JPH0871567A - Movable water-purifying facility - Google Patents
Movable water-purifying facilityInfo
- Publication number
- JPH0871567A JPH0871567A JP6208807A JP20880794A JPH0871567A JP H0871567 A JPH0871567 A JP H0871567A JP 6208807 A JP6208807 A JP 6208807A JP 20880794 A JP20880794 A JP 20880794A JP H0871567 A JPH0871567 A JP H0871567A
- Authority
- JP
- Japan
- Prior art keywords
- filter
- water
- coagulant
- mobile
- water purification
- 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.)
- Granted
Links
Landscapes
- Filtration Of Liquid (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
Description
【０００１】[0001]
【産業上の利用分野】本発明は、飲料水供給設備を持た
ない地域、または台風，地震等の災害が発生した被災地
に移動して現地の原水を浄水し、飲料水として供給する
移動式浄水設備に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention is a mobile system which supplies water as drinking water by moving to a region without a drinking water supply facility or a disaster area where a disaster such as a typhoon or an earthquake has occurred to purify raw water locally. It relates to water purification equipment.
【０００２】[0002]
【従来の技術】従来、現地の原水を濾過して飲料水を得
るための移動式浄水装置として、実公昭62−9997号公報
に記載の浄水装置が知られている。この浄水装置は、図
４に示すようにトラック荷台の搭載シェルタ５０内に収
納されており、その構成は、図５に示すように、取水し
た原水に凝集剤を添加する添加装置５１、原水と凝集剤
を混合させた混合水を貯留する貯留タンク５２、その貯
留タンク５２内に浸漬される回転円筒型長毛濾過装置５
３、その回転円筒型長毛濾過装置５３の濾布を通過して
得られた濾過水を滅菌する滅菌室５４、滅菌された濾過
水をさらに浄化する珪藻土濾過装置５５とから構成され
ている。なお、取水ポンプ５６は、原水を取水する際に
別途取り付けられる。上記浄水装置は、主に国内の河川
水，湖沼水を原水として取り込み、濁質を除去して飲料
水を供給することができるようになっている。2. Description of the Related Art Conventionally, as a mobile water purifying apparatus for filtering local raw water to obtain drinking water, a water purifying apparatus described in Japanese Utility Model Publication No. 62-9997 is known. As shown in FIG. 4, this water purification device is housed in a loading shelter 50 of a truck bed, and its configuration is as shown in FIG. 5, an adding device 51 for adding a coagulant to the raw water taken, and raw water. A storage tank 52 for storing mixed water in which a coagulant is mixed, and a rotary cylindrical long-hair filtration device 5 immersed in the storage tank 52.
3, a sterilization chamber 54 for sterilizing the filtered water obtained by passing through the filter cloth of the rotary cylindrical long-haired filtration device 53, and a diatomaceous earth filtration device 55 for further purifying the sterilized filtered water. The water intake pump 56 is separately attached when the raw water is taken. The above-mentioned water purification device can mainly take in domestic river water and lake water as raw water, remove turbidity, and supply drinking water.
【０００３】また、移動式であって濾過膜を利用した浄
水装置としては、図６に示すように、車載型の海水淡水
化逆浸透装置が知られている。この種の浄水装置は、そ
の規模が大きいため、通常、処理機能毎に複数の車両Ａ
〜Ｃに分散して搭載されており、前処理を行う車両Ａに
は取水ポンプ６０から取水した原水を濾過する濾過器６
１が搭載され、逆浸透膜処理を行う車両Ｂには保安フィ
ルタ６２及び逆浸透膜装置６３が搭載され、各処理に対
し薬剤を注入する車両Ｃには滅菌剤タンク６４，凝集剤
タンク６５，ｐＨ調整剤タンク６６，滅菌剤タンク６７
が搭載されている。このような構成の浄水装置によれ
ば、海水を原水として取り込んで飲料水化することがで
き、また海水以外にも清澄な河川水，湖沼水であれば同
様に飲料水化することができる。なお、図中の車両Ｄ
は、各車両Ａ〜Ｃに電源を供給するための発電機車であ
る。As a mobile water purifying apparatus using a filtration membrane, a vehicle-mounted seawater desalination reverse osmosis apparatus is known as shown in FIG. Since this type of water purifier has a large scale, a plurality of vehicles A are usually provided for each treatment function.
.. to C, the vehicle 6 that performs the pretreatment has a filter 6 for filtering raw water taken from the water intake pump 60 in the vehicle A that performs pretreatment.
1 is installed, a vehicle B for performing reverse osmosis membrane treatment is equipped with a safety filter 62 and a reverse osmosis membrane device 63, and a vehicle C for injecting a medicine for each treatment is equipped with a sterilizing agent tank 64, a coagulant tank 65, pH adjusting agent tank 66, sterilizing agent tank 67
Is installed. According to the water purifier having such a configuration, seawater can be taken in as raw water and made into drinking water, and in addition to seawater, clear river water or lake water can be similarly made into drinking water. In addition, vehicle D in the figure
Is a generator car for supplying power to each of the vehicles A to C.
