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JPH10192853A - Waste water treatment apparatus, membrane filter apparatus therefor and membrane filter method - Google Patents

Waste water treatment apparatus, membrane filter apparatus therefor and membrane filter method

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Publication number
JPH10192853A
JPH10192853A JP156297A JP156297A JPH10192853A JP H10192853 A JPH10192853 A JP H10192853A JP 156297 A JP156297 A JP 156297A JP 156297 A JP156297 A JP 156297A JP H10192853 A JPH10192853 A JP H10192853A
Authority
JP
Japan
Prior art keywords
membrane
raw water
filtration
wastewater treatment
heat
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.)
Withdrawn
Application number
JP156297A
Other languages
Japanese (ja)
Inventor
Kenichiro Mizuno
健一郎 水野
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP156297A priority Critical patent/JPH10192853A/en
Publication of JPH10192853A publication Critical patent/JPH10192853A/en
Withdrawn legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To provide a waste water treatment apparatus capable of reducing water cleaning treatment cost by reducing operation cost by reducing membrane filter differential pressure. SOLUTION: Waste water from a water treatment plant is once stored in a conditioning basin 1 to be supplied to a raw water tank 3 subjecting waste water to sedimentation treatment to discharge the same and the treated water of the raw water tank 3 is supplied to a membrane filter apparatus 5 constituted of a precise filter membrane, and ultrafiltration filter membrane or a reverse osmosis membrane to be filtered. At this time, the waste heat from an independent power plant 12 is supplied to a heat transfer pipe or wall 13 provided to the raw water tank 3 and the raw water in the raw water tank 3 is heated to be lowered in its viscosity to reduce the load of a membrane filter pump 4.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、浄水場から発生す
る砂ろ過逆洗排水等の汚泥水を処理する排水処理装置に
関し、その排水処理装置用の膜ろ過装置及びその膜ろ過
方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a wastewater treatment apparatus for treating sludge water such as sand filtration backwash wastewater generated from a water purification plant, and more particularly to a membrane filtration apparatus for the wastewater treatment apparatus and a membrane filtration method therefor. is there.

【0002】[0002]

【従来の技術】図4は、従来の膜ろ過膜を用いた排水処
理装置を示す図である。浄水場の砂ろ過逆洗排水及び凝
集沈殿池からの引き抜き汚泥等は、図4に示す調整池1
に導かれる。この調整池1に導かれた汚泥水は、ろ過膜
による排水処理装置によって処理されている。調整池1
内の排水は、排水ポンプ2によって原水槽3へと供給さ
れる。そして、原水槽3の原水は、膜ろ過ポンプ4によ
って膜モジュール5に送られてろ過される。このときの
膜ろ過流量は、定流量弁6によって定流量ろ過運転され
ている。膜ろ過を連続して行うと、膜表面に次第に濁質
成分が堆積して、膜差圧が上昇する。その差圧上昇は差
圧計7で計測し、差圧計7が100KPa程度に達した
場合、膜ろ過ポンプ4を停止して、弁8を開いて膜ろ過
側から圧力空気を導入して、膜表面に堆積している濁質
成分を剥離している。その後、弁8を閉じて圧力空気の
供給を遮断し、弁9を開き、膜ろ過ポンプ4を運転する
ことで膜モジュール5内の濁質水は、フラッシュタンク
10に供給されて、凝縮されて原水槽3に戻される。原
水槽3の下部に堆積した汚泥は、連続的に、もしくは適
時、原水槽3の下部に設置した弁11を開くことによっ
て、引き抜かれる。
2. Description of the Related Art FIG. 4 is a diagram showing a conventional wastewater treatment apparatus using a membrane filtration membrane. The sand filtration backwash wastewater from the water treatment plant and the sludge drawn out from the coagulation sedimentation basin are supplied to the regulating pond 1 shown in FIG.
It is led to. Sludge water guided to the regulating pond 1 is treated by a wastewater treatment device using a filtration membrane. Regulating pond 1
The drainage inside is supplied to the raw water tank 3 by the drainage pump 2. The raw water in the raw water tank 3 is sent to the membrane module 5 by the membrane filtration pump 4 and is filtered. The membrane filtration flow rate at this time is a constant flow filtration operation by the constant flow valve 6. When membrane filtration is performed continuously, turbid components gradually accumulate on the membrane surface, and the membrane pressure difference increases. The differential pressure rise is measured by the differential pressure gauge 7, and when the differential pressure gauge 7 reaches about 100 KPa, the membrane filtration pump 4 is stopped, the valve 8 is opened, and pressurized air is introduced from the membrane filtration side. The turbid components deposited on the surface are peeled off. Thereafter, the valve 8 is closed to shut off the supply of the pressurized air, the valve 9 is opened, and the turbid water in the membrane module 5 is supplied to the flash tank 10 by operating the membrane filtration pump 4 to be condensed. It is returned to the raw water tank 3. The sludge deposited at the lower part of the raw water tank 3 is pulled out continuously or at an appropriate time by opening the valve 11 installed at the lower part of the raw water tank 3.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、浄水場
において発生する排水を膜を用いて定流束でろ過処理す
る場合、冬期における膜差圧は夏季におけるそれよりも
高くなる。その結果、膜モジュール5の差圧が高くなる
ので、膜ろ過ポンプ4の負荷が大きくなり、電力消費が
増し、浄水処理のコストを高騰させる要因となる。
However, when the wastewater generated in the water purification plant is filtered at a constant flux using a membrane, the membrane differential pressure in winter becomes higher than that in summer. As a result, the differential pressure of the membrane module 5 increases, which increases the load on the membrane filtration pump 4, increases power consumption, and increases the cost of water purification treatment.

