JP2005097746A - Hydrogen-feeding device using solid polymer type water electrolysis tank - Google Patents

Hydrogen-feeding device using solid polymer type water electrolysis tank Download PDF

Info

Publication number
JP2005097746A
JP2005097746A JP2004313286A JP2004313286A JP2005097746A JP 2005097746 A JP2005097746 A JP 2005097746A JP 2004313286 A JP2004313286 A JP 2004313286A JP 2004313286 A JP2004313286 A JP 2004313286A JP 2005097746 A JP2005097746 A JP 2005097746A
Authority
JP
Japan
Prior art keywords
water
hydrogen
pressure vessel
lid
water electrolysis
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
JP2004313286A
Other languages
Japanese (ja)
Other versions
JP4206500B2 (en
Inventor
Tetsuya Inoue
鉄也 井上
Shogo Hamada
省吾 濱田
Hidehiko Maehata
英彦 前畑
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.)
Hitachi Zosen Corp
Original Assignee
Hitachi Zosen Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hitachi Zosen Corp filed Critical Hitachi Zosen Corp
Priority to JP2004313286A priority Critical patent/JP4206500B2/en
Publication of JP2005097746A publication Critical patent/JP2005097746A/en
Application granted granted Critical
Publication of JP4206500B2 publication Critical patent/JP4206500B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

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
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
    • 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

Abstract

<P>PROBLEM TO BE SOLVED: To provide a hydrogen-feeding device using a solid polymer type water electrolysis tank, which prevents the damage to an electrolyte film even when water is electrolyzed in a high pressure of about several tens MPa, moreover has sufficient pressure resistance, and simplifies/miniaturizes the structure of a pressure vessel. <P>SOLUTION: This hydrogen-feeding device has a pressure vessel 41 provided with a lid 42, for storing the water electrolysis tank 40. An electrolysis-tank-pressing foot 42a for pressing the water electrolysis tank 40 to a bottom wall of a main body of the pressure vessel 41 is installed between the water electrolysis tank 40 and the lid 42. A gap is formed between the water electrolysis tank 40 and the lid 42, which works as a section 43 for separating hydrogen gas from the liquid. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

この発明は、固体高分子電解膜を用いて水を電解し、陽極に酸素、陰極に水素を発生させる水電解槽に関し、より詳しくは、例えば燃料電池用水素ステーションで35〜70MPaの高圧水素ガスを供給することができる水素供給装置に関するものである。   The present invention relates to a water electrolyzer that electrolyzes water using a solid polymer electrolyte membrane and generates oxygen at an anode and hydrogen at a cathode, and more specifically, high-pressure hydrogen gas of 35 to 70 MPa, for example, at a hydrogen station for a fuel cell. The present invention relates to a hydrogen supply apparatus capable of supplying

固体高分子型水電解槽を用いた水素供給装置は、例えば特許文献1に開示されているように、従来より知られているものであり、その水電解槽(51)は、図6および図7に示すように、両端に配された陽極主電極(1)および陰極主電極(2)と、これらの主電極(1)(2)の間に直列に配された複数の単位セル(16)と、陽極主電極(1)−複数の単位セル(16)−陰極主電極(2)の組み合わせを両側から挟む一対の端板(13)とから主として構成されている。1つのセル(16)は、複極板(90)の陽極側、陽極給電体(7)、電極接合体膜(3)、陰極給電体(8)、および隣の複極板(90)の陰極側から主として構成され、電極接合体膜(3)は、イオン交換膜(4)とその両面に設けられた触媒電極層(5)(6)とからなる。各セル(16)の周縁部には、電極接合体膜(3)と複極板(90)の陰極給電体(8)側の面との間に水電解槽内部と外部をシールするOリング(17)が介在されている。また、水電解槽(51)には、下端部の中央に給水ヘッダ(10)が形成されるとともに、上端部に平行状に水素ヘッダ(11)および酸素ヘッダ(12)が形成されている。   A hydrogen supply apparatus using a solid polymer type water electrolyzer is conventionally known as disclosed in, for example, Patent Document 1, and the water electrolyzer (51) is shown in FIGS. 7, the anode main electrode (1) and the cathode main electrode (2) arranged at both ends, and a plurality of unit cells (16) arranged in series between these main electrodes (1) and (2) ) And a pair of end plates (13) sandwiching a combination of an anode main electrode (1) -a plurality of unit cells (16) -cathode main electrode (2) from both sides. One cell (16) consists of the anode side of the bipolar plate (90), the anode feeder (7), the electrode assembly film (3), the cathode feeder (8), and the adjacent bipolar plate (90). The electrode assembly membrane (3) is mainly configured from the cathode side, and includes an ion exchange membrane (4) and catalyst electrode layers (5) and (6) provided on both surfaces thereof. At the periphery of each cell (16) is an O-ring that seals the inside and outside of the water electrolysis cell between the electrode assembly membrane (3) and the surface of the bipolar plate (90) on the cathode feeder (8) side. (17) is interposed. In the water electrolysis tank (51), a water supply header (10) is formed at the center of the lower end portion, and a hydrogen header (11) and an oxygen header (12) are formed in parallel with the upper end portion.

