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JPH05317856A - Regeneration treatment of general waste water - Google Patents

Regeneration treatment of general waste water

Info

Publication number
JPH05317856A
JPH05317856A JP14821392A JP14821392A JPH05317856A JP H05317856 A JPH05317856 A JP H05317856A JP 14821392 A JP14821392 A JP 14821392A JP 14821392 A JP14821392 A JP 14821392A JP H05317856 A JPH05317856 A JP H05317856A
Authority
JP
Japan
Prior art keywords
water
waste water
membrane device
general waste
ultrafiltration membrane
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP14821392A
Other languages
Japanese (ja)
Inventor
Hironori Nagashima
弘典 長島
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.)
Fujita Corp
Original Assignee
Fujita Corp
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 Fujita Corp filed Critical Fujita Corp
Priority to JP14821392A priority Critical patent/JPH05317856A/en
Publication of JPH05317856A publication Critical patent/JPH05317856A/en
Pending legal-status Critical Current

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  • Sink And Installation For Waste Water (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE:To solve the problem of the generation of smells in intermediate water which heretofore occurs in the temp. rise of treated water by changing a method for obtaining the inflow pressure of general waste water to an ultrafilter membrane device by the conventional circulating pressurizing pump to a method for providing a height difference between a general waste water control tank and the ultrafilter membrane device connected to this tank by a water feed pipe, and obtaining this height difference as the pressure of the general waste water flowing downward. CONSTITUTION:The method for making the regeneration treatment of the general waste water by passing the water through the ultrafilter membrane device is constituted in the following manner. The general waste water control tank 2 into which the general waste water flows is installed in the upper story of a building and the ultrafilter membrane device 3 connected to the general waste water control tank 2 by the water feed pipe 1b is installed in the story lower than the story where the general waste water control tank 2 is installed. The general waste water is run to the ultrafilter membrane device 3 and is filtered by utilizing the head pressure from the general waste water control tank 2.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、雑排水から中水を造水
する雑排水の再生処理方法に関し、特に雑排水調整槽と
限外濾過膜装置との設置高低差を利用して限外濾過膜装
置に雑排水を流すようにしたものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for regenerating sewage produced by producing sewage from sewage, and in particular it utilizes the difference in installation height between a sewage adjusting tank and an ultrafiltration membrane device for ultrafiltration. The waste water is passed through the filtration membrane device.

【0002】[0002]

【従来の技術】図2に示すように、従来雑排水を限外濾
過膜装置cにより中水に再処理するためには、雑排水を
地下に設けらけれた雑排水調整槽aに貯留した。その
後、雑排水は雑排水調整槽aから循環加圧ポンプbによ
ってその一定量が加圧され、限外濾過膜装置cによって
有機物や細菌などの濾別処理が行われ、できた中水は貯
留槽dに貯留された。一方、未処理の雑排水はもとに戻
り循環しながら、再度限外濾過膜装置cに送られ濾過さ
れた。このようにして貯留槽dに貯留された中水は、貯
留槽dから給水ポンプeを経て、必要に応じ各送水管を
通して水洗トイレ用に、空調補給水用に、そして散水用
にと送られ使用されていた。なお、貯留槽dの容量を越
えた分の中水は、そのまま排水されていた。一方、この
ような雑排水調整槽a、循環加圧ポンプb、限外濾過膜
装置c及び貯留槽dからなる従来の雑排水の再処理方法
では、貯留槽dを床下ピットに設けることに合わせて全
体が地下機械室などの同一床面に平面的に設置されてい
た。
2. Description of the Related Art As shown in FIG. 2, in order to retreat conventional gray water to gray water by an ultrafiltration membrane device c, the gray water is stored in a gray water adjusting tank a provided underground. .. After that, the sewage is pressurized from the sewage adjusting tank a by a certain amount by the circulation pressurizing pump b, the ultrafiltration membrane device c filters the organic substances and bacteria, and the resulting sewage is stored. It was stored in tank d. On the other hand, untreated miscellaneous wastewater was returned to the original state and circulated, and again sent to the ultrafiltration membrane device c and filtered. The intermediate water stored in the storage tank d in this manner is sent from the storage tank d through the water supply pump e and, if necessary, through each water pipe for flush toilets, air conditioning makeup water, and sprinkling water. Was being used. In addition, the amount of gray water exceeding the capacity of the storage tank d was drained as it was. On the other hand, in the conventional method for reprocessing sewage waste water, which comprises the sewage adjustment tank a, the circulation pressurizing pump b, the ultrafiltration membrane device c and the storage tank d, the storage tank d is provided in the underfloor pit. The entire building was installed flat on the same floor such as the underground machine room.