【０００４】[0004]
【発明が解決しようとする課題】しかしながら、上記し
た従来の移動式浄水装置では、その活動範囲が益々拡大
され多様な水源を原水として利用しなければならない状
況にあるにも拘らず、濁質以外の例えば細菌，ウイルス
類，農薬等を含む化学物質についてはそれらを除去する
機能がないために飲料水化することができないという問
題があった。また、珪藻土濾過器は高濁質の原水の場合
には、約３０分毎に手動で逆流洗浄を実施する必要があ
り、運転員に多大な労力を強いるという問題もあった。However, in the above-mentioned conventional mobile water purifier, the range of its activity has been expanded more and more, and various water sources have to be used as raw water. For example, there is a problem that chemical substances containing bacteria, viruses, pesticides, etc. cannot be made into drinking water because they have no function of removing them. In addition, the diatomaceous earth filter has a problem in that in the case of highly turbid raw water, it is necessary to manually carry out backwashing about every 30 minutes, which requires a great deal of labor for the operator.
【０００５】また、海水淡水化逆浸透装置では、極めて
清澄な原水でないかぎりは逆浸透膜｛以下、ＲＯ（Reve
rse Osmosis ）膜と略称する｝が閉塞してしまい、安定
な淡水化運転ができないという問題があった。従って、
例えば濁度が200 度であるような原水を浄化しようとす
る場合には、ＲＯ膜に原水を供給するにあたり、前段階
として汚濁密度指標（ＳＤＩ）４以下に濾過する必要が
あり、そのための前処理装置を装備すると車両数がさら
に増えるという問題があった。Further, in a seawater desalination reverse osmosis device, a reverse osmosis membrane {hereinafter, RO (Reve
rse Osmosis), which is abbreviated as “membrane”, is clogged, and there is a problem that stable desalination operation cannot be performed. Therefore,
For example, when trying to purify raw water with a turbidity of 200 degrees, it is necessary to filter it to a pollution density index (SDI) of 4 or less as a previous step before supplying the raw water to the RO membrane. There is a problem that the number of vehicles is further increased by equipping the processing device.
【０００６】本発明は以上のような従来の移動式浄水装
置及び淡水化逆浸透装置の課題を考慮してなされたもの
であり、飲料水として不適な細菌，ウイルス，化学物質
を除去することができ、安定して連続運転することがで
き、しかも移動に便利なサイズに構成された移動式浄水
設備を提供することを目的とする。The present invention has been made in consideration of the problems of the conventional mobile water purifying apparatus and desalination reverse osmosis apparatus as described above, and it is possible to remove bacteria, viruses and chemical substances unsuitable for drinking water. It is an object of the present invention to provide a mobile water purification facility that is configured to have a size that is capable of stable, continuous operation, and that is convenient for transportation.
【０００７】[0007]
【課題を解決するための手段】請求項１の本発明は、移
動体に搭載可能な移動式浄水設備において、原水に凝集
剤を添加する凝集剤添加装置と、原水と凝集剤とが混合
された混合水を貯留する貯留槽と、繊維材を濾過筒の主
材とする回転円筒形濾過器から構成され、貯留槽内の混
合水中に浸漬され、回転する濾過筒を通して濾過を行う
第一濾過器と、第一濾過器により得られた濾過水を、さ
らに精密濾過または限外濾過する第二濾過器と、を備え
てなる移動式浄水設備である。According to a first aspect of the present invention, in a mobile water purification facility that can be mounted on a moving body, a flocculant addition device for adding a flocculant to raw water and raw water and a flocculant are mixed. The first filter that consists of a storage tank that stores the mixed water and a rotating cylindrical filter that uses the fiber material as the main material of the filtration cylinder, is immersed in the mixed water in the storage tank, and filters through the rotating filtration cylinder. It is a mobile water purification facility comprising a filter and a second filter for further microfiltration or ultrafiltration of the filtered water obtained by the first filter.
【０００８】請求項２の本発明は、上記移動式浄水設備
にさらに、逆浸透膜装置から構成され第二濾過器により
得られた濾過水から純水を分離する第三濾過器と、その
第三濾過器により得られた純水に対し滅菌剤を導入する
滅菌剤導入装置とを備えた構成の移動式浄水設備であ
る。なお、本発明において、第三濾過器をバイパスさせ
て第二濾過器により得られた濾過水を直接、飲料水とし
て回収するバイパス管を付加することもできる。また、
回収されたその飲料水に滅菌剤を注入するように構成す
ることもできる。According to a second aspect of the present invention, in addition to the above mobile water purification equipment, a third filter for separating pure water from the filtered water obtained by the second filter, which comprises a reverse osmosis membrane device, and a third filter therefor are provided. (3) A mobile water purification system having a configuration including a sterilizing agent introducing device for introducing a sterilizing agent into pure water obtained by the three filters. In the present invention, it is also possible to add a bypass pipe for bypassing the third filter and directly collecting the filtered water obtained by the second filter as drinking water. Also,
It is also possible to inject a sterilant into the collected drinking water.
【０００９】請求項３の本発明は、上記第一濾過器と第
二濾過器とを接続する管路途中に、その管路内を流動す
る濾過水温度を高めるための加熱装置を設けた構成であ
る。請求項４の本発明は、上記第一濾過器及び第二濾過
器に、その濾過能力を回復させるための逆流洗浄装置を
備えた構成である。According to the present invention of claim 3, a heating device for raising the temperature of filtered water flowing in the pipe is provided in the middle of the pipe connecting the first filter and the second filter. Is. According to a fourth aspect of the present invention, the first filter and the second filter are provided with a backwashing device for recovering the filtering ability.