【0004】冬期では、膜モジュール5の差圧が高くな
り、膜ろ過ポンプ4の負荷が大きくなり、電力消費が増
加する。この原因は、冬期における膜ろ過水水温が夏季
のそれに較べて低いことによって、冬期の処理水の粘度
が大きくなるためである。一般に、膜ろ過流束と膜差圧
との関係は、(1)式によつて表すことができる。
In winter, the differential pressure of the membrane module 5 increases, the load on the membrane filtration pump 4 increases, and power consumption increases. This is because the viscosity of the treated water in winter increases because the temperature of the membrane filtration water in winter is lower than that in summer. Generally, the relationship between the membrane filtration flux and the membrane differential pressure can be expressed by equation (1).

【0005】 ΔP=Jv ・μ/K …………(1)ΔP = Jv · μ / K (1)

【0006】ΔP:膜差圧[KPa]、 Jv:膜ろ過
流束[m/日] μ:水の粘度[Pa・s]、 K :膜モジュール定数
ΔP: Membrane differential pressure [KPa], Jv: Membrane filtration flux [m / day] μ: Water viscosity [Pa · s], K: Membrane module constant

【0007】水の粘度は温度により変化する。水温が2
7℃程度となる夏場では、水の粘度が854[μPa・
s]、水温が7℃程度となる冬場では、水の粘度が14
35[μPa・s]となる。すなわち、等流束で膜ろ過
を行う場合、水温が低い冬場は、水温が高い夏場に較べ
て、膜差圧は約1.7倍となる。従って、冬場では、膜
ろ過ポンプの動力費が高くなり、浄水コストが上昇する
という問題があった。
[0007] The viscosity of water changes with temperature. Water temperature is 2
In summer, when the temperature is about 7 ° C, the viscosity of water is 854 [μPa ·
s], in winter when the water temperature is about 7 ° C.,
35 [μPa · s]. That is, when membrane filtration is performed at a uniform flux, the membrane differential pressure is about 1.7 times higher in winter when the water temperature is low than in summer when the water temperature is high. Therefore, in winter, there is a problem that the power cost of the membrane filtration pump is increased and the cost of water purification is increased.

【0008】本発明は、上記のような課題に鑑みなされ
たものであり、膜ろ過差圧を低減することで、運転費を
低減して、浄水処理コストを低減できる排水処理装置、
膜ろ過装置及びその膜ろ過方法を提供することを目的と
する。
[0008] The present invention has been made in view of the above problems, and a wastewater treatment apparatus capable of reducing the operation cost and the water purification treatment cost by reducing the membrane filtration differential pressure.
An object of the present invention is to provide a membrane filtration device and a membrane filtration method thereof.

【0009】[0009]

【課題を解決するための手段】本発明は、上記課題を達
成するためになされたものであり、請求項1の発明のろ
過膜を用いた排水処理装置において、自家発電機からの
排熱を熱源として、原水を加温し、精密ろ過膜、限外ろ
過膜もしくは逆浸透膜によってろ過処理することを特徴
とし、この発明では、膜ろ過処理する際に、原水を加温
することにより、膜ろ過差圧を低減することができる排
水処理装置である。
SUMMARY OF THE INVENTION The present invention has been made to achieve the above object, and in the wastewater treatment apparatus using the filtration membrane according to the first aspect of the present invention, waste heat from a private power generator is removed. As a heat source, the raw water is heated, and is characterized by being subjected to filtration by a microfiltration membrane, an ultrafiltration membrane or a reverse osmosis membrane. This is a wastewater treatment device capable of reducing the filtration pressure difference.

【0010】また、請求項2の発明のろ過膜を用いた排
水処理装置において、自家発電機からの排熱によって、
原水を加温するための熱交換手段を備える原水槽と、前
記原水槽から送られる加温された原水を、精密ろ過膜、
限外ろ過膜もしくは逆浸透膜によって、ろ過処理するろ
過装置と、を具備することを特徴とし、この発明では、
原水槽に自家発電機の排熱を熱源とする熱交換手段を備
えることによって、原水槽中の原水を加温することによ
り、膜ろ過差圧を低減することができる排水処理装置で
ある。
Further, in the wastewater treatment apparatus using the filtration membrane according to the second aspect of the present invention, the waste heat from the private power generator
A raw water tank provided with a heat exchange means for heating the raw water, and a heated raw water sent from the raw water tank, a microfiltration membrane,
With an ultrafiltration membrane or a reverse osmosis membrane, a filtration device for performing a filtration treatment, characterized in that, in the present invention,
This is a wastewater treatment apparatus capable of reducing the membrane filtration differential pressure by heating the raw water in the raw water tank by providing the raw water tank with heat exchange means using the exhaust heat of the private power generator as a heat source.