この水素供給装置では、水電解槽(51)の電解反応によって発熱し、その排熱は、酸素側の循環水による移動と水素側の水蒸気の蒸発潜熱とによって行われている。また、この装置では、内部圧力は、水電解槽(51)外周部に設けられたOリング(17)によって保たれており、その発生ガスの圧力は、1.1MPa(10kg/cmG)未満とされている。 In this hydrogen supply device, heat is generated by the electrolytic reaction of the water electrolysis tank (51), and the exhaust heat is generated by movement by circulating water on the oxygen side and latent heat of vaporization of water vapor on the hydrogen side. In this apparatus, the internal pressure is maintained by an O-ring (17) provided on the outer periphery of the water electrolysis tank (51), and the pressure of the generated gas is 1.1 MPa (10 kg / cm 2 G). It is said that it is less than.

また、水電解槽を圧力容器内に設置することが特許文献2に開示されている。
特開平11−256380号公報 特開平6−33283号公報
Further, Patent Document 2 discloses that a water electrolyzer is installed in a pressure vessel.
JP-A-11-256380 JP-A-6-33283

ところで、水素の燃料電池での使用が進んでおり、そのためには、燃料電池用水素ステーションで35〜70MPaの高圧水素ガスを供給することが課題となっている。   By the way, the use of hydrogen in fuel cells is progressing, and for that purpose, it is a problem to supply high-pressure hydrogen gas of 35 to 70 MPa at a hydrogen station for fuel cells.

しかしながら、上記従来の水素供給装置を使用して、数十MPa程度の高圧にて水電解した場合、Oリングによるシールが破損するという問題があった。そこで、特許文献2に示されているように、水電解槽を圧力容器内に設置することが考えられるが、数十MPa程度の高圧に対応できる点および圧力容器の構造をできるだけ簡素で小容量なものにするという点で、満足なものが得られていない。   However, when water electrolysis is performed at a high pressure of about several tens of MPa using the above-described conventional hydrogen supply apparatus, there is a problem that the seal by the O-ring is broken. Therefore, as shown in Patent Document 2, it is conceivable to install the water electrolyzer in the pressure vessel. However, the point that can handle a high pressure of about several tens of MPa and the structure of the pressure vessel are as simple and small in capacity as possible. Satisfactory things have not been obtained in terms of making things.

本発明は、数十MPa程度の高圧にて水電解した場合でも、電解質膜が破損することが防止され、しかも、十分な耐圧性能を有し、圧力容器の構造をできるだけ簡素で小容量なものにすることができる、固体高分子型水電解槽を用いた水素供給装置を提供することを課題とする。   In the present invention, even when water electrolysis is performed at a high pressure of about several tens of MPa, the electrolyte membrane is prevented from being damaged, and has sufficient pressure resistance performance, and the pressure vessel structure is as simple and small in capacity as possible. It is an object of the present invention to provide a hydrogen supply apparatus using a solid polymer type water electrolyzer that can be used.

この発明による固体高分子型水電解槽を用いた水素供給装置は、高分子電解質膜を用いて水を電解し陽極に酸素を、陰極に水素をそれぞれ発生させる固体高分子型水電解槽と、水電解槽を収める蓋付きの圧力容器とからなる水素供給装置であって、水電解槽を圧力容器本体の底壁に押し付ける電解槽押さえが水電解槽と蓋との間に設けられ、水電解槽と蓋との間に、水素気液分離部とされる間隙が形成されていることを特徴とするものである。   A hydrogen supply apparatus using a solid polymer type water electrolyzer according to the present invention comprises a polymer electrolyte membrane for electrolyzing water to generate oxygen at the anode and hydrogen at the cathode, A hydrogen supply device comprising a pressure vessel with a lid for containing a water electrolyzer, wherein an electrolyzer holder for pressing the water electrolyzer against the bottom wall of the pressure vessel body is provided between the water electrolyzer and the lid, A gap serving as a hydrogen gas-liquid separator is formed between the tank and the lid.

