JP2004167454A - Water purifying apparatus - Google Patents

Water purifying apparatus Download PDF

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Publication number
JP2004167454A
JP2004167454A JP2002339255A JP2002339255A JP2004167454A JP 2004167454 A JP2004167454 A JP 2004167454A JP 2002339255 A JP2002339255 A JP 2002339255A JP 2002339255 A JP2002339255 A JP 2002339255A JP 2004167454 A JP2004167454 A JP 2004167454A
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JP
Japan
Prior art keywords
water
pure water
reverse osmosis
osmosis membrane
softener
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JP2002339255A
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Japanese (ja)
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JP4062433B2 (en
Inventor
Mitsuru Nozue
満 野末
Yoshiteru Misumi
好輝 三角
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Kurita Water Industries Ltd
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Kurita Water Industries Ltd
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Priority to JP2002339255A priority Critical patent/JP4062433B2/en
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a water purifying apparatus which is constituted by combining a water softener with a reverse osmosis membrane and which can continuously produce pure water even when the water softener is under regeneration. <P>SOLUTION: After raw water is subjected to softening treatment via the water softener, pure water is produced via the reverse osmosis membrane. Further the water purifying apparatus is provided with a bypassing means which supplies the raw water to the reverse osmosis membrane during regeneration of the water softener by making the raw water bypass the water softener and with a thickened water amount regulation means which regulates a discharge flow rate of the thickened water separated by the reverse osmosis membrane. <P>COPYRIGHT: (C)2004,JPO

Description

【0001】
【発明の属する技術分野】
本発明は軟水器と逆浸透膜とを組み合わせた純水製造装置に係り、特に軟水器の再生時においても純水を連続生成することが可能な純水製造装置に関する。
【0002】
【関連する背景技術】
近時、給水(原水)を脱塩処理する方法として、給水(原水)に酸等を添加してpH調整して軟化器で処理した後、この軟化器で軟化処理された処理水を逆浸透膜で処理する脱塩方法が知られている(例えば、特許文献1参照)。そして、この脱塩方法を適用した純水製造装置も広く適用されている。
【0003】
このような水処理装置に用いられる逆浸透膜は、給水(原水)中に含まれる塩素成分やカルシウムなどのスケールによって、その特性劣化が生じる。そこで一般的には給水(原水)中に含まれる塩素分を、活性炭や触媒によるろ過等によって除去し、また、カルシウム等の硬質分を軟水器によって除去(軟水化処理)した後、逆浸透膜に与えるようにしている。このため軟水器は、定期的にカルシウム等の硬質分を除去する再生が必要である。