【0011】また、請求項3の発明のろ過膜を用いた排
水処理装置において、原水槽と、精密ろ過膜、限外ろ過
膜もしくは逆浸透膜によって構成され、前記自家発電機
からの排熱を熱源とする熱交換手段によって、前記原水
槽から送られる原水を加温して、ろ過処理する膜ろ過装
置と、を具備することを特徴とし、この発明では、膜ろ
過装置に自家発電機からの排熱を熱源とする熱交換手段
を具備することで、原水を加温することにより、膜ろ過
差圧を低減することができる排水処理装置である。
Further, in the wastewater treatment apparatus using the filtration membrane according to the third aspect of the present invention, the wastewater treatment apparatus includes a raw water tank, a microfiltration membrane, an ultrafiltration membrane, or a reverse osmosis membrane, and discharges waste heat from the private power generator. A heat exchange unit as a heat source, which heats the raw water sent from the raw water tank, and performs a filtration process; and in the present invention, the membrane filtration device is provided with a private generator. The wastewater treatment apparatus is provided with a heat exchange means using waste heat as a heat source, thereby heating raw water to reduce a membrane filtration differential pressure.

【0012】また、請求項4の発明の排水処理装置は、
請求項2または3に記載された発明において、前記熱交
換手段は、原水槽内もしくはろ過膜内に設置した伝熱管
もしくは伝熱壁に、前記自家発電機の冷却系からの蒸気
と温水または排ガスを排熱ボイラに導いて得られる蒸気
の少なくとも一つを選択して供給もしくは循環させるこ
とを特徴とし、この発明では、自家発電機の冷却系から
の蒸気や温水を、伝熱管もしくは伝熱壁内に循環させる
ことで、原水を加温することにより、膜ろ過差圧を低減
することができる排水処理装置である。
Further, the wastewater treatment apparatus of the invention according to claim 4 is:
The invention according to claim 2 or 3, wherein the heat exchanging means comprises a heat transfer pipe or a heat transfer wall installed in a raw water tank or a filtration membrane, and steam and hot water or exhaust gas from a cooling system of the private power generator. Is supplied to a waste heat boiler, and at least one of the obtained steam is selected and supplied or circulated. In the present invention, steam or hot water from a cooling system of a private generator is transferred to a heat transfer tube or a heat transfer wall. This is a wastewater treatment apparatus that can reduce the membrane filtration differential pressure by heating raw water by circulating it inside.

【0013】また、請求項5の発明の排水処理装置で
は、請求項1、2または3記載の発明において、前記自
家発電機は、都市ガスや重油等を燃料としたディーゼル
エンジン、ガスエンジンおよびガスタービン等の自家発
電機から発生する排熱であることを特徴とし、この発明
では、冷却水系からの排熱が容易に熱交換手段に循環で
きる排熱処理装置である。
According to a fifth aspect of the present invention, there is provided the wastewater treatment apparatus according to the first, second or third aspect, wherein the private power generator is a diesel engine, a gas engine and a gas engine using city gas, heavy oil or the like as fuel. The present invention is a waste heat treatment apparatus characterized in that the waste heat is generated from a private power generator such as a turbine, and the waste heat from a cooling water system can be easily circulated to a heat exchange unit.

【0014】また、請求項6の発明の精密ろ過膜、限外
ろ過膜もしくは逆浸透膜を用いた膜ろ過方法において、
自家発電機からの排熱を熱源とし、前記ろ過膜における
原水を加温して前記ろ過膜によってろ過することを特徴
とし、この発明では、原水の温度を上昇させることがで
きるので、ろ過膜差圧を低減することができる膜ろ過方
法である。
[0014] In the membrane filtration method using a microfiltration membrane, an ultrafiltration membrane or a reverse osmosis membrane according to the invention of claim 6,
The waste heat from the private power generator is used as a heat source, and the raw water in the filtration membrane is heated and filtered by the filtration membrane.In the present invention, the temperature of the raw water can be increased, so that the filtration membrane difference is increased. This is a membrane filtration method capable of reducing pressure.

【0015】また、請求項7の発明の膜ろ過方法は、請
求項6に記載の膜ろ過方法において、前記排熱は、前記
自家発電機の冷却水系からの蒸気もしくは温水、前記自
家発電機の排ガスを排熱ボイラに導いて製造した蒸気で
あって、これらのいずれか少なくとも1つ、または併用
して熱源とすることを特徴とし、この発明では、自家発
電機と熱交換機との作用を互いに利用した膜ろ過方法で
ある。
According to a seventh aspect of the present invention, there is provided the membrane filtration method according to the sixth aspect, wherein the waste heat is steam or hot water from a cooling water system of the private power generator, Steam produced by directing exhaust gas to a waste heat boiler, characterized in that at least one of these or a combination thereof is used as a heat source. In the present invention, the action of the private power generator and the action of the heat exchanger are mutually This is a membrane filtration method used.