上端が開口した筒状の容器本体に蓋が被せられることにより、圧力容器が形成され、水電解槽は、例えば、これを構成する複極板、陽極給電体、電極接合体膜および陰極給電体が、全て水平状に配置され、各複極板の表裏いずれか一方に、各セルの電解水および酸素の通路となる水平状並列通路が、同他方に、各セルの水素ガスの通路となる水平状並列通路が形成され、各セルの水素ガス通路が、各複極板を貫通して垂直状にのびる水素ヘッダに合流させられているものとされる。水電解槽内の電解水通路には、電解水がポンプ等によって強制的に通され、これにより、陽極に酸素、陰極に水素が発生する。発生した水素は、水電解槽内を上方に移動して圧力容器の頂部に蓄えられていくことから、圧力容器頂部に水素気液分離部を設けることにより、水素を得ることができる。   A pressure vessel is formed by covering a cylindrical vessel body whose upper end is opened, and a water electrolysis tank is composed of, for example, a bipolar plate, an anode feeder, an electrode assembly film, and a cathode feeder constituting the vessel. However, the horizontal parallel passages, which are the passages for the electrolyzed water and oxygen of each cell, are provided on either the front or back of each bipolar plate, and the hydrogen gas passages for each cell are provided on the other side. A horizontal parallel passage is formed, and the hydrogen gas passage of each cell is joined to a hydrogen header extending vertically through each bipolar plate. Electrolyzed water is forced through the electrolyzed water passage in the water electrolyzer by a pump or the like, thereby generating oxygen at the anode and hydrogen at the cathode. Since the generated hydrogen moves upward in the water electrolysis tank and is stored at the top of the pressure vessel, hydrogen can be obtained by providing a hydrogen gas-liquid separator at the top of the pressure vessel.

水電解槽内の電解水の通路が水平方向並列状に形成されているようにしたものでは、1本の給水ヘッダで電解水を供給しているものに比べて、電解水によって電解槽全体をほぼ均等に冷却することができ、また、電解水の流量も多くすることができることから、電解槽が効率よく冷却され、したがって、電解質膜の温度が局部的に耐熱温度以上になることが抑えられ、数十MPa程度の高圧にて水電解した場合でも、電解質膜が破損することが防止される。   In the electrolyzed water passage in the water electrolyzer, the entire electrolyzer is made up by the electrolyzed water as compared with the case where the electrolyzed water is supplied by a single feed header. Since the water can be cooled almost uniformly and the flow rate of the electrolyzed water can be increased, the electrolytic cell is efficiently cooled, and therefore, the temperature of the electrolyte membrane is suppressed from being locally higher than the heat resistant temperature. Even when water electrolysis is performed at a high pressure of about several tens of MPa, the electrolyte membrane is prevented from being damaged.

外周にOリングが嵌められた複極板が容器本体内に密に積層されることにより、水電解槽が形成されていることが好ましい。このようにすると、Oリングの径方向へののびは圧力容器内周面によって規制され、電解槽内部圧力が高圧になってもOリングが破損することはなく、高圧の水素ガスが必要な場合においても、圧力容器を小さくかつ簡素なものにすることができる。   It is preferable that the water electrolyzer is formed by densely laminating a bipolar plate having an O-ring fitted on the outer periphery in the container body. In this way, when the O-ring extends in the radial direction is regulated by the inner peripheral surface of the pressure vessel, the O-ring does not break even when the internal pressure of the electrolytic cell becomes high, and high-pressure hydrogen gas is required. In this case, the pressure vessel can be made small and simple.

また、圧力容器は、上端が開口した筒状の容器本体に蓋が絶縁層を介して被せられることにより形成されており、容器本体と蓋とが電極とされていることが好ましい。圧力容器と水電解槽の電極とが直接接触することから、通常は金属製である圧力容器を絶縁性材料で形成し、水電解槽の電極を圧力容器外部に取り出すことが考えられるが、圧力容器が金属製であることを利用して、容器本体と蓋とを電極とすることにより、水電解槽の電極を圧力容器外部に取り出すための構成を省略することができる。   Moreover, the pressure vessel is formed by covering a cylindrical vessel body whose upper end is open with an insulating layer interposed therebetween, and the vessel body and the lid are preferably electrodes. Since the pressure vessel and the electrode of the water electrolysis tank are in direct contact with each other, it is conceivable that the pressure vessel, usually made of metal, is formed of an insulating material and the electrode of the water electrolysis vessel is taken out of the pressure vessel. By making use of the fact that the container is made of metal and using the container body and the lid as electrodes, the structure for taking out the electrode of the water electrolysis tank to the outside of the pressure container can be omitted.

この発明の固体高分子型水電解槽を用いた水素供給装置によると、圧力容器内に水電解槽を収める構成を採用し、水電解槽を圧力容器本体の底壁に押し付ける電解槽押さえが水電解槽と蓋との間に設けられているようにすることで、圧力容器の構造をできるだけ簡素で小容量なものにすることができ、数十MPa程度の高圧にて水電解した場合でも、電解質膜の破損を防止して、十分な耐圧性能を確保することが可能となる。しかも、水電解槽と蓋との間に、水素気液分離部とされる間隙が形成されているので、水素供給装置から水素気液分離器を省略することができる。   According to the hydrogen supply apparatus using the solid polymer type water electrolyzer of the present invention, the structure in which the water electrolyzer is accommodated in the pressure vessel is adopted, and the electrolyzer holder that presses the water electrolyzer against the bottom wall of the pressure vessel body is water. By being provided between the electrolytic cell and the lid, the structure of the pressure vessel can be made as simple and small as possible, even when water electrolysis is performed at a high pressure of about several tens of MPa, It is possible to prevent damage to the electrolyte membrane and ensure sufficient pressure resistance. In addition, since a gap serving as a hydrogen gas / liquid separator is formed between the water electrolysis tank and the lid, the hydrogen gas / liquid separator can be omitted from the hydrogen supply device.

