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JP2022043155A - Hydrogen permeation device - Google Patents

Hydrogen permeation device Download PDF

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JP2022043155A
JP2022043155A JP2021202356A JP2021202356A JP2022043155A JP 2022043155 A JP2022043155 A JP 2022043155A JP 2021202356 A JP2021202356 A JP 2021202356A JP 2021202356 A JP2021202356 A JP 2021202356A JP 2022043155 A JP2022043155 A JP 2022043155A
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raw material
primary side
material gas
supply pipe
hydrogen permeation
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JP7105427B2 (en
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和宣 森迫
Kazunobu Morisako
正章 永井
Masaaki Nagai
朋樹 横山
Tomoki Yokoyama
佳久 松本
Yoshihisa Matsumoto
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Institute of National Colleges of Technologies Japan
Hydronext Inc
Sanwa Press Co Ltd
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Hydronext Inc
Sanwa Press Co Ltd
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Abstract

【課題】水素透過性能を高めた水素透過装置を提供する。【解決手段】 原料気体の供給側である1次側と、透過気体の取出側である2次側との間に、水素透過金属膜を有する水素透過装置であって、1次側には、原料気体供給路を形成する原料供給管13と、2次側に透過しない原料気体を排出する原料気体排出路と16a、16bと、前記原料供給管13の先端側と組み合う開孔板14とを有し、該開孔板14の噴出孔15の直径が、原料供給管13の内径より小さく形成されている。【選択図】図1PROBLEM TO BE SOLVED: To provide a hydrogen permeation device having improved hydrogen permeation performance. SOLUTION: The hydrogen permeation device has a hydrogen permeation metal film between a primary side which is a supply side of a raw material gas and a secondary side which is a take-out side of a permeated gas, and the primary side has a hydrogen permeation device. A raw material supply pipe 13 forming a raw material gas supply path, a raw material gas discharge path 16a and 16b for discharging a raw material gas that does not permeate to the secondary side, and an opening plate 14 that is combined with the tip end side of the raw material supply pipe 13 are provided. The diameter of the ejection hole 15 of the opening plate 14 is smaller than the inner diameter of the raw material supply pipe 13. [Selection diagram] Fig. 1

Description

本発明は、水素透過装置に関し、特に水素透過金属膜により水素を透過させるのに適した技術に関する。 The present invention relates to a hydrogen permeation device, and more particularly to a technique suitable for permeating hydrogen through a hydrogen permeation metal membrane.

水素透過に関する技術として、特許文献1に記載の水素分離装置が知られている。
該水素分離装置は、特許文献1の段落0008に記載されているように、水素を透過する非パラジウム系金属又は非パラジウム系金属を主たる金属とする合金により形成された水素透過膜と、水素を含む原料気体を水素透過膜の一次側の表面に供給するための原料気体供給流路と、水素透過膜の二次側の表面へ透過した水素を回収するための水素回収流路と、原料気体供給流路から供給された原料気体を水素透過膜の一次側の表面に沿って分配するための所定の幅の流路を形成するために、水素透過膜の一次側の表面から所定の幅だけ離隔して配置された流路形成部とを備えたものである。
As a technique related to hydrogen permeation, the hydrogen separation device described in Patent Document 1 is known.
As described in paragraph 0008 of Patent Document 1, the hydrogen separator comprises a hydrogen permeable film formed of a non-palladium-based metal that permeates hydrogen or an alloy containing a non-palladium-based metal as a main metal, and hydrogen. A raw material gas supply flow path for supplying the contained raw material gas to the surface on the primary side of the hydrogen permeable film, a hydrogen recovery flow path for recovering hydrogen permeated to the surface on the secondary side of the hydrogen permeable film, and a raw material gas. In order to form a flow path of a predetermined width for distributing the raw material gas supplied from the supply flow path along the surface of the primary side of the hydrogen permeable film, only a predetermined width from the surface of the primary side of the hydrogen permeable film. It is provided with a flow path forming portion arranged at a distance.

該特許文献1の段落0045には、流配フランジ60を設けることで、高い水素透過度が得られることが記載されている。 Paragraph 0045 of the Patent Document 1 describes that high hydrogen permeability can be obtained by providing the flow distribution flange 60.