【0016】また、請求項8の発明は、精密ろ過膜、限
外ろ過膜もしくは逆浸透膜によって構成された排水処理
装置用膜ろ過装置において、前記膜ろ過装置の処理水が
供給される側に伝熱管または伝熱壁を備えることを特徴
とし、この発明では、浄水場の汚泥水を処理する排水処
理装置用膜ろ過装置であり、低温時の処理水を加温して
ろ過することができる。
Further, the invention according to claim 8 is a membrane filtration device for a wastewater treatment device comprising a microfiltration membrane, an ultrafiltration membrane or a reverse osmosis membrane, wherein the membrane filtration device is provided on the side where treated water is supplied. The present invention is characterized by having a heat transfer tube or a heat transfer wall, and in the present invention, a membrane filtration device for a wastewater treatment device for treating sludge water in a water purification plant, which can heat and filter treated water at a low temperature. .

【0017】[0017]

【発明の実施の形態】以下、本発明の排水処理装置、排
水処理装置用膜ろ過装置及びその膜ろ過方に関する実施
の形態について、図面を参照して説明する。図1は、本
発明の排水処理装置の一実施形態であり、この排水処理
装置は、浄水場にて発生する砂ろ過逆洗排水及び凝集沈
殿池等からの引き抜き汚泥等が調整池1に導かれ、この
排水をろ過膜で処理する装置である。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a perspective view of a wastewater treatment apparatus according to a first embodiment of the present invention; FIG. 1 shows an embodiment of a wastewater treatment apparatus according to the present invention. In this wastewater treatment apparatus, sand filtration backwash wastewater generated in a water purification plant and sludge drawn out from a coagulation sedimentation tank and the like are guided to a regulating pond 1. It is a device that treats this wastewater with a filtration membrane.

【0018】同図において、排水処理装置は、調整池1
からの排水が排水ポンプ2で供給され、汚泥を濃縮して
排出する原水槽3と、原水槽3からの排水を膜ろ過ポン
プ4から供給される膜モジュール(膜ろ過装置)5と、
逆洗浄工程において、膜ろ過装置5の汚濁水側5aに接
続された配管に設けられた弁9を介してろ過膜に付着す
る汚濁物質供給して凝縮した汚泥とするフラッシュタン
ク10とが備えられ、膜ろ過装置5には、圧力空気をろ
過水側5bに供給するための弁8が設けられ、膜ろ過水
を取り出す定流量弁6が設けられている。膜ろ過装置5
の汚濁水側5aとろ過水側5bの圧力を計測する圧力セ
ンサが設けられ、それらの圧力センサの出力の差を検出
する差圧計7が設けられている。原水槽3には、伝熱管
または伝熱壁13が設けられ、伝熱管または伝熱壁13
がガスエンジン等の自家発電機12のジャケット冷却系
12aと配管で接続されている。自家発電機12の排ガ
スは、排熱ボイラ14に導かれている。膜ろ過装置5
は、排水を精密ろ過膜(以下、MF膜と記す)、限外ろ
過膜(以下、UF膜と記す)もしくは逆浸透膜(以下、
RO膜と記す)によって膜ろ過処理する装置である。
In FIG. 1, a wastewater treatment device is a regulating pond 1.
A raw water tank 3 for supplying wastewater from the raw water tank 2 to condense and discharge sludge, a membrane module (membrane filtration device) 5 for supplying wastewater from the raw water tank 3 from a membrane filtration pump 4,
In the back washing step, there is provided a flash tank 10 which supplies polluting substances adhering to the filtration membrane through a valve 9 provided in a pipe connected to the polluted water side 5a of the membrane filtration device 5 to make condensed sludge. The membrane filtration device 5 is provided with a valve 8 for supplying pressurized air to the filtered water side 5b, and a constant flow valve 6 for taking out the membrane filtered water. Membrane filtration device 5
A pressure sensor for measuring the pressure on the polluted water side 5a and the filtered water side 5b is provided, and a differential pressure gauge 7 for detecting a difference between the outputs of the pressure sensors is provided. The raw water tank 3 is provided with a heat transfer tube or a heat transfer wall 13.
Is connected by a pipe to a jacket cooling system 12a of a private generator 12 such as a gas engine. The exhaust gas from the private generator 12 is guided to a waste heat boiler 14. Membrane filtration device 5
Refers to wastewater with a microfiltration membrane (hereinafter referred to as MF membrane), ultrafiltration membrane (hereinafter referred to as UF membrane) or reverse osmosis membrane (hereinafter referred to as MF membrane)
RO membrane).

