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JPH038809B2 - - Google Patents
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JPH038809B2 - - Google Patents

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Publication number
JPH038809B2
JPH038809B2 JP59274805A JP27480584A JPH038809B2 JP H038809 B2 JPH038809 B2 JP H038809B2 JP 59274805 A JP59274805 A JP 59274805A JP 27480584 A JP27480584 A JP 27480584A JP H038809 B2 JPH038809 B2 JP H038809B2
Authority
JP
Japan
Prior art keywords
tubular membrane
hydrogen
membrane
purity
stainless steel
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
Application number
JP59274805A
Other languages
Japanese (ja)
Other versions
JPS61157326A (en
Inventor
Tadahiro Oomi
Toshio Hayashi
Yoshasu Maehane
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.)
Ulvac Inc
Original Assignee
Nihon Shinku Gijutsu KK
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 Nihon Shinku Gijutsu KK filed Critical Nihon Shinku Gijutsu KK
Priority to JP59274805A priority Critical patent/JPS61157326A/en
Publication of JPS61157326A publication Critical patent/JPS61157326A/en
Publication of JPH038809B2 publication Critical patent/JPH038809B2/ja
Granted legal-status Critical Current

Links

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
    • Y02E30/00Energy generation of nuclear origin
    • Y02E30/10Nuclear fusion reactors

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)
  • Hydrogen, Water And Hydrids (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製造プロセス等に利
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 manufacturing process, and the like.

従来の技術 従来、高純度水素の精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、不純物
を含んだ水素ガス中の水素のみ上記膜を透過さ
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 refining high-purity hydrogen, and this method takes advantage of the extremely high hydrogen permeability of palladium to separate impurities and hydrogen. It is something.
In other words, a palladium-based alloy membrane is heated, and only the hydrogen in hydrogen gas containing impurities permeates through the membrane to purify high-purity hydrogen. This method is the most pure hydrogen available 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
ステンレス精等の本体に溶接し、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 the main body, such as stainless steel, 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 of the tube to the inside 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
は非常にもろいもので上述のように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が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 conventional equipment like this, palladium alloy is extremely brittle, and as mentioned above, when a Pd-Ag alloy membrane tube is welded directly to a main body made of stainless steel, etc., cracks tend to form in the weld, which can cause leaks. However, 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 and fat. 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 ensure uniform heating, impurities may be generated therefrom, corroding the palladium alloy film and creating 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 and fixed 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 このような改良型の装置により上述のような
種々の欠点は解決され得るが、しかしパラジウム
系合金の管状膜の外側には圧力がかかるため機械
的強度が問題となる。
Problems to be Solved by the Invention Although the various drawbacks mentioned above can be solved by such an improved device, mechanical strength is a problem because pressure is applied to the outside of the palladium-based alloy tubular membrane. Become.

水素の透過量は、Pd−Ag膜の面積、加熱温度
および一次側圧力に依存し、これらが増すことに
より水素の透過量も増加する。そしてまた水素の
透過量は膜厚に反比例する。従つて同一面積では
膜を薄くした方が経済的ではあるが、上述のよう
な従来構造のものではしばしば管状膜がつぶれて
リークの発生する場合がある。一方、機械的強度
を上げるために膜を厚くすることが考えられる
が、その結果水素の透過量が減り、結局膜面積を
増大させなければならず不経済である。
The amount of hydrogen permeation depends on the area of the Pd-Ag membrane, heating temperature, and primary side pressure, and as these increase, the amount of hydrogen permeation also increases. Furthermore, the amount of hydrogen permeation is inversely proportional to the film thickness. Therefore, it is more economical to make the membrane thinner for the same area, but in the conventional structure as described above, the tubular membrane often collapses and leakage occurs. On the other hand, it is conceivable to make the membrane thicker in order to increase its mechanical strength, but as a result, the amount of permeation of hydrogen decreases, and as a result, the membrane area must be increased, which is uneconomical.

このような観点から機械的強度を保つ方法とし
て従来Pd−Ag管の内にステンレス等のばねを入
れたものも知られているが、これら材質は放出ガ
スが多く、しかも二次側にあるため精製した水素
の純度を著しく下げる原因となつている。
From this point of view, a conventional method of maintaining mechanical strength is to insert a spring made of stainless steel or other material inside a Pd-Ag pipe, but these materials emit a lot of gas and are located on the secondary side. This causes a significant decrease in the purity of purified hydrogen.