特開2019-5684号公報JP-A-2019-5684

本発明の課題は、流配フランジとは全く別の手段によって高い水素透過度が得られる手段を提供することである。 An object of the present invention is to provide a means for obtaining high hydrogen permeability by a means completely different from the flow distribution flange.

本発明の課題を解決するための手段は、下記のとおりである。 The means for solving the problem of the present invention is as follows.

第1に、
原料気体の供給側である1次側と、透過気体の取出側である2次側との間に、水素透過金属膜を有する水素透過装置であって、
1次側には、
原料気体供給路を形成する原料供給管と、
2次側に透過しない原料気体を排出する原料気体排出路と、
前記原料供給管の先端側と組み合う開孔板を有し、
該開孔板の噴出孔の大きさが、原料供給管より小さいことを特徴とする、水素透過装置。
ここで、噴出孔の大きさとは、噴出孔が円の場合には直径のことをいう。
従って、噴出孔が円の場合には、噴出孔の直径が、原料供給管の内径より小さい場合が該当する。
また、噴出孔の形状としては、円の他に、三角形、四角形、五角形等の多角形や星型多角形等の各種形状が採用することができる。
ここで、多角形や星型多角形の場合に、「噴出孔の大きさが、原料供給管より小さい」とは、多角形や星型多角形の形状自体が、原料供給管の内径を形成する円内に収まることをいう。
First,
A hydrogen permeation device having a hydrogen permeation metal film between the primary side, which is the supply side of the raw material gas, and the secondary side, which is the takeout side of the permeated gas.
On the primary side
The raw material supply pipe that forms the raw material gas supply path,
A raw material gas discharge path that discharges raw material gas that does not permeate to the secondary side,
It has a perforated plate that is combined with the tip end side of the raw material supply pipe.
A hydrogen permeation device characterized in that the size of the ejection hole of the opening plate is smaller than that of the raw material supply pipe.
Here, the size of the ejection hole means the diameter when the ejection hole is a circle.
Therefore, when the ejection hole is a circle, the diameter of the ejection hole is smaller than the inner diameter of the raw material supply pipe.
In addition to the circle, various shapes such as a polygon such as a triangle, a quadrangle, and a pentagon, and a star-shaped polygon can be adopted as the shape of the ejection hole.
Here, in the case of a polygon or a star-shaped polygon, "the size of the ejection hole is smaller than that of the raw material supply pipe" means that the shape of the polygon or the star-shaped polygon itself forms the inner diameter of the raw material supply pipe. It means that it fits within the circle.

第2に、
原料気体の供給側である1次側と、透過気体の取出側である2次側との間に、水素透過金属膜を有する水素透過装置であって、
1次側には、
原料気体供給路を形成する原料供給管と、
2次側に透過しない原料気体を排出する原料気体排出路と、
前記原料供給管の先端側と組み合う開孔板を有し、
該開孔板の噴出孔の直径が、原料供給管の内径より小さいことを特徴とする、水素透過装置。
Second,
A hydrogen permeation device having a hydrogen permeation metal film between the primary side, which is the supply side of the raw material gas, and the secondary side, which is the takeout side of the permeated gas.
On the primary side
The raw material supply pipe that forms the raw material gas supply path,
A raw material gas discharge path that discharges raw material gas that does not permeate to the secondary side,
It has a perforated plate that is combined with the tip end side of the raw material supply pipe.
A hydrogen permeation device characterized in that the diameter of the ejection hole of the opening plate is smaller than the inner diameter of the raw material supply pipe.

第3に、
前記開孔板の噴出孔が、1次側から2次側に向けて、テーパ形状を有することを特徴とする、前記第1または第2に記載の水素透過装置。
ここで、テーパ形状を有するとは、1次側から2次側に向けて、噴出孔の形状が徐々に小さくなるようにテーパを形成する他に、1次側から2次側に向けて、噴出孔の形状が徐々に大きくなるようにテーパを形成する場合も含まれる。
前記テーパを形成する場合の噴出孔の形状は、加工性を考慮すると、円の場合が望ましいが、三角形、四角形、五角形等の多角形や星型多角形等の各種形状の場合であっても、採用することができる。
Third,
The hydrogen permeation device according to the first or second aspect, wherein the ejection hole of the opening plate has a tapered shape from the primary side to the secondary side.
Here, having a tapered shape means that the shape of the ejection hole is gradually reduced from the primary side to the secondary side, and in addition, the taper is formed from the primary side to the secondary side. It also includes the case where a taper is formed so that the shape of the ejection hole gradually increases.
The shape of the ejection hole when forming the taper is preferably a circle in consideration of workability, but even in the case of various shapes such as a polygon such as a triangle, a quadrangle, and a pentagon, and a star-shaped polygon. , Can be adopted.