以下、この発明を図面に基づいて具体的に説明する。以下の説明において、左右および上下は、図1の左右および上下をいうものとし、これらに直交する方向を前後というものとする。   Hereinafter, the present invention will be specifically described with reference to the drawings. In the following description, left and right and top and bottom refer to left and right and top and bottom in FIG. 1, and a direction orthogonal to these is referred to as front and back.

図1において、固体高分子型水電解槽を用いた水素供給装置は、高分子電解質膜を用いて水を電解し、陽極に酸素を、陰極に水素をそれぞれ発生させる固体高分子型水電解槽(40)と、水電解槽(40)を収める蓋(42)付きの圧力容器(41)と、圧力容器(41)の頂部に設けられた水素気液分離部(43)と、水素気液分離部(43)に設けられた水素ライン(44)と、圧力容器(41)の周壁の水・酸素排出口に接続された酸素ライン(45)と、酸素ライン(45)に設けられて水電解槽(40)の陽極にて発生した酸素と水を分離する酸素気液分離器(46)と、循環ポンプ(48)を有し、酸素気液分離器(46)と圧力容器(41)の水入口とを接続する水循環ライン(47)と、水電解槽(40)に接続された直流電源(図示略)とを備えている。   In FIG. 1, a hydrogen supply apparatus using a solid polymer type water electrolyzer uses a polymer electrolyte membrane to electrolyze water, and generates oxygen at the anode and hydrogen at the cathode, respectively. (40), a pressure vessel (41) with a lid (42) for housing the water electrolyzer (40), a hydrogen gas / liquid separation unit (43) provided on the top of the pressure vessel (41), and a hydrogen gas / liquid A hydrogen line (44) provided in the separation part (43), an oxygen line (45) connected to the water / oxygen discharge port on the peripheral wall of the pressure vessel (41), and an oxygen line (45) provided with water An oxygen gas-liquid separator (46) for separating oxygen and water generated at the anode of the electrolytic cell (40), and a circulation pump (48), an oxygen gas-liquid separator (46) and a pressure vessel (41) A water circulation line (47) for connecting to the water inlet and a DC power source (not shown) connected to the water electrolysis tank (40).

水電解槽(40)の各セル(16)は、図3に示すように、複極板(19)の陽極側、陽極給電体(7)、電極接合体膜(3)、陰極給電体(8)および隣の複極板(19)の陰極側から主として構成されている。電極接合体膜(3)は、イオン交換膜(4)とその両面に設けられた触媒電極層(5)(6)とからなる。   As shown in FIG. 3, each cell (16) of the water electrolysis tank (40) has an anode side of the bipolar plate (19), an anode feeder (7), an electrode assembly film (3), a cathode feeder ( 8) and the cathode side of the adjacent bipolar plate (19). The electrode assembly membrane (3) includes an ion exchange membrane (4) and catalyst electrode layers (5) and (6) provided on both sides thereof.

複極板(19)は、厚板を研削加工したもので、図2(a)および図4に示すように、円板状で、その両面に、並列状通路(19a)(19b)が形成されるとともに、外周に設けられた環状溝に、Oリング(50)が嵌め入れられている。図4において、複極板の上面に設けられている通路は、酸素発生側の通路(19a)で、同下面に設けられている通路は、水素発生側の通路(19b)とされている。水素発生側の通路(19b)は、同図(c)に示すように、複極板(19)の外周には開口しておらず、これに対し、酸素発生側の通路(19a)には、同図(a)(b)に示すように、複極板(19)の外周に開口し水の導入口と水および酸素の排出口となる開口連通路(19c)が連通させられている。開口連通路(19c)は、複極板(19)の上下面には開口せず、外周にだけ開口している。   The bipolar plate (19) is obtained by grinding a thick plate. As shown in FIG. 2 (a) and FIG. 4, the bipolar plate (19) has a disk shape, and parallel passages (19a, 19b) are formed on both sides thereof. In addition, an O-ring (50) is fitted in an annular groove provided on the outer periphery. In FIG. 4, the passage provided on the upper surface of the bipolar plate is the passage (19a) on the oxygen generation side, and the passage provided on the lower surface is the passage (19b) on the hydrogen generation side. The hydrogen generation side passage (19b) does not open to the outer periphery of the bipolar plate (19) as shown in FIG. 5C, whereas the oxygen generation side passage (19a) As shown in FIGS. 5A and 5B, an open communication passage (19c) that opens to the outer periphery of the bipolar plate (19) and that serves as an inlet for water and an outlet for water and oxygen is communicated. . The open communication path (19c) does not open on the upper and lower surfaces of the bipolar plate (19), but opens only on the outer periphery.