【0004】
ところでこのような純水製造装置にあっては、軟水器の再生期間中、逆浸透膜に軟水を供給することができず、純水製造が中断されてしまう。そこで、純水の連続供給が必要な場合、軟水器の再生中であっても純水製造が中断されないよう、一般的には純水タンクを用意して純水製造装置で生成される純水の剰余分を蓄えておき、軟水器の再生中は、上記純水タンクに蓄えられた純水をその供給先に供給するようにしている。
【0005】
【特許文献1】
特許第3278918号公報
【0006】
【発明が解決しようとする課題】
しかしながら、上述した純水タンクに蓄えておく純水を生成するためには、常時必要とする純水量以上の純水生成能力のある純水製造装置を用意する必要がある。更には軟水器の再生中は、純水タンクに備蓄した純水を供給先に送り出すためのポンプ動力等を用意する必要がある等の問題があった。
【0007】
本発明はこのような事情を考慮してなされたもので、その目的は、軟水器と逆浸透膜とを組み合わせて構成された純水製造装置において、軟水器の再生中であっても、連続的に純水を生成することのできる純水製造装置を提供することにある。
【0008】
【課題を解決するための手段】
前述した目的を達成するため、本発明に係る純水製造装置は、例えば燃料電池に連続的に供給する純水を製造するに好適なものであり、軟水器を介して原水を軟水化処理した後、逆浸透膜により純水を生成する純水製造装置であって、前記軟水器の再生時に該軟水器をバイパスして前記逆浸透膜に原水を供給するバイパス手段と、前記逆浸透膜で分離した濃縮水の排出流量を調整する濃縮水量調整手段とを具備したことを特徴としている。
【0009】
また、更に前記逆浸透膜で分離した純水の排出圧力を検出する純水圧力センサと、この純水圧力センサで検出した純水の排出圧力が予め設定された圧力より高い場合、前記逆浸透膜への軟水および/または原水の供給を遮断する供給遮断手段とを備えることを特徴としている。
そして、前記濃縮水量調整手段は、前記軟水器の再生時に所定の濃縮水の排出流量を調整するものとして構成される。
したがって、本発明の純水製造装置によれば軟水器の再生中であっても、連続的に純水を生成することが可能な純水製造装置を提供することができる。
【0010】
【発明の実施の形態】
以下、図面を参照して本発明に係る純水製造装置について説明する。
図1はこの一実施形態に係る純水製造装置の概略構成図を示す図であり、例えば燃料電池に連続的に供給する軟水を製造するに好適な純水製造装置を例示したものである。
【0011】
この純水製造装置は基本的には、給水(原水)を逆浸透膜1で純水と濃縮水とに分離するもので、逆浸透膜1に供給する原水中の塩素やカルシウム成分を除去する前処理フィルタ2と軟水器3とを備えている。この前処理フィルタ2は、原水から塩素分を取り除くものである。そして、この塩素分が取り除かれた原水に含まれるカルシウムなどの硬質成分を軟水器3で取り除いた後、逆浸透膜1に供給するよう構成されている。また、逆浸透膜1には、純水の製造に伴って生成される濃縮水の流量を調整して排出する流量調整継ぎ手4が設けられ、ピット5などに連続ブローされる。尚、前記流量継ぎ手4の代わりに手動で開度調整できる流量調整弁(図示せず)を適用してもよい。
【0012】
さて、前記軟水器3は、前述したように原水中のカルシウム分などの硬度成分を除去する目的で設けられている。しかし、原水を軟水処理することによって取り除かれたカルシウム分が軟水器3内に蓄積されるため、軟水器3を定期的に再生処理する必要がある。この再生処理を行うため、塩化ナトリウムの水溶液を蓄えた塩水タンク6が軟水器3に接続されている。そして、この塩水を軟水器3に充填されているイオン交換樹脂に蓄積されたカルシウムとイオン交換させることで軟水器3の再生を行うよう構成されている。尚、好ましくは、この塩水タンク6内の塩水の供給は、原水流入圧力によるエゼクター効果を利用するように構成すると良い。
【0013】
ところで、本発明の純水製造装置には、軟水器3の再生処理中であっても、給水を逆浸透膜1に供給可能となるよう軟水器3をバイパスするバイパス弁10が軟水器3の入口配管および出口配管との間に併設されている。そして、このバイパス弁10を開くことによって、軟水器3の再生中であっても、原水の一部を逆浸透膜1に供給し、純水の生成を中断しないように構成されている。
【0014】
更には逆浸透膜1から生成される純水の供給路に流れる水圧を検出する圧力センサ20が、この供給路に設けられている。この圧力センサ20は、検出した圧力が所定の圧力を超えたとき逆浸透膜1への給水を遮断する閉止弁11を駆動する役割を担う。
また、前述したように軟水器3の再生処理中に、前処理フィルタ2からバイパス弁10を介してバイパスされた硬度成分を含む原水が逆浸透膜1に供給された際、硬度成分(カルシウム分)によるスケールの付着を抑えるため、逆浸透膜1の回収率を低下させる再生用流量継ぎ手12と、再生ブロー弁13とが逆浸透膜1に設けられている。尚、特に図示しないが再生用流量継ぎ手の部分に手動で開度調整できる流量調整弁を適用してもよい。
【0015】
このように構成された純水製造装置によれば、常時は前処理フィルタ2で塩素分が除去され、この塩素分が除去された原水を更に軟水器3で軟水化処理した後、逆浸透膜1に供給することで純水が生成される。