第4に、
前記開孔板の噴出孔の直径が、原料供給管の内径の2分の1以下、望ましくは3分の1以下、より望ましくは4分の1程度であることを特徴とする、前記第2または第3に記載の水素透過装置。
ここで、4分の1程度とは、4分の1の値に加えて、実質的に4分の1の場合と同等の作用効果を有する範囲を含むことを意味している。
Fourth,
The second characteristic is that the diameter of the ejection hole of the opening plate is one-half or less, preferably one-third or less, more preferably about one-fourth of the inner diameter of the raw material supply pipe. Or the hydrogen permeation device according to the third.
Here, about one-fourth means that, in addition to the one-fourth value, a range having substantially the same action and effect as in the case of one-fourth is included.

水素透過金属膜としては、水素を透過する性質を有する、V、Nb、Taなどの5族元素の純金属や、合金により形成される5類金属であれば良いが、純バナジウムが望ましい。
また、水素透過金属膜の両表面には、触媒としてパラジウムまたはパラジウム系合金をスパッタリングすることが望ましい。
The hydrogen-permeable metal film may be a pure metal of a Group 5 element such as V, Nb, or Ta, which has a property of transmitting hydrogen, or a class 5 metal formed of an alloy, but pure vanadium is preferable.
Further, it is desirable to sputter palladium or a palladium-based alloy as a catalyst on both surfaces of the hydrogen permeable metal film.

本発明によれば、水素透過性能を高めることができる。 According to the present invention, hydrogen permeation performance can be enhanced.

本発明の実施例1に係る要部の縦断面図である。It is a vertical sectional view of the main part which concerns on Example 1 of this invention. 本発明の実施例1に係る全体の縦断面図である。It is a vertical sectional view of the whole which concerns on Example 1 of this invention. 本発明の実施例1に係る1次側の斜視図である。It is a perspective view of the primary side which concerns on Example 1 of this invention. 本発明の実施例1に係る全体の縦断面の斜視図である。It is a perspective view of the whole vertical cross section which concerns on Example 1 of this invention. 比較例に係る要部の縦断面図である。It is a vertical sectional view of the main part which concerns on a comparative example. 比較例に係る全体の縦断面の斜視図である。It is a perspective view of the whole vertical cross section which concerns on a comparative example. 試験例の結果を流量で示すグラフである。It is a graph which shows the result of a test example by a flow rate. 試験例の結果を透過係数で示すグラフである。It is a graph which shows the result of a test example by a transmission coefficient. 本発明の実施例2に係る噴出孔の部分の縦断面図である。It is a vertical sectional view of the part of the ejection hole which concerns on Example 2 of this invention. 本発明の実施例3に係る噴出孔の平面図である。It is a top view of the ejection hole which concerns on Example 3 of this invention.

以下、本発明を実施するための形態を、図面を参照しつつ具体的に説明する。
ここで、添付図面において同一の部材には同一符号を付しており、また重複した説明は省略されている。
なお、ここでの説明は本発明が実施される一形態であることから、本発明は該当形態に限定されるものではない。
Hereinafter, embodiments for carrying out the present invention will be specifically described with reference to the drawings.
Here, in the attached drawings, the same members are designated by the same reference numerals, and duplicate explanations are omitted.
Since the description here is one embodiment of the present invention, the present invention is not limited to the corresponding embodiment.

[実施例1] [Example 1]

本発明に係る水素透過装置の一例は、図1に要部を示すとおり、水素含有ガス等の原料気体の供給側である1次側円筒体10と、透過気体である水素の取出側である2次側円筒体20との間に、純バナジウムによる水素透過金属膜30を有するものである。
該水素透過金属膜30の両面には、触媒としてパラジウム銀(Pd-25%Ag)がスパッタリングされている。
An example of the hydrogen permeation device according to the present invention is a primary side cylinder 10 which is a supply side of a raw material gas such as a hydrogen-containing gas and a extraction side of hydrogen which is a permeation gas, as shown in FIG. It has a hydrogen permeable metal film 30 made of pure vanadium between it and the secondary side cylinder 20.
Palladium silver (Pd-25% Ag) is sputtered on both sides of the hydrogen permeable metal film 30 as a catalyst.

