JPH038812B2 - - Google Patents
Info
- Publication number
- JPH038812B2 JPH038812B2 JP59274808A JP27480884A JPH038812B2 JP H038812 B2 JPH038812 B2 JP H038812B2 JP 59274808 A JP59274808 A JP 59274808A JP 27480884 A JP27480884 A JP 27480884A JP H038812 B2 JPH038812 B2 JP H038812B2
- Authority
- JP
- Japan
- Prior art keywords
- hydrogen
- tubular membrane
- atmospheric pressure
- membrane
- gas
- 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.)
- Expired - Lifetime
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E30/00—Energy generation of nuclear origin
- Y02E30/10—Nuclear fusion reactors
Landscapes
- Hydrogen, Water And Hydrids (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、例えば核融合炉燃料給排気系におけ
る不純物の除去工程や半導体プロセス等に利用さ
れ得る高純度水素精製装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a high-purity hydrogen purification device that can be used, for example, in an impurity removal process in a nuclear fusion reactor fuel supply and exhaust system, a semiconductor process, and the like.
従来の技術
従来、高純度水素の製造法としてパラジウム合
金膜を用いたものが知られており、この方法はパ
ラジウムの水素透過性が極めて大きいことを利用
して不純物と水素との分離を行なうものである。
すなわちパラジウム系合金の膜を加熱し、この膜
を介して不純物を含んだ水素ガス中の水素のみ透
過させ、高純度の水素を精製するものであり、こ
の方法は今日最も高純度の水素を得ることのでき
る方法であるとされている。Conventional technology Conventionally, a method using a palladium alloy membrane has been known as a method for producing high-purity hydrogen, and this method takes advantage of palladium's extremely high hydrogen permeability to separate impurities and hydrogen. It is.
In other words, a palladium-based alloy membrane is heated, and only the hydrogen in the hydrogen gas containing impurities permeates through the membrane to purify high-purity hydrogen. This method obtains the highest purity hydrogen today. It is said that this is a possible method.
ところでパラジウム合金膜を用いた従来の水素
精製装置としてはPd−Ag合金膜管の一端を直接
ステンレス製等の本体に溶接し、他端は同じ材質
のもので封じられており、そしてPd−Ag合金膜
管の外側(すなわち一次側)には加熱用ヒーター
が設けられ、加熱温度を均一にするためステンレ
スの粉等を入れる場合がある。処理すべき水素ガ
スはPd−Ag合金膜管の外側に供給され水素だけ
が管の外側より内側へ透過して二次側へ引き出さ
れるようにされている。 By the way, in conventional hydrogen purification equipment using palladium alloy membranes, one end of the Pd-Ag alloy membrane tube is directly welded to a main body made of stainless steel or the like, and the other end is sealed with the same material. A heater is provided on the outside (ie, the primary side) of the alloy membrane tube, and stainless steel powder or the like may be added to the tube to make the heating temperature uniform. Hydrogen gas to be treated is supplied to the outside of the Pd-Ag alloy membrane tube, so that only hydrogen permeates from the outside to the inside of the tube and is drawn out to the secondary side.
しかしこのような従来装置ではパラジウム合金
は非常にもろいので上述のようにPd−Ag合金膜
管を直接ステンレス等の本体に溶接した場合には
溶接部に割れが入り易く、それによりリークが発
生し、二次側(高純度水素側)に不純物が流入す
る恐れがある。またこのようなPd−Ag合金膜管
は通常機械工作的方法で製作されるため、管の内
側および外側とも油脂やほこり等で相当汚れてい
る。そのため先端の封じている構造では管内部の
洗浄を十分に行なうことができず、二次側に不純
物ガスが発生し、水素の純度を低下させる原因と
なつている。さらに加熱の均一化のために一次側
にステンレス等の粉を多量に充填したものではそ
こから不純物が発生し、パラジウム合金膜を腐食
させて穴をあけてしまう場合が生じ得る。 However, in such conventional equipment, palladium alloy is extremely brittle, so when the Pd-Ag alloy membrane tube is welded directly to the main body made of stainless steel, etc., as mentioned above, cracks tend to form in the weld, which can cause leaks. , there is a risk that impurities may flow into the secondary side (high-purity hydrogen side). Furthermore, since such Pd-Ag alloy membrane tubes are usually manufactured using a mechanical method, both the inside and outside of the tubes are considerably contaminated with oil, fat, and dust. Therefore, with a structure in which the tip is sealed, the inside of the tube cannot be sufficiently cleaned, and impurity gas is generated on the secondary side, causing a decrease in the purity of hydrogen. Furthermore, if the primary side is filled with a large amount of powder of stainless steel or the like in order to make heating uniform, impurities may be generated therefrom, corroding the palladium alloy film and causing holes.
