JP2003157869A - Water treating device for fuel cell - Google Patents

Water treating device for fuel cell

Info

Publication number
JP2003157869A
JP2003157869A JP2001357909A JP2001357909A JP2003157869A JP 2003157869 A JP2003157869 A JP 2003157869A JP 2001357909 A JP2001357909 A JP 2001357909A JP 2001357909 A JP2001357909 A JP 2001357909A JP 2003157869 A JP2003157869 A JP 2003157869A
Authority
JP
Japan
Prior art keywords
water
fuel cell
raw water
heat
treatment device
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
Application number
JP2001357909A
Other languages
Japanese (ja)
Other versions
JP3906677B2 (en
Inventor
Yoshiteru Misumi
好輝 三角
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.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries 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 Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP2001357909A priority Critical patent/JP3906677B2/en
Publication of JP2003157869A publication Critical patent/JP2003157869A/en
Application granted granted Critical
Publication of JP3906677B2 publication Critical patent/JP3906677B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)
  • Fuel Cell (AREA)

Abstract

PROBLEM TO BE SOLVED: To miniaturize an installation by stabilizing a resupply water amount and a resupply water temperature of a fuel cell regardless a water temperature fluctuation at season in a water treating device for the fuel cell. SOLUTION: In this water treating device for the fuel cell, after raw water in a raw water tank 1 is subjected to deionizing treatment in an RO membrane separation device 2 and an electric deionizing device 3, the water is supplied to the fuel cell 4, and before the raw water is subjected to membrane treatment, it is warmed by utilizing exhaust heat of the fuel cell 4. For example, air at a high temperature generated in the fuel cell 4 is sent to the raw water tank 1 by blower B.

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、燃料電池へ用水を
供給する水処理装置に係り、特に、原水を膜処理手段を
有する浄化手段で浄化した後燃料電池に供給する水処理
装置において、原水の水温の季節変動に対する給水量の
安定化を実現した燃料電池用水処理装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water treatment device for supplying water to a fuel cell, and more particularly to a water treatment device for supplying raw water to a fuel cell after purifying the raw water by a purification means having a membrane treatment means. The present invention relates to a fuel cell water treatment device that realizes stabilization of the amount of supplied water with respect to seasonal fluctuations in the water temperature.

【0002】[0002]

【従来の技術】燃料電池は、水素と酸素を電気化学的に
反応させることにより直接電気を取り出す発電システム
であり、発電容量にかかわらず発電効率が高く、窒素酸
化物の排出量も少ない。
2. Description of the Related Art A fuel cell is a power generation system that directly takes out electricity by electrochemically reacting hydrogen and oxygen, has high power generation efficiency regardless of power generation capacity, and emits a small amount of nitrogen oxides.

【0003】燃料電池には、電解質の種類により、アル
カリ型、固体高分子型、リン酸型、溶融炭酸塩型、固体
電解質型といった各種のものがあるが、いずれの燃料電
池にあっても、改質器の水蒸気用水として、またリン酸
型燃料電池では燃料電池本体や固体高分子の冷却水とし
て、水を補給する必要があり、このため、市水等を浄化
して燃料電池に供給するための水処理装置が付設されて
いる。
There are various types of fuel cells such as alkaline type, solid polymer type, phosphoric acid type, molten carbonate type, and solid electrolyte type, depending on the type of electrolyte. It is necessary to replenish water as steam water for the reformer, and as cooling water for the fuel cell body and solid polymer in phosphoric acid fuel cells. Therefore, city water is purified and supplied to the fuel cell. Water treatment equipment is attached.

【0004】図5は、燃料電池とその水処理装置の一例
を示す系統図である。市水は、水処理装置の原水槽1か
らポンプPで逆浸透(RO)膜分離装置2に導入され
て脱イオン処理され、更に電気脱イオン装置3で脱イオ
ン処理された後、燃料電池4の純水タンク4Aに送給さ
れる。
FIG. 5 is a system diagram showing an example of a fuel cell and its water treatment device. City water is introduced into the reverse osmosis (RO) membrane separation device 2 from the raw water tank 1 of the water treatment device by the pump P 1 to be deionized, and further deionized by the electric deionization device 3, and then the fuel cell. 4 is fed to the pure water tank 4A.