【0003】[0003]

【発明が解決しようとする課題】従来の雑排水の再処理
方法では、一度雑排水調整槽に貯留した雑排水は、循環
加圧ポンプにより水圧を上げられて限外濾過膜装置に送
られていた。雑排水は、雑排水調整槽と限外濾過膜装置
とを循環する循環加圧ポンプを用いることにより、循環
加圧ポンプに使用されるモーターの発熱等で暖められ、
雑排水の温度が上昇し水質が変化した。このようにして
水質が変化した雑排水は、限外濾過膜装置で処理して
も、できた中水には水洗トイレや空調用補給水または散
水等に使用する際に臭気が発生するという問題があっ
た。
In the conventional method for reprocessing gray water, the gray water once stored in the gray water adjusting tank is sent to the ultrafiltration membrane device after increasing the water pressure by the circulation pressurizing pump. It was By using a circulation pressurizing pump that circulates the wastewater adjusting tank and the ultrafiltration membrane device, the sewage is warmed by the heat of the motor used for the circulation pressurizing pump, etc.
The temperature of the gray water increased and the water quality changed. Even if the wastewater whose water quality has changed in this way is treated with an ultrafiltration membrane device, the resulting sewage produces an odor when used for flushing toilets, makeup water for air conditioning, or sprinkling. was there.

【0004】そこで本発明は、雑排水の流れ込む雑排水
調整槽と限外濾過膜装置との間に高低差を設け、雑排水
調整槽より限外濾過膜装置へ送られる雑排水の水頭圧を
限外濾過膜装置に作用させるようにし、従来の循環加圧
ポンプのモーターによる処理水の温度上昇を防ぎ、それ
により中水の臭気発生を解消することを目的とした。
In view of the above, the present invention provides a height difference between the extraneous discharge adjusting tank into which the extraneous wastewater flows and the ultrafiltration membrane device, and controls the head pressure of the extraneous wastewater sent from the extraneous water adjusting tank to the ultrafiltration membrane device. The purpose of the invention is to prevent the odor generation of the intermediate water by preventing the temperature rise of the treated water by the motor of the conventional circulation pressurizing pump by making it act on the ultrafiltration membrane device.

【0005】[0005]

【課題を解決するための手段】本発明は上記目的を達成
するために、雑排水の流れ込む雑排水調整槽を建築物の
上層階に設置し、雑排水調整槽と送水管により結ばれた
限外濾過膜装置を雑排水調整槽の設置場所より下層階に
設置し、雑排水調整槽から水頭圧を利用して雑排水を限
外濾過膜装置へ流して濾過するようにした。
In order to achieve the above object, the present invention installs a sewage control tank into which sewage flows into the upper floors of a building, and connects the sewage control tank with a water supply pipe. The outer filtration membrane device was installed on the lower floor from the place where the miscellaneous drainage adjustment tank was installed, and the miscellaneous wastewater was flowed from the miscellaneous drainage adjustment tank to the ultrafiltration membrane device using the head pressure to perform filtration.

【0006】[0006]

【作用】建物の各所で使用された水は、雑排水として建
築物の上層階に設置された雑排水調整槽に集められる。
雑排水調整槽に集められた雑排水は、雑排水調整槽の設
置場所より下層階に設置される限外濾過膜装置へ送水管
を通って流れ落ちる。この流れ落ちる雑排水により、雑
排水調整槽と限外濾過膜装置との間の高低差に対応した
水頭圧が発生し、この水頭圧が限外濾過膜装置で雑排水
が濾過される際に必要な流入圧として作用する。このよ
うにして循環加圧ポンプを使用せずに雑排水の限外濾過
膜装置による濾過が行われるため、循環加圧ポンプのモ
ーターの発熱による雑排水の温度上昇がなく、雑排水の
水質の変化による中水の臭気発生が押さえられる。
[Operation] Water used in various places in the building is collected as miscellaneous wastewater in a miscellaneous wastewater adjustment tank installed on the upper floors of the building.
The sewage collected in the sewage adjustment tank flows down from the installation location of the sewage adjustment tank to the ultrafiltration membrane device installed on the lower floor through the water pipe. Due to this spilled effluent, a head pressure corresponding to the height difference between the effluent adjustment tank and the ultrafiltration membrane device is generated, and this head pressure is required when the effluent is filtered by the ultrafiltration membrane device. Acts as an inflow pressure. In this way, the wastewater is filtered by the ultrafiltration membrane device without using the circulation pressurizing pump, so there is no rise in the temperature of the wastewater due to the heat generated by the motor of the circulation pressurizing pump. The generation of odor in the inside water due to changes is suppressed.