Oリング(50)付き複極板(19)は、それらの通路(19a)(19b)を水平に向けてかつOリング(50)が圧力容器(41)の内周に接するようにして水平層状に積層されている。複極板(19)、陽極給電体(7)、電極接合体膜(3)および陰極給電体(8)が積層されて形成された水電解槽(40)には、これを垂直に貫通する方向に水素ヘッダ(49)が形成されている。   The bipolar plate (19) with the O-ring (50) is horizontally layered so that the passages (19a) and (19b) are oriented horizontally and the O-ring (50) is in contact with the inner periphery of the pressure vessel (41). Are stacked. A water electrolysis tank (40) formed by laminating a bipolar plate (19), an anode feeder (7), an electrode assembly film (3) and a cathode feeder (8) penetrates this vertically. A hydrogen header (49) is formed in the direction.

図5に示すように、水素ヘッダ(49)は、複極板(19)、陽極給電体(7)、電極接合体膜(3)および陰極給電体(8)を貫通する垂直貫通孔(49a)と、各複極板(19)に設けられた段付き孔部(57)(58)にOリング(53)(54)を介して嵌め入れられた1対の通路形成リング(55)(56)とによって形成されている。各通路形成リング(55)(56)は、セラミックまたは耐熱樹脂(例えばエンジニアリングプラスチック)製であり、それぞれ、一端に、内径は同じで外径が小さい小径部を有している。そして、一方のOリング(53)は、小径部の外周に、他方のOリング(54)は、小径部がない方の端面の環状溝に、それぞれ通路に露出しないように嵌め入れられ、通路形成リング(55)(56)の大径部の端面同士が隣り合うもの同士突き合わされ、小径部の端面が、複極板の最も内径が小さい部分に当接させられている。水素側の通路形成リング(56)には、側面に1〜2mm程度の小孔(56a)が複数設けられている。   As shown in FIG. 5, the hydrogen header (49) has a vertical through-hole (49a) that penetrates the bipolar plate (19), the anode feeder (7), the electrode assembly film (3), and the cathode feeder (8). ) And a pair of passage forming rings (55) (55) (55) (58) fitted into stepped holes (57) (58) provided in each bipolar plate (19) via O-rings (53) (54). 56). Each of the passage forming rings (55) and (56) is made of ceramic or heat-resistant resin (for example, engineering plastic), and has a small diameter portion having the same inner diameter and a smaller outer diameter at one end. One O-ring (53) is fitted into the outer periphery of the small-diameter portion, and the other O-ring (54) is fitted into the annular groove on the end surface without the small-diameter portion so as not to be exposed to the passage. The end surfaces of the large-diameter portions of the forming rings (55) and (56) are abutted with each other, and the end surfaces of the small-diameter portions are brought into contact with the portion having the smallest inner diameter of the bipolar plate. The hydrogen side passage forming ring (56) is provided with a plurality of small holes (56a) of about 1 to 2 mm on the side surface.

こうして、水電解槽(40)には、各セルの電解水および酸素の通路となる水平状並列通路(19a)(19c)と、各セルの水素ガスの通路となる水平状並列通路(19b)およびこれらの水素ガス通路が合流させられる垂直状水素ヘッダ(49)とが形成されている。そして、複極板(19)の外周に嵌められたOリング(50)は、圧力容器(41)の内周によってその径の増大が抑えられている。   Thus, in the water electrolysis tank (40), horizontal parallel passages (19a) (19c) that serve as electrolytic water and oxygen passages for each cell, and horizontal parallel passages (19b) that serve as hydrogen gas passages for each cell. And a vertical hydrogen header (49) in which these hydrogen gas passages are merged. The O-ring (50) fitted to the outer periphery of the bipolar plate (19) is suppressed from increasing in diameter by the inner periphery of the pressure vessel (41).