【0005】なお、図5に示す燃料電池システムは、燃
料電池4の排熱を風呂の給湯に利用するものであり、燃
料電池本体4Bの発生熱で貯湯槽5内の市水を加熱する
ように構成されている。この貯湯槽5内の湯はポンプP
で風呂に送給されている。
The fuel cell system shown in FIG. 5 uses the exhaust heat of the fuel cell 4 to supply hot water to the bath, so that the heat generated by the fuel cell body 4B heats the city water in the hot water storage tank 5. Is configured. The hot water in this hot water storage tank 5 is pump P
It is sent to the bath at 2 .

【0006】なお、この水処理装置において、RO膜分
離装置2の濃縮水は系外へ排出されるが、電気脱イオン
装置3の濃縮水は原水槽1に戻され、循環処理される。
In this water treatment device, the concentrated water of the RO membrane separation device 2 is discharged to the outside of the system, but the concentrated water of the electric deionization device 3 is returned to the raw water tank 1 and circulated.

【0007】[0007]

【発明が解決しようとする課題】RO膜分離装置等の膜
分離装置では、導入される原水の水温により生産水量が
大きく影響され、原水の水温が低下すると生産水量が大
幅に低下する。
In a membrane separation device such as an RO membrane separation device, the amount of produced water is greatly affected by the temperature of the raw water introduced, and when the temperature of the raw water decreases, the amount of produced water decreases significantly.

【0008】即ち、水の粘性は水温により変化し、水温
が低いと粘性が著しく高まる。例えば、水温20℃の水
の粘性率は1.0020cpであるのに対して、水温5
℃の水では粘性率は1.25cpに約25%も上昇す
る。そして、このように粘性の高くなった低温の水は膜
面を通過し難く、このため膜分離装置の生産水量は大幅
に低下する。
That is, the viscosity of water changes depending on the water temperature, and when the water temperature is low, the viscosity remarkably increases. For example, the viscosity of water at a water temperature of 20 ° C. is 1.0020 cp, while the water temperature of 5 ° C.
With water at 0 ° C, the viscosity increases to 1.25 cp by about 25%. Then, the low-temperature water whose viscosity becomes high hardly passes through the membrane surface, so that the amount of water produced by the membrane separation apparatus is significantly reduced.

【0009】従って、従来の燃料電池用水処理装置で
は、水温の低い冬期は、水温の高い夏期よりもRO膜分
離装置の生産水量が低下する。そこで、この生産水量が
低下する冬期において、燃料電池の補給水量が不足しな
いように、RO膜分離装置を含む水処理装置の給水量に
余裕を持たせるようにしている。
Therefore, in the conventional fuel cell water treatment device, the amount of water produced by the RO membrane separator is lower in the winter when the water temperature is low than in the summer when the water temperature is high. Therefore, in the winter when the amount of produced water decreases, a sufficient amount of water is supplied to the water treatment device including the RO membrane separation device so that the amount of supplementary water to the fuel cell does not become insufficient.

【0010】具体的には、冬期の水温が7℃、夏期の水
温が22℃と想定した場合、冬期のRO膜分離装置の生
産水量の低下を見込んで、夏期の水温で設計される設備
能力に対して、約45%の余裕を持たせるように設備が
大型化されている。
[0010] Specifically, assuming that the water temperature in winter is 7 ° C and the water temperature in summer is 22 ° C, the facility capacity designed at the water temperature in summer is expected in consideration of the decrease in the amount of water produced by the RO membrane separator in winter. On the other hand, the equipment has been enlarged so as to have a margin of about 45%.

【0011】また、水温の季節変動で燃料電池の補給水
の水温が変動するため、燃料電池の運転が不安定になる
おそれもあった。
Further, the water temperature of the makeup water of the fuel cell fluctuates due to the seasonal fluctuation of the water temperature, so that the operation of the fuel cell may become unstable.