一方、軟水器3の再生処理中は、軟水器3へ供給される原水の一部をバイパス弁10を介して逆浸透膜1へ供給する。そして、逆浸透膜1は、この原水供給を受けて純水を製造する。つまり、従来の純水製造装置では、このバイパス弁10が無いため、軟水器再生中は純水を得ることができなかったが、本発明の純水製造装置によれば、バイパス弁10を介して逆浸透膜1に原水を供給することができるので軟水器3の再生中であっても、純水の製造を継続することが可能となる。しかし、原水を逆浸透膜1に直接供給することになるので原水に含まれるスケールが逆浸透膜1に付着する虞がある。そこで本装置においては、軟水器3の再生中は再生用流量継ぎ手12および再生ブロー弁13によって逆浸透膜1の濃縮水量を増加させて純水の回収率を下げることで、逆浸透膜1に生ずるスケールを抑制している。
【0016】
ちなみに、軟水器3の再生に必要な塩水タンク6に蓄えられた塩水は、給水圧力によるエゼクター効果を利用して軟水器3に供給されるので、ポンプ等の動力を用いる必要がない。
ところで、軟水器3の再生処理中におけるバイパス弁10および再生ブロー弁13は、例えば軟水器3が再生中であるかどうかを示す電気信号により開閉制御すると良い。或いは、軟水器3の再生をタイマ(図示せず)によって制御する場合、バイパス弁10および再生ブロー弁13とを開閉制御する弁制御タイマ(図示せず)を設けるとよい。そして、この弁制御タイマの指令によって、それぞれの弁の開閉制御を行うように構成するとよい。この場合、純水の生成が中断することが無いように、弁制御タイマは軟水器3の再生開始時間よりもやや早く弁の開指令を出すとともに、軟水器3の再生終了時間よりもやや遅く弁の閉指令を出すように設定するのが望ましい。
【0017】
さて、本発明に係る純水製造装置の逆浸透膜1で生成された純水は、例えば燃料電池(図示せず)の改質器等、純水を必要とする供給先に供給路を介して送出される。この供給路には前述したように、供給路を流れる純水の圧力を検出する圧力センサ20が設けられ、供給路の内圧が所定の圧力値を超えたとき、逆浸透膜1への給水を遮断する閉止弁11が設けられている。
【0018】
そして、純水を使用する供給先側で純水の受給/停止を制御するよう構成されている場合、逆浸透膜1の純水排出側の配管に設けられた圧力センサ20によって、供給先における純水受給の停止を検出する。
すなわち、従来の純水製造装置にあっては、純水の供給先で純水の受給が停止された場合、その受給停止を検出する手段がないため、逆浸透膜1への供給水は全て濃縮水としてピット5に排出されていた。しかし、本発明の純水製造装置は、上述したように逆浸透膜1の純水排出側の配管に設けられた圧力センサ20によって検出された圧力が所定の圧力値を超えたとき、純水の供給先で受給の停止があったものとして検出している。そして、逆浸透膜1の入口に設けられた閉止弁11を閉止する。このため給水が無駄に消費されることがない。
【0019】
更には、この閉止弁11が逆浸透膜1の入口に設けられているので、純水の生成を行わない場合であっても、軟水器3の再生処理を行わせることが可能である。
更には、本発明で用いる弁をバッテリ7で駆動可能な電磁弁で構成することが望ましい。バッテリ7で駆動可能な電磁弁を用いることで、純水製造装置に電源を供給することなく純水を製造することができる。また、軟水器10に設けた弁にシングルコントロール弁を用いると、電源喪失時(停電時)でも給水の供給を継続することが可能となる。この為、外部から電源供給が無いような場所でも純水を製造することが可能となり、燃料電池の発電を始動させることができるため、燃料電池用の純水製造装置として好適である。
尚、本発明は上述した実施形態に限定されるものではなく、その要旨を逸脱しない範囲で種々変型して実施することができる。
【0020】
【発明の効果】
以上述べたように、本発明の純水製造装置によれば、軟水器の再生中であっても、バイパス弁で給水(原水)を逆浸透膜へバイパスさせているので、純水を連続生成することが可能となる。このため、純水を保存するタンクおよびポンプ等の付帯設備が不要となり、純水製造装置を小型化することができる。
【0021】
更には各種制御弁類をバッテリで駆動制御しているので、外部から電源供給が無いような場所で燃料電池を起動させる場合であっても、純水の製造が可能となり、燃料電池用の純水製造装置として好適である等の実用上多大なる効果が奏せられる。
【図面の簡単な説明】
【図1】本発明の一実施形態に係る純水製造装置の概略構成を示す図。
【符号の説明】
1 逆浸透膜
3 軟水器
4 流量調整継ぎ手
10 バイパス弁
11 閉止弁
12 再生用流量継ぎ手
13 再生ブロー弁
20 圧力センサ
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a pure water producing apparatus combining a water softener and a reverse osmosis membrane, and more particularly to a pure water producing apparatus capable of continuously producing pure water even during regeneration of a water softener.
