Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JP5305526B2 - Domestic wastewater treatment system - Google Patents
[go: Go Back, main page]

JP5305526B2 - Domestic wastewater treatment system - Google Patents

Domestic wastewater treatment system Download PDF

Info

Publication number
JP5305526B2
JP5305526B2 JP2009237954A JP2009237954A JP5305526B2 JP 5305526 B2 JP5305526 B2 JP 5305526B2 JP 2009237954 A JP2009237954 A JP 2009237954A JP 2009237954 A JP2009237954 A JP 2009237954A JP 5305526 B2 JP5305526 B2 JP 5305526B2
Authority
JP
Japan
Prior art keywords
wastewater
tank
water
evaporation
incineration
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 - Fee Related
Application number
JP2009237954A
Other languages
Japanese (ja)
Other versions
JP2011083691A (en
Inventor
仁司 藤原
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP2009237954A priority Critical patent/JP5305526B2/en
Publication of JP2011083691A publication Critical patent/JP2011083691A/en
Application granted granted Critical
Publication of JP5305526B2 publication Critical patent/JP5305526B2/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Domestic Plumbing Installations (AREA)
  • Processing Of Solid Wastes (AREA)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a domestic wastewater treatment system contributing to the conservation of resources and the suppression of a discharge amount of carbon dioxide in a form easy to use by a user. <P>SOLUTION: The domestic wastewater treatment system is provided with a disposer 15 for crushing leftover food to allow the crushed one to flow to a wastewater route, a wastewater stock yard 1 for once storing the wastewater from the wastewater route, an evaporation tank 2 for taking the wastewater out of the wastewater stock yard to separate the same into steam and solid matter under a reduced pressure environment, condensed water storage tanks 4A and 4B for liquefying the steam from the evaporation tank to store condensed water, and a tap water route for taking water out of the condensed water storage tanks to supply the same as tap water. When the wastewater of the wastewater stock yard reaches a predetermined amount or becomes a preset time zone, the wastewater is moved to the evaporation tank and forcible evaporation by a heater is performed in the preset time zone in the evaporation tank in addition to natural evaporation under a reduced pressure. <P>COPYRIGHT: (C)2011,JPO&amp;INPIT

Description

この発明は、住宅において台所、風呂、洗面から生じる雑廃水やトイレから生じる汚水を浄化して、再利用するための生活廃水処理システムに関する。   TECHNICAL FIELD The present invention relates to a domestic wastewater treatment system for purifying and reusing miscellaneous wastewater generated from a kitchen, bath, and wash surface and wastewater generated from a toilet in a house.

住宅から出る生活廃水の発生量は、1人1日当たり約200リットルといわれており、世帯別にすると大量の生活廃水が発生することになる。   It is said that the amount of domestic wastewater generated from houses is about 200 liters per person per day, and a large amount of domestic wastewater is generated by household.

これらの生活廃水は都市部ではそのまま下水道に流し、下水処理施設ではそれを浄化して河川、湖沼または海へ放流していた。また、下水道が完備していない地域では浄化槽で処理した後、河川などに放流したり、地中に浸透させていた。   These domestic wastewaters flowed directly into the sewers in urban areas, and the sewage treatment facilities purified them and released them into rivers, lakes, and the sea. Also, in areas where sewerage is not complete, after treatment in septic tanks, they were discharged into rivers and permeated into the ground.

一方、台所で生じる残飯は通常は生ゴミとして収集場所に廃棄し、それを公的な回収事業者が回収し焼却場で焼却するか、流し台に設けたディスポーザで破砕して雑廃水と共に下水道に流していた。   On the other hand, the leftovers generated in the kitchen are usually disposed of in the collection place as raw garbage, which is collected by a public collection company and incinerated at the incineration site, or crushed with a disposer installed in the sink and put into the sewer together with the waste water. It was flowing.

また、エコロジーの観点から生ゴミをコンポスト化する試みもなされている(例えば、特許文献1)。   In addition, attempts have been made to compost garbage from the viewpoint of ecology (for example, Patent Document 1).

特開2003−104785号公報JP 2003-104785 A

前記の通り、住宅から出る生活廃水の発生量は、1人1日当たり約200リットルといわれているが、これを言い換えれば1人1日当たり200リットルの上水を消費しているということであり、これは限りある水資源の保護の観点から考慮しなければならない問題であった。   As mentioned above, it is said that the amount of domestic wastewater generated from houses is about 200 liters per person per day. In other words, 200 liters of water is consumed per person per day. This was a problem that had to be considered from the perspective of protecting limited water resources.

一方、収集場所に廃棄された生ゴミは焼却場まで搬送されなればならず、そのための車両の走行により化石燃料が消費され、また、焼却処理するに際しても化石燃料が消費され、省資源および二酸化炭素排出による地球温暖化防止の観点から解決が望まれた。   On the other hand, the garbage discarded at the collection site must be transported to the incineration site, and the fossil fuel is consumed by the traveling of the vehicle for that purpose. A solution was desired from the viewpoint of preventing global warming due to carbon emissions.

この場合、生ゴミを廃棄しないでディスポーザで破砕して雑廃水と共に下水道に流す場合は、結局、下水処理施設で処理をしなくてはならない問題を生じた。   In this case, if the garbage is crushed with a disposer without being disposed of and then sent to the sewer along with miscellaneous wastewater, there is a problem that the wastewater treatment facility must be treated.

一方、生ゴミをコンポスト化することはエコロジーの観点から好ましく、地球環境にも優しいが一般家庭で日常的に実践するには手間などの負担が増大し、実施が敬遠されやすい問題があった。   On the other hand, composting garbage is preferable from the viewpoint of ecology, and it is friendly to the global environment, but there is a problem that it is difficult to carry out daily practice in ordinary households because it increases the burden of labor.

