JPS6389742A - Flash toilet apparatus - Google Patents
Flash toilet apparatusInfo
- Publication number
- JPS6389742A JPS6389742A JP23383986A JP23383986A JPS6389742A JP S6389742 A JPS6389742 A JP S6389742A JP 23383986 A JP23383986 A JP 23383986A JP 23383986 A JP23383986 A JP 23383986A JP S6389742 A JPS6389742 A JP S6389742A
- Authority
- JP
- Japan
- Prior art keywords
- water
- flush toilet
- room
- heated
- low
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 115
- 239000010865 sewage Substances 0.000 description 20
- 239000002699 waste material Substances 0.000 description 20
- 238000005406 washing Methods 0.000 description 18
- 239000007789 gas Substances 0.000 description 16
- 235000019645 odor Nutrition 0.000 description 15
- 238000004140 cleaning Methods 0.000 description 13
- 238000011010 flushing procedure Methods 0.000 description 13
- 238000009423 ventilation Methods 0.000 description 11
- 238000000034 method Methods 0.000 description 10
- 239000002351 wastewater Substances 0.000 description 9
- 238000010438 heat treatment Methods 0.000 description 6
- 239000010802 sludge Substances 0.000 description 6
- 238000001816 cooling Methods 0.000 description 5
- 230000032258 transport Effects 0.000 description 5
- 230000013872 defecation Effects 0.000 description 4
- 230000007613 environmental effect Effects 0.000 description 4
- 230000006378 damage Effects 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 3
- 238000009434 installation Methods 0.000 description 3
- 244000005700 microbiome Species 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 210000002700 urine Anatomy 0.000 description 3
- 238000010790 dilution Methods 0.000 description 2
- 239000012895 dilution Substances 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000008400 supply water Substances 0.000 description 2
- 230000005068 transpiration Effects 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000003749 cleanliness Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000009931 harmful effect Effects 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 239000012212 insulator Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000009965 odorless effect Effects 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000002250 progressing effect Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 241001148471 unidentified anaerobic bacterium Species 0.000 description 1
Landscapes
- Non-Flushing Toilets (AREA)
- Sanitary Device For Flush Toilet (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Abstract] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は水洗トイレ装置に関し、特に電源があればあら
ゆるところで衛生的に水洗使用でき、しかも水資源を効
率的且つ効果的に保清することのできるトイレ装置に関
する。[Detailed Description of the Invention] (Industrial Application Field) The present invention relates to a flushing toilet device, and particularly to a flushing toilet device that can be used hygienically anywhere as long as there is a power source, and that efficiently and effectively preserves water resources. This article relates to a toilet device that allows for
(従来の技術)
トイレは衛生的に使用することができるのが望ましく、
その代表例としては、大量の洗浄水を梁床の運搬水にお
よび稀釈水として用いて下水道を通じて遠くの処理場に
運び、浄化処理した後に放流するようになっているとこ
ろの水洗トイレシステム所謂本水洗であり、他に、床法
を大量の洗浄水でもある稀釈水ともどもその場で浄化処
理して放流するようになっているところの浄化槽との組
合せによる水洗トイレ、さらには少l (500cc以
下)の洗浄水をボール面の洗浄水および臭気の封水とし
て、その梁床汚水を汲取り便槽内に溜め、適時バキュー
ムカー等で汲取りして遠くの処理場に運搬して浄化処理
した後に放流するようになっている溜め式簡易水洗トイ
レがある。(Prior art) It is desirable that toilets can be used hygienically.
A typical example is the so-called flush toilet system, in which a large amount of washing water is used as transport water for the beam floor and as dilution water, and is transported to a distant treatment plant through the sewer system, where it is purified and then released. In addition, there are flush toilets that are combined with septic tanks that purify large amounts of dilution water, which is also a large amount of washing water, before discharging it. ) was used as cleaning water for the ball surface and odor sealing water, and the sewage from the beam floor was collected and stored in a waste tank, which was then pumped up with a vacuum truck or the like at the appropriate time and transported to a distant treatment plant for purification. There is a simple flush toilet with a reservoir that drains water afterwards.
又、断る溜め式簡易水洗トイレにおける増加汚水を加熱
して蒸発させて大気中に放散するようになっている水洗
トイレ(特公昭58−26999号公報)もある。There is also a flush toilet (Japanese Patent Publication No. 58-26999) that heats and evaporates the increased sewage in a simple flush toilet that refuses to do so and releases it into the atmosphere.