【００１０】請求項５の本発明は、第二濾過器における
入口及び出口の圧力差を検知する膜差圧計を設け、検知
された圧力差が所定範囲から逸脱した場合に、第二濾過
器に設けた逆流洗浄装置を動作させる構成である。本発
明の逆流洗浄装置に供給する水は、第三濾過器から得ら
れる濃縮水、または第二濾過器から得られる透過水を貯
留したもの、または運転中の第二濾過器から得られる透
過水のいずれかを利用することができる。According to a fifth aspect of the present invention, a membrane differential pressure gauge for detecting the pressure difference between the inlet and the outlet of the second filter is provided, and when the detected pressure difference deviates from a predetermined range, the second filter is provided. This is a configuration for operating the provided backflow cleaning device. The water supplied to the backwashing apparatus of the present invention is the concentrated water obtained from the third filter, or the permeated water obtained from the second filter, or the permeated water obtained from the second filter in operation. Either of them can be used.
【００１１】[0011]
【作用】請求項１の本発明に従えば、移動式浄水設備か
ら延長された取水ポンプを例えば河川に浸漬させて運転
を開始すれば、取水された原水に凝集剤が添加され、原
水と凝集剤は混合された後、混合水として貯留槽内に貯
留され、次いで回転円筒形濾過器の濾過筒を透過して濾
過され、次いで第二濾過器に供給されて精密濾過または
限外濾過され、濁質，細菌，ウイルス等が除去された飲
料水が得られる。請求項２に従えば、第二濾過器を透過
した後、第三濾過器に供給されて純水が分離され、次に
その純水に滅菌剤が導入され、濁質，細菌，ウイルスだ
けでなく化学物質も除去された飲料水が得られる。According to the present invention of claim 1, when the intake pump extended from the mobile water purification facility is immersed in, for example, a river to start the operation, a coagulant is added to the taken raw water to coagulate with the raw water. The agents are mixed and then stored in a storage tank as mixed water, then filtered through a filter cylinder of a rotary cylindrical filter, and then supplied to a second filter for microfiltration or ultrafiltration, Drinking water from which suspended substances, bacteria, viruses, etc. have been removed is obtained. According to claim 2, after passing through the second filter, it is supplied to the third filter to separate pure water, and then a sterilizing agent is introduced into the pure water so that only turbidity, bacteria, and viruses are introduced. Without drinking chemicals is obtained.
【００１２】請求項３に従えば、第二濾過器、第三濾過
器に供給される濾過水の温度が高められ、各濾過器にお
ける透過水量の低下が防止される。請求項４に従えば、
第一濾過器及び第二濾過器の濾過能力が回復される。請
求項５に従えば、第二濾過器の濾過能力が低下したこと
を検知して、第二濾過器の濾過能力を回復させるべく逆
流洗浄装置が作動する。According to the third aspect of the present invention, the temperature of the filtered water supplied to the second filter and the third filter is raised, and a decrease in the amount of permeated water in each filter is prevented. According to claim 4,
The filtering capabilities of the first and second filters are restored. According to the fifth aspect, the backwashing device is operated to detect that the filtration capacity of the second filter is lowered and restore the filtration capacity of the second filter.
【００１３】[0013]
【実施例】以下、図面に示した実施例に基づいて本発明
を詳細に説明する。図１〜３は、本発明に係る移動式浄
水設備の一実施例の構成を示したものである。まず図１
において、Ｅは本設備を収納するためのシェルタであ
り、図４に示したシェルタ５０と同様にトラックに搭載
できるものである。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described in detail below with reference to the embodiments shown in the drawings. 1 to 3 show the configuration of an embodiment of the mobile water purification facility according to the present invention. Figure 1
In the figure, E is a shelter for accommodating the present equipment, and can be mounted on a truck like the shelter 50 shown in FIG.
【００１４】取水ポンプ１は移動先である現地の原水を
汲み上げるためのものであり、移動中においてはシェル
タＥ内またはトラックの荷物室内に収納されている。そ
の取水ポンプ１より取水した原水は、そのポンプ出口に
接続された取水ホース２及びホース取付管２ａを介して
シェルタＥ内の混合器３に導かれるようになっている。
また、ホース取付管２ａには凝集剤注入管４が接続され
ており、凝集剤タンク５から凝集剤用ポンプ６を用いて
汲み上げた凝集剤を、その凝集剤注入管４より原水中に
注入できるようになっている。上記凝集剤タンク５及び
凝集剤用ポンプ６は凝集剤添加装置としてみなすことが
できる。上記混合器３は例えばスタティックミキサまた
はラインミキサから構成され、配管内で原水と凝集剤と
を混合するようになっている。The water intake pump 1 is for pumping up the raw water at the destination, and is stored in the shelter E or the luggage compartment of the truck during the movement. Raw water taken from the water intake pump 1 is guided to the mixer 3 in the shelter E via a water intake hose 2 and a hose mounting pipe 2a connected to the pump outlet.
A coagulant injection pipe 4 is connected to the hose mounting pipe 2 a, and the coagulant pumped from the coagulant tank 5 using the coagulant pump 6 can be injected into the raw water through the coagulant injection pipe 4. It is like this. The coagulant tank 5 and the coagulant pump 6 can be regarded as a coagulant addition device. The mixer 3 is composed of, for example, a static mixer or a line mixer, and mixes raw water and a coagulant in a pipe.