[0002]
[Related background art]
Recently, as a method of desalinating feed water (raw water), an acid or the like is added to the feed water (raw water), the pH is adjusted, and the water is softened by the softener. A desalination method of treating with a membrane is known (for example, see Patent Document 1). And the pure water production apparatus which applied this desalination method is also widely applied.
[0003]
The characteristics of the reverse osmosis membrane used in such a water treatment apparatus are degraded due to the scale of a chlorine component or calcium contained in the feed water (raw water). Therefore, in general, chlorine contained in the feed water (raw water) is removed by filtration with activated carbon or a catalyst, and hard components such as calcium are removed by a water softener (water softening treatment). To give to. For this reason, the water softener needs to be periodically regenerated to remove hard components such as calcium.
[0004]
By the way, in such a pure water production apparatus, the soft water cannot be supplied to the reverse osmosis membrane during the regeneration period of the water softener, and the pure water production is interrupted. Therefore, when continuous supply of pure water is required, a pure water tank is generally prepared to prepare a pure water tank so that production of pure water is not interrupted even during regeneration of the water softener. Is stored, and during the regeneration of the water softener, the pure water stored in the pure water tank is supplied to its supply destination.
[0005]
[Patent Document 1]
Japanese Patent No. 3278918 [0006]
[Problems to be solved by the invention]
However, in order to generate the pure water stored in the above-described pure water tank, it is necessary to prepare a pure water producing apparatus having a pure water generating capacity equal to or higher than a pure water amount which is always required. Further, during regeneration of the water softener, there is a problem that it is necessary to prepare a pump power or the like for sending out the pure water stored in the pure water tank to a supply destination.
[0007]
The present invention has been made in view of such circumstances, and its object is to provide a pure water production apparatus configured by combining a water softener and a reverse osmosis membrane, even during regeneration of the water softener, An object of the present invention is to provide a pure water producing apparatus capable of generating pure water.
[0008]
[Means for Solving the Problems]
In order to achieve the above-described object, the pure water production apparatus according to the present invention is suitable for producing pure water to be continuously supplied to a fuel cell, for example, in which raw water is softened through a water softener. A pure water producing apparatus for generating pure water by a reverse osmosis membrane, wherein bypass means for supplying raw water to the reverse osmosis membrane by bypassing the water softener at the time of regeneration of the water softener; A concentrated water amount adjusting means for adjusting a discharge flow rate of the separated concentrated water.
[0009]
Further, a pure water pressure sensor for detecting a discharge pressure of the pure water separated by the reverse osmosis membrane, and the reverse osmosis when the discharge pressure of the pure water detected by the pure water pressure sensor is higher than a preset pressure. And a supply shutoff means for interrupting the supply of soft water and / or raw water to the membrane.
The concentrated water amount adjusting means is configured to adjust a predetermined concentrated water discharge flow rate during regeneration of the water softener.
Therefore, according to the pure water production apparatus of the present invention, it is possible to provide a pure water production apparatus capable of continuously producing pure water even during regeneration of the water softener.
[0010]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, a pure water production apparatus according to the present invention will be described with reference to the drawings.
FIG. 1 is a diagram showing a schematic configuration of a pure water producing apparatus according to one embodiment, and illustrates, for example, a pure water producing apparatus suitable for producing soft water to be continuously supplied to a fuel cell.