圧力容器(41)は、上端が開口した筒状の容器本体に蓋(42)が絶縁層を介して被せられることにより形成されており、この実施例では、容器本体が陰極に、蓋(42)が陽極とされている。圧力容器(41)の蓋(42)の下面には、下方突出状の電解槽押さえ(42a)が設けられている。この電解槽押さえ(42a)は、水電解槽(40)全体を容器本体底壁に押し付けるもので、圧力容器(41)の蓋(42)と水電解槽(40)上面との間には、電解槽押さえ(42a)の長さに相当する間隙が形成されている。水電解槽(40)に供給される純水の圧力を調整することにより、この間隙には、電解水層が確保され、この電解水層の上方に、発生した水素ガスの層が形成され、こうして、圧力容器(41)の頂部に、水素気液分離部(43)が形成されている。   The pressure vessel (41) is formed by covering a cylindrical vessel body whose upper end is open with a lid (42) through an insulating layer.In this embodiment, the vessel body is a cathode and a lid (42 ) Is the anode. A downwardly projecting electrolytic cell holder (42a) is provided on the lower surface of the lid (42) of the pressure vessel (41). This electrolytic cell holder (42a) presses the entire water electrolytic cell (40) against the bottom wall of the container body, and between the lid (42) of the pressure vessel (41) and the upper surface of the water electrolytic cell (40), A gap corresponding to the length of the electrolytic cell holder (42a) is formed. By adjusting the pressure of pure water supplied to the water electrolysis tank (40), an electrolyzed water layer is secured in this gap, and a layer of generated hydrogen gas is formed above the electrolyzed water layer, Thus, a hydrogen gas-liquid separation part (43) is formed at the top of the pressure vessel (41).

この実施形態の固体高分子型水電解槽を用いた水素供給装置によると、循環ポンプ(48)によって水電解槽(40)に強制的に送り込まれた電解水は、複極板(19)の水平状並列通路(19a)(19c)を左から右に流れ、水素および酸素に分解されるとともに、水電解槽(40)の冷却水の機能を果たして、圧力容器(41)から排出される。陽極で発生した酸素は、電解水とともに複極板(19)の水平状並列通路(19a)(19c)を流れ、陰極に発生した水素は、各セルの複極板(19)の水平状並列通路(19b)を流れて、水素ヘッダ(49)に合流させられ、圧力容器(41)の頂部に蓄えられていく。水素ガスは、圧力容器(41)頂部の水素気液分離部(43)においてその純度を高められ、水素ライン(44)に設けられた逆止弁式圧力弁(44a)により所定圧力に調整されて外部に供給される。従来の複極板は、薄板を超塑性加工により波形に成形したものであり、圧力によるたわみなどにより、イオン交換膜(4)と触媒電極層(5)(6)との接触にばらつきを生じることがあったが、厚板を研削加工した複極板(19)を使用することにより、ばらつきが抑えられ、安定して水素を得ることができる。   According to the hydrogen supply device using the solid polymer type water electrolyzer of this embodiment, the electrolyzed water forcedly fed into the water electrolyzer (40) by the circulation pump (48) is supplied to the bipolar plate (19). It flows from the left to the right through the horizontal parallel passages (19a) and (19c), is decomposed into hydrogen and oxygen, functions as cooling water in the water electrolysis tank (40), and is discharged from the pressure vessel (41). Oxygen generated at the anode flows through the parallel parallel passages (19a) and (19c) of the bipolar plate (19) together with the electrolyzed water, and hydrogen generated at the cathode is horizontal parallel of the bipolar plates (19) of each cell. It flows through the passage (19b), joins the hydrogen header (49), and is stored at the top of the pressure vessel (41). The purity of the hydrogen gas is increased in the hydrogen gas-liquid separator (43) at the top of the pressure vessel (41), and is adjusted to a predetermined pressure by a check valve pressure valve (44a) provided in the hydrogen line (44). Supplied to the outside. A conventional bipolar plate is formed by corrugating thin plates into a corrugated shape, resulting in variations in contact between the ion exchange membrane (4) and the catalyst electrode layers (5) and (6) due to pressure deflection. However, by using the bipolar plate (19) obtained by grinding a thick plate, variation can be suppressed and hydrogen can be stably obtained.

水電解槽(40)の排熱は、圧力容器(41)内に冷却された循環水が導入されて水電解槽(40)との間隙を充満していることによって行われている。高圧にて水電解した場合には、水素側の水蒸気の発生量が極端に減少するが、この水蒸気の蒸発潜熱による排熱が水平状通路(19b)を流れる大量の水への熱移動による排熱によって補償される。こうして、高圧水素ガスを発生させる場合でも、電極接合体膜(電解質膜)(3)が破損することが防止される。   Exhaust heat of the water electrolysis tank (40) is performed by introducing cooled circulating water into the pressure vessel (41) and filling the gap with the water electrolysis tank (40). When water electrolysis is performed at high pressure, the amount of water vapor generated on the hydrogen side is drastically reduced. Compensated by heat. Thus, even when high-pressure hydrogen gas is generated, the electrode assembly membrane (electrolyte membrane) (3) is prevented from being damaged.

また、水素ヘッダ(49)を形成するのに、従来使用されていたゴムブッシュを使用していないため、ゴムブッシュに起因する加工精度が悪くかつ熱的な変形が大きいという問題が解消されている。   In addition, since the conventional rubber bushing is not used to form the hydrogen header (49), the problem of poor processing accuracy and large thermal deformation due to the rubber bushing has been eliminated. .