そして又、洗浄化した処理水を洗浄水として循環再使用
するようになっている水洗トイレ(特公昭56−162
66号公報)や、床法と時差をおいて流出させる洗浄水
を礪構的に回収して循環再使用するようになっている水
洗トイレ(特開昭51−52643号公報)、床法と比
重が異なる否水溶性の洗浄液で洗浄と果尿の回収とを行
ない、循環使用するようになっている水洗トイレ(特公
昭51−13342号公報)がある。Also, there is a flush toilet (Special Publication Publication No. 56-162
66 Publication), a flush toilet that systematically collects and recirculates the flushing water that flows out at a time lag with the floor method (Japanese Patent Application Laid-open No. 51-52643), and the floor method. There is a flush toilet (Japanese Patent Publication No. 13342/1983) which performs cleaning and recovery of fruit and urine using water-insoluble cleaning liquids having different specific gravity and is reused.
(発明が解決しようとする問題点)
ところで、従来のような水洗トイレではあらゆるところ
で衛生的に水洗使用することは次の理由により問題があ
る。(Problems to be Solved by the Invention) By the way, with conventional flush toilets, there is a problem in using flushes everywhere hygienically for the following reasons.
本水洗は床法を遠くへ運び去るための大量の水と下水道
が必要条件であり、そのどちらかが欠けても利用できな
い。又その設備規模面からの制約があるばかりか特に処
理側では自から作り出す大量の汚水の処理に重大な問題
を抱えている。すなわち、その臭気洩れ対策はもとより
、放流水には微生物を含む活性汚泥特有の悪臭があり、
さらにBOO等の除去率を85〜95%まで高級処理し
ていても、水質保全の面から近年では第三次処理の必要
性を検討されている。このことは放流水nがあまりにも
大儀で自然の浄化能力を上回り、水質の環境破壊が地球
的規模で進行していることに起因する。Honshui requires a large amount of water and sewage to transport the bed method far away, and if either of these is lacking, it cannot be used. Moreover, not only are there restrictions in terms of the scale of the equipment, but the treatment side in particular has serious problems in treating the large amount of sewage it produces. In other words, in addition to countermeasures against odor leakage, the discharged water has the characteristic odor of activated sludge containing microorganisms.
Furthermore, even if high-grade treatment is performed to achieve a removal rate of 85 to 95% of BOO, etc., the necessity of tertiary treatment has been considered in recent years from the perspective of water quality conservation. This is due to the fact that the amount of discharged water is so large that it exceeds the purifying ability of nature, and environmental destruction of water quality is progressing on a global scale.
又、浄化槽との組合せによる水洗トイレも、床法を稀釈
するための大量の水を必要不可欠としており、給水を受
けられないところでの利用はできない。又、設備的にも
設置のための庭がある家庭用程度までで、それ以下の小
形化は無理があり、しかも、大量に作り出す放流水には
活性汚泥特有の悪臭があるばかりか、河川汚濁の大きな
原因になっている。Flush toilets combined with septic tanks also require a large amount of water to dilute the bed method, and cannot be used in places where water supply is not available. In addition, the equipment is limited to household use with a garden for installation, and it is impossible to make it smaller than that. Moreover, the discharged water produced in large quantities not only has the foul odor characteristic of activated sludge, but also causes river pollution. It is a major cause of
溜め式簡易水洗トイレにおいても、給水を受けられない
ところでの利用は不可能であり、そうかといって便器洗
浄水をバケツで汲み込むのは大変な作業である。Even with a simple flush toilet, it is impossible to use it in places where there is no water supply, and on the other hand, it is a difficult task to draw water for flushing the toilet with a bucket.
同様に、溜め式簡易水洗トイレにおける増加汚水を蒸散
処理するところの特公昭58−26999号公報に記載
されている水洗トイレでも、給水を受けられないと′こ
ろでの利用はかなわぬところであり、なによりもその蒸
発空気を大組発生させるために高温度で加熱されて一層
強烈となった臭気がそのまま大気中に放散されるため、
環境が著しく破壊され、側底実用に供し得ない致命的な
問題がある。Similarly, even the flush toilet described in Japanese Patent Publication No. 58-26999, which evaporates the increased sewage in a simple flush toilet, cannot be used in places where there is no water supply. Above all, in order to generate a large amount of evaporated air, the air is heated to high temperatures and the even more intense odor is released into the atmosphere.
There is a fatal problem in that the environment is severely destroyed and it cannot be put to practical use.
この臭気問題について、蒸発空気の排気管途中にトラッ
プを形成して臭気洩れを阻止しようとしているも、実際
にはその強烈な臭気の蒸発空気圧が一定圧力まで上昇す
る毎に同1〜ラツプを通過して大気中に放散し、実質的
に臭気問題はいつこうに解決されていない。Regarding this odor problem, attempts have been made to prevent the odor from leaking by forming a trap in the middle of the exhaust pipe of the evaporated air, but in reality, each time the evaporating air pressure of the strong odor rises to a certain pressure, the trap passes through the trap. The odor problem remains virtually unsolved.
一方、洗浄水を繰返し使用する水洗トイレでは、給水を
必要としないものの次の問題がある。On the other hand, flush toilets that use flush water repeatedly have the following problems, although they do not require a water supply.
