JPS61122103A - Recovery of hydrogen from low pressure mixed gas containing hydrogen - Google Patents
Recovery of hydrogen from low pressure mixed gas containing hydrogenInfo
- Publication number
- JPS61122103A JPS61122103A JP59239396A JP23939684A JPS61122103A JP S61122103 A JPS61122103 A JP S61122103A JP 59239396 A JP59239396 A JP 59239396A JP 23939684 A JP23939684 A JP 23939684A JP S61122103 A JPS61122103 A JP S61122103A
- Authority
- JP
- Japan
- Prior art keywords
- hydrogen
- mixed gas
- pressure
- container
- alloy
- 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
Links
Landscapes
- Hydrogen, Water And Hydrids (AREA)
- Gas Separation By Absorption (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野1
本発明は、水素及びその他のガス(窒素、炭化水素、ア
ンモニア等)からなる低圧水素混合ガスから、水素貯蔵
合金を用いて水素を分離回収する方法に関する。Detailed Description of the Invention [Industrial Application Field 1] The present invention is a method for separating and recovering hydrogen from a low-pressure hydrogen mixed gas consisting of hydrogen and other gases (nitrogen, hydrocarbons, ammonia, etc.) using a hydrogen storage alloy. Regarding how to.
[従来の技術1
化学工業、電子工業等においては、多量の水素がスが使
用されている。特に半導体工場においては、シリコンの
雰囲気ガスとして多量の高純度ガスを使用している。そ
の各工程では水素がスを窒素等の不活性ガスで置換する
操作を行なうため、使用済みの水素は窒素等の不活性ガ
スと混合された状態で放出される。また、化学プラント
等においては副産物として水素ガスが発生する場合があ
り、これらは炭化水素、アンモニア等のガスとの混合物
として放出される。これら混合ガスの大部分は工場排気
として大気中へ放棄される。しかし水素ガスを大気中へ
放棄するということは、資源を無駄に消費して不経済で
あるとともに、水素濃度によっては爆発の危険性もある
。[Prior art 1] Large amounts of hydrogen gas are used in the chemical industry, electronic industry, etc. Particularly in semiconductor factories, a large amount of high-purity gas is used as an atmospheric gas for silicon. In each step, hydrogen is replaced with an inert gas such as nitrogen, so the used hydrogen is released in a state mixed with an inert gas such as nitrogen. Further, in chemical plants and the like, hydrogen gas may be generated as a byproduct, and these gases are released as a mixture with gases such as hydrocarbons and ammonia. Most of these mixed gases are discarded into the atmosphere as factory exhaust. However, releasing hydrogen gas into the atmosphere wastes resources and is uneconomical, and depending on the hydrogen concentration, there is a risk of explosion.
[発明が解決しようとする問題点]
水素を含む混合ガスから水素ガスを分離する方法として
は、従来上り膜分離法、圧力サイクル式吸着精製法、サ
イロジェニック法等があるが、これらの方法は工場排気
を処1!!rる大規模な設備として実施することは不適
切なものであり、経済的にも実際的でない、待に水素が
他の窒素ガス、その他のガスによr)s釈された混合水
素ガスの場合には、希釈ガスが水素の吸蔵を妨げるため
低圧では閤単に水素の回収が行なわれない。しかし、二
のような希釈された水素の混合ガスからの回収に対する
強い要望がある。[Problems to be Solved by the Invention] Conventional methods for separating hydrogen gas from a mixed gas containing hydrogen include upstream membrane separation method, pressure cycle adsorption purification method, and cyrogenic method. Treat factory exhaust 1! ! It is inappropriate and economically impractical to implement this as a large-scale facility. In some cases, hydrogen cannot be easily recovered at low pressures because the diluent gas prevents hydrogen storage. However, there is a strong desire to recover such dilute hydrogen from a gas mixture.
本発明は上記のような問題点を解決し、窒素、炭化水素
又はアンモニアと水素との混合ガスから低圧なysシは
中圧で水素を回収することを目的とする。The present invention aims to solve the above-mentioned problems and recover hydrogen from a mixed gas of nitrogen, hydrocarbon, or ammonia and hydrogen at low pressure or medium pressure.