【0012】本発明は、上記従来の問題点を解決し、燃
料電池用水処理装置において、水温の季節変動にかかわ
らず燃料電池の補給水量と補給水温を安定化させること
により、設備の小型化を図ると共に、燃料電池の安定運
転を可能とする燃料電池用水処理装置を提供することを
目的とする。
The present invention solves the above-mentioned conventional problems, and in a fuel cell water treatment apparatus, by stabilizing the amount of water supplied and the temperature of the water supplied to the fuel cell regardless of seasonal fluctuations in water temperature, the equipment can be made smaller. An object of the present invention is to provide a water treatment device for a fuel cell, which aims at achieving stable operation of the fuel cell.

【0013】[0013]

【課題を解決するための手段】本発明の燃料電池用水処
理装置は、原水を膜処理手段を有する浄化手段により浄
化した後、燃料電池に供給する水処理装置において、膜
処理前の原水を該燃料電池の排熱を利用して加温する加
温手段を有することを特徴とするものである。
A water treatment apparatus for a fuel cell according to the present invention is a water treatment apparatus for supplying raw water to a fuel cell after purifying the raw water by a purifying means having a membrane treatment means. It is characterized by having a heating means for heating by utilizing exhaust heat of the fuel cell.

【0014】本発明の燃料電池用水処理装置では、燃料
電池の排熱を利用して水処理装置の膜処理用の原水を加
温することにより、冬期の水温低下による生産水量の低
下を防止して、常に高い生産水量を確保することができ
る。このため、RO膜分離装置等の水処理装置の設備能
力を過剰に設定する必要がなくなり、設備の小型化を図
ることが可能となる。また、膜処理用の原水の水温を安
定化させることにより、燃料電池の補給水の水温が安定
し、燃料電池を安定に運転することが可能となる。
In the fuel cell water treatment device of the present invention, the exhaust heat of the fuel cell is used to heat the raw water for membrane treatment of the water treatment device, thereby preventing a decrease in the amount of water produced due to a decrease in the water temperature in winter. Therefore, it is possible to always secure a high production water amount. Therefore, it becomes unnecessary to excessively set the facility capacity of the water treatment device such as the RO membrane separation device, and the facility can be downsized. Further, by stabilizing the water temperature of the raw water for membrane treatment, the water temperature of the makeup water of the fuel cell becomes stable, and the fuel cell can be operated stably.

【0015】本発明では、この膜処理用の原水の加温に
燃料電池の排熱を利用するため、加温のための大掛かり
な設備を増設する必要がなく、また燃料電池の総合的な
効率を高めることができ、経済的である。
In the present invention, since the exhaust heat of the fuel cell is used to heat the raw water for membrane treatment, it is not necessary to add large-scale equipment for heating, and the overall efficiency of the fuel cell is increased. Can be increased and is economical.

【0016】本発明において、加温手段としては、次の
,,が好適である。 燃料電池の箱体内に設置された熱交換器と、原水を
該熱交換器に導入して熱交換した後、浄化手段に導入す
る配管とを備えるもの; 燃料電池の箱体内の空気を送出する空気送出手段
と、該空気送出手段が送出した空気と原水とを熱交換さ
せる熱交換手段とを備えるもの。 貯湯槽内の温水の一部を原水に混ぜるもの。
In the present invention, the following are preferable as the heating means. A heat exchanger installed in the box of the fuel cell and a pipe for introducing raw water into the heat exchanger for heat exchange and then introducing it into the purifying means; Delivering air in the box of the fuel cell An air delivery means and a heat exchange means for exchanging heat between the air delivered by the air delivery means and the raw water. Mixing part of the warm water in the hot water tank with raw water.

【0017】このような加温手段は、原水を膜の耐熱温
度以下に加温する加温量調節手段を有することが好まし
い。
Such a heating means preferably has a heating amount adjusting means for heating the raw water to a temperature not higher than the heat resistant temperature of the membrane.

【0018】[0018]

【発明の実施の形態】以下に図面を参照して本発明の実
施の形態を詳細に説明する。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described in detail below with reference to the drawings.