たとえば、特公昭56−16266号公報に記載されて
いる水洗トイレでは、汚水を土壌中に毛管浸透させて、
微生物により浄化して洗浄水を得るために、設備規模が
どうしても大形となり、浄化槽以上の敷地の設置スペー
スを要求されるばかりか、その処理能力は気候条件に左
右され、なによりも今だ行政庁の認可が得られず、実施
できない現状である。For example, in the flush toilet described in Japanese Patent Publication No. 56-16266, sewage is permeated into the soil through capillary tubes.
In order to obtain washing water by purifying it with microorganisms, the scale of the equipment inevitably becomes large, and not only does it require more installation space than a septic tank, but its processing capacity is affected by climate conditions, and above all, it is still difficult to manage administratively. The current situation is that it cannot be implemented as approval from the agency has not been obtained.
又、特開昭51−52643号公報および特公昭51−
13342号公報に記載されている水洗トイレでは、そ
の洗浄水が洗浄回数に比例して次第に汚れ、その臭気を
ともなう汚れを我慢して使用するか、或いは早くに汚物
とともに洗浄水を廃棄しなければならず、衛生的な使用
を望み難い問題がある。しかも、戻尿槽の大きさおよび
汲取り回数は従来とかわらず、又、処理側においてはそ
の絶対量がかわらない集尿を大口の水で稀釈して浄化す
ることによるところの種々の問題、すなわち臭気対策、
大口の放流水がもたらす活性汚泥特有の悪臭および水質
による環境の破壊の問題がある。Also, JP-A-51-52643 and JP-A-51-52643
In the flushing toilet described in Publication No. 13342, the flushing water gradually becomes dirty in proportion to the number of flushes, and the toilet must either endure the smelly dirt or dispose of the flushing water along with the filth as soon as possible. However, there is a problem in that it is difficult to use it hygienically. Moreover, the size of the return urine tank and the number of times it is pumped out remain the same as before, and on the processing side, there are various problems caused by diluting and purifying the collected urine, the absolute amount of which does not change, with a large mouth of water. In other words, odor control,
There are problems with environmental destruction due to the odor peculiar to activated sludge and water quality caused by large volumes of discharged water.
斯様にいずれの水洗トイレにおいても、あらゆるところ
での衛生的な水洗使用および水資源効率的且つ効果的な
保清をできないでいるが、床法処理行政の方向として国
民総水洗化の目標があり、そのため処理側にまで好結果
をもたらす有効な水洗トイレ装置の出現を持たれている
。In this way, all types of flush toilets do not allow for hygienic flushing and efficient and effective cleaning of water resources in all places, but the goal of universal flushing is the direction of the floor law treatment administration. This has led to the emergence of effective flush toilet devices that bring good results to the treatment side.
本発明は斯る要望に鑑みてなされたもので、電源を確保
できるところでありさえすれば、衛生的に水洗使用でき
、しかも処理側における絶対処理量を少なくして水資源
を効率的且つ効果的に保清することのできる水洗トイレ
装置を提供することを目的とする。The present invention has been made in view of such demands, and can be used hygienically for washing with water as long as a power supply is available, and moreover, it reduces the absolute amount of treatment on the treatment side, making water resources efficient and effective. The purpose of the present invention is to provide a flush toilet device that can maintain cleanliness.
(問題点を解決するための手段)
本発明が叙上の目的を達成するために講じた手段は、水
洗便器と加温汚物室を連通せしめ、この加温汚物室と低
温液化室を加温汚物室から低温液化室に至る通気往路お
よび低温液化室より加温汚物室に至る通気復路からなる
気体の循環系路で連通せしめ、且つ低温液化室における
衛生水貯水部と水洗便器を給水系路で直接又は洗浄水タ
ンクを経て連通したことを特徴とする。(Means for Solving the Problems) The means taken by the present invention to achieve the above-mentioned objects is to connect the flush toilet bowl and the heated filth chamber, and to heat the heated filth chamber and the low-temperature liquefaction chamber. A gas circulation system path consisting of an outgoing ventilation path from the waste room to the low temperature liquefaction room and a return path from the low temperature liquefaction room to the heated waste room is connected to the sanitary water storage section in the low temperature liquefaction room and the flush toilet via a water supply system path. It is characterized by being connected directly or through a wash water tank.
さらに詳しくは、汚水中より水分のみを循環によるとこ
ろの蒸散→凝縮により集めて純水に近い成分の衛生水を
得、この衛生水を洗浄水として環流して繰返し再使用す
るものであって、原汚水の濃度性状の如何に拘らず、高
級処理以上の衛生水を(q、且つ汚水中の水分を搬送循
環する気体通路を完全に密閉して従来の蒸散処理のよう
に大気中に臭気を出さずに処理する。More specifically, only water is collected from wastewater through transpiration and condensation through circulation to obtain sanitary water with components close to pure water, and this sanitary water is recycled as cleaning water and reused repeatedly. Regardless of the concentration characteristics of the raw sewage, it is possible to produce sanitary water that is higher than high-grade treatment (q), and to completely seal the gas passage that transports and circulates the water in the sewage, eliminating odors from the atmosphere unlike conventional transpiration treatment. Process it without releasing it.