上記において、複極板(19)は、円板状とされているが、図2(b)に示すように、方形板状で、その角部が面取りされて丸くなっている複極板を使用することもできる。なお、複極板(19)は、アルミニウム製の厚板に研削加工を施して、通路(19a)(19b)を形成したものであり、その表面には、チタン/白金コーティングが施されており、その通路(19a)(19b)は曲線状または屈曲状にしてもよい。   In the above description, the bipolar plate (19) has a disc shape. However, as shown in FIG. 2 (b), the bipolar plate (19) is a square plate shape with corners chamfered and rounded. It can also be used. The bipolar plate (19) is formed by grinding a thick aluminum plate to form passages (19a) and (19b). The surface is coated with titanium / platinum. The passages (19a) and (19b) may be curved or bent.

厚板に溝研削加工する製造方法で複極板(19)を製造することにより、複極板(19)の周縁部を厚くすることができ、複極板(19)の強度が上がり、高圧ガスを発生させる場合でも、セルに歪みが生じることがなく、耐圧性が向上する。さらに、締め付けによりセル全体としての剛性も大きくなり、高強度の水電解槽が得られる。   By manufacturing the bipolar plate (19) with a manufacturing method that performs groove grinding on a thick plate, the peripheral edge of the bipolar plate (19) can be made thicker, the strength of the bipolar plate (19) is increased, and the high pressure Even when the gas is generated, the cell is not distorted and the pressure resistance is improved. Furthermore, the rigidity of the entire cell is increased by tightening, and a high-strength water electrolyzer is obtained.

この発明による固体高分子型電解槽を用いた水素供給装置を示す概略図である。It is the schematic which shows the hydrogen supply apparatus using the solid polymer electrolytic cell by this invention. 複極板の一例およびその変形例を示す斜視図である。It is a perspective view which shows an example of a bipolar plate, and its modification. 固体高分子型水電解槽の要部を示す垂直縦断面図である。It is a vertical longitudinal cross-sectional view which shows the principal part of a solid polymer type water electrolyzer. 複極板の通路形状の詳細を示す図であり、(a)は、水の進行方向から見た正面図、(b)は平面図、(c)は、底面図である。It is a figure which shows the detail of the channel | path shape of a bipolar plate, (a) is the front view seen from the advancing direction of water, (b) is a top view, (c) is a bottom view. 水素ヘッダの詳細を示す断面図である。It is sectional drawing which shows the detail of a hydrogen header. 従来の高分子型水電解槽を示す分解斜視図である。It is a disassembled perspective view which shows the conventional polymer-type water electrolyzer. 従来の高分子型水電解槽を示す垂直断面図である。It is a vertical sectional view showing a conventional polymer type water electrolyzer.

符号の説明Explanation of symbols

(40):固体高分子型水電解槽
(41):圧力容器
(42):蓋
(42a):電解槽押さえ
(43):水素気液分離部
(49):水素ヘッダ
(50):Oリング
(40): Solid polymer water electrolyzer
(41): Pressure vessel
(42): Lid
(42a): Electrolyzer holder
(43): Hydrogen gas-liquid separator
(49): Hydrogen header
(50): O-ring

Claims (3)

高分子電解質膜を用いて水を電解し陽極に酸素を、陰極に水素をそれぞれ発生させる固体高分子型水電解槽と、水電解槽を収める蓋付きの圧力容器とからなる水素供給装置であって、
水電解槽を圧力容器本体の底壁に押し付ける電解槽押さえが水電解槽と蓋との間に設けられ、水電解槽と蓋との間に、水素気液分離部とされる間隙が形成されていることを特徴とする固体高分子型電解槽を用いた水素供給装置。
A hydrogen supply device comprising a solid polymer water electrolyzer that electrolyzes water using a polymer electrolyte membrane and generates oxygen at the anode and hydrogen at the cathode, and a pressure vessel with a lid for housing the water electrolyzer. And
An electrolytic cell holder that presses the water electrolytic cell against the bottom wall of the pressure vessel body is provided between the water electrolytic cell and the lid, and a gap is formed between the water electrolytic cell and the lid as a hydrogen gas-liquid separation unit. A hydrogen supply apparatus using a solid polymer electrolytic cell, characterized in that
外周にOリングが嵌められた複極板が容器本体内に密に積層されることにより、水電解槽が形成されていることを特徴とする、請求項1記載の固体高分子型水電解槽を用いた水素供給装置。   2. The polymer electrolyte water electrolyzer according to claim 1, wherein a water electrolyzer is formed by densely laminating a bipolar plate having an O-ring fitted on the outer periphery thereof in the container body. Hydrogen supply device using 圧力容器は、上端が開口した筒状の容器本体に蓋が絶縁層を介して被せられることにより形成されており、容器本体と蓋とが電極とされている、請求項1または2記載の固体高分子型水電解槽を用いた水素供給装置。   The solid container according to claim 1 or 2, wherein the pressure vessel is formed by covering a cylindrical vessel body having an open upper end with an insulating layer interposed between the lid and the vessel body and the lid as electrodes. A hydrogen supply device using a polymer water electrolyzer.
JP2004313286A 2004-10-28 2004-10-28 Hydrogen supply device using solid polymer water electrolyzer Expired - Fee Related JP4206500B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2004313286A JP4206500B2 (en) 2004-10-28 2004-10-28 Hydrogen supply device using solid polymer water electrolyzer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2004313286A JP4206500B2 (en) 2004-10-28 2004-10-28 Hydrogen supply device using solid polymer water electrolyzer