この発明は以上の従来技術の問題点を解消した生活廃水処理システムを提供することを目的として創作されたものであり、住宅より生じる生活廃水を浄化、再処理するシステムにおいて、残飯を破砕して廃水経路に流すディスポーザ、廃水経路からの廃水を一旦貯水する廃水ストックヤード、廃水ストックヤードから廃水を取り出して減圧環境下で水蒸気と固体物に分離する蒸発槽、蒸発槽からの水蒸気を液化して貯水する復水貯水槽、復水貯水槽から水を取り出して上水として供給する上水経路を設け、廃水ストックヤードの廃水が所定量に達するか、または予め設定した時間帯になると廃水を蒸発槽に移動し、蒸発槽では減圧による自然蒸発に加えて予め設定した時間帯に加熱装置による強制蒸発を行うことを特徴とする。   This invention was created for the purpose of providing a domestic wastewater treatment system that has solved the above-mentioned problems of the prior art. In a system for purifying and reprocessing domestic wastewater generated from a house, the remaining rice is crushed. Disposer that flows into the wastewater route, wastewater stockyard that temporarily stores wastewater from the wastewater route, an evaporation tank that takes out the wastewater from the wastewater stockyard and separates it into water vapor and solid matter in a reduced pressure environment, and liquefies the water vapor from the evaporation tank A condensate storage tank that stores water and a water supply channel that takes out water from the condensate storage tank and supplies it as clean water is provided, and the waste water evaporates when the waste water in the waste water stock yard reaches a predetermined amount or reaches a preset time zone. In the evaporation tank, in addition to natural evaporation due to reduced pressure, forced evaporation by a heating device is performed in a preset time zone.

また、ここでは第2発明として前記の生活廃水処理システムにおいて、夜間の就寝時間帯に廃水の蒸発槽への移動を開始し、さらに予め電力契約で決定された深夜の低額時間帯に加熱装置による強制蒸発を行う生活廃水処理システムも開示する。   Further, here, as the second invention, in the above-mentioned domestic wastewater treatment system, the movement of the wastewater to the evaporating tank is started during the nighttime bedtime, and further, the heating device is used in the low-cost time zone of midnight determined in advance by the power contract. A domestic wastewater treatment system that performs forced evaporation is also disclosed.

また、ここでは第3発明として前記の生活廃水処理システムにおいて、トイレからの汚水を廃水ストックヤードとは別系統の蒸発焼却槽に貯留し、上記の蒸発焼却槽で減圧環境下で水蒸気と固体分に分離し、蒸気は液化して廃貯水槽に貯留した後に廃水するとともに、固形分は蒸発焼却槽で焼却する生活廃水処理システムも開示する。   Further, here, as the third invention, in the above-mentioned domestic wastewater treatment system, the sewage from the toilet is stored in a separate evaporative incineration tank from the wastewater stockyard, and in the evaporative incineration tank described above, water vapor and solids are contained in a reduced pressure environment. Also disclosed is a domestic wastewater treatment system in which steam is liquefied and stored in a waste water tank and then waste water, and solids are incinerated in an evaporative incinerator.

また、ここでは第4発明として前記の第3発明の生活廃水処理システムにおいて、蒸発焼却槽を並列に2つ設け、水蒸気と固体分への分離および固形分の焼却作業と汚水の貯留作業を時間ごとに交代に振り分けて行う生活廃水処理システムも開示する。   Further, here, as the fourth invention, in the domestic wastewater treatment system according to the third invention, two evaporative incineration tanks are provided in parallel, and separation into water vapor and solids, incineration of solids and storage of sewage are timed. Also disclosed is a domestic wastewater treatment system that is assigned to each turn.

この発明の生活廃水処理システムの第1発明および第2発明は次の作用・効果を生じる。
(1) 生活廃水は水分の沸点が降下する減圧環境下での自然蒸発および加熱装置による強制蒸発により水蒸気と固体物に分離され、水蒸気は液化して上水として再使用されるので、新たに補給する上水は最小限で済み、省資源に寄与する。
(2) 残飯はディスポーザにより破砕され生活廃水とともに廃水経路に流されるが、減圧環境下での自然蒸発および加熱装置による強制蒸発により水分が抜かれて最小限の容積の残渣となるので、生ゴミに比べて焼却場までの搬送エネルギーや焼却場での焼却エネルギーが小さく済み、化石燃料の消費量が軽減され、省資源および二酸化炭素排出量の抑制に寄与する。
(3) 生活廃水は廃水されて直ちに蒸発槽で水蒸気と固体物に分離されるのでなく、廃水ストックヤードに一旦貯水された後に、廃水が所定量に達するか、または予め設定した時間帯になってから蒸発槽に移動されるので、水蒸気と固体物の分離作業を予め設定したスケジュールで行うことが可能となる。よって、回収すべき残渣が生じる時間を毎日一定時刻に設定したり、第2発明のように電力を要する加熱装置による強制蒸発を予め電力契約で決定された深夜の低額時間帯に設定することにより、この生活廃水処理システムの稼働のために居住者が行うべき作業をルーチン化したり、負担すべき電力コストを最小限に押さえることが可能となり、無理なくこのシステムを導入することができる。
(4) 前記の場合、加熱装置による強制蒸発に電力を使用しても、それまでの時間は水分の沸点が降下する減圧環境下での自然蒸発が行われるシステムとしているので、加熱装置の稼働時間を短縮でき電力コストを軽減できる。
The first invention and the second invention of the domestic wastewater treatment system of the present invention produce the following actions and effects.
(1) Domestic wastewater is separated into water vapor and solid matter by natural evaporation in a reduced pressure environment where the boiling point of water drops and forced evaporation by a heating device, and the water vapor is liquefied and reused as clean water. The supply of water is minimal, contributing to resource conservation.
(2) The leftovers are crushed by the disposer and flowed along with the domestic wastewater into the wastewater route.However, since the water is removed by natural evaporation in a reduced pressure environment and forced evaporation by the heating device, it becomes a residue of a minimum volume, so Compared to transport energy up to the incineration site and incineration energy at the incineration site, the consumption of fossil fuel is reduced, contributing to resource saving and carbon dioxide emission control.
(3) The domestic wastewater is not drained and immediately separated into water vapor and solid matter in the evaporation tank, but once it is stored in the wastewater stockyard, the wastewater reaches a predetermined amount or reaches a preset time zone. After that, since it is moved to the evaporation tank, it is possible to carry out the work for separating the water vapor and the solid material according to a preset schedule. Therefore, by setting the time when the residue to be collected is generated every day to a certain time, or by setting forced evaporation by a heating device that requires power as in the second invention to a low-cost time zone in the middle of the night determined in advance by a power contract Therefore, it is possible to routineize the work to be performed by the resident for the operation of this domestic wastewater treatment system, or to minimize the power cost to be borne, and this system can be introduced without difficulty.
(4) In the above case, even if electric power is used for forced evaporation by the heating device, since the system is a system where natural evaporation is performed in a reduced pressure environment where the boiling point of moisture falls, the operation of the heating device Time can be reduced and power costs can be reduced.