【００１５】混合器３から送出された混合水は、バルブ
７を介して貯留槽としての貯留タンク８内に貯留され、
その混合水中に浸漬するようにして第一濾過器としての
回転円筒型濾過器９が配設されている。繊維材を濾過筒
の主材とするその回転円筒型濾過器９は、凝集済みの混
合水を濾過してフロックを除去し、それにより、最大20
0 度の濁度であった混合水の濁度を10度以下に低減させ
るようになっている。また、回転円筒型濾過器９には濾
過筒のつまりを防止して濾過能力を回復させるための逆
流洗浄装置が備えられている。この逆流洗浄装置は、濾
過筒外周面に近接して開口するホッパ１０及びこのホッ
パ１０から管１１を介して濾過懸濁物質及び固形物を吸
引し、排出する逆流洗浄用ポンプ１２とから構成され、
浄水設備の運転時には常時作動されるようになってい
る。The mixed water sent from the mixer 3 is stored in a storage tank 8 as a storage tank via a valve 7.
A rotary cylindrical filter 9 as a first filter is arranged so as to be immersed in the mixed water. The rotary cylinder type filter 9 which uses the fiber material as the main material of the filter cylinder filters the flocculated mixed water to remove the flocs, whereby a maximum of 20
The turbidity of the mixed water, which was 0 degree, was reduced to 10 degrees or less. Further, the rotary cylindrical filter 9 is equipped with a backwashing device for preventing the filter cylinder from being clogged and recovering the filtering ability. This backwashing apparatus is composed of a hopper 10 that is opened close to the outer peripheral surface of the filter cylinder, and a backwashing pump 12 that sucks and discharges filtered suspended solids and solids from the hopper 10 through a pipe 11. ,
When the water purification equipment is in operation, it is always activated.
【００１６】この回転円筒型濾過器９によって濾過され
た濾過水は、濾過ポンプ１３によって加圧され、精密濾
過または限外濾過を行う第二濾過器１４へ送られる。こ
の第二濾過器１４は、例えばポリプロピレン等を濾材と
した精密濾過膜（Microfiltration ：以下ＭＦ膜と略称
する）またはポリアクリルニトリル等を浸透膜に用いた
限外濾過膜（Ultrafiltration ：以下ＵＦ膜と略称す
る）等から構成され、上記回転円筒型濾過器９における
濾過処理においてリークした微細な濁質，細菌，ウイル
スを除去することができるようになっている。The filtered water filtered by the rotary cylindrical filter 9 is pressurized by a filtering pump 13 and sent to a second filter 14 for performing microfiltration or ultrafiltration. The second filter 14 is, for example, a microfiltration membrane using polypropylene or the like as a filter material (Microfiltration: hereinafter abbreviated as MF membrane) or an ultrafiltration membrane (Ultrafiltration: hereinafter referred to as UF membrane) using polyacrylonitrile or the like as a permeation membrane. Abbreviated) and the like, and is capable of removing fine suspended matter, bacteria, and viruses that have leaked during the filtering process in the rotary cylindrical filter 9.
【００１７】濾過ポンプ１３と第二濾過器１４とを接続
する管１５の胴部には加熱装置としての温水配管１６が
添設されており、この温水配管１６の加熱源は、トラッ
クのエンジンを冷却するためラジエターから強制循環さ
れる冷却水を利用している。この温水配管１６を設ける
ことにより、取水した原水が低温であるような状況にお
いても、第二濾過器１４及びその後段の逆浸透膜装置２
０における浄化水量を低減させることなく設備を連続運
転することができるようになる。具体的には、原水の温
度が２５℃以下になると、５〜３０℃の範囲に維持させ
るように加熱制御を行う。A hot water pipe 16 as a heating device is attached to the body of a pipe 15 connecting the filtration pump 13 and the second filter 14, and the heating source of the hot water pipe 16 is a truck engine. The cooling water that is forcedly circulated from the radiator is used for cooling. By providing this hot water pipe 16, even in a situation where the raw water taken in is at a low temperature, the second filter 14 and the reverse osmosis membrane device 2 in the subsequent stage are provided.
The facility can be continuously operated without reducing the amount of purified water at 0. Specifically, when the temperature of the raw water becomes 25 ° C. or lower, heating control is performed so as to maintain the temperature in the range of 5 to 30 ° C.
【００１８】このようにして第二濾過器１４により、Ｓ
ＤＩが“４”以下になるまで濁質が除去された濾過水
は、次に高圧ポンプ１８によって５〜７０kg/cm2に加圧
され、流量調節弁１９を介して第三濾過器としての逆浸
透膜装置２０に供給される。逆浸透膜装置２０では、高
圧ポンプ１８によって加えられた圧力エネルギによって
濾過水から純水を分離し、濾過水中のイオン、第二濾過
器１４を通過した細菌，ウイルス，有害な有機物等を除
去し、それにより無菌化され有害物質が極力排除された
飲料水が生成される。In this way, the second filter 14 causes S
The filtered water from which turbidity has been removed until the DI becomes "4" or less is then pressurized to 5 to 70 kg / cm 2 by the high-pressure pump 18, and is supplied to the reverse filter as a third filter via the flow control valve 19. It is supplied to the osmosis membrane device 20. In the reverse osmosis membrane device 20, the pure water is separated from the filtered water by the pressure energy applied by the high-pressure pump 18, and the ions in the filtered water, bacteria, viruses, harmful organic substances and the like that have passed through the second filter 14 are removed. As a result, drinking water that is sterilized and is free of harmful substances is produced.
