed in the conduction chamber 26 shown in FIG. 9 in the upper part 7 of the thermostatic chamber shown in chain lines and covered with a cover 17 shown in FIG. It is installed inside the thermostatic chamber upper part 7, is located below the gutter 23, and is located within the filtration tank 9.

濾過槽は第14図に図示する如く沢過槽9〜11に分解
され各種は上下開口とし、4面の壁面で形成され、沢過
槽9,10の壁面下部を貫通して網目状の通気管12を
並列に挿通させ第15図に図示す如く中央部に支持板を
固着して通気管12が支えられている。
As shown in FIG. 14, the filtration tank is divided into swell tanks 9 to 11, each of which has upper and lower openings, and is formed by four walls, with a mesh-like passage passing through the lower part of the walls of the swell tanks 9 and 10. The ventilation pipes 12 are supported by inserting the tracheas 12 in parallel and fixing a support plate to the center as shown in FIG.

濾過槽11の下部には第14図に示す如く丸材を簀の千
秋に敷設される。
At the bottom of the filtration tank 11, as shown in FIG. 14, round timbers are laid in rows.

尚、第14図に示す如く通気管12の上下面に長繊維多
層マット13を第16図に図示する要領で全面を掩被し
、また、濾過槽11に敷設された簀の千秋底に第13図
に於ける鎖線図マット13を底面に掩被して、鎖線図・
・ツチングに示す有機炭素系(草炭、泥炭類)P材Cが
個々に充填されて、各種9〜11を積重ねて恒温槽下部
8に収納される。
As shown in FIG. 14, the upper and lower surfaces of the ventilation pipe 12 are covered with long fiber multilayer mats 13 in the manner shown in FIG. By covering the bottom surface with the chain line diagram mat 13 in Figure 13, the chain line diagram/
- The organic carbon-based (grass charcoal, peat) P material C shown in the drawing is filled individually, and each type of material 9 to 11 is stacked and stored in the lower part 8 of the thermostatic chamber.

上記の如く構成された、し原種の容量は1日当り***量
の20日分とし、第1図に示すし尿沈殿室に於いて糞及
び附随汚物(トイレットペーパーなど)は沈殿或は浮遊
などして、図示する流動線の如(第4図に於けるトラフ
20を介して破砕機2により攪拌され汚物類は溶融性粒
状或は短繊維状に破砕混合されて対流口21を介して形
成された可溶化室に於いて対流循環が行はれ、沈殿物は
し尿沈殿室に沈殿して、スラリーは越流堰22より流出
して樋23を介して第11図に示す撒布盤6に流入され
る。
The capacity of the original species configured as described above is equivalent to the amount of excretion per day for 20 days, and the feces and accompanying filth (toilet paper, etc.) are settled or suspended in the human urine sedimentation chamber shown in Figure 1. As shown in the flow line shown in the figure (see FIG. 4), the waste is stirred by the crusher 2 through the trough 20, crushed and mixed into meltable particles or short fibers, and formed through the convection port 21. Convection circulation is carried out in the solubilization chamber, and the precipitate is deposited in the human waste settling chamber, and the slurry flows out from the overflow weir 22 and flows into the spreading plate 6 shown in FIG. 11 through the gutter 23. Ru.

流入スラリーは撒布盤6に於ける掻寄せ羽根5の区分域
に溜り設定された時間に於いて濾過槽9のE床に撒布さ
れる。
The inflowing slurry accumulates in the divided area of the scraping blades 5 on the spreading plate 6 and is spread onto the E bed of the filtration tank 9 at a set time.

即ち***回数に拘らず破砕機2を1時間毎に約2分程度
駆動させた際、その攪拌波が越流堰22を溢流するので
ある。
That is, when the crusher 2 is driven for about 2 minutes every hour regardless of the number of times of excretion, the stirring waves overflow the overflow weir 22.

撒布装置の動作目的は、第11図に示す撒布軸40及び
掻寄せ軸42は共に時計方向廻りとし、撒布軸40を介
する撒布盤6及び掻寄せ軸42を介する掻寄せ羽根5を
、前者を遅く後者は早く回転させて、第12図に示す区
分域に滞溜せるスラリーSを掻寄せ羽根5により、撒布
盤6に設げた撒布口54に於いて排出させる。
The purpose of operation of the spreading device is that both the spreading shaft 40 and the raking shaft 42 shown in FIG. The later one is rotated faster, and the slurry S accumulated in the divided area shown in FIG.