1次側円筒体10の先端側には、1次側フランジ11が一体となって形成されている。
2次側円筒体20の先端側には、2次側フランジ21が一体となって形成されている。
A primary side flange 11 is integrally formed on the tip end side of the primary side cylindrical body 10.
A secondary side flange 21 is integrally formed on the tip end side of the secondary side cylindrical body 20.

1次側フランジ11及び2次側フランジ21の内周面側には、凹部が各々形成されている。
1次側の凹部には、銅による1次側ガスケット12が位置している。
2次側の凹部には、銅による2次側ガスケット22が位置している。
なお、ガスケットの素材としては、銅に限定されず、ステンレス等の他の素材で形成することもできる。
Recesses are formed on the inner peripheral surface side of the primary side flange 11 and the secondary side flange 21, respectively.
A copper primary gasket 12 is located in the primary concave.
A copper secondary gasket 22 is located in the secondary recess.
The material of the gasket is not limited to copper, and may be formed of other materials such as stainless steel.

1次側ガスケット12と2次側ガスケット22との間には、水素透過金属膜30が位置している。
該水素透過金属膜30の直径は、1次側ガスケット12及び2次側ガスケット22の外径より、わずかに大きく、ガスケットで挟み込まれて密閉性が保たれた状態で、水素透過金属膜30の外周縁部が1次側ガスケット12及び2次側ガスケット22の外周端から僅かにはみ出すように形成されている。
1次側ガスケット12及び2次側ガスケット22による挟み込みは、図示は省略するが、1次側フランジ11及び2次側フランジ21に形成された4個の貫通穴に、ボルトを通してナットで締め付けることで行われている。
A hydrogen permeable metal film 30 is located between the primary side gasket 12 and the secondary side gasket 22.
The diameter of the hydrogen permeable metal film 30 is slightly larger than the outer diameters of the primary side gasket 12 and the secondary side gasket 22, and the hydrogen permeable metal film 30 is sandwiched between the gaskets to maintain hermeticity. The outer peripheral edge portion is formed so as to slightly protrude from the outer peripheral ends of the primary side gasket 12 and the secondary side gasket 22.
The sandwiching between the primary side gasket 12 and the secondary side gasket 22 is not shown, but by passing bolts through the four through holes formed in the primary side flange 11 and the secondary side flange 21 and tightening them with nuts. It is done.

前記1次側円筒体10の内部には、図1及び図2に示すとおり、原料気体供給路を形成する原料供給管13が配置されている。
該原料供給路13の先端側には、図3に示すとおり、中心部に円状の噴出孔15を有する略円形状の開孔板14が組み合わせられている。
As shown in FIGS. 1 and 2, a raw material supply pipe 13 forming a raw material gas supply path is arranged inside the primary side cylinder 10.
As shown in FIG. 3, a substantially circular opening plate 14 having a circular ejection hole 15 at the center thereof is combined with the tip end side of the raw material supply path 13.

前記噴出孔15の直径は、図1及び図2に示すとおり、原料供給管13の内径の4分の1のサイズで形成されている。
本実施例1では、原料供給管13の内径が4.4mmであり、噴出孔15の孔径が1.1mmとなるように形成されている。
また、1次側円筒体10及び2次側円筒体20の内径は、30mmである。
As shown in FIGS. 1 and 2, the diameter of the ejection hole 15 is formed to be one-fourth the size of the inner diameter of the raw material supply pipe 13.
In the first embodiment, the inner diameter of the raw material supply pipe 13 is 4.4 mm, and the hole diameter of the ejection hole 15 is 1.1 mm.
The inner diameters of the primary side cylinder 10 and the secondary side cylinder 20 are 30 mm.