このような種々の欠点を解決した高純度水素精
製装置が特願昭59−198500号明細書に提案されて
おり、この装置においてはパラジウム系合金の管
状膜の両端部を開放端としその一方の端部は溶接
やロウ付けの容易なニツケル等の高純度金属の管
状部材を介して本体に固着し、他方の端部には管
状部材と同じ材質の封止部材が嵌合固着され、ま
た管状膜に対する加熱ヒータは不純物の発生の少
ない物質の支持体で支持され、さらに各シール部
には超高真空フランジが用いられている。 A high-purity hydrogen purification device that solves these various drawbacks has been proposed in Japanese Patent Application No. 198500/1983, and in this device, both ends of a palladium-based alloy tubular membrane are open ends, and one of the ends is open. The end is fixed to the main body via a tubular member made of high-purity metal such as nickel that can be easily welded or brazed, and the other end is fitted with a sealing member made of the same material as the tubular member. The heater for the membrane is supported by a support made of a material that generates few impurities, and an ultra-high vacuum flange is used at each sealing part.
発明が解決しようとする問題点
しかしながら、このような従来装置においては
装置の休止時に例えば内部をクリーニングするた
め、一次側の未透過ガス(ブリードガス)を排気
系を通して排出する際に装置内部が大気圧かまた
はそれ以下に下がると微粒子が侵入する恐れがあ
り、これがPd−Ag膜に付着すると微結晶成長核
となり、ピンホール発生の原因となる。その結果
Pd−Ag膜の寿命は短かくなり、頻繁に交換しな
ければならなくなる。Problems to be Solved by the Invention However, in such conventional devices, when the device is stopped, for example, the inside is cleaned, and when the unpermeated gas (bleed gas) on the primary side is discharged through the exhaust system, the inside of the device becomes large. If the atmospheric pressure drops to or below the atmospheric pressure, there is a risk that fine particles may enter the Pd-Ag film, and if these particles adhere to the Pd-Ag film, they will become nuclei for microcrystal growth and cause pinholes. the result
The lifespan of the Pd-Ag film is shortened and must be replaced frequently.
そこで、本発明の目的は、このような装置の休
止時に排気系からの微粒子の侵入を阻止して精製
膜をそれらによる損傷から保護することにある。 Therefore, an object of the present invention is to prevent the intrusion of fine particles from the exhaust system when such an apparatus is stopped, and to protect the purification membrane from damage caused by them.
問題点を解決するための手段
この目的を達成するために、本発明によれば、
ステンレス等の本体にパラジウム系合金の管状膜
の一端を溶接し、管状態の他端には封止部材を装
着し、この管状膜を加熱し、上記管状膜を介して
不純物を含んだ水素ガス中の水素のみを透過さ
せ、高純度の水素を精製し、また休止時には内部
を大気圧または大気圧以下にできる高純度水素精
製装置において、一次側に不純物成分の濃縮され
た水素ガスを排出するための排出系を連結し、こ
の排出系に、装置の内部を大気圧または大気圧以
下にする際に大気からの微粒子の侵入を防止する
フイルタを設けたことを特徴としている。Means for solving the problem To achieve this objective, according to the invention:
One end of a palladium-based alloy tubular membrane is welded to a main body made of stainless steel, etc., a sealing member is attached to the other end of the tube, this tubular membrane is heated, and hydrogen gas containing impurities is passed through the tubular membrane. In high-purity hydrogen purification equipment, which allows only the hydrogen inside to permeate and refines high-purity hydrogen, and which can reduce the internal pressure to atmospheric pressure or below atmospheric pressure when it is not in operation, discharges hydrogen gas with concentrated impurity components to the primary side. The device is characterized in that the exhaust system is connected to an exhaust system, and this exhaust system is provided with a filter that prevents particulates from entering from the atmosphere when the inside of the device is brought to atmospheric pressure or below atmospheric pressure.