つまり撒布装置を作動時間15秒とする間欠運転に設定
して撒布口54の停止位置を等分放射状に停止させ、そ
の間欠動作に於いてスラリーSをP床面に円形状に撒布
が行はれる。
In other words, the spreading device is set to intermittent operation with an operating time of 15 seconds, and the stopping positions of the spreading ports 54 are stopped in a radial manner, and during this intermittent operation, the slurry S is spread in a circular shape onto the P floor surface. It will be done.

なお、掻取り羽根5に於いてスラリーSを区分域に捕集
して、且つ、撒布盤6内の汚物類を除去する動作を取り
入れた構成にしている。
In addition, the configuration is such that the scraping blade 5 collects the slurry S in a divided area and also removes the dirt in the spreading plate 6.

沢過槽9に撒布されたスラリーSは濾過槽9,10,1
1に充填せる沢材層CK滲透するも、難融物及び未破砕
物は濾過槽9の沢床に残留し、稀薄汚水は沢材Cに吸収
され、なお沢床面に堆積された未分解物の可橋は均しゴ
ム52に於いて掻き均らされる。
The slurry S spread in the filtration tank 9 is filtered into the filtration tanks 9, 10, 1.
Although the slough material layer CK to be filled in 1 permeates through, the refractory and uncrushed materials remain on the slough bed of the filtration tank 9, and the dilute sewage is absorbed by the slough material C, and the undecomposed substances deposited on the slough bed surface remain. The surface of the object is leveled with a leveling rubber 52.

これらのスラリーSは、し原種に於いて腐敗菌または、
適応された自然培養従属栄養微生物の作用により分子量
の大きい有機物も殆んど有機酸になる工程を経て可溶化
されて、微生物の捕食する中間栄養基質に分解されてい
る。
These slurries S contain spoilage bacteria or
Due to the action of adapted naturally cultured heterotrophic microorganisms, most of the organic substances with large molecular weights are solubilized through the process of becoming organic acids and decomposed into intermediate trophic substrates that are preyed on by the microorganisms.

沢過槽に充填されている沢材Cに予め適応した微生物を
接種しておき、撒布されたスラIJ Sを沢床面及び
沢槽内に於いて捕食分解させる。
Adapted microorganisms are inoculated in advance into the slough material C filled in the slough tank, and the spread slough IJS is captured and decomposed on the slough bed surface and inside the slough tank.

従ってこれらの微生物は濾過槽な培地として培養される
と共に勢力的に分解活動を行はせる為に、好気的条件を
保持する上に於いて、沢過槽9〜10に通気管12を敷
設し、且つマット13を接液してp槽に於ける温風通気
面積を大きくとり、また、通気条件を良好にさせている
Therefore, in order to cultivate these microorganisms as a culture medium in a filter tank and to actively decompose them, ventilation pipes 12 are installed in the filter tanks 9 and 10 in order to maintain aerobic conditions. In addition, the mat 13 is brought into contact with the liquid to increase the hot air ventilation area in the p-tank and to improve the ventilation conditions.

撒布装置によりP床面が有効に利用でき、且つ好気条件
を保持す培地構成により沢過槽9〜10を多段式に積み
重ねることが可能となり、従ってp過表面積を立体的に
得ることが延いては恒温槽7,8を小型化させることに
なる。
The spreading device makes it possible to effectively use the P floor surface, and the culture medium structure that maintains aerobic conditions makes it possible to stack the overflow tanks 9 to 10 in multiple stages, making it possible to obtain the P oversurface area three-dimensionally. In this case, the constant temperature chambers 7 and 8 will be downsized.

汚物収集皿14は、第1図に示す恒温槽下部8送風室2
7に収納させる。
The filth collecting tray 14 is located in the lower part of the thermostatic chamber 8 in the ventilation chamber 2 shown in FIG.
Store it in 7.

収集汚物は極めて微量の無機堆肥化物で、滲透吸収ある
いは沢過途上にあるスラIJ Sは、分解作用を受け
て殆んど二酸化炭素、窒素前ガス、水分とになり、未分
解物は沢槽内に残留して分解物は放散または蒸発して大
気中に放散される。
The collected sewage is an extremely small amount of inorganic compost, and the sura IJS that is in the process of permeating and absorbing is decomposed and becomes mostly carbon dioxide, nitrogen gas, and moisture, and undecomposed materials are stored in the wastewater tank. The decomposed products remaining in the atmosphere are dissipated or evaporated into the atmosphere.