【0019】図1〜4は、それぞれ本発明の実施の形態
を示す系統図である。なお、図1〜4の燃料電池用水処
理装置は、RO膜分離装置2に導入される水の加温手段
が設けられていること以外は、図5に示す燃料電池用水
処理装置と同様の構成とされており、図1〜3におい
て、図5に示す部材と同一機能を奏する部材には同一符
号を付してある。
1 to 4 are system diagrams each showing an embodiment of the present invention. The fuel cell water treatment device of FIGS. 1 to 4 has the same configuration as that of the fuel cell water treatment device shown in FIG. 5, except that a heating means for water introduced into the RO membrane separation device 2 is provided. In FIGS. 1 to 3, members having the same functions as those shown in FIG. 5 are designated by the same reference numerals.

【0020】図1〜4のいずれにおいても、原水槽1内
の市水は、ポンプPで逆浸透(RO)膜分離装置2に
導入されて脱イオン処理され、更に電気脱イオン装置3
で脱イオン処理された後、燃料電池4の純水タンク4A
に送給される。燃料電池本体4Bの発生熱で貯湯槽5内
の市水が加熱される。貯湯槽5内の湯はポンプPで風
呂に送給される。
In any of FIGS. 1 to 4, the city water in the raw water tank 1 is introduced into the reverse osmosis (RO) membrane separation device 2 by the pump P 1 and is deionized, and further the electric deionization device 3 is used.
After being deionized in, the pure water tank 4A of the fuel cell 4
Sent to. The city water in the hot water storage tank 5 is heated by the heat generated by the fuel cell body 4B. The hot water in the hot water storage tank 5 is sent to the bath by the pump P 2 .

【0021】図1の燃料電池用水処理装置では、燃料電
池4内に、燃料電池4内の高温の空気を排出するブロワ
(空気送出手段)Bを設けており、この高温の空気を原
水槽1に送給して原水槽1内の原水を曝気することによ
り加温する。この水処理装置においては、RO膜分離装
置2の入口側の配管に温度計Tを設け、図示しない制御
装置(インバータ回路等)により、この温度計Tの測定
結果に基いてブロワBの送風量を調整して原水槽1へ送
給する空気量を調節することにより、膜処理用の原水の
水温が後述の好適温度となるように制御する。
In the fuel cell water treatment apparatus of FIG. 1, a blower (air delivery means) B for discharging the high temperature air in the fuel cell 4 is provided in the fuel cell 4, and the high temperature air is supplied to the raw water tank 1. To heat the raw water in the raw water tank 1 by aeration. In this water treatment device, a thermometer T is provided in the pipe on the inlet side of the RO membrane separation device 2, and a blower B of the blower B is blown based on the measurement result of the thermometer T by a control device (inverter circuit or the like) not shown. Is adjusted to adjust the amount of air sent to the raw water tank 1 to control the water temperature of the raw water for membrane treatment to a suitable temperature described later.

【0022】なお、このように、ブロワBを設け燃料電
池4内の高温の空気により原水を加温する場合、RO膜
分離装置2の入口側の配管に熱交換器を設け、この熱交
換器において、RO膜分離装置2に導入される原水と高
温の空気とで熱交換を行って膜処理用の原水を加温して
も良い。この場合において、水温の調節は、ブロワBの
送風量の調節によらず、原水をこの熱交換器に導入した
後RO膜分離装置2に給水するバイパス配管を、原水槽
1からRO膜分離装置2に原水を給水する配管に設け、
熱交換器に導入して加温する原水量を調節することによ
り行ってもよい。
In this way, when the blower B is provided and the raw water is heated by the high temperature air in the fuel cell 4, a heat exchanger is provided in the pipe on the inlet side of the RO membrane separation device 2, and this heat exchanger is used. In the above, the raw water for membrane treatment may be heated by exchanging heat between the raw water introduced into the RO membrane separation device 2 and the high temperature air. In this case, the water temperature is not adjusted by adjusting the air flow rate of the blower B, and the bypass pipe for supplying raw water to the RO membrane separation device 2 after introducing the raw water into the heat exchanger is connected to the RO membrane separation device from the raw water tank 1. Installed in the pipe for supplying raw water to 2,
It may be carried out by adjusting the amount of raw water introduced into the heat exchanger and heated.