[問題点を解決するための手段]
即ち本発明は、水素貯蔵合金が充JiEされた容器に水
素を含む低圧混合ガスを導入し、混合ガス中の水素を金
属水素化物として該水素貯蔵合金に吸蔵させた後、該容
器中の混合ガスを水素吸蔵平衡圧付近の圧力まで放出し
、その後再び新たな混合がスを該容器中に導入し、水素
の吸蔵、混合ガスの放出を繰り返すことを特徴とする低
圧水素混合ガスからの水素の回収方法である。[Means for Solving the Problems] That is, the present invention introduces a low-pressure mixed gas containing hydrogen into a container filled with a hydrogen storage alloy, and transfers the hydrogen in the mixed gas to the hydrogen storage alloy as a metal hydride. After occlusion, the mixed gas in the container is released to a pressure near the hydrogen storage equilibrium pressure, and then a new mixed gas is introduced into the container again, and hydrogen storage and mixed gas release are repeated. This is a method for recovering hydrogen from low-pressure hydrogen mixed gas.
[作 用1
、 水素貯蔵合金は水素を選択的に吸蔵する性質を持ち
、低温では水素を多量に吸蔵し、同時に熱を発生する。[Function 1: Hydrogen storage alloys have the property of selectively absorbing hydrogen, and at low temperatures they absorb a large amount of hydrogen and at the same time generate heat.
水素貯蔵合金を高温にした場合、水素を放出して熱を奪
つ。即ち、水素貯蔵合金は所定温度において混合ガス中
の水素分圧に対応した水素吸蔵平衡圧以上の圧力で水素
を吸蔵するので、水素圧力を水素U&蔵平衡圧以上とす
るか、又は水素貯蔵合金の平衡圧を回収すべき水素ガス
の圧力以下になるように水素貯蔵合金の温度を保持する
ことによりて、混合ガス中の水素を金属水素化物として
分離回収することができる。When a hydrogen storage alloy is heated to high temperatures, it releases hydrogen and takes away heat. In other words, since the hydrogen storage alloy stores hydrogen at a pressure higher than the hydrogen storage equilibrium pressure corresponding to the hydrogen partial pressure in the mixed gas at a given temperature, either the hydrogen pressure is set to be higher than the hydrogen storage equilibrium pressure, or the hydrogen storage alloy By maintaining the temperature of the hydrogen storage alloy so that the equilibrium pressure of the hydrogen gas is lower than the pressure of the hydrogen gas to be recovered, hydrogen in the mixed gas can be separated and recovered as a metal hydride.
本発明の実施には、まず水素貯蔵合金が充填された容器
内に水素を含む混合ガスを導入する。この時発熱反応に
より合金が所定の温度以上に上昇することもあり、この
場合にはその後の水素と合金の反応が抑制される。従っ
て、反応を促進させるために所定の温度以下に保持する
必要があり、場合によりでは水冷を行なう、水素は水素
貯蔵合金に1毀越されるが、窒素等の成分はガス状態の
まま及び水素貯蔵合金の吸y11分子(原子)としで存
在する。To carry out the present invention, first, a mixed gas containing hydrogen is introduced into a container filled with a hydrogen storage alloy. At this time, the alloy may rise to a predetermined temperature or higher due to an exothermic reaction, and in this case, the subsequent reaction between hydrogen and the alloy is suppressed. Therefore, in order to accelerate the reaction, it is necessary to maintain the temperature below a certain level, and in some cases, water cooling is performed.Hydrogen is transferred to the hydrogen storage alloy, but components such as nitrogen remain in a gaseous state, and hydrogen It exists as 11 molecules (atoms) of the storage alloy.
次いで、この水素濃度が低下した混合ガスを容器から放
出(パーツ)させる、その際、かなりの量の水素以外の
吸着分子(原子)が初期のうちに脱離して放出されるの
で、放出されるが人中の水素濃度は放出の時間とともに
次第に高くなっていく。Next, this mixed gas with reduced hydrogen concentration is released (parts) from the container.At this time, a considerable amount of adsorbed molecules (atoms) other than hydrogen are initially desorbed and released, so they are released. However, the hydrogen concentration in the human body gradually increases with the time of release.
パークは水素貯蔵合金の水素吸蔵平衡圧付近の圧力まで
行なう。Parking is performed to a pressure close to the hydrogen storage equilibrium pressure of the hydrogen storage alloy.
混合ガスを容器からパー7した後、再び新たな混合ガス
を上記容器に導入し、水素貯蔵合金に水素を吸蔵させる
。次いで水素濃度が低下した混合ガスを容器からパーツ
させる1以上の混合ガスの導入−パーク操作を繰り返す
ことにより、混合γ人中の水素を金属水素化物として回
収することができる。After paring the mixed gas from the container, a new mixed gas is introduced into the container again to cause the hydrogen storage alloy to store hydrogen. Next, by repeating the introduction-parking operation of one or more mixed gases in which the mixed gas with reduced hydrogen concentration is removed from the container, the hydrogen in the mixed γ gas can be recovered as a metal hydride.