従って汚物収集皿14に収集されるものは小量の乾燥さ
れた沢材Cを主体とする無機堆肥化物で、1ケ年の収集
量約201程度のものである。
Therefore, what is collected in the filth collection tray 14 is an inorganic compost mainly consisting of a small amount of dried swamp material C, and the amount collected in one year is about 201.

なお、脱着は取出し口30を介して行はれる。Note that attachment and detachment are performed through the outlet 30.

温風発生器3は第4図に示す如く、し原種1に区分形成
されている底部に収納し、外気を吸入して発生器本体内
部に収納せる電気抵抗体(カートリッジヒーター)によ
り加温された温風を吹出室1′を介して恒温槽下部8通
気室7を通風し、第10図に示す開口部28に於いて沢
過槽11の簀の子状底面に通気作用を当え、更に温風は
通風口29を介して沢過槽9,100通気管12へと送
風され、マット13の空間を介して沢材Cに通気される
As shown in Fig. 4, the hot air generator 3 is housed in the bottom section of the raw material 1, and is heated by an electric resistor (cartridge heater) that draws in outside air and is housed inside the generator body. The heated air is passed through the lower part 8 of the thermostatic chamber 8 through the ventilation chamber 7 through the blowing chamber 1', and aeration is applied to the screen-like bottom surface of the filtration tank 11 through the opening 28 shown in FIG. Air is blown through the ventilation opening 29 to the swamp tank 9, 100 and the ventilation pipe 12, and is vented to the swamp material C through the space of the mat 13.

これらのP層通気温風及び余剰温風は恒温槽上部7に於
いて集合され設けられている排気口15′より大気中に
放散される。
These P-layer ventilation hot air and surplus hot air are collected in the thermostatic chamber upper part 7 and are radiated into the atmosphere through the exhaust port 15' provided therein.

なお、し原種1に於いて発生するガスも第4図に示す通
気口24及び対流口21より越流堰22の開口部を介し
て恒温槽上部7に流動し、排気口15′より大気中に放
出される。
In addition, the gas generated in the raw material 1 also flows into the thermostatic chamber upper part 7 through the opening of the overflow weir 22 from the vent port 24 and convection port 21 shown in FIG. is released.

この発明は、し原種に於いて破砕機を用ひ***物及び附
随汚物などを攪拌して破砕し、且つ混合液に威し可溶化
工程を経たスラリーを生成し、微生物酸化分解を基礎と
する上に於ける中間栄養基質を得ることに始り、これを
好気的環境条件に構成された有機炭素系沢材培地(濾過
槽)に均等に撒布させて沢過分解作用を円滑に行はさせ
ることにある。
This invention is based on microbial oxidation and decomposition by using a crusher to agitate and crush the excreta and accompanying filth, and then adding to the mixed liquid to produce a slurry that undergoes a solubilization process. The process begins by obtaining an intermediate nutrient substrate, and then evenly distributing it on an organic carbon-based slough medium (filter tank) configured in an aerobic environment to ensure smooth slough decomposition. It's about letting people know.

従来、行はれている方法及び構成などに於ける未分解、
沢過不良、嫌気醗酵による悪臭の発生など欠点は、既述
の如き方法、構成に於いて十分にクレームを処理するこ
とが可能になり、然も汲み取りを要しない便槽、あるい
は水洗浄化を行はない便槽として無公害のうちに、し尿
を処理することができよう。
undisassembled in conventional methods and configurations, etc.
Disadvantages such as poor drainage and the generation of bad odors due to anaerobic fermentation can be resolved satisfactorily with the method and structure described above, but it is possible to solve the problems by using a toilet tank that does not require pumping or using water for flushing. It would be possible to dispose of human waste in a non-polluting manner using a toilet tank.

また、当該方法、構成によれば多人数の***物の処理を
行うことも可能であり、製作工法も簡単になり、且つ製
作費も廉価におさまるであろう。
Further, according to the method and configuration, it is possible to treat the excreta of a large number of people, and the manufacturing method will be simple, and the manufacturing cost will be low.