次に、この発明の生活廃水処理システムの第3発明および第4発明は次の作用・効果を生じる。
(1) 汚水は水分の沸点が降下する減圧環境下での自然蒸発および加熱装置による強制蒸発により水蒸気と固体物に分離され、水蒸気は液化して浄化した水として排出されるので河川などに放流しても環境を損なうことがなく、また、下水道に放流しても処理施設に負担を与えることがない。
(2) 第4発明によれば、蒸発焼却槽を並列に2つ設け、水蒸気と固体分への分離および固形分の焼却作業と汚水の貯留作業を時間ごとに交代に振り分けて行うので、水蒸気と固体物の分離作業を予め設定したスケジュールで行うことが可能となる。よって、回収すべき残渣が生じる時間を毎日一定時刻に設定したり、電力を要する加熱装置による強制蒸発を予め電力契約で決定された深夜の低額時間帯に設定することにより、この生活廃水処理システムの稼働のために居住者が行うべき作業をルーチン化したり、負担すべき電力コストを最小限に押さえることが可能となり、無理なくこのシステムを導入することができる。(3) 前記の場合、加熱装置による強制蒸発に電力を使用しても、水分の沸点が降下する減圧環境下での自然蒸発が行われるシステムを併用しているので、加熱装置の稼働時間を短縮でき電力コストを軽減できる。
Next, the 3rd invention and 4th invention of the domestic wastewater treatment system of this invention produce the following operation and effect.
(1) Sewage is separated into water vapor and solid matter by natural evaporation in a reduced pressure environment where the boiling point of water drops and forced evaporation by a heating device, and the water vapor is liquefied and discharged as purified water, so it is discharged into rivers, etc. Even if it does not damage the environment, it does not impose a burden on the treatment facility even if it is discharged into the sewer.
(2) According to the fourth invention, two evaporative incineration tanks are provided in parallel, and separation into water vapor and solids and incineration of solids and storage of sewage are performed alternately by time. It is possible to carry out the separation work of the solid matter with a preset schedule. Therefore, this domestic wastewater treatment system can be set by setting the time when the residue to be collected is generated every day at a certain time, or by setting forced evaporation by a heating device that requires power in a low-cost time zone determined in advance in the power contract. It is possible to routineize the work to be done by the resident for the operation of the system and to minimize the power cost to be borne, and this system can be introduced without difficulty. (3) In the above case, even if electric power is used for forced evaporation by the heating device, a system that spontaneously evaporates in a reduced pressure environment where the boiling point of moisture falls is also used. It can be shortened and power cost can be reduced.

この発明の生活廃水処理システムの第1発明のブロック図。The block diagram of 1st invention of the domestic wastewater treatment system of this invention. 同上、第4発明のブロック図。The block diagram of 4th invention same as the above.

図1はこの発明の生活廃水処理システムの第1発明の構成を示すブロック図である。この発明においては住宅内の風呂11、洗面12、洗濯13、シンク(台所)14から生じる生活廃水は廃水経路を介して先ず廃水ストックヤード1に貯水される。この場合、台所から出る残飯はシンク14の排水口に設けられたディスポーザ15により破砕され、廃水とともに廃水ストックヤード1に貯水される。すなわち、廃水経路には固形分を含んだ水が廃水される。   FIG. 1 is a block diagram showing the configuration of the first aspect of the domestic wastewater treatment system of the present invention. In the present invention, domestic wastewater generated from the bath 11, wash surface 12, laundry 13 and sink (kitchen) 14 in the house is first stored in the wastewater stockyard 1 through the wastewater path. In this case, the remaining rice from the kitchen is crushed by the disposer 15 provided at the drain of the sink 14 and stored in the waste water stock yard 1 together with the waste water. That is, water containing solid content is discharged into the wastewater path.