[0011]
This pure water production apparatus basically separates feed water (raw water) into pure water and concentrated water with a reverse osmosis membrane 1, and removes chlorine and calcium components in the raw water supplied to the reverse osmosis membrane 1. A pre-processing filter 2 and a water softener 3 are provided. The pretreatment filter 2 removes chlorine from raw water. Then, after a hard component such as calcium contained in the raw water from which the chlorine content has been removed is removed by the water softener 3, the water is supplied to the reverse osmosis membrane 1. Further, the reverse osmosis membrane 1 is provided with a flow rate adjusting joint 4 for adjusting and discharging the flow rate of the concentrated water generated during the production of pure water, and is continuously blown to the pits 5 and the like. It should be noted that a flow control valve (not shown) capable of manually adjusting the opening degree may be applied instead of the flow connection 4.
[0012]
The water softener 3 is provided for the purpose of removing hardness components such as calcium in raw water as described above. However, since the calcium removed by the softening of the raw water is accumulated in the water softener 3, it is necessary to periodically regenerate the water softener 3. In order to perform this regeneration treatment, a salt water tank 6 storing an aqueous solution of sodium chloride is connected to the water softener 3. Then, the salt water is ion-exchanged with the calcium accumulated in the ion exchange resin filled in the water softener 3 to regenerate the water softener 3. Preferably, the supply of the salt water in the salt water tank 6 is configured to use the ejector effect by the raw water inflow pressure.
[0013]
By the way, in the pure water production apparatus of the present invention, the bypass valve 10 for bypassing the water softener 3 is provided with the water softener 3 so that the water can be supplied to the reverse osmosis membrane 1 even during the regeneration treatment of the water softener 3. It is provided between the inlet pipe and the outlet pipe. By opening the bypass valve 10, a part of the raw water is supplied to the reverse osmosis membrane 1 even during regeneration of the water softener 3, so that the generation of pure water is not interrupted.
[0014]
Further, a pressure sensor 20 for detecting a water pressure flowing in a supply path of pure water generated from the reverse osmosis membrane 1 is provided in the supply path. The pressure sensor 20 plays a role of driving the shutoff valve 11 that shuts off water supply to the reverse osmosis membrane 1 when the detected pressure exceeds a predetermined pressure.
Also, as described above, during the regeneration process of the water softener 3, when the raw water containing the hardness component bypassed from the pretreatment filter 2 via the bypass valve 10 is supplied to the reverse osmosis membrane 1, the hardness component (calcium content) is reduced. In order to suppress the adhesion of scale due to (1), a flow joint 12 for regeneration for reducing the recovery rate of the reverse osmosis membrane 1 and a regeneration blow valve 13 are provided on the reverse osmosis membrane 1. Although not particularly shown, a flow rate adjusting valve that can manually adjust the opening degree may be applied to the regeneration flow rate joint.
[0015]
According to the pure water producing apparatus configured as described above, the chlorine content is always removed by the pretreatment filter 2, and the raw water from which the chlorine content has been removed is further softened by the water softener 3. The pure water is generated by supplying it to 1.
On the other hand, during the regeneration process of the water softener 3, a part of the raw water supplied to the water softener 3 is supplied to the reverse osmosis membrane 1 via the bypass valve 10. Then, the reverse osmosis membrane 1 receives this raw water supply and produces pure water. That is, in the conventional pure water production apparatus, pure water cannot be obtained during regeneration of the water softener because the bypass valve 10 is not provided, but according to the pure water production apparatus of the present invention, As a result, the raw water can be supplied to the reverse osmosis membrane 1, so that the production of pure water can be continued even during the regeneration of the water softener 3. However, since the raw water is directly supplied to the reverse osmosis membrane 1, the scale contained in the raw water may adhere to the reverse osmosis membrane 1. Therefore, in the present apparatus, during the regeneration of the water softener 3, the concentrated flow rate of the reverse osmosis membrane 1 is increased by the regeneration flow rate joint 12 and the regeneration blow valve 13 to reduce the recovery rate of the pure water, so that the reverse osmosis membrane 1 The resulting scale is suppressed.