図3に示すように、前記開孔板14の外周は、1次側円筒体10の内径より小さく切欠状により原料気体排出路16aを形成する部分と、1次側フランジ11の凹部に収まる部分である接続縁部14aとを有している。
該接続縁部14aの一部は、図示は省略するが、1次側フランジ11に形成された凹部に溶接されている。
該原料気体排出路16aは、図1及び図2に示すように、1次側円筒体10と原料供給管13との間に形成された原料気体排出路16bに通じている。
該原料気体排出路16bは、図2に示すように、1次側円筒体10の後端側に接続された原料気体排出管17による原料気体排出路16cに通じている。
As shown in FIG. 3, the outer periphery of the perforated plate 14 is smaller than the inner diameter of the primary side cylinder 10 and has a notch shape to form a raw material gas discharge path 16a and a portion that fits in the recess of the primary side flange 11. It has a connecting edge portion 14a which is.
Although not shown, a part of the connection edge portion 14a is welded to a recess formed in the primary side flange 11.
As shown in FIGS. 1 and 2, the raw material gas discharge path 16a leads to a raw material gas discharge path 16b formed between the primary side cylinder 10 and the raw material supply pipe 13.
As shown in FIG. 2, the raw material gas discharge path 16b leads to the raw material gas discharge path 16c by the raw material gas discharge pipe 17 connected to the rear end side of the primary side cylinder 10.

図1に示すように、2次側フランジ21の凹部には、2次側ガスケット22と共に、円形状のメタルフィルター23と円形状の孔有支持板24が、水素透過金属膜30側から順に配置されている。
該孔有支持板24には、水素透過金属膜30を透過した水素が通過するための複数の透過気体通過孔25が形成されている。
As shown in FIG. 1, in the recess of the secondary side flange 21, a circular metal filter 23 and a circular perforated support plate 24 are arranged in order from the hydrogen permeable metal film 30 side together with the secondary side gasket 22. Has been done.
The perforated support plate 24 is formed with a plurality of permeated gas passage holes 25 for passing hydrogen that has permeated through the hydrogen permeation metal film 30.

図1及び図2に示すように、2次側円筒体20の内部には、前記透過気体通過孔25を通過した水素が流れ込む透過気体取出路26bが形成されている。
図2に示すように、該2次側円筒体20の後端側には、内径4.4mmの透過気体取出管27が接続されている。
As shown in FIGS. 1 and 2, a permeated gas outlet path 26b into which hydrogen that has passed through the permeated gas passing hole 25 flows is formed inside the secondary side cylinder 20.
As shown in FIG. 2, a permeation gas take-out pipe 27 having an inner diameter of 4.4 mm is connected to the rear end side of the secondary side cylinder 20.

該透過気体取出管27の内部には、透過気体取出路26cが形成されている。
該当化気体取出路26cは、透過気体取出路26bに通じている。
A permeated gas take-out path 26c is formed inside the permeated gas take-out pipe 27.
The corresponding gas take-out passage 26c leads to the permeated gas take-out passage 26b.

次に、前記の水素透過装置の作用について説明する。 Next, the operation of the hydrogen permeation device will be described.

図1から図4に示すとおり、水素を含有する気体は、原料供給管13から調整された圧力で供給される。
供給された気体は、図1に示すとおり、原料供給管13先端部分で、開孔板14によって流路が制限されているので、そのまま流れることなく、原料供給管13の内径より小さい直径の噴出孔15から水素透過金属膜30側に噴出する際に、流速が早められることになる。
As shown in FIGS. 1 to 4, the hydrogen-containing gas is supplied from the raw material supply pipe 13 at an adjusted pressure.
As shown in FIG. 1, the supplied gas does not flow as it is because the flow path is restricted by the opening plate 14 at the tip of the raw material supply pipe 13, and the gas has a diameter smaller than the inner diameter of the raw material supply pipe 13. When ejecting from the hole 15 toward the hydrogen permeable metal film 30, the flow velocity is increased.

早い流速で噴出した気体は、水素透過金属膜30の中心部付近に当たってから、水素透過金属膜30の外縁側に流れ出す。
この際、一部の水素分子が乖離して水素原子となって水素透過金属膜30に入り込み、圧力差により2次側に進み、最後には水素透過金属膜30を透過する。
The gas ejected at a high flow velocity hits the vicinity of the central portion of the hydrogen permeable metal film 30, and then flows out to the outer edge side of the hydrogen permeable metal film 30.
At this time, some hydrogen molecules are separated to form hydrogen atoms and enter the hydrogen permeable metal membrane 30, proceed to the secondary side due to the pressure difference, and finally permeate the hydrogen permeable metal membrane 30.