【0019】本実施形態の排水処理装置の排水処理は、
浄水場から汚泥を含む排水は、調整池1に送られる。調
整池1内の排水(原水)は、排水ポンプ2によつて原水
槽3へと供給され、原水槽3で加温された原水は膜ろ過
ポンプ4を介してろ過膜装置5の汚濁水側5aに供給さ
れる。原水、ろ過膜でろ過されたろ過水が定流量弁6を
介して得られる。また、膜ろ過装置5は、ろ過膜の逆洗
浄時に、弁8を介して圧力空気がろ過水側5bに供給さ
れ、ろ過膜に付着した汚濁物質が剥離して、弁9を介し
て、フラッシュタンク10に供給されて凝縮され、原水
槽3へと処理水が送られる。
The wastewater treatment of the wastewater treatment apparatus of the present embodiment is as follows.
Wastewater containing sludge from the water treatment plant is sent to the regulating pond 1. The drainage (raw water) in the regulating pond 1 is supplied to the raw water tank 3 by the drain pump 2, and the raw water heated in the raw water tank 3 is passed through the membrane filtration pump 4 to the polluted water side of the filtration membrane device 5. 5a. Raw water and filtered water filtered by a filtration membrane are obtained through a constant flow valve 6. Further, in the membrane filtration device 5, at the time of back washing of the filtration membrane, the pressurized air is supplied to the filtration water side 5 b via the valve 8, the contaminants adhering to the filtration membrane are separated, and the membrane is flushed via the valve 9. The water is supplied to the tank 10, condensed, and the treated water is sent to the raw water tank 3.

【0020】この浄水場で使用される自家発電機12
は、都市ガスを燃料とするガスエンジンであり、その電
力を浄水場内のポンプ等の電力として用いると共に、ガ
スエンジンから排出される約600℃の燃焼排ガスが廃
熱ポイラ14に導かれ、7kg/cm2 程度の高圧蒸気
を製造して汚泥の乾燥用熱源として利用する。更に、ガ
スエンジンの自家発電機12のジャケット冷却系12a
で9℃の水から1Kgcm2 の低圧蒸気を製造し、低圧
蒸気を伝熱管13へ導き、そこで90℃の水に戻るまで
冷却されて、再び自家発電機12へと循環させつつ、膜
ろ過ポンプ4によって原水槽3内の排水が膜ろ過装置5
でろ過される。
The private power generator 12 used in this water purification plant
Is a gas engine using city gas as a fuel. The electric power is used as electric power for a pump and the like in a water purification plant, and a combustion exhaust gas of about 600 ° C. discharged from the gas engine is guided to a waste heat poirer 14 to generate 7 kg / High pressure steam of about 2 cm2 is produced and used as a heat source for drying sludge. Furthermore, the jacket cooling system 12a of the private generator 12 of the gas engine
Produces low-pressure steam of 1 Kgcm 2 from water at 9 ° C., guides the low-pressure steam to the heat transfer tube 13, where it is cooled until it returns to water at 90 ° C. The wastewater in the raw water tank 3 is changed by the membrane filtration device 5
Filtered.

【0021】このときの膜ろ過流量は、定流量弁7によ
って定流量ろ過運転となる。膜ろ過を連続して行うと、
膜表面に濁質成分が堆積することによって膜差圧が上昇
し、その差圧上昇を差圧計7で検出する。差圧計7が1
00KPa程度に達した場合、膜ろ過ポンプ4を停止
し、弁8を開いて膜ろ過側から圧力空気を導入すること
によって、膜表面に堆積している濁質成分を膜表面から
剥離させた後、弁8を閉じ、さらに弁9を開き、膜ろ過
ポンプ4を運転することでろ過膜装置5内の汚濁水をフ
ラッシュタンク10を通過させた後、原水槽3に供給す
る。原水槽3の下部に堆積した汚泥は連続もしくは適
時、原水槽3の下部に設置した弁11を開くことによっ
て引き抜かれる。
At this time, the membrane filtration flow rate is set to a constant flow filtration operation by the constant flow valve 7. When performing membrane filtration continuously,
As the turbid component accumulates on the membrane surface, the membrane differential pressure increases, and the increase in the differential pressure is detected by the differential pressure gauge 7. Differential pressure gauge 7 is 1
When the pressure reaches about 00 KPa, the membrane filtration pump 4 is stopped, the valve 8 is opened, and pressurized air is introduced from the membrane filtration side to separate the turbid component deposited on the membrane surface from the membrane surface. Then, the valve 8 is closed, the valve 9 is opened, and the membrane filtration pump 4 is operated so that the contaminated water in the filtration membrane device 5 is passed through the flash tank 10 and then supplied to the raw water tank 3. Sludge deposited at the lower part of the raw water tank 3 is pulled out continuously or at an appropriate time by opening the valve 11 installed at the lower part of the raw water tank 3.