【0007】[0007]

【実施例】本発明を図1により説明する。雑排水の再生
処理においては、例えば建物の各所の雑排水は排水管1
aを通って雑排水調整槽2に送られ、雑排水調整槽2か
ら送水管1bを通って限外濾過膜装置3へ送られるよう
になっている。雑排水調整槽2は建築物の上層階に設置
され、限外濾過膜装置3は雑排水調整槽2より下の下層
階に設けられている。なお、限外濾過膜装置3の濾過膜
は、雑排水の水質に応じて選択される。さらに限外濾過
膜装置3で処理されてできた中水は、貯留槽4に貯めら
れ、給水ポンプ5及び送水管1dを通って建物の各所に
供給されるようになっている。
The present invention will be described with reference to FIG. When regenerating wastewater, for example, wastewater from various places in the building is drained 1
It is sent to the miscellaneous waste water adjusting tank 2 through a, and is sent from the miscellaneous waste water adjusting tank 2 to the ultrafiltration membrane device 3 through the water supply pipe 1b. The gray water control tank 2 is installed on the upper floor of the building, and the ultrafiltration membrane device 3 is provided on the lower floor below the water control tank 2. The filtration membrane of the ultrafiltration membrane device 3 is selected according to the quality of the gray water. Further, the intermediate water treated by the ultrafiltration membrane device 3 is stored in the storage tank 4 and is supplied to various parts of the building through the water supply pump 5 and the water supply pipe 1d.

【0008】このように構成された再生処理では、建物
内の各所で使用した水は、雑排水として各所に配管され
た排水管1aを通って雑排水調整槽2に送られる。一
方、厨房設備等より流される油脂や夾雑物を多く含んだ
排水の場合は、グリーストラップ1等の一次処理装置に
より油脂や夾雑物を除いた後、雑排水調整槽2に送られ
る。雑排水調整槽2に一度貯留された雑排水は、雑排水
調整槽2と限外濾過膜装置3との間に予め設けられた高
低差により送水管1bを下って限外濾過膜装置3に流入
する。この高低差Hは送水管1bを流下する雑排水の水
頭圧が、限外濾過膜装置3が機能するのに必要な流入圧
になるように設定される。このようにして雑排水は、こ
の高低差Hを利用した水頭圧が限外濾過膜装置3に流入
圧として作用し、濾過されて中水になる。中水は送水管
1cを通って建築物の床下ピット等の貯留槽4に貯めら
れる。一度貯められた中水は、給水ポンプ5を経て建築
物の各階の必要な箇所に送水管1dを通して送られ、随
時水洗トイレ、空調用補給水、散水等々に用いられる。
また、雑排水調整槽2において、限外濾過膜装置3への
送水量より流入雑排水が多いときは、排水管2aを通し
てその分排水され、さらに、限外濾過膜装置3でも再生
された中水の量が貯留槽4への送水量を上回ったとき
は、排水管2bを通して排水される。また、設置場所と
しての雑排水調整槽2の上層階、限外濾過膜装置3の下
層階は、必要な高低差が得られる範囲内であれば建築物
の他の高所、低所を選んでもよい。
In the regenerating process constructed as described above, the water used at various places in the building is sent to the miscellaneous drainage adjusting tank 2 as the miscellaneous drainage through the drainage pipes 1a provided at the various places. On the other hand, in the case of wastewater containing a large amount of fats and oils discharged from the kitchen equipment or the like, it is sent to the wastewater adjusting tank 2 after removing the fats and oils and contaminants by the primary treatment device such as the grease trap 1. The miscellaneous wastewater once stored in the miscellaneous wastewater adjusting tank 2 goes down the water pipe 1b to the ultrafiltration membrane device 3 due to the height difference previously provided between the miscellaneous wastewater adjusting tank 2 and the ultrafiltration membrane device 3. Inflow. The height difference H is set so that the head pressure of the miscellaneous waste water flowing down the water supply pipe 1b becomes the inflow pressure required for the ultrafiltration membrane device 3 to function. In this way, the miscellaneous wastewater is filtered to be gray water by the water head pressure utilizing the height difference H acting as an inflow pressure to the ultrafiltration membrane device 3. Middle water is stored in a storage tank 4 such as an underfloor pit of a building through a water pipe 1c. The stored once stored water is sent to a necessary place on each floor of the building through the water supply pipe 1d via the water supply pump 5, and is used for flush toilets, air-conditioning makeup water, water sprinkling, etc. at any time.
In addition, when there is more inflowing effluent than the amount of water sent to the ultrafiltration membrane device 3 in the effluent drainage adjustment tank 2, it is drained by that amount through the drainage pipe 2a, and is also regenerated by the ultrafiltration membrane device 3. When the amount of water exceeds the amount of water sent to the storage tank 4, the water is drained through the drain pipe 2b. In addition, the upper floor of the gray water control tank 2 and the lower floor of the ultrafiltration membrane device 3 as installation locations are selected from other high and low places of the building as long as the required height difference is obtained. But it's okay.