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

図面はこの発明の実施例を示すもので、第1図・・・・
・・縦断組立正面図、第2図・・・・・・半分を縦断し
て示す組立側面図、第3図・・・・・・半分を断面して
示す組立平面図、第4図・・・・・・し原種の縦断正面
図、第5図・・・・・・し原種のA−A断面図、第6図
・・・・・・し原種の平面図、第7図・・・・・・し原
種のB−B断面図、第8図・・・・・・恒温槽の縦断正
面図、第9図・・・・・・恒温槽のA−A断面図、第1
0図・・・・・・分割された恒温槽下部を示す平面図、
第11図・・・・・・恒温槽に装着された撒布装置を示
す縦断正面図、第12図・・・・・・恒温槽に装着され
た撒布装置を示す部分平面とAA断面図、第13図・・
・・・・沢過程の縦断正面図、第14図・・・・・・p
過程の縦断側面図、第15図・・・・・・沢過程の通気
構造を示す平面図、第16図・・・・・・第14図A部
に於ける通気構造を示す拡大図。 1・・・・・・し原種、2・・・・・・破砕機、3・・
・・・・温風発生器、4・・・・・・電動機、5・・・
・・・掻寄せ羽根、6・・・・・・撒布盤、7・・・・
・・恒温槽上部、8・・・・・・恒温槽下部、9゜10
.11・・・・・・沢過程、12・・・・・・通気管、
13・・・・・・マット、14・・・・・・汚物収集皿
、15・・・・・・盲蓋、15’・・・・・・排気口、
16・・・・・・破砕機カバー、17・・・・・・カバ
ー、18・・・・・・便座、19・・・・・・仕切板、
20・・・・・・トラフ、21・・・・・・対流口、2
2・・・・・・越流堰、23・・・・・・樋、24・・
・・・・通気口、25,25’、25“・・・・・・接
手、26・・・・・・伝動室、27・・・・・・送風室
、28・・・・・・開口部、29・・・・・・送風口、
30・・・・・・取出し口、31,31’・・・−・・
接手、32・・・・・・駆動ギヤー33.34,35,
36,37・・・・・・減速ギヤー38.39・・・・
・・軸受、40・・・・・・撒布軸、41・・・・・・
減速ギヤー、42・・・・・・掻寄せ軸、43・・・・
・・減速ギヤー、44・・・・・・取付げ板、45・・
・・・・支柱、46・・・・・・取付は板、47・・・
・・・軸受、48・・・・・・固定板、49・・・・・
・ゴムヘラ、50・・・・・・固定板、51・・・・・
・掻き均し板、52・・・・・・均しゴム、53・・・
・・・締付ナツト、54・・・・・・撒布口。
The drawings show an embodiment of this invention, and Fig. 1...
・・Longitudinal assembly front view, Fig. 2 ・・・Assembly side view showing half in longitudinal section, FIG. 3 ・・・Assembly plan view showing half in cross section, FIG. 4 ・・・...Longitudinal front view of the original species, Fig. 5...A cross-sectional view of the original species, Fig. 6...Front view of the original species, Fig. 7... ...B-B sectional view of the original species, Fig. 8... Longitudinal front view of the thermostatic chamber, Fig. 9... A-A sectional view of the thermostatic chamber, No. 1
Figure 0: A plan view showing the lower part of the divided thermostatic chamber.
Fig. 11... A vertical sectional front view showing the spreading device attached to the thermostatic oven, Fig. 12... Partial plan view and AA sectional view showing the dispersing device attached to the thermostatic oven. Figure 13...
...Longitudinal front view of the stream process, Figure 14...p
A longitudinal side view of the process, FIG. 15... A plan view showing the ventilation structure of the stream process, FIG. 16... An enlarged view showing the ventilation structure in part A of FIG. 14. 1... original species, 2... crusher, 3...
...Hot air generator, 4...Electric motor, 5...
...Raking blade, 6...Spreading board, 7...
・・Top of thermostatic chamber, 8・・・・Bottom of thermostatic chamber, 9゜10
.. 11... Sawa process, 12... Ventilation pipe,
13...mat, 14...dirt collection tray, 15...blind lid, 15'...exhaust port,
16... Crusher cover, 17... Cover, 18... Toilet seat, 19... Partition plate,
20...Trough, 21...Convection port, 2
2... Overflow weir, 23... Gutter, 24...
...Vent, 25, 25', 25"...Joint, 26...Transmission chamber, 27...Blower chamber, 28...Opening Part, 29...Blower port,
30... Outlet port, 31, 31'...-...
Joint, 32... Drive gear 33, 34, 35,
36, 37...Reduction gear 38.39...
... Bearing, 40 ... Spreading shaft, 41 ...
Reduction gear, 42... Scraping shaft, 43...
...Reduction gear, 44...Mounting plate, 45...
...Pole, 46...Mounting is by plate, 47...
...Bearing, 48...Fixing plate, 49...
・Rubber spatula, 50...Fixing plate, 51...
- Leveling board, 52... Leveling rubber, 53...
...Tightening nut, 54...Spraying port.