図中符号2は前記の廃水ストックヤード1から廃水を取り出して減圧環境下で水蒸気と固体物に分離する蒸発槽である。この蒸発槽2では固形分を含んだ廃水は、水分の沸点が降下する減圧環境下での自然蒸発および加熱装置2Cによる強制蒸発により水蒸気と固体物に分離される。加熱装置2Cとしては電熱ヒータが想定される。前記の固形分は、残渣は残渣取り出し口2Aより、油脂は油脂取り出し口2Bよりそれぞれ取り出されて廃棄される。蒸発槽2において図中符号S4は蒸発槽負圧保護センサ、S5は蒸発槽内圧センサ、S6は蒸発槽内廃水温度センサ、S7は蒸発槽内水位センサである。蒸発条件は蒸発槽2内に取り込まれる廃水の温度により異なってくるので、それにより負圧の度合いを制御するためにこれらのセンサが必要となる。   Reference numeral 2 in the figure denotes an evaporation tank that takes out waste water from the waste water stock yard 1 and separates it into water vapor and solid matter in a reduced pressure environment. In the evaporating tank 2, the waste water containing solids is separated into water vapor and solid matter by natural evaporation in a reduced pressure environment where the boiling point of water drops and forced evaporation by the heating device 2C. An electric heater is assumed as the heating device 2C. From the solid content, the residue is taken out from the residue takeout port 2A, and the oil and fat is taken out from the oil takeout port 2B and discarded. In the evaporating tank 2, reference numeral S4 in the figure denotes an evaporating tank negative pressure protection sensor, S5 denotes an evaporating tank internal pressure sensor, S6 denotes an evaporating tank waste water temperature sensor, and S7 denotes an evaporating tank water level sensor. Since the evaporation conditions vary depending on the temperature of the waste water taken into the evaporation tank 2, these sensors are required to control the degree of negative pressure.

水蒸気は復水器3により液化され、復水経路を介してA復水貯水槽4A、B復水貯水槽4Bに貯水される。貯水された水は復水経路から上水経路に流されて風呂11、洗面12、洗濯13、シンク(台所)14の他、トイレ16で上水として利用される。なお、A復水貯水槽4A、B復水貯水槽4Bに貯水された復水は塩素滅菌装置7により消毒が行われるとともに、臭気抜き装置5により臭気が抜かれる。上記の滅菌は予め設定した時間に水位センサS9、S10により検出した貯水槽内の水位により濃度を調整して行われる。   The water vapor is liquefied by the condenser 3 and stored in the A condensate water storage tank 4A and the B condensate water storage tank 4B through the condensate path. The stored water flows from the condensate path to the water supply path and is used as water in the bathroom 11, wash surface 12, laundry 13, sink (kitchen) 14 and toilet 16. The condensed water stored in the A condensate water storage tank 4A and the B condensate water storage tank 4B is sterilized by the chlorine sterilization device 7 and the odor removing device 5 removes the odor. The sterilization is performed by adjusting the concentration according to the water level in the water tank detected by the water level sensors S9 and S10 at a preset time.

以上のシステムは漫然と稼働されるのでなく、下記の24時間サイクルのタイムスケジュールに沿って稼働される。
−昼間モード−
(1) A復水貯水槽4A、B復水貯水槽4Bのいずれにも貯水されていない場合は、それを水位センサS9、S10で検出して、バルブV2、V3を閉じ、水源側のバルブV1を開くことにより上水経路は復水経路から遮断され、水道などの外部の水源から水が供給される。一方、A復水貯水槽4A、B復水貯水槽4Bのいずれかに貯水されている場合は、水源側のバルブV1を閉じ、バルブV2、V3を開くことにより上水経路は水源側から遮断され、吸水ポンプ9により貯水槽から水が供給される。この状態で風呂11、洗面12、洗濯13、シンク(台所)14などで水が使用され、廃水は廃水ストックヤード1に貯水されていく。
The above system is not operated at random, but is operated according to the time schedule of the following 24-hour cycle.
-Daytime mode-
(1) If water is not stored in either the A condensate reservoir 4A or the B condensate reservoir 4B, it is detected by the water level sensors S9 and S10, the valves V2 and V3 are closed, and the water source side valve By opening V1, the water supply path is blocked from the condensate path, and water is supplied from an external water source such as a water supply. On the other hand, when water is stored in either the A condensate reservoir 4A or the B condensate reservoir 4B, the water supply path is shut off from the water source side by closing the valve V1 on the water source side and opening the valves V2 and V3. Then, water is supplied from the water storage tank by the water absorption pump 9. In this state, water is used in the bath 11, the washbasin 12, the laundry 13, the sink (kitchen) 14, etc., and the wastewater is stored in the wastewater stockyard 1.

(2) 廃水ストックヤード1の廃水が所定量に達すると、ストックカウンターセンサS1によりそれを検出し、真空ポンプ6からの吸引により蒸発槽2の負圧が上昇され、これに合わせて廃水ストックヤードと蒸発槽間の連動バルブV4が開放され廃水ストックヤードの廃水は蒸発槽に取り込まれ、取り込みが終了すると吸引終了センサS2によりそれを検出して連動バルブV4は閉じられる。 (2) When the waste water in the waste water stock yard 1 reaches a predetermined amount, it is detected by the stock counter sensor S1, and the negative pressure in the evaporation tank 2 is increased by suction from the vacuum pump 6, and the waste water stock yard is accordingly adjusted. And the interlock valve V4 between the evaporation tank and the waste water in the waste water stockyard is taken into the evaporation tank, and when the intake is completed, the suction end sensor S2 detects it and the interlock valve V4 is closed.

(3) 蒸発槽2では水分の沸点が降下する減圧環境下での廃水の自然蒸発が開始され、水蒸気は復水器3により液化され、復水経路を介してA復水貯水槽4A、B復水貯水槽4Bのいずれかに貯水される。 (3) In the evaporating tank 2, the natural evaporation of the wastewater in a reduced pressure environment where the boiling point of the water drops is started, the water vapor is liquefied by the condenser 3, and the A condensate water storage tanks 4A, B are passed through the condensate path. Water is stored in one of the condensate water storage tanks 4B.