【００１９】上記逆浸透膜装置２０によって得られた飲
料水は、貯留中において生物汚染を防止するため滅菌剤
が注入される。その滅菌剤の注入は、滅菌剤タンク２
１，滅菌剤を汲み上げる滅菌剤用ポンプ２２，及びその
ポンプ出口と浄水管２３とを接続する管２４から構成さ
れる滅菌剤導入装置によって行われる。The drinking water obtained by the reverse osmosis membrane device 20 is injected with a sterilizing agent in order to prevent biological contamination during storage. The sterilizing agent is injected into the sterilizing agent tank 2
1. A sterilizing agent introducing device including a sterilizing agent pump 22 for pumping up the sterilizing agent, and a pipe 24 connecting the pump outlet and the water purification pipe 23.
【００２０】なお、上記第二濾過器１４もまた、その濾
過能力を回復させるための逆流洗浄装置が備えられてい
る。この逆流洗浄装置は、図１に示すように、逆浸透膜
装置２０から得られる濃縮水をバルブ２５を介して注入
するとともに、逆流洗浄用ブロワ２６を併用して逆流洗
浄を行うものである。The second filter 14 is also provided with a backwashing device for recovering its filtering ability. As shown in FIG. 1, this backflow cleaning apparatus is one in which concentrated water obtained from the reverse osmosis membrane apparatus 20 is injected through a valve 25, and a backflow cleaning blower 26 is also used for backflow cleaning.
【００２１】また、逆流洗浄装置は、上記の構成に限ら
ず、図２に示すように、ＭＦ膜またはＵＦ膜の透過水を
濾過タンク２７に貯留して逆流洗浄用ポンプ２８から送
り込むとともに、逆流洗浄用ブロワ２６を併用して逆流
洗浄を行うよう構成することもできる。さらにまた、図
３に示すように、複数のＭＦ膜またはＵＦ膜２９，３０
を使用している場合には、運転中のそれぞれ膜の透過水
を注入するとともに、逆流洗浄ブロワ２６を併用して逆
流洗浄を行うよう構成することもできる。なお、図２及
び図３において図１と同じ構成要素については同一符号
を付してその説明を省略している。また、図１中の記号
Ｇは発電機を示している。Further, the backflow cleaning device is not limited to the above-mentioned structure, and as shown in FIG. 2, the permeated water of the MF membrane or the UF membrane is stored in the filtration tank 27 and fed from the backflow cleaning pump 28, and the backflow cleaning is performed. It is also possible to use the cleaning blower 26 together to perform backwashing. Furthermore, as shown in FIG. 3, a plurality of MF or UF membranes 29, 30 are used.
In the case of using the above, it is possible to inject the permeated water of the respective membranes during operation and use the backflow cleaning blower 26 together to perform the backflow cleaning. 2 and 3, the same components as those in FIG. 1 are designated by the same reference numerals and the description thereof is omitted. The symbol G in FIG. 1 indicates a generator.
【００２２】図１において、ＭＦ膜またはＵＦ膜の逆流
洗浄は、膜差圧計３１によって検知された圧力差に基づ
いて自動的に行われる。すなわち、第二濾過器１４の入
口及び出口の圧力差を検知し、その検知された圧力差が
所定範囲0.5kg/cm2 〜3.0kg/cm2 から逸脱した場合に、
第二濾過器１４の濾過能力が低下したとみなし、逆流洗
浄装置を動作させるようになっている。この逆流洗浄の
自動化は、図２に示した第二濾過器１４、及び図３に示
した第二濾過器２９，３０にも適用することができる。In FIG. 1, the backflow cleaning of the MF membrane or the UF membrane is automatically performed based on the pressure difference detected by the membrane pressure gauge 31. That is, when the pressure difference inlet and senses the pressure difference between the outlet was the detection of the second filter 14 deviates from the predetermined range 0.5kg / cm 2 ~3.0kg / cm 2 ,
It is considered that the filtration capacity of the second filter 14 is lowered, and the backwashing device is operated. This automation of backwashing can be applied to the second filter 14 shown in FIG. 2 and the second filters 29 and 30 shown in FIG.
【００２３】また、図１において、取水ホース２に濁度
計３１を取り付けて原水の濁度を計測できるようにし、
貯留槽８内にｐＨ計３２を取り付けて原水のｐＨを測定
できるようにし、また、浄水管２３に電気伝導度計３３
を取り付けて水質の管理ができるように構成することが
好ましい。このような各センサと、逆流洗浄用ポンプ１
２，流量調整弁１９，逆流洗浄弁２５等の自動弁とを組
み合わせることにより、浄水設備の全自動無人運転が可
能となる。なお、ｐＨが低い場合にはアルカリが投入さ
れることになる。In FIG. 1, a turbidimeter 31 is attached to the intake hose 2 so that the turbidity of the raw water can be measured.
A pH meter 32 is installed in the storage tank 8 so that the pH of the raw water can be measured, and an electric conductivity meter 33 is attached to the water purification pipe 23.
It is preferable to install the above so that the water quality can be controlled. Each such sensor and the backwash pump 1
2. By combining automatic valves such as the flow rate adjusting valve 19 and the backwashing valve 25, fully automatic unmanned operation of the water purification equipment becomes possible. When the pH is low, alkali is added.