又、加温室の温度を必要に応じて変え、たとえば車輌、
航空機等のように加温エネルギーの消費量よりも水洗処
理能力を優先的に求められる場合には、高エネルギーを
用いて加温室と液化室の温度差を大きくして洗浄水とし
ての衛生水を多く得られるようにし、家庭規模の使用形
態にあっては低いエネルギー消費で適当な温度差を作る
ことにより使用人数に合せた適量の洗浄水が得られ、そ
して加温室の温度を年間を通じ嫌気性微生物の生育条件
に適するようにしてやることにより、床法中の全ての固
型右曙物を水とガス体とに分解し、殆ど汚泥を残さない
までにすることが可能である。In addition, the temperature of the heating room can be changed as necessary, for example, for vehicles,
In cases such as aircraft, where washing capacity is prioritized over heating energy consumption, high energy is used to increase the temperature difference between the heating chamber and the liquefaction chamber, and sanitary water is used as washing water. For household use, by creating an appropriate temperature difference with low energy consumption, the appropriate amount of washing water can be obtained according to the number of users, and the temperature of the heating room can be maintained at an anaerobic level throughout the year. By optimizing the growth conditions for microorganisms, it is possible to decompose all the solid waste in the bed method into water and gas, leaving almost no sludge.
(作 用)
気体が循環系路を経て加温汚物室と低温液化室との間を
巡回し、その加温汚物室では汚水から蒸発した水分を含
んで通気往路より低温液化室に入り、同空内にてその水
分が凝縮されて液化回収されて乾燥空気となった後、通
気復路から加温汚物室に入り、以下これを繰返して加温
汚物室側の汚水中から低温液化室側に衛生水を浄化回収
し、この低温液化室からは衛生水が洗浄水として給水系
路を経て水洗便器、そして加温汚物室に環流する。(Function) The gas circulates between the heated sewage chamber and the low-temperature liquefaction chamber via the circulation system path, and in the heated sewage chamber, it enters the low-temperature liquefaction chamber from the ventilation path, containing the water that has evaporated from the wastewater, and enters the same. After the moisture is condensed in the air and liquefied and recovered to become dry air, it enters the heated waste room through the ventilation return path, and this process is repeated from the heated waste room side to the low-temperature liquefaction room side. The sanitary water is purified and recovered, and from the low-temperature liquefaction chamber, the sanitary water is circulated as washing water through the water supply line to the flush toilet bowl and then to the heated filth chamber.
それにより、巡回する気体により汚水中から衛生水であ
る洗浄水を生成回収して継続して水洗使用し得、又、そ
の余剰衛生水は放流等し、そして汲取り処理される加温
汚物室内の汚泥量は年単位で汲取れば良いまで減h1シ
得る。As a result, cleaning water, which is sanitary water, can be generated and recovered from waste water using the circulating gas and used for continuous washing, and the surplus sanitary water is discharged, etc., and then pumped out and treated in the heated waste room. The amount of sludge can be reduced by one hour to the point where it only needs to be pumped out on a yearly basis.
(実論例)
以下図面を参照して本発明の実施の一例を詳細に説明す
る。(Practical example) An example of the implementation of the present invention will be described in detail below with reference to the drawings.
第1図は本発明水洗トイレ装置の概略を示すものである
。FIG. 1 schematically shows the flush toilet device of the present invention.
水洗トイレ装置(A>は水洗便器(1)、加温汚物室(
2)、低温液化室(3)、循環系路(4)、給水系路(
5)から構成されている。Flush toilet device (A> is a flush toilet (1), a heated waste room (
2), low temperature liquefaction chamber (3), circulation system path (4), water supply system path (
5).
水洗便器(1)は200cc〜124程度の洗浄水mを
要する各種構成のものであり、吐水口(6)には給水系
路(5)が直接又は洗浄水タンク(7)を経て連通し、
そして排便管〈8)を経て加温汚物室(2)と連通して
いて、床入および洗浄水が排便管(8)を通って加温汚
物室(2)に流入するにようにしている。The flushing toilet (1) has various configurations that require about 200 cc to 124 m of flushing water, and the water outlet (6) is connected to the water supply line (5) directly or through the flushing water tank (7).
It communicates with the heated filth room (2) through the defecation pipe (8), so that water for bed filling and washing flows into the heated filth room (2) through the defecation pipe (8). .