(4) この発明においては廃水ストックヤード1の貯水可能容量(この実施例では200リットルを想定)に対し蒸発槽2の容量(この実施例では1756リットルを想定)を大きく設定しており、前記の廃水ストックヤードから蒸発槽への移動作業は1日のうちに何回か繰り返されることになる。 (4) In the present invention, the capacity of the evaporating tank 2 (assuming 1756 liters in this embodiment) is set larger than the capacity of the wastewater yard 1 that can store water (assuming 200 liters in this embodiment). The transfer work from the waste water stockyard to the evaporation tank will be repeated several times a day.

−夜間モード−
(5) 夜間の予め設定した時間(この実施例では午後10時を設定)になると、廃水ストックヤード1の状態とかかわりなく、強制的に内部の廃水は蒸発槽2に移動して廃水ストックヤードは一旦空になる。この場合、廃水経路から廃水が廃水ストックヤードに貯留され満杯になった場合にはストックカウンターセンサS1によりそれを検出し、上水経路中の復水経路側のバルブV3と水源側のバルブV1を閉じ、風呂11、洗面12、洗濯13、シンク(台所)14の上水の供給を遮断する。つまり、夜間モードにおいてこれらで使用できる水の量は廃水ストックヤードの貯水可能容量分(この実施例では200リットル)ということになる。なお、この場合トイレ16に関してはバルブV3をそれより水源側に配することにより復水経路からの上水を使えるようにしている。
−Night mode−
(5) At the preset time of the night (10:00 pm in this example), the waste water inside the waste water yard is forcibly moved to the evaporation tank 2 regardless of the state of the waste water yard 1 Will be empty once. In this case, when the wastewater from the wastewater path is stored in the wastewater stockyard and becomes full, it is detected by the stock counter sensor S1, and the condensate path valve V3 and the water source side valve V1 in the water supply path are detected. Close and shut off the supply of clean water to the bath 11, the washbasin 12, the laundry 13 and the sink (kitchen) 14. In other words, the amount of water that can be used in the night mode is equivalent to the water storage capacity of the waste water stockyard (200 liters in this embodiment). In this case, with respect to the toilet 16, the valve V3 is arranged on the water source side so that the water from the condensate path can be used.

(6) 蒸発槽2では予め電力契約で決定された深夜の低額時間帯(この実施例では午後11時を設定)になると加熱装置2Cによる強制蒸発を行って蒸発を促進させ、これを設定した時間(この実施例では午前5時を設定)まで行う。 (6) In the evaporating tank 2, in the low-night time zone (in this example, 11:00 pm) determined in advance by an electric power contract, forced evaporation by the heating device 2C is performed to promote evaporation, and this is set. Until the time (in this embodiment, 5 am is set).

−早朝モード−
(7) 早朝の予め設定した時間(この実施例では午前5時〜6時を設定)に蒸発槽2の残渣取り出し口2Aより残渣を、油脂取り出し口2Bより油脂をそれぞれ取り出して回収のために所定の容器にストックする。この実施例においては利用者が上記作業を懈怠することのないために、残渣取り出し口2Aおよび油脂取り出し口2Bを開くことにより生活廃水処理システムの稼働が停止し、取り出し口を閉じてリセットボタンを押すことにより稼働が開始されるようにしている。
-Early morning mode-
(7) In order to recover by removing the residue from the residue outlet 2A of the evaporating tank 2 and the oil and fat from the oil outlet 2B at a preset time in the morning (in this embodiment, 5:00 to 6:00). Stock in the designated container. In this embodiment, since the user does not carry out the above work, the operation of the domestic wastewater treatment system is stopped by opening the residue outlet 2A and the oil outlet 2B, and the outlet is closed and the reset button is pressed. Operation is started by pressing.

この発明の生活廃水処理システムにおいては、廃水は経路内を循環して外部に排出することはない。一方、廃水ストックヤード1が満杯になった場合は、新たな廃水によりオーバーフローしないように上水経路を一旦遮断して、廃水ストックヤードの廃水を蒸発槽2に移動する。従って、前記したように24時間のサイクルで稼働されるこの発明のシステムでは、1日で使用できる水は「(廃水ストックヤードの貯水可能容量)×(廃水ストックヤードから蒸発槽への24時間あたりの水の最大移動回数)+(廃水ストックヤードの貯水可能容量)」となる。この実施例では上記移動回数を6回と想定し、廃水ストックヤードの貯水可能容量は200リットルと想定しているので、1日で使用できる水は1200リットル+200リットルとなる。この発明においてはこのように規制することにより利用者に水資源の節約を促すことになる。   In the domestic wastewater treatment system of this invention, the wastewater does not circulate in the path and be discharged outside. On the other hand, when the waste water stock yard 1 is full, the water supply path is temporarily interrupted so as not to overflow with new waste water, and the waste water in the waste water stock yard is moved to the evaporation tank 2. Therefore, as described above, in the system of the present invention that is operated in a cycle of 24 hours, the water that can be used in one day is “(capacity of storage of wastewater stockyard) × (per 24 hours from wastewater stockyard to evaporation tank” The maximum number of movements of water) + (capacity to store water in the wastewater stockyard). In this embodiment, the number of times of movement is assumed to be 6 and the water storage capacity of the wastewater stockyard is assumed to be 200 liters. Therefore, the water that can be used in one day is 1200 liters + 200 liters. In this invention, by restricting in this way, the user is encouraged to save water resources.

図2はこの発明の生活廃水処理システムの第4発明の構成を示すブロック図である。この発明においてはトイレからの汚水はトイレ導入管20を経て廃水ストックヤードとは別系統の蒸発焼却槽であるA蒸発焼却便槽21A、B蒸発焼却便槽21Bに貯留され、これらの蒸発焼却槽において減圧環境下で水蒸気と固体分に分離され、水蒸気は復水器24により液化して廃貯水槽25に貯留した後に排水ポンプ31により廃水経路30に放流されるとともに、固形分は蒸発焼却槽で焼却される。   FIG. 2 is a block diagram showing the configuration of the fourth aspect of the domestic wastewater treatment system of the present invention. In this invention, the sewage from the toilet is stored in the A evaporative incineration tank 21A and the B evaporative incineration tank 21B, which are separate from the waste water stockyard, through the toilet introduction pipe 20, and these evaporative incineration tanks. In the reduced pressure environment, the water vapor is separated into the solid and the water vapor is liquefied by the condenser 24 and stored in the waste water storage tank 25 and then discharged into the waste water path 30 by the drain pump 31 and the solid content is evaporated and incinerated. Incinerated at.