図2及び図4に示すとおり、1次側において、水素透過金属膜30に入り込まない気体は、開孔板14の外周縁に形成された原料気体排出路16aを通り、更に、原料気体排出路16b、原料気体排出路16cを通って、排出される。 As shown in FIGS. 2 and 4, the gas that does not enter the hydrogen permeable metal film 30 on the primary side passes through the raw material gas discharge path 16a formed on the outer peripheral edge of the perforated plate 14, and further, the raw material gas discharge path. 16b, the raw material gas is discharged through the discharge path 16c.

2次側において、水素透過金属膜30を透過した理論純度100パーセントの水素は、図1に示すとおり、メタルフィルター23及び孔有支持板24の透過気体通過孔25を通る。
透過気体通過孔25を通った超高純度の水素は、図2及び図4に示すとおり、透過気体取出路26b,26cを通り、容器(図示は省略)に分離回収される。
On the secondary side, hydrogen having a theoretical purity of 100% that has permeated through the hydrogen permeation metal film 30 passes through the permeation gas passage holes 25 of the metal filter 23 and the perforated support plate 24, as shown in FIG.
As shown in FIGS. 2 and 4, the ultra-high-purity hydrogen that has passed through the permeated gas passage hole 25 passes through the permeated gas outlet paths 26b and 26c and is separated and recovered in a container (not shown).

[比較例] [Comparison example]

図5、図6に示すとおり、原料供給管13の内径と等しく孔径が4.4mmの供給管径噴出孔18を設けた水素透過装置を準備した。
該比較例の水素透過装置は、供給管径噴出孔18の孔径以外は、前記実施例の水素透過装置と同様の構成なので、説明は省略する。
As shown in FIGS. 5 and 6, a hydrogen permeation device provided with a supply pipe diameter ejection hole 18 having a hole diameter equal to the inner diameter of the raw material supply pipe 13 and a hole diameter of 4.4 mm was prepared.
Since the hydrogen permeation device of the comparative example has the same configuration as the hydrogen permeation device of the above embodiment except for the hole diameter of the supply pipe diameter ejection hole 18, the description thereof will be omitted.

[比較試験] [Comparative test]

前記実施例の水素透過装置と、前記比較例の水素透過装置について、同一の条件で、水素透過試験を行った。
試験結果について、流量を図7に、透過係数を図8に示す。
The hydrogen permeation device of the above example and the hydrogen permeation device of the comparative example were subjected to a hydrogen permeation test under the same conditions.
Regarding the test results, the flow rate is shown in FIG. 7, and the permeability coefficient is shown in FIG.

結果を考察すると、比較例の4.4mm孔よりも、実施例の1.1mm孔の方が、良好なデータを示し、孔径を小さくすることが有効であることが確認された。 Considering the results, it was confirmed that the 1.1 mm hole of the example showed better data than the 4.4 mm hole of the comparative example, and it was effective to reduce the hole diameter.

[実施例2] [Example 2]

図9に示すとおり、本実施例2における開孔板14の円状の噴出孔15は、実施例1の噴出孔15と異なり、原料供給管13が取り付けられている原料気体の供給側である1次側から、透過気体の取出側である2次側に向けて、テーパ形状を有するように形成されている。
すなわち、本実施例2の場合は、円状の噴出孔15の直径が、テーパ状に変化するように形成されている。
As shown in FIG. 9, the circular ejection hole 15 of the opening plate 14 in the second embodiment is different from the ejection hole 15 of the first embodiment and is on the supply side of the raw material gas to which the raw material supply pipe 13 is attached. It is formed so as to have a tapered shape from the primary side toward the secondary side, which is the extraction side of the permeated gas.
That is, in the case of the second embodiment, the diameter of the circular ejection hole 15 is formed so as to change in a tapered shape.