作 用
このように構成したことによつて本発明の装置
においては、大気中からの微粒子の侵入を阻止す
るフイルタは例えば0.02μmフイルタから成るこ
とができ、それにより大気から排出管系を通つて
一次側への微粒子の侵入は実質的に防止され、従
つて管状膜に対する排気管系からの微粒子による
侵食は末然に防止され得る。また、本体に近くに
取付けられたブリード配管のバルブを操作時に微
粒子の発生しないバルブで構成することにより、
一次側への微粒子の侵入をより確実に防止するこ
とができる。これにより精製膜は長期間安定して
動作することができる。Effect With this configuration, in the device of the present invention, the filter for preventing the intrusion of fine particles from the atmosphere can be composed of, for example, a 0.02 μm filter, so that the filter that prevents the intrusion of fine particles from the atmosphere through the exhaust pipe system. The ingress of particulates into the primary side is substantially prevented, so that attack of the tubular membrane by particulates from the exhaust pipe system can ultimately be prevented. In addition, by configuring the bleed piping valve installed near the main body with a valve that does not generate particulates when operated,
It is possible to more reliably prevent fine particles from entering the primary side. This allows the purification membrane to operate stably for a long period of time.
実施例
以下添付図面を参照して本発明の実施例につい
て説明する。Embodiments Hereinafter, embodiments of the present invention will be described with reference to the accompanying drawings.
第1図には本発明の一実施例を示し、1はステ
ンレス製の本体、2はPd−Ag管状膜で、この管
状膜2の一方の開端2aはニツケルの管状部材3
の一端にパラジウムロウ材を用いてロウ付けさ
れ、管状部材3の他端は本体1の端壁4に溶接さ
れている。一方、管状膜2の他方の開端2bには
ニツケルの封止部材5が嵌合ロウ付けされてい
る。こうして構成された管状膜組立体は図面には
二つだけ示されているが、その数は任意に設計す
ることができる。各管状膜2内にはその全長に沿
つて、表面を窒化チタンでコーテイングしたステ
ンレスまたはタングステン等のばね状体6が内装
した状態で挿置されている。これにより管状膜2
は一次側の圧力に十分耐えることができる。管状
膜組立体の外周にはその全長にわたつてのびる無
酸素銅製の内筒体7が配置されており、この円筒
体7は一端で本体1の端壁8に固定されており、
そしてこの円筒体7の外周面上にはヒータ9が装
着されている。このヒータ9は図示してない導線
を介して外部電源に接続される。また10は精製
すべき水素ガスの導入管であり、その先端には各
管状膜2の一部分に局所的に水素ガスが吹き付け
るのを避け、本体1内で比較的均一なガス流を得
るため、第2図に示すように横方向の多数の吹き
出し口11aを備えたドラム状の導入部1が設け
られている。これにより一次側ガスの精製筒すな
わち各管状膜2への水素ガスの吹き出しが制御さ
れ、その結果管状膜2の寿命を延ばすことができ
る。 FIG. 1 shows an embodiment of the present invention, in which 1 is a stainless steel main body, 2 is a Pd-Ag tubular membrane, and one open end 2a of this tubular membrane 2 is a nickel tubular member 3.
One end of the tubular member 3 is brazed using palladium brazing material, and the other end of the tubular member 3 is welded to the end wall 4 of the main body 1. On the other hand, a nickel sealing member 5 is fitted and brazed to the other open end 2b of the tubular membrane 2. Although only two tubular membrane assemblies constructed in this manner are shown in the drawings, the number can be designed arbitrarily. A spring-like body 6 made of stainless steel or tungsten whose surface is coated with titanium nitride is inserted inside each tubular membrane 2 along its entire length. This allows the tubular membrane 2
can withstand the pressure on the primary side. Arranged on the outer periphery of the tubular membrane assembly is an inner cylinder 7 made of oxygen-free copper that extends over its entire length and is fixed at one end to the end wall 8 of the main body 1.
A heater 9 is mounted on the outer peripheral surface of the cylindrical body 7. This heater 9 is connected to an external power source via a conductor (not shown). Reference numeral 10 denotes an inlet pipe for introducing hydrogen gas to be purified, and its tip is equipped with a pipe in order to avoid blowing hydrogen gas locally onto a portion of each tubular membrane 2 and to obtain a relatively uniform gas flow within the main body 1. As shown in FIG. 2, a drum-shaped introduction section 1 is provided with a large number of lateral air outlets 11a. This controls the blowing of hydrogen gas to the primary gas purification cylinder, that is, each tubular membrane 2, and as a result, the life of the tubular membrane 2 can be extended.