[0016]
Incidentally, since the salt water stored in the salt water tank 6 necessary for regeneration of the water softener 3 is supplied to the water softener 3 by using the ejector effect by the feed water pressure, it is not necessary to use the power of a pump or the like.
Incidentally, the bypass valve 10 and the regeneration blow valve 13 during the regeneration process of the water softener 3 may be controlled to open and close by an electric signal indicating whether or not the water softener 3 is being regenerated, for example. Alternatively, when the regeneration of the water softener 3 is controlled by a timer (not shown), a valve control timer (not shown) for controlling the opening and closing of the bypass valve 10 and the regeneration blow valve 13 may be provided. And it is good to be comprised so that opening / closing control of each valve may be performed by the command of this valve control timer. In this case, the valve control timer issues a valve opening command slightly earlier than the regeneration start time of the water softener 3 and slightly later than the regeneration end time of the water softener 3 so that the generation of pure water is not interrupted. It is desirable to set so as to issue a valve closing command.
[0017]
Now, the pure water generated by the reverse osmosis membrane 1 of the pure water producing apparatus according to the present invention passes through a supply path to a supply destination requiring the pure water, such as a reformer of a fuel cell (not shown). Sent out. As described above, the supply path is provided with the pressure sensor 20 for detecting the pressure of the pure water flowing through the supply path, and when the internal pressure of the supply path exceeds a predetermined pressure value, the supply of water to the reverse osmosis membrane 1 is performed. A shutoff valve 11 for shutting off is provided.
[0018]
When the supply / stop of the pure water is controlled on the supply side using the pure water, the pressure sensor 20 provided on the pipe on the pure water discharge side of the reverse osmosis membrane 1 causes the supply at the supply destination to be stopped. Detects stoppage of pure water supply.
That is, in the conventional pure water production apparatus, when the supply of pure water is stopped at the destination of pure water, there is no means for detecting the stop of the supply of pure water, so that the supply of water to the reverse osmosis membrane 1 is all It was discharged to pit 5 as concentrated water. However, as described above, when the pressure detected by the pressure sensor 20 provided on the pipe on the pure water discharge side of the reverse osmosis membrane 1 exceeds the predetermined pressure value, the pure water production apparatus of the present invention Has been detected as having stopped receiving at the supply destination. Then, the closing valve 11 provided at the inlet of the reverse osmosis membrane 1 is closed. Therefore, the water supply is not wasted.
[0019]
Further, since the shut-off valve 11 is provided at the inlet of the reverse osmosis membrane 1, the regeneration of the water softener 3 can be performed even when pure water is not generated.
Furthermore, it is desirable that the valve used in the present invention is constituted by an electromagnetic valve that can be driven by the battery 7. By using an electromagnetic valve that can be driven by the battery 7, pure water can be produced without supplying power to the pure water producing apparatus. Further, if a single control valve is used as a valve provided in the water softener 10, the supply of water can be continued even when the power is lost (at the time of a power failure). For this reason, pure water can be produced even in a place where there is no power supply from the outside, and power generation of the fuel cell can be started, which is suitable as a pure water producing apparatus for a fuel cell.
Note that the present invention is not limited to the above-described embodiment, and can be implemented with various modifications without departing from the gist thereof.
[0020]
【The invention's effect】
As described above, according to the pure water production apparatus of the present invention, even during regeneration of the water softener, the feed water (raw water) is bypassed to the reverse osmosis membrane by the bypass valve, so that pure water is continuously produced. It is possible to do. For this reason, ancillary equipment such as a tank and a pump for storing pure water is not required, and the pure water producing apparatus can be downsized.
[0021]
Furthermore, since the various control valves are driven and controlled by the battery, even when the fuel cell is started in a place where there is no external power supply, pure water can be produced, and the pure water for the fuel cell can be produced. Practically great effects such as being suitable as a water production device can be obtained.