図9中、(A)は、円状の噴出孔15について、1次側から2次側に向けて、径が徐々に小さくなるようにテーパを形成したもので、1次側の孔径を3.1mm、2次側の孔径を1.1mmに形成したものである。
図9中、(B)は、円状の噴出孔15について、1次側から2次側に向けて、径が徐々に大きくなるようにテーパを形成したもので、1次側の孔径を1.1mm、2次側の孔径を3.1mmに形成したものである。
In FIG. 9, (A) shows a circular ejection hole 15 having a taper formed so that the diameter gradually decreases from the primary side to the secondary side, and the hole diameter on the primary side is 3 .1 mm, the hole diameter on the secondary side is formed to 1.1 mm.
In FIG. 9, (B) shows a circular ejection hole 15 having a taper formed so that the diameter gradually increases from the primary side to the secondary side, and the hole diameter on the primary side is 1. The hole diameter on the secondary side is 3.1 mm and is formed to 3.1 mm.

本実施例2による円状の噴出孔15によると、径がテーパ状に変化するように形成されているので、流速が早まるだけでなく、乱流や速度変化等により、噴出孔15通過後の気流の変化が多面的に引き起こされ、より効果的に水素透過金属膜30(図1参照)に噴出される。
[実施例3]
According to the circular ejection hole 15 according to the second embodiment, since the diameter is formed so as to change in a tapered shape, not only the flow velocity is increased, but also due to turbulence, speed change, etc., after passing through the ejection hole 15. Changes in the air flow are caused in many ways and are more effectively ejected onto the hydrogen permeable metal film 30 (see FIG. 1).
[Example 3]

図10に示すとおり、本実施例3における開孔板14の噴出孔15の形状は、実施例1における円状の噴出孔15(図3参照)と異なるものであるが、該開孔板14の噴出孔15の大きさが、原料供給管13(図1~図3参照)の内径より小さいという特徴は、実施例1と共通するものである。 As shown in FIG. 10, the shape of the ejection hole 15 of the opening plate 14 in the third embodiment is different from the circular ejection hole 15 (see FIG. 3) in the first embodiment, but the opening plate 14 The feature that the size of the ejection hole 15 is smaller than the inner diameter of the raw material supply pipe 13 (see FIGS. 1 to 3) is common to the first embodiment.

図10中、(A)は、星型5角形の形状の噴出孔15の部分を拡大して示すもの、全体が直径1.1mmの円内に収まるように形成されている。
図10中、(B)は、6角形の形状の噴出孔15の部分を拡大して示すもの、全体が直径1.1mmの円内に収まるように形成されている。
In FIG. 10, (A) shows an enlarged portion of the ejection hole 15 having a star-shaped pentagon shape, and is formed so as to fit within a circle having a diameter of 1.1 mm as a whole.
In FIG. 10, (B) shows an enlarged portion of the hexagonal shape of the ejection hole 15, and is formed so that the entire portion fits within a circle having a diameter of 1.1 mm.

本実施例3による多角形や星型多角形による噴出孔15によると、形状自体が円形と異なる形状で形成されているので、流速が早まるだけでなく、乱流や部分的な速度変化等により、噴出孔15通過後の気流の変化がより多面的に引き起こされ、より一層効果的に水素透過金属膜30(図1参照)に噴出される。 According to the polygonal and star-shaped polygonal ejection holes 15 according to the third embodiment, since the shape itself is formed in a shape different from the circular shape, not only the flow velocity is increased, but also due to turbulence, partial velocity change, and the like. , The change in the airflow after passing through the ejection hole 15 is caused in a more multifaceted manner, and is more effectively ejected to the hydrogen permeable metal film 30 (see FIG. 1).

10 1次側円筒体
11 1次側フランジ
12 1次側ガスケット
13 原料供給管
14 開孔板
14a 接続縁部
15 噴出孔
16a,16b,16c 原料気体排出路
17 原料気体排出管
18 供給管径噴出孔
20 2次側円筒体
21 2次側フランジ
22 2次側ガスケット
23 メタルフィルター
24 孔有支持板
25 透過気体通過孔
26b,26c 透過気体取出路
27 透過気体取出管
30 水素透過金属膜
10 Primary side cylinder 11 Primary side flange 12 Primary side gasket 13 Raw material supply pipe 14 Opening plate 14a Connection edge 15 Injection holes 16a, 16b, 16c Raw material gas discharge path 17 Raw material gas discharge pipe 18 Supply pipe diameter ejection Hole 20 Secondary side Cylindrical body 21 Secondary side flange 22 Secondary side gasket 23 Metal filter 24 Perforated support plate 25 Permeated gas passage holes 26b, 26c Permeation gas outlet path 27 Permeation gas outlet pipe 30 Hydrogen permeation metal film