【0023】図2に示す燃料電池用水処理装置は、貯湯
槽5を熱交換器とし、原水槽1からRO膜分離装置2に
原水を送給する配管にバイパス配管を設けて、このバイ
パス配管で膜処理用の原水の少なくとも一部を貯湯槽5
に送り、貯湯槽5内の湯で加温した後、RO膜分離装置
2に導入するようにしたものである。
In the fuel cell water treatment apparatus shown in FIG. 2, the hot water storage tank 5 is used as a heat exchanger, and a bypass pipe is provided in the pipe for feeding raw water from the raw water tank 1 to the RO membrane separation device 2. Hot water storage tank 5 for at least a part of raw water for membrane treatment
And is heated by the hot water in the hot water storage tank 5, and then introduced into the RO membrane separation device 2.

【0024】この水処理装置にあっても、RO膜分離装
置2の入口側の配管に温度計Tを設け、図示しない制御
装置(PIDコントローラ等)により、この温度計Tの
測定結果に基いてバルブVの開度を調整して、貯湯槽5
へ送給して加温する原水量を調節することにより、膜処
理用の原水の水温が後述の好適温度となるように制御す
る。
Also in this water treatment device, a thermometer T is provided in the pipe on the inlet side of the RO membrane separation device 2, and a control device (PID controller or the like) (not shown) is used to measure the temperature based on the thermometer T. Adjust the opening of the valve V to adjust the hot water storage tank 5
By controlling the amount of raw water that is fed to and heated, the water temperature of the raw water for membrane treatment is controlled to a suitable temperature described below.

【0025】図3に示す燃料電池用水処理装置は、燃料
電池4内の貯湯槽5の加熱のための伝熱管を熱交換器と
し、原水槽1からRO膜分離装置2に原水を送給する配
管にバイパス配管を設けて、このバイパス配管で膜処理
用の原水の少なくとも一部を燃料電池4の伝熱管で熱交
換して加温した後、RO膜分離装置2に導入するように
したものである。
In the fuel cell water treatment device shown in FIG. 3, a heat transfer tube for heating the hot water storage tank 5 in the fuel cell 4 is used as a heat exchanger, and raw water is fed from the raw water tank 1 to the RO membrane separation device 2. A bypass pipe is provided in the pipe, and at least a part of the raw water for membrane treatment is heat-exchanged and heated in the heat transfer pipe of the fuel cell 4 in the bypass pipe and then introduced into the RO membrane separation device 2. Is.

【0026】この水処理装置にあっても、RO膜分離装
置2の入口側の配管に温度計Tを設け、図示しない制御
装置(PIDコントローラ等)により、この温度計Tの
測定結果に基いてバルブVの開度を調整して、燃料電池
4内へ送給して加温する原水量を調節することにより、
膜処理用の原水の水温が後述の好適温度となるように制
御する。
Also in this water treatment device, a thermometer T is provided in the pipe on the inlet side of the RO membrane separation device 2, and a control device (PID controller or the like) (not shown) determines the temperature based on the measurement result of the thermometer T. By adjusting the opening degree of the valve V and adjusting the amount of raw water that is fed into the fuel cell 4 and heated.
The water temperature of the raw water for membrane treatment is controlled to a suitable temperature described later.

【0027】図4に示す燃料電池用水処理装置は、原水
槽1からRO膜分離装置2に原水を供給する配管に貯湯
槽5内の温水をポンプPにより導入するようにしたも
のである。
In the fuel cell water treatment apparatus shown in FIG. 4, hot water in the hot water storage tank 5 is introduced by a pump P 3 into a pipe for supplying raw water from the raw water tank 1 to the RO membrane separation device 2.