加温汚物室(2)は望ましくは汚水の蒸発面積が大きい
扁平状の槽(9〉により形成し、そして室内は感温セン
サー等で自動制罪された面発熱ヒーター等の低エネルギ
ーで加温する発熱体(10)によって常時およそ40℃
±5〜10℃に保温されるようにしており、嫌気状態の
室内で中温細菌が活発に生息して、同細菌による汚物の
分解が促進し、特にレルローズ系の液化そしてガス化が
スムーズに行なわれるようにしである。又、室内におけ
る汚水レベルは水位センサー等により監視して循環系路
(4)のポンプ(11)を制御し一定レベルに整える。The heated waste room (2) is preferably formed by a flat tank (9) with a large evaporation area of wastewater, and the room is heated with low energy such as a surface heating heater automatically controlled by a temperature sensor etc. The heating element (10) keeps the temperature around 40°C.
The temperature is kept at ±5 to 10 degrees Celsius, and mesophilic bacteria actively live in the anaerobic room, which promotes the decomposition of waste materials and facilitates the smooth liquefaction and gasification of relrose-based substances. It is designed so that it can be used. In addition, the level of sewage in the room is monitored by a water level sensor, etc., and the pump (11) of the circulation system path (4) is controlled to keep it at a constant level.
低温液化室(3)は槽(12〉内の同室温度が加温汚物
室(2)との間に望ましくは20℃程度の差を有するよ
うにし、且つ必要とする液化能力に応じて地中温度を利
用したり或いは半導体による冷却システム、汎用の冷却
システム等の冷却要素(13)を任意に備え、この低温
液化室(3)は循環系路(4)を巡回する気体中から衛
生水分を液化除去して槽(12)内に貯溜して回収する
。又、低温液化室(3)はオーバーフロー(14)を備
えていて、浄化回収した余剰衛生水を適当に槽外に放流
或いは蒸散するようにしている。The temperature of the low-temperature liquefaction chamber (3) in the tank (12) should preferably be about 20°C different from that of the heated sewage chamber (2), and it should be installed underground according to the required liquefaction capacity. This low-temperature liquefaction chamber (3) is optionally equipped with a cooling element (13) such as a cooling system using temperature, a semiconductor cooling system, or a general-purpose cooling system, and removes sanitary moisture from the gas circulating in the circulation path (4). It is liquefied and removed, stored in a tank (12), and recovered.The low-temperature liquefaction chamber (3) is equipped with an overflow (14), and the purified and recovered surplus sanitary water is appropriately discharged to the outside of the tank or evaporated. That's what I do.
循環系路(4)は加温汚物室(2)から低温液化室(3
)に至る通気往路(15)と、低温液化室(3)より加
温汚物室(2)に至る通気復路(16)からなり、糸路
(4)途中のポンプ(11)により気体を加温汚物室(
2)から通気往路〈15)そして低温液化室(3)さら
に通気復路(16)を経て加温汚物室(2)へと強制巡
回せしめて、ポンプ(11)を用いない自然対流よりも
さらに一層効率的な回収処理が行なわれるようにし、且
つ気体が外気との交流なく酸素の極めて少ないまま巡回
するようにして、加温汚物室(2)内の嫌気状態を損な
わず、嫌気菌による床法汚水の嫌気分解が活発に行なわ
れるようにしている。尚、ポンプ(11)を設置しない
場合でも、加温汚物室(2)と低温液化室(3)との間
の温度差により、気体が自然対流して、衛生水の回収処
理が行なわれる。The circulation system path (4) runs from the heated waste room (2) to the low temperature liquefaction room (3).
), and a ventilation return path (16) that leads from the low-temperature liquefaction chamber (3) to the heated waste chamber (2), and the gas is heated by a pump (11) in the middle of the yarn path (4). Filth room (
2) through the ventilation outgoing path (15), the low-temperature liquefaction chamber (3), and the ventilation return path (16) to the heated waste room (2), which is even more effective than natural convection without using the pump (11). In order to ensure efficient collection processing, and to allow the gas to circulate with extremely low oxygen content without any interaction with the outside air, the anaerobic state within the heated waste room (2) is not impaired, and the bed method using anaerobic bacteria is used. Anaerobic decomposition of wastewater is actively carried out. Note that even if the pump (11) is not installed, the temperature difference between the heated filth chamber (2) and the low-temperature liquefaction chamber (3) causes natural convection of gas, and the sanitary water recovery process is performed.
給水系路(5)は水洗便器(1)の吐水口(6)と低温
液化室(3)における衛生水貯水部(3a)との間を直
接又は洗浄水タンク(7)を経て連通していて、光路途
中のポンプ〈17)で低温液化室(3)内の衛生水を水
洗便器(1)にその洗浄水として給水しうるようにして
いる。The water supply line (5) communicates between the water outlet (6) of the flush toilet (1) and the sanitary water storage section (3a) in the low temperature liquefaction room (3) either directly or via the flush water tank (7). The sanitary water in the low-temperature liquefaction chamber (3) can be supplied to the flush toilet bowl (1) as flush water using a pump (17) in the middle of the optical path.