[Brief description of the drawings]
FIG. 1 is a diagram showing a schematic configuration of a pure water production apparatus according to one embodiment of the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Reverse osmosis membrane 3 Water softener 4 Flow rate adjustment joint 10 Bypass valve 11 Shut off valve 12 Regeneration flow rate joint 13 Regeneration blow valve 20 Pressure sensor

Claims (4)

軟水器を介して原水を軟水化処理した後、逆浸透膜を介して純水を生成する純水製造装置であって、
前記軟水器の再生時に該軟水器をバイパスして前記逆浸透膜に原水を供給するバイパス手段と、
前記逆浸透膜で分離した濃縮水の排出流量を調整する濃縮水量調整手段と
を具備したことを特徴とする純水製造装置。
A pure water production device for producing pure water through a reverse osmosis membrane after softening raw water through a water softener,
Bypass means for supplying raw water to the reverse osmosis membrane by bypassing the water softener during regeneration of the water softener,
A pure water production apparatus comprising: a concentrated water amount adjusting means for adjusting a discharge flow rate of the concentrated water separated by the reverse osmosis membrane.
請求項1に記載の純水製造装置において、更に前記逆浸透膜で分離した純水の排出圧力を検出する純水圧力センサと、
この純水圧力センサで検出した純水の排出圧力が予め設定された圧力より高い場合、前記逆浸透膜への軟水および/または原水の供給を遮断する供給遮断手段と
を備えたことを特徴とする純水製造装置。
The pure water production apparatus according to claim 1, further comprising: a pure water pressure sensor for detecting a discharge pressure of the pure water separated by the reverse osmosis membrane;
When the discharge pressure of the pure water detected by the pure water pressure sensor is higher than a preset pressure, a supply shut-off means for shutting off the supply of soft water and / or raw water to the reverse osmosis membrane is provided. Pure water production equipment.
前記濃縮水量調整手段は、前記軟水器の再生時に所定の濃縮水の排出流量に調整するものである請求項1または2に記載の純水製造装置。3. The pure water production apparatus according to claim 1, wherein the concentrated water amount adjusting means adjusts the discharged flow rate of the concentrated water to a predetermined flow rate during regeneration of the water softener. 4. 請求項1または2に記載の純水製造装置において、
前記逆浸透膜で分離された前記純水を燃料電池に供給するものである純水製造装置。
The pure water production apparatus according to claim 1 or 2,
A pure water production apparatus for supplying the pure water separated by the reverse osmosis membrane to a fuel cell.
JP2002339255A 2002-11-22 2002-11-22 Pure water production equipment Expired - Fee Related JP4062433B2 (en)

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009112921A (en) * 2007-11-05 2009-05-28 Miura Co Ltd Water treatment system
WO2011052505A1 (en) * 2009-10-27 2011-05-05 パナソニック電工株式会社 Water processing device
CN102765824A (en) * 2011-05-05 2012-11-07 吴光夏 Water treatment method and equipment
JP2013188682A (en) * 2012-03-13 2013-09-26 Miura Co Ltd Water treatment system
JP2019188270A (en) * 2018-04-18 2019-10-31 日本ウォーターシステム株式会社 Water treatment apparatus
WO2020110852A1 (en) * 2018-11-27 2020-06-04 シャープ株式会社 Water purification device and household water purifier
JP2021087912A (en) * 2019-12-04 2021-06-10 Jr東日本コンサルタンツ株式会社 Cleaning device

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009112921A (en) * 2007-11-05 2009-05-28 Miura Co Ltd Water treatment system
WO2011052505A1 (en) * 2009-10-27 2011-05-05 パナソニック電工株式会社 Water processing device
CN102765824A (en) * 2011-05-05 2012-11-07 吴光夏 Water treatment method and equipment
JP2013188682A (en) * 2012-03-13 2013-09-26 Miura Co Ltd Water treatment system
JP2019188270A (en) * 2018-04-18 2019-10-31 日本ウォーターシステム株式会社 Water treatment apparatus
JP7078983B2 (en) 2018-04-18 2022-06-01 日本ウォーターシステム株式会社 Water treatment equipment
WO2020110852A1 (en) * 2018-11-27 2020-06-04 シャープ株式会社 Water purification device and household water purifier
JP7337839B2 (en) 2018-11-27 2023-09-04 シャープ株式会社 Water purifiers and household water purifiers
JP2021087912A (en) * 2019-12-04 2021-06-10 Jr東日本コンサルタンツ株式会社 Cleaning device

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