そこで、本発明の目的は、所望の水素透過量を
保持できる膜厚でしかも精製される水素の純度を
低下させず管状膜の機械的強度を保証して安定し
た精製を行なうことのできる高純度水素精製装置
を提供することにある。
Therefore, an object of the present invention is to provide a high purity membrane that has a membrane thickness that can maintain a desired amount of hydrogen permeation, and that can ensure stable purification by guaranteeing the mechanical strength of the tubular membrane without reducing the purity of hydrogen to be purified. Our objective is to provide hydrogen purification equipment.

問題点を解決するための手段 上記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するようにした高純度
水素精製装置において、パラジウム系合金の管状
膜の全体に沿つて、表面にガス放出防止層をコー
テイングした機械的強度保持用の補強部材を装着
したことを特徴としている。
Means for Solving the Problems In order to achieve the above object, according to the present invention, one end of a palladium-based alloy tubular membrane is welded to a main body made of stainless steel, etc., and a sealing member is attached to the other end of the tubular membrane. In a high-purity hydrogen purification device that purifies high-purity hydrogen by heating this tubular membrane and permeating only the hydrogen in hydrogen gas containing impurities through the tubular membrane, palladium-based It is characterized in that a reinforcing member for maintaining mechanical strength, whose surface is coated with a gas release prevention layer, is attached along the entire tubular alloy membrane.

この補強部材は好ましくは表面を窒化チタンで
コーテイングしたステンレスやタングステン等か
ら成るばね状体であり、管状膜内に挿置され得
る。
This reinforcing member is preferably a spring-like member made of stainless steel, tungsten, or the like whose surface is coated with titanium nitride, and can be inserted into the tubular membrane.

作用 このように構成した本発明の装置においては、
窒化チタン等から成るガス放出防止層を表面にコ
ーテイングした補強部材を設けることによつて、
膜厚の薄いPd−Ag膜でも十分な強度を保持で
き、極めわ効率よく水素を精製でき、しかも二次
側の精製水素の純度を保つことができる。また補
強部材は管状膜の内側および外側のいずれに設け
てもよく、そしてばね状体の他にフイン状、網状
等種々の形状に設計することができる。
Effect In the device of the present invention configured as described above,
By providing a reinforcing member whose surface is coated with a gas release prevention layer made of titanium nitride, etc.
Even a thin Pd-Ag film can maintain sufficient strength, making it possible to purify hydrogen extremely efficiently and maintain the purity of purified hydrogen on the secondary side. Further, the reinforcing member may be provided on either the inside or outside of the tubular membrane, and can be designed in various shapes such as a fin shape, a net shape, etc. in addition to a spring shape.

実施例 以下添附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(好ましくはSUS316L)製の本体、2は
Pd−Ag管状膜で、この管状膜2の一方の開端2
a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、表面に窒化チタンか
ら成るガス放出防止層を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が内接し
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
素銅製の円筒体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を備えたドラム状導入部11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, where 1 is a main body made of stainless steel (preferably SUS316L), and 2 is a main body made of stainless steel (preferably SUS316L).
A Pd-Ag tubular membrane, one open end 2 of this tubular membrane 2.
A is brazed to one end of a nickel tubular member 3 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 way are shown in the drawing,
The number can be arbitrarily designed. A spring-like body 6 made of stainless steel or tungsten, whose surface is coated with a gas release prevention layer made of titanium nitride, is inserted inwardly inside each tubular membrane 2 along its entire length. This allows the tubular membrane 2 to sufficiently withstand the pressure on the primary side. Arranged on the outer periphery of the tubular membrane assembly is a cylinder 7 made of oxygen-free copper extending over its entire length, which cylinder 7 is fixed at one end to the end wall 8 of the body 1; A heater 9 is mounted on the outer circumferential surface of 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 11 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1
5,16,17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
In order to purify hydrogen with a high purity of 99.99999% or more, the inside of the device can be made into an ultra-high vacuum at the sealing parts between the end walls 4 and 8 combined with b and between the end wall 4 and the lid member 12. Moreover, in order to withstand high temperatures of over 200℃, each metal O-ring 1
5, 16, 17 are used. These metal O
The ring is made of, for example, stainless steel, Ni, or Al coated with titanium nitride, and preferably has 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、ダイヤフラムバル
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.
Further, 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.