【0022】常用発電ブロセスにおける自家発電機から
発生する排熱を排水を膜ろ過処理する装置に供給し、膜
ろ過水を加温することによって、原水の粘性を低下させ
て、膜ろ過装置の膜ろ過ポンプの動力費を低減できる。
これによって、自家発電機を用いた常用発電ブロセスに
おける熱電利用効率が高くなり、その結果、常用発電ブ
ロセスを行うことによる運転費低減が図られ、それに伴
って、浄水費用も低減される。
The waste heat generated from the private power generator in the commercial power generation process is supplied to a device for performing membrane filtration of waste water, and the membrane filtered water is heated to lower the viscosity of the raw water, thereby reducing the viscosity of the membrane filtration device. The power cost of the filtration pump can be reduced.
As a result, the efficiency of using thermoelectric power in the regular power generation process using the private power generator is increased. As a result, the operation cost is reduced by performing the regular power generation process, and the cost of water purification is reduced accordingly.

【0023】また、都市ガスや重油等を燃料としたディ
ーゼルエンジン、ガスエンジン及びガスタービン等の自
家発電機の少なくとも一部を常時稼働させることで発電
を行いながら、自家発電機から発生する排熱を原水の加
温に利用する。熱の回収方法は、自家発電機12のジャ
ケット冷却水系12aから低圧蒸気もしくは温水、自家
発電機12からの排ガスを排熱ポイラ14に導き蒸気、
及び自家発電機12からの排ガスを直接熱源として利用
する法があり、それらの一つの熱源あるいは併用して熱
源として利用する。
In addition, while at least part of a private generator such as a diesel engine, a gas engine, and a gas turbine using city gas or heavy oil as fuel is constantly operated to generate power, waste heat generated from the private generator is generated. Is used to heat the raw water. The heat recovery method is as follows: low-pressure steam or hot water from the jacket cooling water system 12a of the private power generator 12, exhaust gas from the private power generator 12 to the exhaust heat
In addition, there is a method in which the exhaust gas from the private power generator 12 is directly used as a heat source, and one of these heat sources or a combination thereof is used as a heat source.

【0024】次に、本発明の他の実施形態である排水処
理装置について、図2を参照して説明する。上記実施形
態では、伝熱管または伝熱壁13が原水槽3に設けられ
ていたが、本実施形態では、ろ過膜装置5の汚濁水側5
aに設けられている。自家発電機12のジャケット冷却
系12aに接続された配管は、伝熱管または伝熱壁13
に接続され、排ガスを排熱ボイラ14に供給され、排熱
ボイラ14の高圧蒸気が汚泥の乾燥に用いられる。他の
構成は、図1の実施形態と同様であるのでその構成の説
明は省略する。
Next, a waste water treatment apparatus according to another embodiment of the present invention will be described with reference to FIG. In the above embodiment, the heat transfer tube or the heat transfer wall 13 is provided in the raw water tank 3. However, in the present embodiment, the contaminated water side 5 of the filtration membrane device 5 is provided.
a. The pipe connected to the jacket cooling system 12 a of the private generator 12 is a heat transfer pipe or a heat transfer wall 13.
The exhaust gas is supplied to the waste heat boiler 14, and the high pressure steam of the waste heat boiler 14 is used for drying sludge. The other configuration is the same as that of the embodiment of FIG. 1, and the description of the configuration is omitted.

【0025】また、本発明の他の実施形態である排水処
理装置について、図3を参照して説明する。図3の実施
形態は、排熱ボイラ14からの排ガスを、原水槽3に直
接供給して利用している。他の構成は、図2の実施形態
と同様であるのでその説明は省略する。
A waste water treatment apparatus according to another embodiment of the present invention will be described with reference to FIG. In the embodiment of FIG. 3, the exhaust gas from the waste heat boiler 14 is directly supplied to the raw water tank 3 for use. Other configurations are the same as those of the embodiment of FIG.

【0026】上記のように、本実施形態では、都市ガス
や重油等を燃料としたディーゼルエンジン、ガスエンジ
ン及びガスタ一ビン等の自家発電機を稼働させることで
発電を行い、浄水場の動力として用い、その自家発電機
から発生する排熱を、原水槽や膜ろ過装置の熱源として
用いる。膜ろ過装置に供給される原水を加温して、膜ろ
過装置に供給することで、原水の粘性を低下させること
で、排水処理を行う排水処理装置である。
As described above, in the present embodiment, power is generated by operating a private generator such as a diesel engine, a gas engine, and a gas turbine using city gas or heavy oil as fuel, and is used as power for a water purification plant. Waste heat generated from the private power generator is used as a heat source for a raw water tank and a membrane filtration device. The wastewater treatment apparatus performs a wastewater treatment by heating raw water supplied to the membrane filtration apparatus and supplying the heated raw water to the membrane filtration apparatus to reduce the viscosity of the raw water.

【0027】また、自家発電機からの排熱の回収方法と
しては、エンジンの冷却水系から蒸気もしくは温水を製
造する方法、自家発電機からの排ガスを排熱ボイラに導
き蒸気を製造する方法、自家発電機からの排ガスを直接
熱源とする方法を単独あるいは併用する方法がなされ
る。従って、自家発電機に隣接して、原水槽や膜ろ過装
置を設置すると排熱を有効に利用できる利点がある。
As a method of recovering exhaust heat from the private generator, a method of producing steam or hot water from a cooling water system of an engine, a method of producing steam by introducing exhaust gas from a private generator to a waste heat boiler, A method of using exhaust gas from a generator directly as a heat source may be used alone or in combination. Therefore, if a raw water tank and a membrane filtration device are installed adjacent to the private power generator, there is an advantage that the waste heat can be effectively used.