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP2002158685A Division JP3772261B2 (en) 2002-05-31 2002-05-31 Hydrogen supply device using solid polymer water electrolyzer

Publications (2)

Publication Number Publication Date
JP2005097746A true JP2005097746A (en) 2005-04-14
JP4206500B2 JP4206500B2 (en) 2009-01-14

Family

ID=34464232

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2004313286A Expired - Fee Related JP4206500B2 (en) 2004-10-28 2004-10-28 Hydrogen supply device using solid polymer water electrolyzer

Country Status (1)

Country Link
JP (1) JP4206500B2 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100862004B1 (en) 2007-04-26 2008-10-07 삼성전기주식회사 Hydrogen generating apparatus using polymer membranes and fuel cell system using the same
KR100863725B1 (en) 2007-04-25 2008-10-16 삼성전기주식회사 Hydrogen generating apparatus and fuel cell power generation system
KR100878052B1 (en) 2008-04-23 2009-01-15 모진희 Gas generator using electrolysis
US7846307B2 (en) 2005-05-10 2010-12-07 Honda Motor Co., Ltd. High-pressure hydrogen production apparatus
JP2012041568A (en) * 2010-08-12 2012-03-01 Honda Motor Co Ltd Water electrolysis apparatus

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7846307B2 (en) 2005-05-10 2010-12-07 Honda Motor Co., Ltd. High-pressure hydrogen production apparatus
KR100863725B1 (en) 2007-04-25 2008-10-16 삼성전기주식회사 Hydrogen generating apparatus and fuel cell power generation system
KR100862004B1 (en) 2007-04-26 2008-10-07 삼성전기주식회사 Hydrogen generating apparatus using polymer membranes and fuel cell system using the same
KR100878052B1 (en) 2008-04-23 2009-01-15 모진희 Gas generator using electrolysis
JP2012041568A (en) * 2010-08-12 2012-03-01 Honda Motor Co Ltd Water electrolysis apparatus

Also Published As

Publication number Publication date
JP4206500B2 (en) 2009-01-14

Similar Documents

Publication Publication Date Title
JP3772261B2 (en) Hydrogen supply device using solid polymer water electrolyzer
JP2911381B2 (en) Hydrogen / oxygen generator
JP2006316288A (en) High-pressure hydrogen production apparatus
US10053784B2 (en) Differential pressure water electrolysis system
US8894829B2 (en) Water electrolysis apparatus
JP2010236087A (en) Water electrolysis system
US9828682B2 (en) Differential pressure water electrolysis apparatus
EP1528126A1 (en) An integrated electrolyser module with an internal gas/liquid separator
JP5341547B2 (en) Water electrolysis system
TWI406972B (en) Ozone producing system
JP4206500B2 (en) Hydrogen supply device using solid polymer water electrolyzer
JP2012067343A (en) Method for stopping operation of high-pressure water electrolysis device
JPH07252682A (en) Water electrolyzing cell using high-polymer electrolyte membrane
JP7037965B2 (en) Water electrolyzer
JP3766893B2 (en) Hydrogen supply device using solid polymer water electrolyzer
JPH08260180A (en) Hydrogen and oxygen generator
JPH08260177A (en) Water electrolytic cell using solid high molecular electrolyte membrane
JP3772260B2 (en) Hydrogen supply device using solid polymer water electrolyzer
JP5415168B2 (en) Water electrolysis system
JP2005248246A (en) Apparatus for generating hydrogen by water electrolysis accommodated in high-pressure vessel
JP3991146B2 (en) Solid polymer water electrolyzer
JP2006307248A (en) Hydrogen production equipment
JPH09202985A (en) Hydrogen and oxygen generator
JPH08325772A (en) Spiral type cell for electrolysis
JP2001081589A (en) Separator and electrolytic cell structure using the same

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20070502

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20080129

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20080318

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20080909

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20081006

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20111031

Year of fee payment: 3

LAPS Cancellation because of no payment of annual fees