JPH032237B2 - - Google Patents
Info
- Publication number
- JPH032237B2 JPH032237B2 JP58080955A JP8095583A JPH032237B2 JP H032237 B2 JPH032237 B2 JP H032237B2 JP 58080955 A JP58080955 A JP 58080955A JP 8095583 A JP8095583 A JP 8095583A JP H032237 B2 JPH032237 B2 JP H032237B2
- Authority
- JP
- Japan
- Prior art keywords
- electrolysis
- hydrogen
- water
- supplied
- 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
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Landscapes
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Description
【発明の詳細な説明】
本発明は、電解により高純度水素を製造する方
法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing high purity hydrogen by electrolysis.
水素は、メタノール、アンモニア及び塩素等の
合成原料、燃料、IC用等の原料等に広く利用さ
れており、特に近年、IC用の高付加価値を求め
る特定分野への需要量が増大している。これに伴
い、それらに用いる水素は窒素、酸素、不飽和炭
化水素等の不純物、特に窒素含量の少ない高純度
なものが要求されている。 Hydrogen is widely used as a synthetic raw material such as methanol, ammonia, and chlorine, as fuel, and as a raw material for ICs, etc. In recent years, demand has increased particularly in specific fields that require high added value for ICs. . In line with this, the hydrogen used in these applications is required to be highly pure, with a low content of impurities such as nitrogen, oxygen, and unsaturated hydrocarbons, especially with a low nitrogen content.
水素の工業的な製造方法としては、水の電解に
よる方法やアルカリ金属塩化物の電解による方法
(副生水素)が一般的であるが、従来のそれらの
方法で得られる水素は不純物のガス濃度が高いた
め上記特定分野へ用いることが困難であつた。例
えばイオン交換膜電解槽を用いて、アルカリ金属
塩化物の電解により得られる水素は、窒素分が一
般に30〜40ppmであるため、IC用等高純度水素
ガスを必要とする場合は更に精製を必要とした。 Common industrial methods for producing hydrogen include water electrolysis and alkali metal chloride electrolysis (by-product hydrogen), but the hydrogen obtained by these conventional methods is limited by the gas concentration of impurities. It was difficult to use it in the above-mentioned specific field because of its high value. For example, hydrogen obtained by electrolysis of alkali metal chlorides using an ion exchange membrane electrolyzer generally has a nitrogen content of 30 to 40 ppm, so further purification is required if high purity hydrogen gas is required, such as for IC use. And so.
本発明者等は、電解により得られる水素中の不
純物ガス濃度は主に電解に供給する水中の溶解ガ
ス濃度に極めて関係することを知り、該供給水を
予め脱気して、該ガス溶解量を少なくすることに
より、上記問題が解決することを見出し、本発明
を提供するに至つた。 The present inventors found that the concentration of impurity gases in hydrogen obtained by electrolysis is extremely related to the concentration of dissolved gases in the water mainly supplied to the electrolysis. The inventors have discovered that the above-mentioned problem can be solved by reducing .
即ち、本発明は電解により水素を製造する方法
において、電解工程へ供給する水を、予め脱気す
ることを特徴とする高純度水素の製造方法であ
る。 That is, the present invention is a method for producing hydrogen by electrolysis, which is characterized in that water supplied to the electrolysis step is degassed in advance.
本発明における水素を製造するための電解方法
は、例えば、水の電解による方法、或いはイオン
交換膜法、水銀法によるアルカリ金属塩化物の電
解などに特に制限なく適用されるが、特にイオン
交換膜電解法に好適である。 The electrolysis method for producing hydrogen in the present invention can be applied without particular limitation to, for example, a method using water electrolysis, an ion exchange membrane method, or an alkali metal chloride electrolysis method using a mercury method. Suitable for electrolytic method.