各管状膜組立体の内部はふた部材12に設けら
れた精製水素取出管13へ空所14を介して連通
している。また本体1の両端のフランジ1a,1
bと組合さつた端壁4,8との間および端壁4と
ふた部材12との間のシール部には、99,99999
%以上の高純度の水素を精製する観点から装置内
部を超高真空にでき(すなわち精製される水素の
純度を高くする目的で、装置内部の水素ガスに触
れる部分に付着した不純物ガスやその部分の内部
からの放出ガスをできるだけ低減するため)しか
も200℃以上の高温にも耐え得るようにするため
それぞれメタルOリング15,16,17が使用
される。これらのメタルOリングは例えばステン
レス、Ni,Alに窒化チタンをコーテイングした
ものから成り、つぶれないようにするため内部に
ばねを入れたものが好ましい。 The inside of each tubular membrane assembly communicates via a cavity 14 to a purified hydrogen take-off pipe 13 provided in the lid member 12. Also, the flanges 1a, 1 at both ends of the main body 1
99,99999 in the seal portion between the end walls 4 and 8 assembled with b and between the end wall 4 and the lid member 12.
In order to purify hydrogen with a purity of over 100%, the inside of the device can be made into an ultra-high vacuum (i.e., in order to increase the purity of hydrogen to be purified, impurity gases attached to the parts inside the device that come in contact with hydrogen gas and those parts) Metal O-rings 15, 16, and 17 are used, respectively, in order to reduce the amount of gas released from the inside of the device as much as possible) and to withstand high temperatures of 200° C. or higher. These metal O-rings are made of, for example, stainless steel, Ni, or Al coated with titanium nitride, and preferably have a spring inside to prevent crushing.
また本体1の内壁の水素ガスと接触する部分お
よび二次側の空所14の内壁部分には図示された
ように高温に耐え安定でしかも放出ガスの少ない
導電性材料例えば窒化チタンコーテイング18,
19が施されており、これにより放出ガスを少な
くして管状膜2の腐食や精製水素の純度低下を防
止している。このコーテイング材料としては上記
窒化チタンの他に放出ガスの少ない材料例えば
CrN,AlN,BN等を挙げることができる。 In addition, as shown in the figure, the inner wall of the main body 1 in the portion that comes into contact with the hydrogen gas and the inner wall of the secondary side cavity 14 is coated with a conductive material that can withstand high temperatures, is stable, and emits less gas, such as titanium nitride coating 18.
19 is applied, thereby reducing the amount of released gas to prevent corrosion of the tubular membrane 2 and a decrease in the purity of purified hydrogen. In addition to the above-mentioned titanium nitride, materials for this coating include materials that emit less gas, such as
Examples include CrN, AlN, BN, etc.
さらに第1図において20は一次側で不純物成
分の濃縮された水素ガスを排出するための排出系
で、この排出系20は図示されたように二つのバ
ルブ20a,20bとフイルタ20cとを備えて
いる。フイルタ20cは大気中から微粒子が一次
側に侵入して管状膜2に付着するのを阻止する働
きをし、例えば0.02μmフイルタから成り得る。
またバルブ20aには操作時に微粒子発生のない
バルブ、例えばベローバルブ、ダイアフラムバル
ブ等が使用され得る。管状膜2に微粒子が付着す
ると微結晶成長核となり、ピンホール発生の原因
となるため、微粒子の侵入を防ぐことは安定動作
の観点からも重要である。 Furthermore, in FIG. 1, reference numeral 20 denotes an exhaust system for discharging hydrogen gas enriched with impurity components on the primary side, and this exhaust system 20 is equipped with two valves 20a, 20b and a filter 20c as shown. There is. The filter 20c functions to prevent fine particles from the atmosphere from entering the primary side and adhering to the tubular membrane 2, and may be made of, for example, a 0.02 μm filter.
Furthermore, a valve that does not generate particulates during operation, such as a bellows valve or a diaphragm valve, may be used as the valve 20a. When fine particles adhere to the tubular membrane 2, they become nuclei for microcrystal growth and cause pinholes, so preventing the intrusion of fine particles is also important from the viewpoint of stable operation.
第3〜4図には変形実施例を示し、水素ガスの
導入部21がドーナツ状を成し、端壁8に向つて
多数の吹き出し口21aを備えている点を除いて
第1図に示す構造と同じである。 3 and 4 show a modified embodiment, which is shown in FIG. 1 except that the hydrogen gas introduction part 21 has a donut shape and is provided with a large number of outlets 21a toward the end wall 8. The structure is the same.