【0028】この水処理装置にあっても温度計Tの測定
結果に基づいてポンプPの吐出量を調整して、原水へ
の温水導入量を調節することにより、膜処理用の原水の
水温が後述の好適温度となるように制御する。
Even in this water treatment apparatus, the temperature of the raw water for membrane treatment is controlled by adjusting the discharge amount of the pump P 3 based on the measurement result of the thermometer T and adjusting the amount of hot water introduced into the raw water. Is controlled to a suitable temperature described later.

【0029】なお、図2,3,4の水処理装置におい
て、流量調整バルブVは原水槽1からの原水を直接RO
膜分離装置2に給水する配管に設けても良い。
In the water treatment device shown in FIGS. 2, 3 and 4, the flow rate adjusting valve V directly feeds the raw water from the raw water tank 1.
You may provide in the piping which supplies water to the membrane separation apparatus 2.

【0030】本発明において、膜処理用の原水の加温温
度は、膜の耐熱温度以下とする必要がある。この耐熱温
度は膜の材質によっても異なるが、一般的には約40℃
であり、従って、膜処理用の原水の加温温度は40℃以
下、特に35℃以下とするのが好ましい。ただし、この
加温温度が低過ぎると加温による生産水量の向上を図る
ことが困難であることから20℃以上とすることが好ま
しい。また、膜処理用の原水の水温が30〜35℃であ
ると、わずかではあるがイオン除去率が低減し、また、
バクテリアが発生し易くなることから、本発明において
は、膜処理される原水の加温温度は20〜30℃程度と
するのが好ましい。
In the present invention, the heating temperature of the raw water for membrane treatment must be lower than the heat resistant temperature of the membrane. This heat-resistant temperature varies depending on the material of the film, but is generally about 40 ° C.
Therefore, the heating temperature of the raw water for membrane treatment is preferably 40 ° C. or lower, and particularly preferably 35 ° C. or lower. However, if the heating temperature is too low, it is difficult to increase the amount of water produced by heating, so it is preferably set to 20 ° C. or higher. Further, when the water temperature of the raw water for membrane treatment is 30 to 35 ° C., the ion removal rate is slightly reduced, and
In the present invention, the heating temperature of the raw water to be membrane-treated is preferably about 20 to 30 ° C., since bacteria are easily generated.

【0031】なお、図1〜4に示す水処理装置は、RO
膜分離装置2と電気脱イオン装置3とを組み合わせたも
のであるが、本発明の水処理装置は、膜分離装置を備え
るものであれば良く、何ら図1〜4に示すものに限定さ
れれるものではない。本発明は、例えば、次のような構
成の燃料電池用水処理装置にも適用することができる。 RO膜分離装置 → 混床式イオン交換樹脂塔 RO膜分離装置 → RO膜分離装置 ナノ濾過(ルーズRO)膜分離装置 → 電気脱イ
オン装置 ナノ濾過膜分離装置 → 混床式イオン交換樹脂塔
The water treatment apparatus shown in FIGS.
Although the membrane separation device 2 and the electric deionization device 3 are combined, the water treatment device of the present invention is not limited as long as it has a membrane separation device, and is not limited to those shown in FIGS. Not a thing. The present invention can be applied to, for example, a fuel cell water treatment device having the following configuration. RO membrane separator → Mixed bed type ion exchange resin tower RO membrane separator → RO membrane separator Nano filtration (loose RO) membrane separator → Electrodeionization device Nano filtration membrane separator → Mixed bed ion exchange resin tower

【0032】また、図1〜4に示す燃料電池用水処理装
置の燃料電池4は、排熱を利用した貯湯槽5を有する
が、本発明において、燃料電池の構成については特に限
定されるものではなく、貯湯槽5のないものであっても
良い。
Further, the fuel cell 4 of the fuel cell water treatment apparatus shown in FIGS. 1 to 4 has a hot water storage tank 5 utilizing exhaust heat, but in the present invention, the structure of the fuel cell is not particularly limited. Alternatively, the hot water storage tank 5 may be omitted.