即ち、イオン交換膜法によるアルカリ金属塩化
物の電解においては、イオン交換膜を隔膜とした
電解槽の陰極室に予め脱気した水を供給すること
によつて、苛性アルカリの生成と共に、高純度の
水素ガスを得ることが出来る。また、水電解にお
いては、電解槽に供給する電解液を予め脱気する
ことによつて、高純度の水素ガスを製造すること
が出来る。さらにまた、水銀法電解においては、
電解槽で生成したアマルガムを解汞槽において予
め脱気した水を供給することによつて反応させ、
苛性アルカリと共に高純度の水素を得ることが出
来る。したがつて、本発明において電解工程に供
給する水とは、上記したように水素を製造する電
解方法によつて異なるが、いずれも反応して水素
ガスを生成するために供給する水または水溶液を
意味する。 That is, in the electrolysis of alkali metal chlorides using the ion-exchange membrane method, by supplying previously degassed water to the cathode chamber of an electrolytic cell using an ion-exchange membrane as a diaphragm, caustic alkali is produced and high purity is produced. of hydrogen gas can be obtained. Furthermore, in water electrolysis, high purity hydrogen gas can be produced by degassing the electrolytic solution supplied to the electrolytic cell in advance. Furthermore, in mercury electrolysis,
The amalgam produced in the electrolytic tank is reacted by supplying previously degassed water in the demolition tank,
High purity hydrogen can be obtained together with caustic alkali. Therefore, in the present invention, the water supplied to the electrolytic process differs depending on the electrolytic method for producing hydrogen as described above, but in any case water or aqueous solution supplied to react to produce hydrogen gas is used. means.
本発明の脱気方法は、電解工程中へ供給する水
中の溶解ガス、特に窒素ガスを除去する方法であ
れば特に制限されるものでないが、一般に、水中
での溶解ガスはガスの分圧が高いほど、又、水温
が低いほど溶解度が大きいため、脱気方法として
は、前記と逆になるような操作を行えばよい。即
ち、脱気方法としては、減圧下で脱気する方法が
好ましく、特に減圧下で供給水をフラツシユさせ
る方法が好ましく用いられる。この際の圧力(真
空度)及び水温は、水の供給温度と減圧装置の能
力等の関係より適宜選定すればよいが、一般には
45〜60℃の温度で110mmHg前後の圧力が用いられ
る。脱気後の水中の溶解ガスは、特に窒素ガスに
ついては、ほぼゼロに近い値を示す。 The degassing method of the present invention is not particularly limited as long as it is a method for removing dissolved gas, especially nitrogen gas, from water supplied during the electrolysis process, but generally, dissolved gas in water has a gas partial pressure. Since the higher the water temperature and the lower the water temperature, the higher the solubility, the degassing method may be performed in the opposite manner to the above. That is, as a degassing method, a method of degassing under reduced pressure is preferable, and a method of flushing the supplied water under reduced pressure is particularly preferably used. The pressure (degree of vacuum) and water temperature at this time may be selected appropriately based on the relationship between the water supply temperature and the capacity of the pressure reducing device, but in general,
A pressure of around 110 mmHg at a temperature of 45-60°C is used. Dissolved gases in water after deaeration, especially nitrogen gas, show values close to zero.
本発明方法によつて得た水素ガスは、該水素中
の窒素をほとんどゼロ近くすることが出来るた
め、あらゆる用途にそのまま適用することが出来
る。 Since the hydrogen gas obtained by the method of the present invention can reduce the nitrogen content to almost zero, it can be used as is for any purpose.
尚、本発明方法は、一般に行なわれているよう
な脱酸方法など他のガスの除去法も併用すること
により、水素中の窒素以外の他のガスについても
より効果的に除去することが出来るため好まし
い。 In addition, the method of the present invention can more effectively remove gases other than nitrogen from hydrogen by also using other gas removal methods such as commonly used deoxidizing methods. Therefore, it is preferable.
以下、本発明を具体的に説明するために実施例
を示すが、本発明は、以下の実施例に特に限定さ
れるものでない。 EXAMPLES Hereinafter, examples will be shown to specifically explain the present invention, but the present invention is not particularly limited to the following examples.