【００２４】次に、上記構成を有する本実施例の動作に
ついて説明する。なお、説明に際しては河川を原水とし
て浄水する場合を例に取り説明する。河川に取水ポンプ
１を浸漬させて移動式浄水設備の運転を開始すると、取
水ホース２，ホース取付管２ａを介して混合器３に原水
が送られる。このとき、その原水中に凝集剤が添加さ
れ、それにより混合器３からは、原水と凝集剤が混合さ
れた混合水が送出されることになる。次いでその混合水
は、貯留槽８内に貯留され、混合水中に浸漬された回転
円筒形濾過器９が回転動作すると、混合水はその濾過筒
の外側から内側に向けて濾過される。次いで回転円筒形
濾過器９にて濾過された濾過水は、取出し管９ａから回
収され、濾過ポンプ１３の作動により第二濾過器１４へ
圧送される。このとき、濾過水の温度が低いために第二
濾過器１４における浄化水量が低減する恐れがある場合
には、エンジン冷却によって受熱した冷却水を温水配管
１６内に循環させることにより、管１５内を流動する濾
過水を加熱する。Next, the operation of this embodiment having the above configuration will be described. In the description, the case of purifying water from a river as raw water will be taken as an example. When the intake pump 1 is immersed in a river to start the operation of the mobile water purification system, raw water is sent to the mixer 3 via the intake hose 2 and the hose mounting pipe 2a. At this time, the coagulant is added to the raw water, so that the mixed water in which the raw water and the coagulant are mixed is delivered from the mixer 3. Then, the mixed water is stored in the storage tank 8, and when the rotary cylindrical filter 9 immersed in the mixed water is rotated, the mixed water is filtered from the outside to the inside of the filter cylinder. Next, the filtered water filtered by the rotary cylindrical filter 9 is collected from the take-out pipe 9 a and is pressure-fed to the second filter 14 by the operation of the filtration pump 13. At this time, if the purified water amount in the second filter 14 may be reduced due to the low temperature of the filtered water, the cooling water received by the engine cooling is circulated in the hot water pipe 16 so that the inside of the pipe 15 is cooled. The filtered water flowing through is heated.
【００２５】第二濾過器１４では供給された濾過水を精
密濾過または限外濾過し、その後段に設けられた逆浸透
膜装置２０が処理できる程度の水質にすべく前処理を行
う。前処理により濁質が除去された濾過水は、次に高圧
ポンプ１８によって加圧され、逆浸透膜装置２０に供給
される。逆浸透膜装置２０では供給された濾過水から純
水を分離し、得られた純水は、次に滅菌剤が注入されて
飲料水として送出される。In the second filter 14, the supplied filtered water is subjected to microfiltration or ultrafiltration, and is pretreated so that the reverse osmosis membrane device 20 provided at the subsequent stage can treat the water to a quality that allows it to be treated. The filtered water from which suspended matter has been removed by the pretreatment is then pressurized by the high-pressure pump 18 and supplied to the reverse osmosis membrane device 20. In the reverse osmosis membrane device 20, pure water is separated from the supplied filtered water, and the pure water thus obtained is then injected with a sterilizing agent and delivered as drinking water.
【００２６】なお、上記実施例では逆浸透膜装置２０を
透過させて飲料水を得る構成について説明したが、原水
中に有害化学部物質が存在しない場合には、図１〜３の
破線Ｆで示す経路で、すなわち逆浸透膜装置２０をバイ
パスさせて飲料水を得るように構成することができる。
また、本発明は、可搬型の水質試験装置を随伴させ、飲
料可能であることを現地で確認できるようにすることが
好ましい。In the above embodiments, the structure for obtaining drinking water by permeating the reverse osmosis membrane device 20 has been described. However, when there is no harmful chemical part substance in the raw water, the broken line F in FIGS. It can be configured to obtain drinking water by the route shown, that is, by bypassing the reverse osmosis membrane device 20.
Further, in the present invention, it is preferable that a portable water quality testing device is provided so that the beverage can be confirmed locally.
【００２７】また、本発明の加熱装置は、上記実施例で
は温水配管で構成したが、これに限らず、例えば管１５
内にシーズヒータを挿入することによっても実現するこ
とができ、要するに流体を所定の温度に高めることがで
きるものであれば任意の加熱手段を使用することができ
る。Further, although the heating device of the present invention is constituted by the hot water pipe in the above-mentioned embodiment, it is not limited to this, and for example, the pipe 15 is used.
It can also be realized by inserting a sheathed heater inside, and any heating means can be used as long as it can raise the temperature of the fluid to a predetermined temperature.
【００２８】また、本発明の移動体は、上記実施例では
自走車両であるトラックに搭載した例について説明し
た、これに限らず、牽引車両、牽引軌道車両にも搭載す
ることができ、さらには貨物飛行機またはヘリコプタ等
の飛行手段にも搭載することができる。Further, the moving body of the present invention has been described in the above embodiment as an example of being mounted on a truck which is a self-propelled vehicle. However, the present invention is not limited to this, and can be mounted on a towing vehicle and a towing track vehicle. Can also be mounted on a flight vehicle such as a freighter or helicopter.
【００２９】[0029]
【発明の効果】以上説明したことから明かなように、請
求項１の本発明によれば、凝集剤注入装置，混合器及び
第一濾過器により、濁度が最大200 度の原水から精密濾
過または限外濾過を安定して行える濁度10度以下の濾過
水が得られ、第二濾過器における濾過により、その前段
でリークした微細な濁質，細菌，ウイルス等が除去され
てＳＤＩが４以下の濾過水が得られる。As is apparent from the above description, according to the present invention of claim 1, the coagulant injection device, the mixer and the first filter are used to perform microfiltration from raw water having a turbidity of up to 200 degrees. Alternatively, filtered water with a turbidity of 10 degrees or less that can stably perform ultrafiltration is obtained, and fine turbidity, bacteria, viruses, etc. leaked in the preceding stage are removed by filtration in the second filter to obtain SDI of 4 The following filtered water is obtained.