又、加温汚物室(2)には必要に応じて送気系路(18
)を備える。この送気系路(18)は汚水中に達してい
て、気体を汚水中に吹き込み、その送気圧により床法汚
水を撹拌混合して嫌気分解および蒸発の妨げとなるスカ
ムが汚水表面に堆積しないようにしていると共に全有機
物が約3ケ月で分解ガス化されるようにしている。In addition, an air supply line (18
). This air supply line (18) reaches into the wastewater, and the gas is blown into the wastewater, and the air supply pressure stirs and mixes the bed method wastewater to prevent scum from accumulating on the surface of the wastewater, which would impede anaerobic decomposition and evaporation. At the same time, all organic matter is decomposed and gasified in about three months.
尚、加温汚物室(2)の槽(9)が家庭用程度である場
合には塩分濃度があまり高くならないうちに3年毎ぐら
いのサイクルで汚泥を取出し口(19)から抜くのが良
いようである。If the tank (9) in the heated sewage room (2) is for household use, it is best to remove the sludge from the outlet (19) every three years or so before the salt concentration becomes too high. It seems so.
又、加温汚物室(2)および低温液化室(3)は夫々保
温のため断熱体(20)でカバーするのが望ましく、気
候条件等にも左右されず定量回収処理しつるようにして
いる。In addition, it is desirable to cover the heated waste room (2) and the low-temperature liquefaction room (3) with a heat insulator (20) to keep them warm, so that they can be collected and processed in a fixed amount regardless of climate conditions. .
そして、給水系路(5)を経て水洗便器(1)に給水す
る衛生水の水質は次表の通りである。The quality of the sanitary water supplied to the flush toilet (1) via the water supply line (5) is as shown in the following table.
■、放流水基準く鎌0市) 次に用途別に実施例を掲げて説明する。■, Effluent water standards (Kama 0 City) Next, examples will be described for each application.
第2図は家庭用を例示している。Figure 2 shows an example for home use.
水洗トイレ装置(A)は低温液化室(3)における気体
の通気路(21)を螺旋状に形設すると共にこの通気路
(21)に同室(3)内の衛生水をポンプ(17)で汲
み上げてシャワー(22)から浴びせて、その凝結液化
能力をアップしている。The flush toilet device (A) has a spiral gas ventilation path (21) in the low-temperature liquefaction chamber (3), and pumps (17) pumps sanitary water in the same room (3) into the ventilation path (21). The water is pumped up and showered in the shower (22) to increase its ability to congeal and liquefy.
これにより、水洗便器(1)から排便管(8)を通して
加温汚物室(2)に流入した置床および洗浄水は、同加
温汚物室(2)内で嫌気分解され、その汚水面から蒸発
させられた蒸発気体は循環系路(4)を巡回している気
体に吸収されて低温液化室(3)に送り込まれ、同室(
3)内で蒸発水分を凝縮液化されて通気路(21)内か
ら通水口(23)を通って回収される。As a result, the bed and washing water that flowed from the flush toilet (1) through the defecation pipe (8) into the heated waste room (2) are anaerobically decomposed in the heated waste room (2) and evaporated from the sewage surface. The evaporated gas is absorbed by the gas circulating in the circulation system path (4) and sent to the low temperature liquefaction chamber (3).
3), the evaporated water is condensed and liquefied and recovered from the air passage (21) through the water inlet (23).
そして、その衛生水はポンプ(17)で洗浄水タンク(
7)に送り込まれ、同タンク(7)から洗浄水として水
洗便器(1)に流出して、ボール面を洗浄した後に加温
汚物室(2)に環流する。Then, the sanitary water is pumped (17) into the cleaning water tank (
7), flows out from the same tank (7) as flush water into the flush toilet bowl (1), and after cleaning the ball surface, flows back into the heated filth chamber (2).
したがって、洗浄水の供給系と、梁床の除去のだめの運
搬或いは水運手段と、浄化のための処理施設を必要とし
ないで、下水道が整備されていない地域での一般家庭用
として、水洗使用できてしかも洗浄水の回収処理および
洗浄水自体による臭気の弊害なく快適に利用することが
できる。特に、水洗便器(1)を洗浄水量が500cc
程度以下で済む簡易タイプとすることにより、発熱体(
10)および冷却要素(13)をその消費エネルギーの
低いものとすることができ、経済的にも有利に継続使用
できる。Therefore, it can be used for general household use in areas without sewage systems, without requiring a washing water supply system, a transport or water transportation means for removing the beam floor, and a treatment facility for purification. In addition, the cleaning water can be collected and used comfortably without the problem of odor caused by the cleaning water itself. In particular, the amount of water used to flush the flush toilet (1) is 500cc.
By making it a simple type that requires less than a heating element (
10) and the cooling element (13) can have low energy consumption, and can be used economically advantageously.
第3図はクローズドシステム化した水洗トイレ装置を例
示している。FIG. 3 illustrates a closed system flush toilet device.
この水洗トイレ装置(A)は水洗便器(1)。This flush toilet device (A) is a flush toilet bowl (1).