【0009】[0009]

【発明の効果】本発明によれば、雑排水調整槽と限外濾
過膜装置との水頭差により、限外濾過膜装置への必要な
流入圧を生じさせ、従来のように循環加圧ポンプを使用
しないため、循環加圧ポンプのモーターの発熱による循
環水の温度上昇要因がなくなり、濾過により再処理され
てできた中水の臭気の発生を解消することができる。さ
らに、循環加圧ポンプを用いない分、システムが簡単に
なりメンテナンスが容易になる。
According to the present invention, due to the head difference between the miscellaneous drainage adjusting tank and the ultrafiltration membrane device, a necessary inflow pressure into the ultrafiltration membrane device is generated, and a circulation pressurizing pump is used as in the conventional case. Since the above is not used, there is no factor for raising the temperature of the circulating water due to the heat generation of the motor of the circulating pressurizing pump, and it is possible to eliminate the generation of the odor of tap water that is reprocessed by filtration. Further, since the circulation pressurizing pump is not used, the system becomes simple and maintenance becomes easy.

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

【図1】本発明の雑排水の再生処理方法の説明図であ
る。
FIG. 1 is an explanatory view of a method for recycling and processing gray water according to the present invention.

【図2】従来の循環加圧ポンプを用いる雑排水の再生処
理方法の説明図である。
FIG. 2 is an explanatory diagram of a method for regenerating and treating gray water using a conventional circulation pressurizing pump.

【符号の説明】[Explanation of symbols]

2 雑排水調整槽 3 限外濾過膜装置 H 雑排水調整槽と限外濾過膜装置の設置高低差 2 Miscellaneous wastewater adjusting tank 3 Ultrafiltration membrane device H Installation height difference between the miscellaneous drainage adjusting tank and ultrafiltration membrane device

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 雑排水を限外濾過膜装置に通して中水を
造水する雑排水の再生処理方法において、雑排水の流れ
込む雑排水調整槽を建築物の上層階に設置し、雑排水調
整槽と送水管により結ばれた限外濾過膜装置を雑排水調
整槽の設置場所より下層階に設置し、雑排水調整槽から
水頭圧を利用して雑排水を限外濾過膜装置へ流し濾過さ
せることを特徴とする雑排水の再生処理方法。
1. A method of reclaiming gray water by passing gray water through an ultrafiltration membrane device to produce gray water, wherein a gray water adjusting tank, into which gray water flows, is installed on an upper floor of a building. Install the ultrafiltration membrane device connected by the adjustment tank and the water supply pipe on the lower floor from the place where the miscellaneous drainage adjustment tank is installed, and use the head pressure from the miscellaneous drainage adjustment tank to flow the miscellaneous wastewater to the ultrafiltration membrane device. A method for reclaiming gray water, which comprises filtering.
JP14821392A 1992-05-14 1992-05-14 Regeneration treatment of general waste water Pending JPH05317856A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14821392A JPH05317856A (en) 1992-05-14 1992-05-14 Regeneration treatment of general waste water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14821392A JPH05317856A (en) 1992-05-14 1992-05-14 Regeneration treatment of general waste water

Publications (1)

Publication Number Publication Date
JPH05317856A true JPH05317856A (en) 1993-12-03

Family

ID=15447804

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14821392A Pending JPH05317856A (en) 1992-05-14 1992-05-14 Regeneration treatment of general waste water

Country Status (1)

Country Link
JP (1) JPH05317856A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019221271A1 (en) * 2018-05-18 2019-11-21 パナソニックIpマネジメント株式会社 Water discharge system
JP2019199775A (en) * 2018-05-18 2019-11-21 パナソニックIpマネジメント株式会社 Drainage system
JP2019218769A (en) * 2018-06-21 2019-12-26 パナソニックIpマネジメント株式会社 Drainage system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019221271A1 (en) * 2018-05-18 2019-11-21 パナソニックIpマネジメント株式会社 Water discharge system
JP2019199775A (en) * 2018-05-18 2019-11-21 パナソニックIpマネジメント株式会社 Drainage system
JP2019218769A (en) * 2018-06-21 2019-12-26 パナソニックIpマネジメント株式会社 Drainage system

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