Claims (1)

【特許請求の範囲】 1 し原種に破砕機を取り付け、温風発生器を内蔵させ
、恒温槽には撒布装置を設置して排気口を設け、内部に
沢過槽を内蔵し、その底部に汚物収集皿を敷設した、し
尿の可溶化r過分解槽。 2 し原種はし尿沈殿室、破砕混合室、可溶化室、温風
発生室など、仕切られた4つの区分により形成され、破
砕混合室(トラフ)に破砕機を取り付け、対流口及び越
流堰、樋を設け、温風発生室に送風機及び電気抵抗体を
内蔵した特許請求の範囲第1項記載の、し尿の可溶化濾
過分解槽。 3 恒温槽に設置された撒布装置は減速伝導機構及び槽
内に収納されている撒布機構とにより形成する特許請求
範囲第1項記載の、し尿の可溶化濾過分解槽。 4 恒温槽に内蔵される沢過槽は立方体の形状を成し、
複数の沢過槽の底面は網目管を挿通したものと、簀の千
秋に丸材を敷設して固着した2種類のものとに分別され
、網目管挿通分に関しては上下、簀の千秋に関しては上
面を各々長繊維多層マットで全面を接液して、複数の沢
過槽を積み重ねて用ふる特許請求範囲第1項記載の、し
尿の可溶化分解槽。
[Scope of Claims] 1. A crusher is attached to the raw seeds, a hot air generator is built in, a spraying device is installed in the constant temperature bath, an exhaust port is provided, a swell tank is built inside, and the bottom of the A human waste solubilization/excess decomposition tank equipped with a waste collection tray. 2 It is formed by four partitioned sections, including a human waste sedimentation chamber, a crushing mixing chamber, a solubilization chamber, and a hot air generation chamber.A crusher is attached to the crushing mixing chamber (trough), and a convection opening and an overflow weir are installed. 2. The human waste solubilization, filtration, and decomposition tank according to claim 1, wherein a gutter is provided, and a blower and an electric resistor are built in the hot air generation chamber. 3. The human waste solubilization, filtration, and decomposition tank according to claim 1, wherein the spreading device installed in the constant temperature tank is formed by a deceleration transmission mechanism and a spreading mechanism housed in the tank. 4 The overflow tank built into the thermostatic chamber has a cubic shape,
The bottoms of multiple drainage tanks are divided into two types: those with mesh pipes inserted through them, and those with round timbers laid and fixed at the bottom of the screen.The bottoms of multiple drainage tanks are divided into two types: those with mesh pipes inserted through them, and those with round timbers laid and fixed in place. 2. The human waste solubilization and decomposition tank according to claim 1, wherein a plurality of filtration tanks are stacked and used by stacking the entire surface of each of the filtration tanks in contact with the liquid with a long fiber multilayer mat.
JP56075990A 1981-05-20 1981-05-20 Human waste solubilization “filtration” overdecomposition tank Expired JPS5846356B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56075990A JPS5846356B2 (en) 1981-05-20 1981-05-20 Human waste solubilization “filtration” overdecomposition tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56075990A JPS5846356B2 (en) 1981-05-20 1981-05-20 Human waste solubilization “filtration” overdecomposition tank

Publications (2)

Publication Number Publication Date
JPS57190624A JPS57190624A (en) 1982-11-24
JPS5846356B2 true JPS5846356B2 (en) 1983-10-15

Family

ID=13592214

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56075990A Expired JPS5846356B2 (en) 1981-05-20 1981-05-20 Human waste solubilization “filtration” overdecomposition tank

Country Status (1)

Country Link
JP (1) JPS5846356B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2021169004A1 (en) * 2020-02-25 2021-09-02 吴志伦 Domestic sewage odor-eliminating environment-friendly filtering device based on microbial reaction

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59177200A (en) * 1983-03-26 1984-10-06 Taisei:Kk Diffusion tank for solubilization, decomposition, filtration and purification of night soil

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2021169004A1 (en) * 2020-02-25 2021-09-02 吴志伦 Domestic sewage odor-eliminating environment-friendly filtering device based on microbial reaction

Also Published As

Publication number Publication date
JPS57190624A (en) 1982-11-24

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