加温汚物室(2)、低温液化室(3)、循環系路(4)
、給水系路(5)をユニット化しており、そして給水系
路(5)途中に電磁弁(24)を配設して、吐水口(6
)への給水を制御しうるようにしている。又、水洗便器
(1)は洗浄水量が500CC程度以下の簡易水洗タイ
プにしている。Heated waste room (2), low temperature liquefaction room (3), circulation system path (4)
, the water supply system path (5) is made into a unit, and a solenoid valve (24) is arranged in the middle of the water supply system path (5) to open the water outlet (6).
) to control water supply. Further, the flush toilet bowl (1) is of a simple flush type with a flushing water volume of about 500 cc or less.
これにより、置床および洗浄水は水洗便器(1)から排
便管(8)を通して加温汚物室(2)に流入し、同加温
汚物室(2)内の汚水面から蒸発させられた蒸発気体は
循環系路(4)を巡回している気体に吸収されて低温液
化室(3)に送り込まれ、同v(3)内で蒸発水分を凝
縮液化されて通気路(21)内から通水口(23)を通
って回収される。そして、その衛生水は指示により開い
た電磁弁(24)を通過して吐水口(6)からボール面
に流出し、ボール面を洗浄した後に加温汚物室(2)に
環流される。As a result, the bed and washing water flow from the flush toilet (1) through the defecation pipe (8) into the heated filth chamber (2), and the evaporated gas evaporated from the sewage surface in the heated filth chamber (2). is absorbed by the gas circulating in the circulation system path (4) and sent to the low-temperature liquefaction chamber (3), where the evaporated water is condensed and liquefied, and then passed from the ventilation path (21) to the water inlet. (23) and is collected. Then, the sanitary water passes through the solenoid valve (24) which is opened according to an instruction, flows out from the spout (6) onto the ball surface, cleans the ball surface, and then flows back into the heated waste chamber (2).
したがって、洗浄水の供給系と、置床の除去のための運
搬或いは水運手段と、浄化のための処理tIIA設を必
要とせず、しかも、−回当りの洗浄水量が少なくてすむ
のにともない、設定利用人数が同じであれば、加温汚物
室(2)および低温液化室(3)を小容積にして装置全
体の小形化を促進できて、一般家庭にはもとより、船舶
、航空機、鉄道、バス等の各種輸送機関そして移動トイ
レさらには屋内用の簡易トイレ等に、・その自己給水お
よび回収処理能力を有するクローズドトイレとして、水
洗使用できて、しかも洗浄水の回収処理および洗浄水自
体による臭気の弊害なく快適且つ広範囲に利用すること
ができる。Therefore, there is no need for a washing water supply system, transportation or water transportation means for removing the bed, and treatment equipment for purification, and the amount of washing water per wash can be reduced, making the setting easier. If the number of users is the same, the volume of the heated waste room (2) and low-temperature liquefaction room (3) can be reduced to promote the downsizing of the entire device, which can be used not only for general households but also for ships, aircraft, trains, and buses. It can be used as a closed toilet with its own water supply and collection processing capabilities, and can be used for various transportation vehicles such as mobile toilets, as well as indoor portable toilets. It can be used comfortably and widely without any harmful effects.
又、図示はしていないが、低温液化室(3)をたとえば
水洗便器(1)上縁面の後部に据付けられているタンク
(7)内に形成する態様もあり、特に水洗便器(1)が
−回当り500CC程度以下の洗浄水量ですむ簡易水洗
タイプである場合、装置全体を一層小形化することが可
能である。Although not shown, there is also a mode in which the low-temperature liquefaction chamber (3) is formed, for example, in a tank (7) installed at the rear of the upper edge of the flush toilet (1). If the cleaning device is of a simple washing type that requires less than about 500 cc of washing water per wash, it is possible to further downsize the entire device.
断る簡易水洗タイプの水洗便器(1)にお(ブる吐水口
(7)としては出願人が開発した実公昭59−3855
2号の吐水ノズルがふされしく、また便器(25)とし
ては同じく実公昭56−9749号のものが有効である
。For the simple flush type flush toilet (1) (the flush spout (7) was developed by the applicant in 1987-3855).
The water discharge nozzle No. 2 is appropriate, and the toilet bowl (25) of Utility Model Publication No. 56-9749 is also effective.
(発明の効果) したがって本発明によれば次の利点がある。(Effect of the invention) Therefore, the present invention has the following advantages.
■ 加温汚物室と低温液化室との間を循環系路に沿い循
環する気体により加温汚物室内の蒸発水分を低温液化室
に運び、同水分を低温液化室にて凝縮液化して、放流水
基準以下の超高級処理値に臭気を全く出さず処理回収し
、そして、そのほぼ無臭透明な衛生水を洗浄水として水
洗便器に給水し、電源さえあれば外部からの給水を受け
ずに、継続して水洗使用することができる。■ Gas circulating along the circulation path between the heated sewage chamber and the low-temperature liquefaction chamber transports the evaporated moisture in the heated sewage chamber to the low-temperature liquefaction chamber, where the moisture is condensed and liquefied before being discharged. We process and recover ultra-high-grade treatment values that are below water standards without emitting any odor, and then supply the almost odorless and transparent sanitary water to the flush toilet as flush water, without receiving water supply from outside as long as there is a power source. Can be used continuously by washing with water.
■ 臭気および洗浄水水質とともに問題がなく、しかも
機械設計による数量設計に基づいて定m回収して給水で
き、そして、システム規模においても大形のものから小
形のものまで自由性に優れているので、一般家庭、各種
輸送礪関、移動トイレ、屋内用簡易トイレ等に、寒冷地
、高温地、水が也めて貴重な砂漠地域であっても、その
設置を要望されるほぼあらゆる用途に、環境破壊の心配
なく利用することができる。■ There are no problems with odor or cleaning water quality, and it is possible to collect and supply water at a fixed meter based on the mechanical design and quantity design, and it has excellent flexibility in terms of system scale, from large to small. , general households, various transportation stations, mobile toilets, indoor portable toilets, etc., even in cold regions, high temperature regions, desert regions where water is precious, and almost any application that requires installation. It can be used without worrying about environmental damage.
■ 特に一般家庭、輸送礪関等の置床の発生源において
、従来のような置床の衛生的処理のだめに汚水を大量に
作り出すことなく、その処理および給水まで自己処理す
ることができ、クローズドシステムとして有用であり、
且つ下水道施設の負担を著しく軽減すると共に水質保全
等の環境面にも好ましい。■ Particularly at the source of floor storage such as general households and transportation stations, it is possible to self-treat and supply water without creating a large amount of sewage due to the conventional hygienic treatment of the floor, and it can be used as a closed system. useful and
In addition, it significantly reduces the burden on sewage facilities, and is also favorable from an environmental standpoint such as water quality conservation.
第1図は本発明水洗トイレ装置の基本構成の概略を示す
断面図。第2図および第3図は夫々他の実施例の概略を
示す断面図である。
図中
(1)は水洗便器
(2)は加温汚物室 (3)は低温液化室(3a)は
衛生水貯水部 (4)は循環系路(5)は給水系路
(7)は洗浄水タンク (15)は通気往路(16)は
通気復路FIG. 1 is a sectional view schematically showing the basic configuration of the flush toilet device of the present invention. FIGS. 2 and 3 are cross-sectional views schematically showing other embodiments. In the figure, (1) is the flush toilet (2) is the heated waste room (3) is the low temperature liquefaction room (3a) is the sanitary water storage area (4) is the circulation system path (5) is the water supply system path (7) is the cleaning area The water tank (15) is the ventilation outgoing path (16) is the ventilation return path.
Claims (1)
低温液化室を加温汚物室から低温液化室に至る通気往路
および低温液化室より加温汚物室に至る通気復路からな
る気体の循環系路で連通せしめ、且つ低温液化室におけ
る衛生水貯水部と水洗便器を給水系路で直接又は洗浄水
タンクを経て連通したことを特徴とする水洗トイレ装置
。The flush toilet bowl and the heated filth room are connected, and the heated filth room and the low-temperature liquefaction room are connected to each other. 1. A flush toilet device, characterized in that the sanitary water storage section in the low-temperature liquefaction chamber and the flush toilet are connected through a circulation system path, and the sanitary water storage section in the low temperature liquefaction chamber and the flush toilet bowl are connected through the water supply system path either directly or through a flush water tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23383986A JPS6389742A (en) | 1986-09-30 | 1986-09-30 | Flash toilet apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23383986A JPS6389742A (en) | 1986-09-30 | 1986-09-30 | Flash toilet apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6389742A true JPS6389742A (en) | 1988-04-20 |
Family
ID=16961371
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP23383986A Pending JPS6389742A (en) | 1986-09-30 | 1986-09-30 | Flash toilet apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6389742A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04222684A (en) * | 1990-12-21 | 1992-08-12 | Japanic:Kk | Human refuse disposal device |
JP2010222869A (en) * | 2009-03-24 | 2010-10-07 | Masayuki Nakaya | Temporary toilet |
JP2012017624A (en) * | 2010-07-09 | 2012-01-26 | Toyohiko Sawada | Temporary toilet |
-
1986
- 1986-09-30 JP JP23383986A patent/JPS6389742A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04222684A (en) * | 1990-12-21 | 1992-08-12 | Japanic:Kk | Human refuse disposal device |
JP2010222869A (en) * | 2009-03-24 | 2010-10-07 | Masayuki Nakaya | Temporary toilet |
JP2012017624A (en) * | 2010-07-09 | 2012-01-26 | Toyohiko Sawada | Temporary toilet |
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