図示実施例では各管状膜2にばね状体6が挿置
されているが、このばね状体6の代りに上記で述
べたように管状膜2の外側にフイン状の補強部材
を設け、或いは内部に網状や環状の補強部材を設
けてもよい。
In the illustrated embodiment, a spring-like body 6 is inserted into each tubular membrane 2, but instead of this spring-like body 6, a fin-like reinforcing member may be provided on the outside of the tubular membrane 2 as described above, or A net-like or annular reinforcing member may be provided inside.

また本発明は図示実施例に限定されるものでは
なく例えば上述の特願昭59−198500号明細書に記
載のような従来型の装置にも適用され得る。
Further, the present invention is not limited to the illustrated embodiment, but may be applied to a conventional device such as that described in the above-mentioned Japanese Patent Application No. 1985-1983.

効 果 以上説明してきたように本発明によれば、管状
膜に補強部材を設けたことにより、管状膜の機械
的強度を十分に保つことができ、一次側の水素ガ
ス圧力を10Kg/cm2程度にしても管状膜はつぶれる
ことがなく、例えば管状膜の厚さを50〜75μm程
度にすると、十分20Kg/cm2程度の圧力での使用が
可能となり、精製ガス流量を十分多くすることが
できる。また管状膜に対して使用される補強部材
はガス放出防止層をコーテイングしているので、
放出ガスは従来より少なくなり、精製水素の純度
の実質的低下を伴なわず、99.99999%以上の純度
を維持することができる。その結果本発明の装置
は長期間安定した精製動作を保証することができ
る。
Effects As explained above, according to the present invention, by providing the reinforcing member to the tubular membrane, the mechanical strength of the tubular membrane can be maintained sufficiently, and the hydrogen gas pressure on the primary side can be reduced to 10 kg/cm 2 For example, if the thickness of the tubular membrane is set to about 50 to 75 μm, it can be used at a pressure of about 20 kg/cm 2 and the purified gas flow rate can be sufficiently increased. can. In addition, the reinforcing member used for the tubular membrane is coated with a gas release prevention layer.
The released gas is lower than before, and the purity of purified hydrogen can be maintained at 99.99999% or higher without any substantial decrease in purity. As a result, the device according to the invention can guarantee stable purification operation over a long period of time.

【図面の簡単な説明】[Brief explanation of the drawing]

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、6:補強部材。
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, 6: reinforcing member.

Claims (1)

【特許請求の範囲】 1 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するようにした高純度
水素精製装置において、パラジウム系合金の管状
膜の全体に沿つて、表面にガス放出防止層をコー
テイングした機械的強度保持用の補強部材を装着
したことを特徴とする高純度水素精製装置。 2 補強部材が表面を窒化チタンでコーテイング
したステンレスやタングステン等から成るばね状
体であり、管状膜内に挿置される特許請求の範囲
第1項に記載の装置。
[Claims] 1. One end of a palladium-based alloy tubular membrane is welded to a main body made of stainless steel or the like, a sealing member is attached to the other end of the tubular membrane, this tubular membrane is heated, and a In a high-purity hydrogen purification device that purifies high-purity hydrogen by passing only hydrogen in hydrogen gas containing impurities, a gas release prevention layer is applied to the surface along the entire tubular membrane of palladium alloy. A high-purity hydrogen purification device characterized by being equipped with a reinforcing member for maintaining mechanical strength that is coated with. 2. The device according to claim 1, wherein the reinforcing member is a spring-like body made of stainless steel, tungsten, etc. whose surface is coated with titanium nitride, and is inserted into the tubular membrane.
JP59274805A 1984-12-28 1984-12-28 Apparatus for purifying high purity hydrogen Granted JPS61157326A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59274805A JPS61157326A (en) 1984-12-28 1984-12-28 Apparatus for purifying high purity hydrogen

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59274805A JPS61157326A (en) 1984-12-28 1984-12-28 Apparatus for purifying high purity hydrogen

Publications (2)

Publication Number Publication Date
JPS61157326A JPS61157326A (en) 1986-07-17
JPH038809B2 true JPH038809B2 (en) 1991-02-07

Family

ID=17546808

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59274805A Granted JPS61157326A (en) 1984-12-28 1984-12-28 Apparatus for purifying high purity hydrogen

Country Status (1)

Country Link
JP (1) JPS61157326A (en)

Also Published As

Publication number Publication date
JPS61157326A (en) 1986-07-17

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