【0028】[0028]

【発明の効果】以上記載したように、本発明によれば、
自家発電機による常用発電装置から発生する排熱によっ
て、排水を加温して膜ろ過装置に供給するか、膜ろ過装
置内で加温する構成としたので、排水処理装置の運転費
が低減できる効果を有するとともに、浄水コストを低減
できる効果をも有する。
As described above, according to the present invention,
The waste heat generated by the private power generator using the private power generator heats the wastewater and supplies it to the membrane filtration device, or heats the wastewater in the membrane filtration device, so that the operating cost of the wastewater treatment device can be reduced. It has the effect and also has the effect of reducing the cost of water purification.

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

【図1】本発明の水処理装置の一実施形態を示す図であ
る。
FIG. 1 is a diagram showing one embodiment of a water treatment apparatus of the present invention.

【図2】本発明の水処理装置の一実施形態を示す図であ
る。
FIG. 2 is a diagram showing an embodiment of the water treatment apparatus of the present invention.

【図3】本発明の水処理装置の一実施形態を示す図であ
る。
FIG. 3 is a diagram showing an embodiment of the water treatment apparatus of the present invention.

【図4】従来の水処理装置の一例を示す図である。FIG. 4 is a diagram showing an example of a conventional water treatment device.

【符号の説明】[Explanation of symbols]

1 調整池 2 排水ポンプ 3 原水槽 4 膜ろ過ポンプ 5 膜モジュール 5a 汚泥水供給側 5b ろ過水側 6 定流量弁 7 差圧計 8、9 弁 10 フラッシュタンク 11 弁 12 自家発電機 13 伝熱管 14 排熱ボイラ DESCRIPTION OF SYMBOLS 1 Regulating pond 2 Drain pump 3 Raw water tank 4 Membrane filtration pump 5 Membrane module 5a Sludge water supply side 5b Filtration water side 6 Constant flow valve 7 Differential pressure gauge 8, 9 valve 10 Flash tank 11 valve 12 Private power generator 13 Heat transfer pipe 14 Discharge Heat boiler