【0033】更に、図1〜4では、原水を原水槽1又は
原水槽1とRO膜分離装置2との間で加温しているが、
原水は、原水槽1の前段で加温しても良く、貯湯槽5へ
分岐される前の原水を加温しても良い。ただし、膜処理
用の原水を効率的に加温するためには、貯湯槽5への分
岐後の原水を加温するのが好ましく、また、原水槽1の
前段或いは原水槽1において原水を加温する場合には、
原水槽1の保温手段を設ける必要がある場合もある。
Further, in FIGS. 1 to 4, the raw water is heated between the raw water tank 1 or the raw water tank 1 and the RO membrane separation device 2.
The raw water may be heated before the raw water tank 1 or may be heated before being branched to the hot water storage tank 5. However, in order to efficiently heat the raw water for membrane treatment, it is preferable to heat the raw water after branching to the hot water storage tank 5, and the raw water is heated before the raw water tank 1 or in the raw water tank 1. If you want to warm
In some cases, it may be necessary to provide a heat insulating means for the raw water tank 1.

【0034】[0034]

【発明の効果】以上詳述した通り、本発明によれば、燃
料電池用水処理装置において、水温の季節変動にかかわ
らず燃料電池の補給水量と補給水温を安定化させること
により、設備の小型化と安定運転が可能となる。
As described in detail above, according to the present invention, in a fuel cell water treatment device, the amount of replenishment water and the replenishment water temperature of the fuel cell are stabilized regardless of the seasonal variation of the water temperature, thereby downsizing the equipment. And stable operation becomes possible.

【0035】しかも、本発明では燃料電池の排熱を有効
利用して原水を加温するため、この加温のための大掛か
りな設備を新たに増設する必要がなく、また、燃料電池
の総合的な効率を高めることができ、経済性にも優れ
る。
Moreover, in the present invention, since the exhaust heat of the fuel cell is effectively used to heat the raw water, it is not necessary to newly add a large-scale facility for this heating, and the total fuel cell The efficiency can be improved and the economy is excellent.

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

【図1】本発明の燃料電池用水処理装置の実施の形態を
示す系統図である。
FIG. 1 is a system diagram showing an embodiment of a fuel cell water treatment device of the present invention.

【図2】本発明の燃料電池用水処理装置の別の実施の形
態を示す系統図である。
FIG. 2 is a system diagram showing another embodiment of the fuel cell water treatment device of the present invention.

【図3】本発明の燃料電池用水処理装置の異なる実施の
形態を示す系統図である。
FIG. 3 is a system diagram showing a different embodiment of the fuel cell water treatment device of the present invention.

【図4】本発明の燃料電池用水処理装置の異なる実施の
形態を示す系統図である。
FIG. 4 is a system diagram showing another embodiment of the fuel cell water treatment device of the present invention.

【図5】従来の燃料電池用水処理装置を示す系統図であ
る。
FIG. 5 is a system diagram showing a conventional fuel cell water treatment device.

【符号の説明】[Explanation of symbols]

1 原水槽 2 RO膜分離装置 3 電気脱イオン装置 4 燃料電池 5 貯湯槽 1 raw water tank 2 RO membrane separator 3 Electric deionization equipment 4 fuel cells 5 hot water storage tank

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) B01D 61/58 B01D 61/58 C02F 1/469 H01M 8/00 Z H01M 8/00 C02F 1/46 103 Fターム(参考) 4D006 GA03 GA04 GA17 KA01 KA52 KA57 KA71 KB11 KB30 KE16P KE16Q PA01 PB06 PC80 4D061 DA03 DB13 EA09 EB04 EB37 EB39 GA09 GC05 5H027 AA02 DD06 KK48 ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI theme code (reference) B01D 61/58 B01D 61/58 C02F 1/469 H01M 8/00 Z H01M 8/00 C02F 1/46 103 F Term (reference) 4D006 GA03 GA04 GA17 KA01 KA52 KA57 KA71 KB11 KB30 KE16P KE16Q PA01 PB06 PC80 4D061 DA03 DB13 EA09 EB04 EB37 EB39 GA09 GC05 5H027 AA02 DD06 KK48