図示実施例は単に例示のためのものであつて各
部分の構造、形状等は種々設計することができ、
また本発明は当然上述で述べたような先行技術の
水素精製装置にも適用され得るものである。 The illustrated embodiments are merely for illustrative purposes, and the structure, shape, etc. of each part can be designed in various ways.
Naturally, the present invention can also be applied to prior art hydrogen purification apparatuses such as those described above.
効 果
以上説明してきたように、本発明によれば、ブ
リードガスの排出系に微粒子の侵入を阻止するフ
イルタを設けているので、これら微粒子が一次側
に入つて精製膜を侵食する恐れがなく、長期間精
製膜は安定して使用することができ、その結果装
置の運転コストを低くおさえることができる。Effects As explained above, according to the present invention, since the bleed gas exhaust system is provided with a filter that prevents the entry of fine particles, there is no fear that these fine particles will enter the primary side and corrode the purification membrane. The purification membrane can be used stably for a long period of time, and as a result, the operating cost of the device can be kept low.
第1図は本発明の一実施例を示す概略断面図、
第2図は第1図の装置の一部を拡大して示す斜視
図、第3図は本発明の変形実施例を示す概略断面
図、第4図は第3図の装置の一部の拡大平面図で
ある。
図中、1:本体、2:管状膜、20c:フイル
タ。
FIG. 1 is a schematic sectional view showing an embodiment of the present invention;
2 is an enlarged perspective view of a part of the device shown in FIG. 1, FIG. 3 is a schematic sectional view showing a modified embodiment of the present invention, and FIG. 4 is an enlarged part of the device shown in FIG. 3. FIG. In the figure, 1: main body, 2: tubular membrane, 20c: filter.
Claims (1)
状膜の一端を溶接し、管状膜の他端には封止部材
を装着し、この管状膜を加熱し、上記管状膜を介
して不純物を含んだ水素ガス中の水素のみを透過
させ、高純度の水素を精製し、また休止時には内
部を大気圧または大気圧以下にできる高純度水素
精製装置において、一次側に不純物成分の濃縮さ
れた水素ガスを排出するための排出系を連結し、
この排出系に、装置の内部を大気圧または大気圧
以下にする際に大気からの微粒子の侵入を防止す
るフイルタを設けたことを特徴とする高純度水素
精製装置。1. One end of a palladium-based alloy tubular membrane is welded to a main body made of stainless steel, etc., a sealing member is attached to the other end of the tubular membrane, this tubular membrane is heated, and hydrogen containing impurities is passed through the tubular membrane. High-purity hydrogen purification equipment that allows only hydrogen in the gas to permeate and refines high-purity hydrogen, and that can reduce the internal pressure to atmospheric pressure or below atmospheric pressure when not in operation, discharges hydrogen gas with concentrated impurity components to the primary side. Connect the discharge system for
A high-purity hydrogen purification device characterized in that the exhaust system is provided with a filter that prevents particulates from entering from the atmosphere when the inside of the device is brought to atmospheric pressure or below atmospheric pressure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59274808A JPS61157324A (en) | 1984-12-28 | 1984-12-28 | Apparatus for purifying high purity hydrogen |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59274808A JPS61157324A (en) | 1984-12-28 | 1984-12-28 | Apparatus for purifying high purity hydrogen |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61157324A JPS61157324A (en) | 1986-07-17 |
| JPH038812B2 true JPH038812B2 (en) | 1991-02-07 |
Family
ID=17546849
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59274808A Granted JPS61157324A (en) | 1984-12-28 | 1984-12-28 | Apparatus for purifying high purity hydrogen |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61157324A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2685218B1 (en) * | 1991-12-19 | 1994-02-11 | Institut Francais Petrole | HYDROGEN PURIFIER COMPRISING AN ALLOY BASE OF THE SAME COMPOSITION AS THAT OF THE TUBES. |
| JP3402515B2 (en) * | 1994-05-23 | 2003-05-06 | 日本碍子株式会社 | Hydrogen separator, hydrogen separator using the same, and method for producing hydrogen separator |
| JP5149050B2 (en) * | 2008-03-25 | 2013-02-20 | 日本特殊陶業株式会社 | Hydrogen separator |
| JP7016116B2 (en) * | 2019-09-19 | 2022-02-04 | 株式会社ハイドロネクスト | Hydrogen permeation device |
-
1984
- 1984-12-28 JP JP59274808A patent/JPS61157324A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61157324A (en) | 1986-07-17 |
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| EXPY | Cancellation because of completion of term |