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】 ろ過膜を用いた排水処理装置において、 自家発電機からの排熱を熱源として、原水を加温し、精
密ろ過膜、限外ろ過膜もしくは逆浸透膜によってろ過処
理することを特徴とする排水処理装置。
1. A wastewater treatment apparatus using a filtration membrane, wherein the raw water is heated using waste heat from a private power generator as a heat source, and the wastewater is filtered through a microfiltration membrane, an ultrafiltration membrane, or a reverse osmosis membrane. Characterized wastewater treatment equipment.
【請求項2】 ろ過膜を用いた排水処理装置において、 自家発電機からの排熱によって、原水を加温するための
熱交換手段を備える原水槽と、 前記原水槽から送られる加温された原水を、精密ろ過
膜、限外ろ過膜もしくは逆浸透膜によって、ろ過処理す
る膜ろ過装置と、を具備することを特徴とする排水処理
装置。
2. A wastewater treatment apparatus using a filtration membrane, comprising: a raw water tank provided with heat exchange means for heating raw water by waste heat from a private power generator; and a heated water sent from the raw water tank. A wastewater treatment device comprising: a membrane filtration device for filtering raw water with a microfiltration membrane, an ultrafiltration membrane, or a reverse osmosis membrane.
【請求項3】 ろ過膜を用いた排水処理装置において、 原水槽と、 精密ろ過膜、限外ろ過膜もしくは逆浸透膜によって構成
され、自家発電機からの排熱を熱源とする熱交換手段に
よって、前記原水槽から送られる原水を加温して、ろ過
処理する膜ろ過装置と、を具備することを特徴とする排
水処理装置。
3. A wastewater treatment apparatus using a filtration membrane, comprising: a raw water tank, a microfiltration membrane, an ultrafiltration membrane, or a reverse osmosis membrane, and heat exchange means using heat exhausted from a private generator as a heat source. And a membrane filtration device for heating and filtering the raw water sent from the raw water tank.
【請求項4】 請求項2または3に記載された排水処理
装置において、 前記熱交換手段は、原水槽内もしくはろ過膜内に設置し
た伝熱管もしくは伝熱壁に、前記自家発電機の冷却系か
らの蒸気と温水または排ガスを排熱ボイラに導いて得ら
れる蒸気の少なくとも一つを選択して供給もしくは循環
させることを特徴とする排水処理装置。
4. The wastewater treatment apparatus according to claim 2, wherein the heat exchange means includes a heat transfer pipe or a heat transfer wall installed in a raw water tank or a filtration membrane, and a cooling system for the private power generator. Waste water treatment apparatus characterized in that at least one of steam obtained by introducing steam and hot water or exhaust gas from a steam to a waste heat boiler is selected and supplied or circulated.
【請求項5】 請求項1、2または3に記載の排水処理
装置において、 前記自家発電機は、都市ガスや重油等を燃料としたディ
ーゼルエンジン、ガスエンジンおよびガスタービン等の
自家発電機から発生する排熱であることを特徴とする排
水処理装置。
5. The wastewater treatment apparatus according to claim 1, wherein the private power generator is generated from a private power generator such as a diesel engine, a gas engine, and a gas turbine using city gas or heavy oil as a fuel. Wastewater treatment equipment characterized by waste heat.
【請求項6】 精密ろ過膜、限外ろ過膜もしくは逆浸透
膜を用いた膜ろ過方法において、 自家発電機からの排熱を熱源とし、前記ろ過膜における
原水を加温して前記ろ過膜によってろ過することを特徴
とする膜ろ過方法。
6. A membrane filtration method using a microfiltration membrane, an ultrafiltration membrane or a reverse osmosis membrane, wherein waste heat from a private power generator is used as a heat source, raw water in the filtration membrane is heated, and A membrane filtration method characterized by performing filtration.
【請求項7】 請求項6に記載の膜ろ過方法において、 前記排熱は、前記自家発電機の冷却水系からの蒸気もし
くは温水、前記自家発電機の排ガスを排熱ボイラに導い
て製造した蒸気であって、これらのいずれか少なくとも
1つ、または併用して熱源とすることを特徴とする膜ろ
過方法。
7. The membrane filtration method according to claim 6, wherein the exhaust heat is steam or hot water from a cooling water system of the private power generator, or steam produced by guiding exhaust gas of the private power generator to a waste heat boiler. Wherein at least one of these or a combination thereof is used as a heat source.
【請求項8】 精密ろ過膜、限外ろ過膜もしくは逆浸透
膜によって構成された排水処理装置用膜ろ過装置におい
て、 前記膜ろ過装置の処理水が供給される側に伝熱管または
伝熱壁を備えることを特徴とする排水処理装置用膜ろ過
装置。
8. A membrane filtration device for a wastewater treatment device comprising a microfiltration membrane, an ultrafiltration membrane or a reverse osmosis membrane, wherein a heat transfer tube or a heat transfer wall is provided on the side of the membrane filtration device to which treated water is supplied. A membrane filtration device for a wastewater treatment device, comprising:
JP156297A 1997-01-08 1997-01-08 Waste water treatment apparatus, membrane filter apparatus therefor and membrane filter method Withdrawn JPH10192853A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP156297A JPH10192853A (en) 1997-01-08 1997-01-08 Waste water treatment apparatus, membrane filter apparatus therefor and membrane filter method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP156297A JPH10192853A (en) 1997-01-08 1997-01-08 Waste water treatment apparatus, membrane filter apparatus therefor and membrane filter method

Publications (1)

Publication Number Publication Date
JPH10192853A true JPH10192853A (en) 1998-07-28

Family

ID=11504973

Family Applications (1)

Application Number Title Priority Date Filing Date
JP156297A Withdrawn JPH10192853A (en) 1997-01-08 1997-01-08 Waste water treatment apparatus, membrane filter apparatus therefor and membrane filter method

Country Status (1)

Country Link
JP (1) JPH10192853A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2820056A1 (en) * 2001-01-31 2002-08-02 Toshiba Kk FILTERING APPARATUS, ASSOCIATED BACKWASHING METHOD, FILTERING DEVICE AND POWER PLANT
US8221628B2 (en) 2010-04-08 2012-07-17 Toyota Motor Engineering & Manufacturing North America, Inc. Method and system to recover waste heat to preheat feed water for a reverse osmosis unit
US8505324B2 (en) 2010-10-25 2013-08-13 Toyota Motor Engineering & Manufacturing North America, Inc. Independent free cooling system
US9314742B2 (en) 2010-03-31 2016-04-19 Toyota Motor Engineering & Manufacturing North America, Inc. Method and system for reverse osmosis predictive maintenance using normalization data

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2820056A1 (en) * 2001-01-31 2002-08-02 Toshiba Kk FILTERING APPARATUS, ASSOCIATED BACKWASHING METHOD, FILTERING DEVICE AND POWER PLANT
US7309424B2 (en) 2001-01-31 2007-12-18 Kabushiki Kaisha Toshiba Filtering apparatus, back wash method therefor, filtering device and power plant
US7754074B2 (en) 2001-01-31 2010-07-13 Kabushiki Kaisha Toshiba Filtering apparatus, back wash method therefor, filtering device and power plant
US9314742B2 (en) 2010-03-31 2016-04-19 Toyota Motor Engineering & Manufacturing North America, Inc. Method and system for reverse osmosis predictive maintenance using normalization data
US8221628B2 (en) 2010-04-08 2012-07-17 Toyota Motor Engineering & Manufacturing North America, Inc. Method and system to recover waste heat to preheat feed water for a reverse osmosis unit
US8505324B2 (en) 2010-10-25 2013-08-13 Toyota Motor Engineering & Manufacturing North America, Inc. Independent free cooling system

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