【００３０】請求項２の本発明によれば、第三濾過器に
おける濾過により、第二濾過器を通過した細菌，ウイル
ス類に加えて飲用に不適な化学物質が除去される。それ
により、浄水設備全体として、有害物質，細菌，ウイル
ス，化学物質等を含む最大濁度200 度までの原水から飲
料用水を浄水し、供給することができる。また、本発明
は移動可能なサイズに構成されているために移動範囲が
限定されず、広範囲の地域に移動して飲料水を供給する
ことができる。According to the second aspect of the present invention, the filtration in the third filter removes not only the bacteria and viruses that have passed through the second filter but also chemical substances unsuitable for drinking. As a result, drinking water can be purified and supplied from raw water containing toxic substances, bacteria, viruses, chemical substances, etc. up to a maximum turbidity of 200 degrees in the entire water purification facility. In addition, since the present invention is configured to have a movable size, the moving range is not limited, and drinking water can be supplied by moving to a wide area.
【図１】本発明の一実施例の構成を示す構成図である。FIG. 1 is a configuration diagram showing a configuration of an embodiment of the present invention.
【図２】同実施例に係る第二濾過器の逆流洗浄装置の他
の構成を示す構成図である。FIG. 2 is a configuration diagram showing another configuration of the backflow cleaning device for the second filter according to the embodiment.
【図３】同実施例に係る逆流洗浄装置のさらに他の構成
を示す構成図である。FIG. 3 is a configuration diagram showing still another configuration of the backwashing apparatus according to the embodiment.
【図４】従来例の移動式浄水装置を示す一部切り欠きを
有する外観図である。FIG. 4 is an external view showing a conventional mobile water purifier having a notch.
【図５】従来例の移動式浄水装置の構成を示す構成図で
ある。FIG. 5 is a configuration diagram showing a configuration of a conventional mobile water purifier.
【図６】従来例の濾過膜を利用した浄水装置の構成を示
す構成図である。FIG. 6 is a configuration diagram showing a configuration of a water purifier using a conventional filtration membrane.
１ 取水ポンプ ３ 混合器 ４ 凝集剤注入管 ５ 凝集剤タンク ８ 貯留タンク ９ 回転円筒型濾過器 １３ 濾過ポンプ １４ 第二濾過器 １６ 温水配管 １８ 高圧ポンプ ２０ 逆浸透膜装置 ２１ 滅菌剤タンク ２２ 滅菌剤用ポンプ 1 Intake Pump 3 Mixer 4 Coagulant Injection Pipe 5 Coagulant Tank 8 Storage Tank 9 Rotating Cylindrical Filter 13 Filtration Pump 14 Second Filter 16 Hot Water Piping 18 High Pressure Pump 20 Reverse Osmosis Membrane Device 21 Sterilizer Tank 22 Sterilizer Pump for
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 ＦＩ 技術表示箇所 Ｃ０２Ｆ 1/44 Ｈ 9538−4Ｄ 1/50 ５１０ Ａ ５２０ Ａ ５５０ Ｃ ５６０ Ｅ Ｚ ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Office reference number FI Technical display location C02F 1/44 H 9538-4D 1/50 510 A 520 A 550 C 560 E Z
Claims (5)
いて、 原水に凝集剤を添加する凝集剤添加装置と、 前記原水と前記凝集剤とが混合された混合水を貯留する
貯留槽と、 繊維材を濾過筒の主材とする回転円筒形濾過器から構成
され、前記貯留槽内の前記混合水中に浸漬され、回転す
る前記濾過筒を通して濾過を行う第一濾過器と、 前記第一濾過器により得られた濾過水を、さらに精密濾
過または限外濾過する第二濾過器と、を備えてなること
を特徴とする移動式浄水設備。1. A mobile water purification system mountable on a mobile body, comprising: a coagulant addition device for adding a coagulant to raw water; and a storage tank for storing mixed water in which the raw water and the coagulant are mixed, A first filter that is composed of a rotating cylindrical filter having a fiber material as a main material of a filter cylinder, is immersed in the mixed water in the storage tank, and filters through the rotating filter cylinder; A mobile water purification system comprising a second filter for further performing microfiltration or ultrafiltration of the filtered water obtained by the filter.
過器により得られた濾過水から純水を分離する第三濾過
器と、その第三濾過器により得られた前記純水に対し滅
菌剤を導入する滅菌剤導入装置と、をさらに備えてなる
請求項１記載の移動式浄水設備。2. A third filter comprising a reverse osmosis membrane device for separating pure water from the filtered water obtained by the second filter, and the pure water obtained by the third filter. The mobile water purification equipment according to claim 1, further comprising a sterilizing agent introducing device for introducing a sterilizing agent.
続する管路途中に、その管路内を流動する濾過水温度を
高めるための加熱装置を設けた請求項１または２に記載
の移動式浄水設備。3. A heating device for raising the temperature of filtered water flowing in the pipeline is provided in the middle of the pipeline connecting the first filter and the second filter. Mobile water purification equipment described.
その濾過能力を回復させるための逆流洗浄装置が備えら
れている請求項１〜３のいずれかに記載の移動式浄水設
備。4. The first filter and the second filter,
The mobile water purification equipment according to any one of claims 1 to 3, further comprising a backwashing device for recovering its filtering ability.