原料混合ガス濃度が低い場合、水素貯蔵合金に水素が吸
蔵されることによ1)−1水素分圧が低くなるため、所
定の温度以下に水素貯蔵合金を保持しても水素と合金と
の反応速度が遅くなり、また合金表面に吸着する水素以
外の混合〃ス戒号が多くなり、水素と合金の反応が抑制
されるために閉じた容器にガスを導入するだけでは充号
な水素量atを得られない、しかし、上記操作を数回繰
り返すことによって、水素を回収することが可能である
。すなわち第2図に示すように、混合ガスの導入−パ−
7を繰り返すことにより1.水素量itが増大すること
がわかる。When the raw material mixed gas concentration is low, hydrogen is stored in the hydrogen storage alloy and the 1)-1 hydrogen partial pressure is lowered, so even if the hydrogen storage alloy is held below a predetermined temperature, the interaction between hydrogen and the alloy is low. The reaction rate slows down, and a large amount of mixed gas other than hydrogen adsorbs on the alloy surface, which inhibits the reaction between hydrogen and the alloy. However, by repeating the above operation several times, it is possible to recover hydrogen. That is, as shown in Fig. 2, the introduction of mixed gas
By repeating step 7, 1. It can be seen that the hydrogen amount it increases.
また、混合ガスを容器に導入する際、〃スパーノ用のガ
ス出口を開いておき、混合ガスの導入と水素量の減少し
た混合ガスの放出を同時に連続的に行なってもよい。Furthermore, when introducing the mixed gas into the container, the gas outlet for the Spano gas may be opened, and the introduction of the mixed gas and the discharge of the mixed gas with a reduced amount of hydrogen may be carried out simultaneously and continuously.
さらに、パーツした混合ガス中の水素濃度をさらに下げ
る場合は、水素吸蔵平衡圧の低い水素貯蔵合金を充填し
た容器に導入することにより、混合が人中の水素をほと
んど回収することが可能である。Furthermore, if the hydrogen concentration in the mixed gas is to be further reduced, it is possible to recover most of the hydrogen in the mixed gas by introducing it into a container filled with a hydrogen storage alloy that has a low hydrogen absorption equilibrium pressure. .
このようにして回収された水素を再利用する場合には、
容器内部の水素貯蔵合金を加熱することにより、水素を
放出させることができる。When reusing hydrogen recovered in this way,
Hydrogen can be released by heating the hydrogen storage alloy inside the container.
本発明においては、水素吸蔵平衡圧が数気圧のものであ
ればいずれの水素貯蔵合金も使用することができる。In the present invention, any hydrogen storage alloy having a hydrogen storage equilibrium pressure of several atmospheres can be used.
以下実施例に基づき本発明を説明する。The present invention will be explained below based on Examples.
[実施例]
第1図に示す小型の試験容器(SO3304製、試料室
容積的2.7 cc)に、水素貯蔵合金としてCa−N
1−M+*−AI系合金6gを充填し、水素濃度がそれ
ぞれ100%、90%、70%及び50%の水素と窒素
の混合ガスを用いて、水素ガスの吸a試験を行なった。[Example] In a small test container (made of SO3304, sample chamber volume: 2.7 cc) shown in Fig. 1, Ca-N was added as a hydrogen storage alloy.
A hydrogen gas absorption test was conducted using a mixed gas of hydrogen and nitrogen with hydrogen concentrations of 100%, 90%, 70%, and 50%, respectively, filled with 6 g of 1-M++-AI alloy.
すなわち、上記水素貯蔵合金を平衡圧が大気圧以下とな
る温度(20℃)に保ち、各組成の水素と窒素の混合ガ
スを試験容器に導入する0次いで試験容器中の水素濃度
の低下した混合がスを合金の水素吸蔵平衡圧付近の圧力
までパーツする0次に、再び新たな混合ガスを試験容器
に導入し、水素の@蔵、パーツの操作を繰り返した。That is, the above hydrogen storage alloy is maintained at a temperature (20°C) at which the equilibrium pressure is below atmospheric pressure, and a mixed gas of hydrogen and nitrogen of each composition is introduced into the test container.Then, the hydrogen concentration in the test container is reduced. Next, a new mixed gas was introduced into the test vessel again, and the hydrogen storage and parts operations were repeated.