A蒸発焼却便槽21A、B蒸発焼却便槽21Bにおいて図中符号G、G1は負圧の制御のための蒸発槽内圧センサ、H、H1は蒸発槽内水位センサである。また、図中符号22A、22Bは残渣を焼却する残渣焼却パンである。この実施例では焼却手段としてマイクロ波による加熱を採用している。   In the A evaporation incineration tank 21A and the B evaporation incineration tank 21B, reference numerals G and G1 in the figure denote evaporation tank internal pressure sensors for controlling negative pressure, and H and H1 denote evaporation tank water level sensors. Reference numerals 22A and 22B in the figure denote residue incineration pans that incinerate the residues. In this embodiment, microwave heating is employed as the incineration means.

前記の蒸発焼却便槽において焼却された残渣の灰は残り灰エアーチューブ22から高圧空気を残渣焼却パンに吹きつけることにより攪拌され、ドラフトチューブ29を介して残り灰集塵機26により集塵される。また、残り灰が酸素不足で炭化して紛状化しないことを防止するために残渣焼却時炭化防止用エアー供給機F、F1により残渣焼却パンに空気が導入される。   The residual ash incinerated in the evaporative incineration tank is agitated by blowing high pressure air from the residual ash air tube 22 onto the residual incineration pan, and is collected by the residual ash dust collector 26 through the draft tube 29. In addition, air is introduced into the residue incineration pan by the carbonizer for preventing carbonization at the time of residue incineration F and F1 in order to prevent the remaining ash from carbonizing due to lack of oxygen and becoming a powder.

前記A蒸発焼却便槽21A、B蒸発焼却便槽21Bは並列に設けられ、水蒸気と固体分への分離および固形分の焼却作業と汚水の貯留作業を下記の24時間サイクルのタイムスケジュールに沿って交互に振り分けて行う。   The A evaporation incineration tank 21A and the B evaporation incineration tank 21B are provided in parallel, and the separation into water vapor and solids and the incineration of solids and the storage of sewage are performed in accordance with the following 24-hour cycle time schedule. Sort them alternately.

(1) 夜間の予め設定した時間(この実施例では午後10時を設定)から汚水をトイレ導入管20を介してA蒸発焼却便槽21Aにストックし始め24時間後に終了する。この場合の各バルブの状態は次の通りである。以下、バルブの開放状態を○で、閉止状態を×で示すこととする。
(トイレ導入管20からの) バルブA−○ バルブA1−×
(復水器24への) バルブB−× バルブB1−○
(残り灰エアーチューブ22の) バルブC−× バルブC1−×
(ドラフトチューブ29の) バルブD−× バルブD1−×
(排煙、排気処理パイプ23の) バルブE−○ バルブE1−×
(1) The sewage is stocked in the A evaporative incineration tank 21A through the toilet introduction pipe 20 from a preset time at night (10:00 pm in this embodiment), and is finished after 24 hours. The state of each valve in this case is as follows. Hereinafter, the open state of the valve is indicated by ◯, and the closed state is indicated by ×.
(From toilet introduction pipe 20) Valve A- ○ Valve A1-X
(To condenser 24) Valve B-x Valve B1- ○
(Remaining ash air tube 22) Valve C-x Valve C1-x
(Draft tube 29) Valve D-x Valve D1-x
(Smoke exhaust, exhaust treatment pipe 23) Valve E- ○ Valve E1-x

(2) 24時間後、A蒸発焼却便槽21Aは汚水の貯留モードから処理モードに切り替わる。一方、B蒸発焼却便槽21Bは汚水の処理モードから貯留モードに切り替わる。この場合の各バルブの状態は次の通りである。
(トイレ導入管20からの) バルブA−× バルブA1−○
(復水器24への) バルブB−○ バルブB1−×
(残り灰エアーチューブ22の) バルブC−× バルブC1−×
(ドラフトチューブ29の) バルブD−× バルブD1−×
(排煙、排気処理パイプ23の) バルブE−× バルブE1−○
(2) After 24 hours, the A evaporative incineration tank 21A is switched from the sewage storage mode to the treatment mode. On the other hand, the B evaporative incineration tub 21B is switched from the sewage treatment mode to the storage mode. The state of each valve in this case is as follows.
(From toilet introduction pipe 20) Valve A-X Valve A1- ○
(To condenser 24) Valve B- ○ Valve B1-x
(Remaining ash air tube 22) Valve C-x Valve C1-x
(Draft tube 29) Valve D-x Valve D1-x
(Smoke exhaust, exhaust treatment pipe 23) Valve E-x Valve E1- ○

(3) 汚水の処理モードに入ったA蒸発焼却便槽21Aにおいては、負圧を上昇させるために真空ポンプ28が始動し、水分の沸点が降下する減圧環境下での汚水の自然蒸発が開始され、水蒸気は復水器24により液化され廃貯水槽25に貯留される。一方、残渣焼却パン22Aの電源も投入される。 (3) In the A evaporative incineration tank 21A that has entered the sewage treatment mode, the vacuum pump 28 is started in order to increase the negative pressure, and the natural evaporation of sewage starts in a reduced pressure environment where the boiling point of the water drops. The water vapor is liquefied by the condenser 24 and stored in the waste water tank 25. On the other hand, the power source of the residue incineration pan 22A is also turned on.