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 原水を膜処理手段を有する浄化手段によ
り浄化した後、燃料電池に供給する水処理装置におい
て、膜処理前の原水を該燃料電池の排熱を利用して加温
する加温手段を有することを特徴とする燃料電池用水処
理装置。
1. A water treatment apparatus for supplying raw water to a fuel cell after purifying the raw water by a purifying means having a membrane treatment means, wherein the raw water before the membrane treatment is heated by utilizing exhaust heat of the fuel cell. A water treatment device for a fuel cell, comprising:
【請求項2】 請求項1において、前記加温手段は、該
燃料電池の箱体内に設置された熱交換器と、 原水を該熱交換器に導入して熱交換した後、前記浄化手
段に導入する配管とを備えることを特徴とする燃料電池
用水処理装置。
2. The heating means according to claim 1, wherein the heating means is a heat exchanger installed in the box body of the fuel cell, and raw water is introduced into the heat exchanger to exchange heat with the heat exchanger. A water treatment device for a fuel cell, comprising: a pipe for introducing the water treatment device.
【請求項3】 請求項1において、前記加温手段は、該
燃料電池の箱体内の空気を送出する空気送出手段と、 該空気送出手段が送出した空気と原水とを熱交換させる
熱交換手段とを備えることを特徴とする燃料電池用水処
理装置。
3. The heating means according to claim 1, wherein the heating means sends out air in the box of the fuel cell, and heat exchange means for exchanging heat between the air sent out by the air sending means and raw water. A water treatment device for a fuel cell, comprising:
【請求項4】 請求項1において、更に該燃料電池の廃
熱により加温された温水を蓄える貯湯槽を備え、前記加
温手段は該貯湯槽内の温水の一部を原水に混ぜる混合手
段であることを特徴とする燃料電池用水処理装置。
4. The mixing means according to claim 1, further comprising a hot water storage tank for storing hot water heated by waste heat of the fuel cell, wherein the heating means mixes a part of the hot water in the hot water storage tank with raw water. A water treatment device for a fuel cell, wherein:
【請求項5】 請求項1ないし4のいずれか1項におい
て、前記加温手段は、原水を膜の耐熱温度以下に加温す
る加温調節手段を有することを特徴とする燃料電池用水
処理装置。
5. The fuel cell water treatment device according to claim 1, wherein the heating means has heating control means for heating the raw water to a temperature equal to or lower than the heat resistant temperature of the membrane. .
JP2001357909A 2001-11-22 2001-11-22 Water treatment device for fuel cell Expired - Fee Related JP3906677B2 (en)

Priority Applications (1)

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Application Number Priority Date Filing Date Title
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Country Link
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005183109A (en) * 2003-12-18 2005-07-07 Toshiba Fuel Cell Power Systems Corp Fuel cell power generation system and operation method therefor
JP2005296944A (en) * 2004-03-19 2005-10-27 Miura Co Ltd Water quality improving system
JP2005296945A (en) * 2004-03-19 2005-10-27 Miura Co Ltd Water quality improving system
WO2006100937A1 (en) * 2005-03-18 2006-09-28 Kurita Water Industries Ltd. Apparatus for producing pure water
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US11502323B1 (en) 2022-05-09 2022-11-15 Rahul S Nana Reverse electrodialysis cell and methods of use thereof
US11502322B1 (en) 2022-05-09 2022-11-15 Rahul S Nana Reverse electrodialysis cell with heat pump

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Publication number Priority date Publication date Assignee Title
JP2005183109A (en) * 2003-12-18 2005-07-07 Toshiba Fuel Cell Power Systems Corp Fuel cell power generation system and operation method therefor
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JP2005296944A (en) * 2004-03-19 2005-10-27 Miura Co Ltd Water quality improving system
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WO2006100937A1 (en) * 2005-03-18 2006-09-28 Kurita Water Industries Ltd. Apparatus for producing pure water
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US7955503B2 (en) 2005-03-18 2011-06-07 Kurita Water Industries Ltd. Pure water producing apparatus

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