FA2図に水素の吸蔵、パーツを繰り返した時の操り返
し回数と水素吸越量の変化を示r、図から、パーツを繰
り返すことにより水素吸蔵量が増加し、水素回収量の増
大を図ることが可能であることがわかる。Figure FA2 shows the changes in hydrogen storage, the number of repetitions when parts are repeated, and the amount of hydrogen absorbed.From the figure, it can be seen that by repeating parts, the amount of hydrogen storage increases, and the amount of hydrogen recovered can be increased. It turns out that it is possible.
アンモニアや炭化水素例えばメタン等と水素との混合ガ
スの場合も同様の結果が得られる。Similar results can be obtained with a mixed gas of hydrogen and ammonia or a hydrocarbon such as methane.
上記のような操作を行なうため、本発明方法を実施する
装置は、水素貯蔵合金が充填された容器内にがスの供給
及び排出をすることができ、また水素貯蔵合金を冷却又
は加熱することのでさる装置であればよく、容易に水素
の回収が行なうことができる。In order to carry out the above-mentioned operations, the apparatus for carrying out the method of the invention is capable of supplying and discharging gas into a container filled with a hydrogen storage alloy, and also capable of cooling or heating the hydrogen storage alloy. Therefore, any type of equipment is sufficient, and hydrogen can be easily recovered.
[発明の効果1
本発明によって、水素混合がスから低圧で水素を回収す
ることができる。また、回収した水素を有効に利用する
ことが可能である。[Effect 1 of the Invention According to the present invention, hydrogen can be recovered from a hydrogen mixing gas at low pressure. Furthermore, it is possible to effectively utilize the recovered hydrogen.
第1図は本発明の実施例で使用する試験容器の断面図、
第2図は実施例において混合ガスの導入−パーツを繰り
返した場合のパーツ回数と水素吸ル量の関係を示す図で
ある6図中、
A・・・本体、B、C・・・止め金具、D・・・上ぶた
、E・・・金属フィルター、F・・・試料室、G・・・
測温用熱電対、H・・・ステンレスパイプ、0・・・0
リング。FIG. 1 is a sectional view of a test container used in an example of the present invention;
Figure 2 is a diagram showing the relationship between the number of parts and the amount of hydrogen suction when introducing mixed gas and parts are repeated in an example. In Figure 6, A: main body, B, C: stopper metal fittings. , D... Upper lid, E... Metal filter, F... Sample chamber, G...
Temperature measuring thermocouple, H...stainless steel pipe, 0...0
ring.
Claims (2)
混合ガスを導入し、混合ガス中の水素を金属水素化物と
して該水素貯蔵合金に吸蔵させた後、該容器中の混合ガ
スを水素吸蔵平衡圧付近の圧力まで放出し、その後再び
新たな混合ガスを該容器中に導入し、水素の吸蔵、混合
ガスの放出を繰り返すことを特徴とする低圧水素混合ガ
スからの水素の回収方法。(1) A low-pressure mixed gas containing hydrogen is introduced into a container filled with a hydrogen storage alloy, and the hydrogen in the mixed gas is stored as a metal hydride in the hydrogen storage alloy. A method for recovering hydrogen from a low-pressure hydrogen mixed gas, characterized in that the pressure is released to a pressure near the storage equilibrium pressure, and then a new mixed gas is introduced into the container again, and hydrogen storage and mixed gas release are repeated.
に行なう特許請求の範囲第1項記載の低圧水素混合ガス
からの水素の回収方法。(2) A method for recovering hydrogen from a low-pressure hydrogen mixed gas according to claim 1, wherein the mixed gas is discharged continuously at the same time as the mixed gas is introduced.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59239396A JPS61122103A (en) | 1984-11-15 | 1984-11-15 | Recovery of hydrogen from low pressure mixed gas containing hydrogen |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59239396A JPS61122103A (en) | 1984-11-15 | 1984-11-15 | Recovery of hydrogen from low pressure mixed gas containing hydrogen |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61122103A true JPS61122103A (en) | 1986-06-10 |
| JPH049725B2 JPH049725B2 (en) | 1992-02-21 |
Family
ID=17044153
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59239396A Granted JPS61122103A (en) | 1984-11-15 | 1984-11-15 | Recovery of hydrogen from low pressure mixed gas containing hydrogen |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61122103A (en) |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS57209801A (en) * | 1981-06-15 | 1982-12-23 | Kyodo Sanso Kk | Preparation of hydrogen |
-
1984
- 1984-11-15 JP JP59239396A patent/JPS61122103A/en active Granted
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS57209801A (en) * | 1981-06-15 | 1982-12-23 | Kyodo Sanso Kk | Preparation of hydrogen |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH049725B2 (en) | 1992-02-21 |
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| Date | Code | Title | Description |
|---|---|---|---|
| EXPY | Cancellation because of completion of term |