圧力差を検知する膜差圧計を設け、検知された圧力差が
所定範囲から逸脱した場合に、前記第二濾過器に設けた
逆流洗浄装置を動作させる請求項４に記載の移動式浄水
設備。5. A membrane differential pressure gauge for detecting the pressure difference between the inlet and the outlet of the second filter is provided, and when the detected pressure difference deviates from a predetermined range, the backwashing provided in the second filter is provided. The mobile water purification equipment according to claim 4, which operates the apparatus.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6208807A JP2755182B2 (en) | 1994-09-01 | 1994-09-01 | Mobile water purification equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6208807A JP2755182B2 (en) | 1994-09-01 | 1994-09-01 | Mobile water purification equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0871567A true JPH0871567A (en) | 1996-03-19 |
| JP2755182B2 JP2755182B2 (en) | 1998-05-20 |
Family
ID=16562453
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6208807A Expired - Lifetime JP2755182B2 (en) | 1994-09-01 | 1994-09-01 | Mobile water purification equipment |
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| Country | Link |
|---|---|
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| JP2004025109A (en) * | 2002-06-27 | 2004-01-29 | Kurita Water Ind Ltd | Water treatment method and water treatment apparatus |
| JP2006263542A (en) * | 2005-03-23 | 2006-10-05 | Kurita Water Ind Ltd | Water making apparatus and water making method |
| JP2006272200A (en) * | 2005-03-30 | 2006-10-12 | Toyobo Engineering Kk | Method for operating emergency water purifying apparatus and emergency water purifying apparatus using it |
| JP2007098338A (en) * | 2005-10-06 | 2007-04-19 | Suido Kiko Kaisha Ltd | Water treatment apparatus |
| WO2011013173A1 (en) * | 2009-07-30 | 2011-02-03 | Ikuta Naoyuki | Portable container |
| WO2011030385A1 (en) * | 2009-09-11 | 2011-03-17 | Ikuta Kazumasa | Container-type water treatment device |
| JP2011177653A (en) * | 2010-03-01 | 2011-09-15 | Asahi Kasei Chemicals Corp | Filter |
| JP2014217821A (en) * | 2013-05-10 | 2014-11-20 | 尚之 生田 | Filter device for drinking water |
| CN109432869A (en) * | 2018-12-14 | 2019-03-08 | 广东百维生物科技有限公司 | For filtering the diatomite filter group and its control method of collagen |
| JP2020032351A (en) * | 2018-08-29 | 2020-03-05 | 株式会社神戸製鋼所 | Mobile water purification device |
| JP2022159423A (en) * | 2018-08-29 | 2022-10-17 | 株式会社神戸製鋼所 | Mobile water purification device |
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| JPS51109545A (en) * | 1975-03-24 | 1976-09-28 | Daicel Ltd | Netsukokankiojusuru makubunrisochi |
| JPS6157290A (en) * | 1984-08-27 | 1986-03-24 | Meitan Seiichi | High purity water making apparatus and sterilization method thereof |
| JPS629997U (en) * | 1985-07-01 | 1987-01-21 | ||
| JPS63294906A (en) * | 1987-05-26 | 1988-12-01 | Nippon Atom Ind Group Co Ltd | Method for operating hollow yarn membrane filter |
| JPS6443392A (en) * | 1987-08-12 | 1989-02-15 | Hitachi Ltd | Sterilization control apparatus |
| JPS6451192A (en) * | 1987-08-24 | 1989-02-27 | Hitachi Ltd | Sterilizing treatment of industrial water |
| JPH02126923A (en) * | 1988-11-02 | 1990-05-15 | Toshiba Corp | Waste liquid filtration device |
| JPH0631271A (en) * | 1992-07-16 | 1994-02-08 | Japan Organo Co Ltd | Film treatment device |
| JPH0691262A (en) * | 1992-09-14 | 1994-04-05 | Airiin:Kk | Water treatment apparatus |
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| JP2004025109A (en) * | 2002-06-27 | 2004-01-29 | Kurita Water Ind Ltd | Water treatment method and water treatment apparatus |
| JP2006263542A (en) * | 2005-03-23 | 2006-10-05 | Kurita Water Ind Ltd | Water making apparatus and water making method |
| JP2006272200A (en) * | 2005-03-30 | 2006-10-12 | Toyobo Engineering Kk | Method for operating emergency water purifying apparatus and emergency water purifying apparatus using it |
| JP2007098338A (en) * | 2005-10-06 | 2007-04-19 | Suido Kiko Kaisha Ltd | Water treatment apparatus |
| WO2011013173A1 (en) * | 2009-07-30 | 2011-02-03 | Ikuta Naoyuki | Portable container |
| WO2011030385A1 (en) * | 2009-09-11 | 2011-03-17 | Ikuta Kazumasa | Container-type water treatment device |
| JP2011177653A (en) * | 2010-03-01 | 2011-09-15 | Asahi Kasei Chemicals Corp | Filter |
| JP2014217821A (en) * | 2013-05-10 | 2014-11-20 | 尚之 生田 | Filter device for drinking water |
| JP2020032351A (en) * | 2018-08-29 | 2020-03-05 | 株式会社神戸製鋼所 | Mobile water purification device |
| JP2022159423A (en) * | 2018-08-29 | 2022-10-17 | 株式会社神戸製鋼所 | Mobile water purification device |
| CN109432869A (en) * | 2018-12-14 | 2019-03-08 | 广东百维生物科技有限公司 | For filtering the diatomite filter group and its control method of collagen |
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