Claims (4)

原料気体の供給側である1次側円筒体と、透過気体の取出側である2次側円筒体との間に、水素透過金属膜を有する水素透過装置であって、
前記1次側円筒体には、
原料気体供給路を形成する原料供給管と、
前記原料供給管の先端に取り付けられ、前記原料供給管と接する領域の中心部に噴出孔を有する略開孔板と、を有し、
該開孔板は、前記1次側円筒体の内径に接すると共に、前記1次側円筒体の内径よりも小さい領域に原料気体排出路が形成され、
該開孔板の噴出孔の直径が、原料供給管の内径より小さく形成されていることを特徴とする、水素透過装置。
A hydrogen permeation device having a hydrogen permeation metal film between the primary side cylinder which is the supply side of the raw material gas and the secondary side cylinder which is the takeout side of the permeated gas.
The primary side cylinder has
The raw material supply pipe that forms the raw material gas supply path,
It has a substantially open plate which is attached to the tip of the raw material supply pipe and has a ejection hole in the center of a region in contact with the raw material supply pipe.
The perforated plate is in contact with the inner diameter of the primary side cylinder, and a raw material gas discharge path is formed in a region smaller than the inner diameter of the primary side cylinder.
A hydrogen permeation device characterized in that the diameter of the ejection hole of the opening plate is formed to be smaller than the inner diameter of the raw material supply pipe.
原料気体の供給側である1次側円筒体と、透過気体の取出側である2次側円筒体との間に、水素透過金属膜を有する水素透過装置であって、
1次側円筒体の先端側には、1次側フランジが形成され、
該1次側フランジには、凹部が形成され、
前記1次側円筒体には、
原料気体供給路を形成する原料供給管と、
2次側に透過しない原料気体を排出する原料気体排出路と、
前記原料供給管の先端側に中心部に噴出孔を有する略円形状の開孔板を有し、
該開孔板の外周は、1次側円筒体の内径より小さく切欠状により原料気体排出路を形成する部分と、1次側フランジの凹部に収まる部分である接続縁部とを有し、
該開孔板の噴出孔の直径が、原料供給管の内径より小さく形成されていることを特徴とする、水素透過装置。
A hydrogen permeation device having a hydrogen permeation metal film between the primary side cylinder which is the supply side of the raw material gas and the secondary side cylinder which is the takeout side of the permeated gas.
A primary side flange is formed on the tip side of the primary side cylinder, and a primary side flange is formed.
A recess is formed in the primary flange.
The primary side cylinder has
The raw material supply pipe that forms the raw material gas supply path,
A raw material gas discharge path that discharges raw material gas that does not permeate to the secondary side,
A substantially circular opening plate having a ejection hole in the center on the tip end side of the raw material supply pipe is provided.
The outer periphery of the perforated plate has a portion that is smaller than the inner diameter of the primary side cylinder and forms a raw material gas discharge path by a notch shape, and a connection edge portion that is a portion that fits in the recess of the primary side flange.
A hydrogen permeation device characterized in that the diameter of the ejection hole of the opening plate is formed to be smaller than the inner diameter of the raw material supply pipe.
前記原料気体排出路は、1次側円筒体と原料供給管との間に形成された原料気体排出路に通じており、
該1次側円筒体と原料供給管との間に形成された原料気体排出路は、1次側円筒体の後端側に接続された原料気体排出管による原料気体排出路に通じていることを特徴とする、請求項1または2に記載の水素透過装置。
The raw material gas discharge path leads to a raw material gas discharge path formed between the primary side cylinder and the raw material supply pipe.
The raw material gas discharge path formed between the primary side cylinder and the raw material supply pipe is connected to the raw material gas discharge path by the raw material gas discharge pipe connected to the rear end side of the primary side cylinder. The hydrogen permeation device according to claim 1 or 2, wherein the hydrogen permeation device is characterized.
前記開孔板の噴出孔が、1次側から2次側に向けて、テーパ形状を有することを特徴とする、請求項1から3のいずれか一つに記載の水素透過装置。
The hydrogen permeation device according to any one of claims 1 to 3, wherein the ejection hole of the opening plate has a tapered shape from the primary side to the secondary side.
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