(4) 前記の蒸発工程は18時間で完了するように、負圧を調整するとともに、残渣焼却パン22Aの加熱による槽内の温度管理も行われる。 (4) The negative pressure is adjusted so that the evaporation step is completed in 18 hours, and the temperature in the tank is also controlled by heating the residue incineration pan 22A.

(5) 18時間経過後は、残渣中の水分と残渣焼却排気(熱)を大気中に放出する排煙、排気工程に入り、これは2時間続く。この間に残渣焼却時炭化防止用エアー供給機Fにより残渣焼却パンに空気が15分間導入される。この場合の各バルブの状態は次の通りである。
(トイレ導入管20からの) バルブA−× バルブA1−○
(復水器24への) バルブB−× バルブB1−×
(残り灰エアーチューブ22の) バルブC−× バルブC1−×
(ドラフトチューブ29の) バルブD−× バルブD1−×
(排煙、排気処理パイプ23の) バルブE−○ バルブE1−○
(5) After 18 hours, the process enters a flue gas and exhaust process in which the moisture in the residue and the residue incineration exhaust (heat) are released into the atmosphere, which lasts for 2 hours. During this period, air is introduced into the residue incineration pan for 15 minutes by the air feeder F for preventing carbonization during residue incineration. The state of each valve in this case is as follows.
(From toilet introduction pipe 20) Valve A-X Valve A1- ○
(To condenser 24) Valve B-x Valve B1-x
(Remaining ash air tube 22) Valve C-x Valve C1-x
(Draft tube 29) Valve D-x Valve D1-x
(Smoke exhaust, exhaust processing pipe 23) Valve E- ○ Valve E1- ○

(6) 2時間経過後は、残渣焼却パン22Aの電源が切断され。残り灰の攪拌と集塵工程に入り、これは30分間続く。一方、A槽、B槽コントロールバルブLが開放されるとともに、排水ポンプ31が作動して廃貯水槽25に貯留した水を放流して空にする。この場合の各バルブの状態は次の通りである。
(トイレ導入管20からの) バルブA−× バルブA1−○
(復水器24への) バルブB−× バルブB1−×
(残り灰エアーチューブ22の) バルブC−○ バルブC1−×
(ドラフトチューブ29の) バルブD−○ バルブD1−×
(排煙、排気処理パイプ23の) バルブE−× バルブE1−○
(6) After 2 hours, the residue incineration pan 22A is turned off. The remaining ash is stirred and collected, which lasts for 30 minutes. On the other hand, the tank A and the tank B control valve L are opened, and the drain pump 31 is operated to discharge and empty the water stored in the waste water tank 25. The state of each valve in this case is as follows.
(From toilet introduction pipe 20) Valve A-X Valve A1- ○
(To condenser 24) Valve B-x Valve B1-x
(Remaining ash air tube 22) Valve C- ○ Valve C1-x
(Draft tube 29) Valve D- ○ Valve D1-x
(Smoke exhaust, exhaust treatment pipe 23) Valve E-x Valve E1- ○

(7) 30分経過後は、受け入れ準備工程に入り、これは3時間30分間続く。この場合の各バルブの状態は次の通りである。
(トイレ導入管20からの) バルブA−× バルブA1−○
(復水器24への) バルブB−× バルブB1−×
(残り灰エアーチューブ22の) バルブC−× バルブC1−×
(ドラフトチューブ29の) バルブD−× バルブD1−×
(排煙、排気処理パイプ23の) バルブE−○ バルブE1−○
(8) 3時間30分後、B蒸発焼却便槽21Bは汚水の貯留モードから処理モードに切り替わり、前記(2) 〜(7) のA蒸発焼却便槽21と同じ作用を果たす。A蒸発焼却便槽21は汚水の貯留モードに切り替わり、前記(1) の作用を果たす。
(7) After 30 minutes, enter the acceptance preparation process, which lasts 3 hours 30 minutes. The state of each valve in this case is as follows.
(From toilet introduction pipe 20) Valve A-X Valve A1- ○
(To condenser 24) Valve B-x Valve B1-x
(Remaining ash air tube 22) Valve C-x Valve C1-x
(Draft tube 29) Valve D-x Valve D1-x
(Smoke exhaust, exhaust processing pipe 23) Valve E- ○ Valve E1- ○
(8) After 3 hours and 30 minutes, the B evaporation incineration tank 21B is switched from the sewage storage mode to the treatment mode, and performs the same function as the A evaporation incineration tank 21 of (2) to (7). The A evaporative incineration tank 21 is switched to the sewage storage mode and performs the function (1).

1 廃水ストックヤード
2 蒸発槽
4A、4B 復水貯水槽
1 Wastewater stockyard 2 Evaporation tank 4A, 4B Condensate water storage tank

Claims (4)