実施例 1
イオン交換樹脂により、工学用水中の陽イオン
及び陰イオンを除去した、純水(温度25℃)を排
熱回収装置により50℃に昇温した。Example 1 Pure water (temperature 25°C) from which cations and anions in engineering water were removed using an ion exchange resin was heated to 50°C using an exhaust heat recovery device.
昇温後の純水を脱気塔に供給し、操作圧力80mm
Hgでフラツシユ蒸発させた。フラツシユ後の純
水温度は47℃であつた。 The purified water after heating is supplied to the degassing tower, and the operating pressure is 80 mm.
Flash evaporated with Hg. The pure water temperature after flashing was 47°C.
イオン交換膜法食塩電解槽の陰極室へフラツシ
ユ処理した純水を185/Hrの速度で供給し、陽
極室へは食塩水(NaCl濃度300g/)を1.7
m3/Hrの速度で供給した。通電電流100KAで電
解し、発生した水素ガスをガスクロマトグラフイ
ー(JIS K 0512の方法)にかけ分析した。水素
中の窒素は1ppm以下であつた。 Flash-treated pure water is supplied to the cathode chamber of the ion-exchange membrane salt electrolyzer at a rate of 185/Hr, and saline water (NaCl concentration 300 g/Hr) is supplied to the anode chamber at a rate of 1.7
It was fed at a rate of m 3 /Hr. Electrolysis was performed with a current of 100 KA, and the generated hydrogen gas was analyzed using gas chromatography (JIS K 0512 method). Nitrogen in hydrogen was less than 1 ppm.
実施例 1
排熱回収により昇温した純水をフラツシユ蒸発
させずに電解槽の陰極室へ供給した。その他の条
件は実施例1と同一にして電解した。発生水素ガ
スをガスクロマトグラフイーより分析した結果水
素中の窒素濃度は30ppmであつた。Example 1 Pure water whose temperature was raised by exhaust heat recovery was supplied to the cathode chamber of an electrolytic cell without flash evaporation. Other conditions were the same as in Example 1 for electrolysis. Analysis of the generated hydrogen gas by gas chromatography revealed that the nitrogen concentration in the hydrogen was 30 ppm.
Claims (1)
工程へ供給する水を、予め脱気することを特徴と
する高純度水素の製造方法。 2 アルカリ金属塩化物の電解により水素を製造
する特許請求の範囲第1項記載の製造方法。 3 イオン交換膜電解槽の陰極室へ供給する水で
ある特許請求の範囲第1項及び第2項記載の製造
方法。 4 減圧下でフラツシユさせ脱気する特許請求の
範囲第1項記載の製造方法。[Scope of Claims] 1. A method for producing high-purity hydrogen, characterized in that water supplied to an electrolysis step in a method for producing hydrogen by electrolysis is degassed in advance. 2. The manufacturing method according to claim 1, wherein hydrogen is produced by electrolysis of an alkali metal chloride. 3. The manufacturing method according to claims 1 and 2, wherein the water is supplied to the cathode chamber of an ion exchange membrane electrolytic cell. 4. The manufacturing method according to claim 1, which comprises flashing and degassing under reduced pressure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58080955A JPS59208085A (en) | 1983-05-11 | 1983-05-11 | Production of high purity hydrogen |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58080955A JPS59208085A (en) | 1983-05-11 | 1983-05-11 | Production of high purity hydrogen |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59208085A JPS59208085A (en) | 1984-11-26 |
| JPH032237B2 true JPH032237B2 (en) | 1991-01-14 |
Family
ID=13732926
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58080955A Granted JPS59208085A (en) | 1983-05-11 | 1983-05-11 | Production of high purity hydrogen |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59208085A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110965069B (en) * | 2019-12-25 | 2022-07-12 | 乔治洛德方法研究和开发液化空气有限公司 | Apparatus and method for producing high-purity hydrogen and/or oxygen by electrolyzing water |
-
1983
- 1983-05-11 JP JP58080955A patent/JPS59208085A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59208085A (en) | 1984-11-26 |
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