住宅より生じる生活廃水を浄化、再処理するシステムにおいて、残飯を破砕して廃水経路に流すディスポーザ、廃水経路からの廃水を一旦貯水する廃水ストックヤード、廃水ストックヤードから廃水を取り出して減圧環境下で水蒸気と固体物に分離する蒸発槽、蒸発槽からの水蒸気を液化して貯水する復水貯水槽、復水貯水槽から水を取り出して上水として供給する上水経路を設け、廃水ストックヤードの廃水が所定量に達するか、または予め設定した時間帯になると廃水を蒸発槽に移動し、蒸発槽では減圧による自然蒸発に加えて予め設定した時間帯に加熱装置による強制蒸発を行うことを特徴とする生活廃水処理システム。 In a system that purifies and reprocesses domestic wastewater generated from houses, a disposer that crushes leftover food and flows it into the wastewater route, a wastewater stockyard that temporarily stores wastewater from the wastewater route, and takes out wastewater from the wastewater stockyard under reduced pressure. Establishing an evaporating tank that separates water vapor and solids, a condensate water tank that liquefies and stores water vapor from the evaporating tank, and a water supply path that takes out water from the condensate water tank and supplies it as clean water. When the amount of wastewater reaches a predetermined amount or when a preset time zone is reached, the wastewater is moved to the evaporation tank, and in the evaporation tank, in addition to natural evaporation due to reduced pressure, forced evaporation is performed by a heating device during a preset time zone. A domestic wastewater treatment system. 夜間の就寝時間帯に廃水の蒸発槽への移動を開始し、さらに予め電力契約で決定された深夜の低額時間帯に加熱装置による強制蒸発を行う請求項1記載の生活廃水処理システム。 The domestic wastewater treatment system according to claim 1, wherein the wastewater is started to move to the evaporation tank at nighttime sleeping hours, and is further subjected to forced evaporation by a heating device in a low-cost time zone determined in advance by a power contract. トイレからの汚水は廃水ストックヤードとは別系統の蒸発焼却槽に貯留し、上記の蒸発焼却槽で減圧環境下で水蒸気と固体分に分離し、蒸気は液化して廃貯水槽に貯留した後に廃水するとともに、固形分は蒸発焼却槽で焼却する請求項1または2記載の生活廃水処理システム。 Wastewater from the toilet is stored in a separate evaporative incineration tank from the wastewater stockyard, separated into water vapor and solids in a reduced pressure environment in the above evaporative incineration tank, and the vapor is liquefied and stored in the waste water tank. The domestic wastewater treatment system according to claim 1 or 2, wherein the solid content is incinerated in an evaporative incinerator while being wastewater. 蒸発焼却槽を並列に2つ設け、水蒸気と固体分への分離および固形分の焼却作業と汚水の貯留作業を時間ごとに交代に振り分けて行う請求項3に記載の生活廃水処理システム。
The domestic wastewater treatment system according to claim 3, wherein two evaporative incineration tanks are provided in parallel, and the separation into water vapor and solids, and the solids incineration work and the sewage storage work are performed alternately in accordance with time.
JP2009237954A 2009-10-15 2009-10-15 Domestic wastewater treatment system Expired - Fee Related JP5305526B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2009237954A JP5305526B2 (en) 2009-10-15 2009-10-15 Domestic wastewater treatment system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2009237954A JP5305526B2 (en) 2009-10-15 2009-10-15 Domestic wastewater treatment system

Publications (2)

Publication Number Publication Date
JP2011083691A JP2011083691A (en) 2011-04-28
JP5305526B2 true JP5305526B2 (en) 2013-10-02

Family

ID=44077058

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2009237954A Expired - Fee Related JP5305526B2 (en) 2009-10-15 2009-10-15 Domestic wastewater treatment system

Country Status (1)

Country Link
JP (1) JP5305526B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107754398A (en) * 2017-10-17 2018-03-06 广州雅津水处理设备有限公司 A kind of domestic sewage recycling and processing device

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NO752285L (en) * 1975-06-25 1976-12-28 Magnar Morkve
JP2645924B2 (en) * 1991-05-15 1997-08-25 三洋電機株式会社 Garbage processing equipment
JP3362743B2 (en) * 1993-06-04 2003-01-07 株式会社オメガ Night soil treatment equipment
JPH11138144A (en) * 1997-11-12 1999-05-25 Toshiba Corp Garbage drying equipment
JP2000325999A (en) * 1999-05-20 2000-11-28 Matsushita Electric Ind Co Ltd Slurry processing equipment
JP2005238119A (en) * 2004-02-26 2005-09-08 Katsumi Iida Wastewater treatment method

Also Published As

Publication number Publication date
JP2011083691A (en) 2011-04-28

Similar Documents

Publication Publication Date Title
JP2012521293A (en) Method and apparatus for automatic collection pipeline discharge and solid waste recycling
CN102374543A (en) Anaerobic fermentation-incineration combined treatment method for organic wastes
JP4693916B2 (en) Anhydrous manure treatment method and anhydrous manure treatment toilet system
CN201793398U (en) Household garbage leachate harmless treatment device
JP2008246373A (en) 厨 芥 Treatment system
KR101448950B1 (en) Waste processing system linked sewage processing facilities
CN111233287A (en) a waste disposal system
JPWO2021117195A1 (en) Waste treatment plant
CN106232530A (en) Waste treatment system
JP5305526B2 (en) Domestic wastewater treatment system
CN106439859A (en) Two-stage sludge carbonization and incineration method and system
JP2005125185A (en) Biogas generator and biogas power generation system
JP3581143B2 (en) Treatment method of garbage disposer wastewater at sewage treatment plant
CN207738607U (en) A kind of device of sanitary sewage disposal and circulating and recovering
WO2002064273A1 (en) Method and system for treating organic matter utilizing substance circulation system
JP4417060B2 (en) Garbage and human waste collection processing method and apparatus
CN108405549B (en) Method and device for preventing and controlling scaling and clogging of waste landfill by using slag and landfill gas
CN210888171U (en) Ecological toilet
CN201760437U (en) System for treating urban household garbage
CN211896576U (en) Excrement treatment system
CA2687629A1 (en) Wastewater treatment apparatus
CN110054241A (en) A kind of excreta automatic processing device and processing method
CN208108126U (en) A kind of domestic garbage burning electricity generation collaboration sludge drying treatment system
WO2014076725A2 (en) Linear synergistic system of digestion, dehydration and composting (ldcc)
CN110981100A (en) Landfill leachate disposal system and method suitable for cement kiln

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20120127

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20120223

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20130228

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20130312

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20130513

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20130604

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20130624

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

Ref document number: 5305526

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees