JPS5841701A - Thermochemical decomposition of water by magnesium- iodine system cycle - Google Patents
Thermochemical decomposition of water by magnesium- iodine system cycleInfo
- Publication number
- JPS5841701A JPS5841701A JP56140696A JP14069681A JPS5841701A JP S5841701 A JPS5841701 A JP S5841701A JP 56140696 A JP56140696 A JP 56140696A JP 14069681 A JP14069681 A JP 14069681A JP S5841701 A JPS5841701 A JP S5841701A
- Authority
- JP
- Japan
- Prior art keywords
- magnesium
- water
- aqueous solution
- iodine
- mgi2
- 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
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
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
- Treating Waste Gases (AREA)
Abstract
Description
【発明の詳細な説明】
杢発明は、既に報告され九−化マグネシウムとヨウ素と
を用いる水の熱化学分解法(公開特許公報昭53−60
393)につき、新規な操作方法を提供するものである
。この方法におけるサイクルは次の4段反応によって構
成される。[Detailed Description of the Invention] The present invention is based on a method for thermochemical decomposition of water using magnesium nonaride and iodine (Public Patent Publication No. 53-60), which has already been reported.
393), it provides a new operating method. The cycle in this method consists of the following four-stage reactions.
+Mg (■0.>、・・・、(1)
Mll (IO2)2−乙00”(と−)MgO+I、
+2.sO,−・(2)5MpI、+5H,O−u回り
5M、1ilO+10HI 、、−(3)300〜70
0℃
10HI□5H,+5I、、−−−(4)6 幌フ1、
このサイクル−は操作面からすると、反応(l)によっ
て生成した混合物からM I (I Os)沈殿物をr
別し、得られるM9I2溶液(過剰ヨウ素含有)を濃縮
後、MpI2の加水分解反応である反応(3)によって
HIガスを発生させる。この濃縮工程は、過剰の水分と
ヨウ素を分離するものであるが、加熱蒸発を行なって、
H20/JI I 2モル比が約6の段階に達すると、
以後脱水と反応(3)の加水分解反応が併発する。この
ため、単なる濃縮では脱水率に自ら限界があり、従って
MpI2゜6H20→JIO+2HI+5H20の反応
からも知られるように、M9 I 、の加水分解反応に
よって発生するガスの最終的な組成はH工1モル当り少
なくとも2.5モルの水分を共存させることになる。+Mg (■0.>,..., (1) Mll (IO2)2-Otsu00" (and-) MgO+I,
+2. sO, -・(2) 5MpI, +5H, 5M around O-u, 1ilO+10HI,, -(3) 300~70
0°C 10HI□5H, +5I, ---(4)6 Canopy 1,
From an operational point of view, this cycle converts the M I (IOs) precipitate from the mixture produced by reaction (l) into
After separating and concentrating the resulting M9I2 solution (containing excess iodine), HI gas is generated by reaction (3), which is a hydrolysis reaction of MpI2. This concentration process is to separate excess water and iodine, but by heating and evaporating it,
When the H20/JI I 2 molar ratio reaches a stage of about 6,
Thereafter, dehydration and the hydrolysis reaction of reaction (3) occur simultaneously. For this reason, there is a limit to the dehydration rate with simple concentration, and therefore, as is known from the reaction MpI2゜6H20→JIO+2HI+5H20, the final composition of the gas generated by the hydrolysis reaction of MpI is 1 mol of H At least 2.5 mol of water per mol of water is allowed to coexist.
本発明は、このような限界を克服して、高濃度のHIガ
スを発生させ、一方、この濃縮工程で発生する過剰の水
分とヨウ素め蒸気の熱楡を有効に回収することを目的と
する。The purpose of the present invention is to overcome these limitations and generate highly concentrated HI gas, while effectively recovering the excess water and iodine vapor generated in this concentration process. .
際発生する水蒸気とヨウ素ガスとを、分割された他方の
JII、溶液に吸収させて蒸気熱量を回収し、かくして
稀薄となったMpI、溶液は反応(1)の装置に戻すも
のとし、一方同相として生成した3Mf?(OH)、・
MpI、からは、高温熱分解によりygoとH,O/H
Iモル比1/1のガスを発生させる。The water vapor and iodine gas generated during the reaction are absorbed into the other divided JII solution and the steam heat is recovered, and the thus diluted MpI solution is returned to the apparatus for reaction (1). 3Mf generated as? (OH),・
From MpI, ygo and H, O/H are produced by high temperature pyrolysis.
A gas with a molar ratio of 1/1 is generated.
以下、本発明の詳細な説明する。The present invention will be explained in detail below.
MpI、溶液にJIO/M9I、モル比3の割合で酸化
マグネシウムを添加した混合物を加熱蒸発すると、過剰
の水分等は蒸発して、固形分として3M9 (OH)、
・M、9Ilの生成を認めた。この物質は300℃以下
では安定で、さらに高温度に加熱すると、水蒸気及びヨ
ウ化水素を゛発生しながら分解し、350℃以上で分解
を終了し、固形分として酸化マグネシウムを残す。即ち
、この熱分解により、HI/H20モル比の濃厚なヨウ
”化水素ガスを回収することができ、以後の反応(4)
によって水素を製造するi、取扱い、芦ス容積を減少し
て操作を有利にするばかりでなく、究極的にはモル当り
の水素製造の熱効率を向上させる。When a mixture of MpI, JIO/M9I, and magnesium oxide added at a molar ratio of 3 is heated and evaporated, excess moisture is evaporated and solid content is 3M9 (OH).
- Generation of M, 9Il was observed. This substance is stable at temperatures below 300°C, and when heated to even higher temperatures, it decomposes while producing water vapor and hydrogen iodide, and the decomposition ends at temperatures above 350°C, leaving magnesium oxide as a solid content. That is, by this thermal decomposition, concentrated hydrogen iodide gas with a HI/H molar ratio of 20 can be recovered, which can be used in the subsequent reaction (4).
The process of producing hydrogen by reducing the handling and volume not only improves the operation, but also ultimately improves the thermal efficiency of hydrogen production per mole.
ヨウ化マグネシウム水溶液は、塩類水溶液のうちで、最
も高い沸点を示す部類に属する。一般に塩類水溶液は水
の沸点(100℃)に比べて沸点上昇分だけ高温で、常
圧の水蒸気を凝縮させる能力をもつが、ヨウ化マグネシ
ウムの沸点上昇効果は特に優れている。従ってこの属性
を利用すると、該溶液に吸収させることにより水蒸気の
凝縮潜熱分を、より高温で回収することができる。さら
に、該溶液は、ヨウ素蒸気もよく吸収する性質をもつ。Magnesium iodide aqueous solution belongs to the category showing the highest boiling point among salt aqueous solutions. In general, an aqueous salt solution has the ability to condense water vapor at normal pressure at a higher temperature than the boiling point of water (100° C.) by the amount that increases the boiling point, but magnesium iodide has a particularly excellent boiling point increasing effect. Therefore, by utilizing this attribute, the latent heat of condensation of water vapor can be recovered at a higher temperature by absorbing it into the solution. Furthermore, the solution has the property of absorbing iodine vapor well.
このことから、前記3’JI (OH)、・JI I
2の生成時に発生する過剰な水蒸気およびヨウ素の蒸気
は、例えば、シェルアンド九−プ型熱交換装置を例えば
水の加熱に用いることが出来る。従って、該媒体が水で
あるなら高温ム圧の水蒸気の発生に利用できる。なお、
水蒸気およびヨウ素蒸気の枦収(よって稀薄となったヨ
ウ化マグネシウム水溶液は、反応(1)の装置に涙し、
反応(1>により濃厚液に再生できる。From this, the above 3'JI (OH), ・JI I
Excess water vapor and iodine vapor generated during the production of 2 can be used, for example, in a shell-and-keep heat exchanger to heat water, for example. Therefore, if the medium is water, it can be used to generate steam at high temperature and pressure. In addition,
Collection of water vapor and iodine vapor (thus, the diluted magnesium iodide aqueous solution is poured into the apparatus for reaction (1),
It can be regenerated into a concentrated liquid by reaction (1).
以下実施例により本発明を説明する。The present invention will be explained below with reference to Examples.
実施例1゜
ヨウ化マグネシウム水溶液(濃度55チ、モル組成、M
pI、・12,5H,O)に対し、M、90/JII2
210℃の温度域で脱水の停滞があり、210℃より再
び活発に脱水し、280℃で固相としてマグネシウムヒ
ドロキシヨウ化物を生成した。脱水量による計算及びX
線分析から3Mg (OH)g−Mugと一定した。一
方、上記スラリーに’ v’Ml/ T !−F−ル比
6になるようにヨウ素を添加し九試料では、類似の熱減
量曲線を画き、約200℃までにヨウ素はほぼ全量蒸発
し、約280℃で同じ<3Mg(OH)、・M、9I、
の組成物を生成した。Example 1 Magnesium iodide aqueous solution (concentration 55%, molar composition, M
pI, ・12,5H,O), M, 90/JII2
There was a stagnation of dehydration in the temperature range of 210°C, and active dehydration occurred again from 210°C, and magnesium hydroxyiodide was produced as a solid phase at 280°C. Calculation based on dehydration amount and X
From line analysis, it was determined to be 3Mg (OH)g-Mug. On the other hand, the above slurry contains 'v'Ml/T! The nine samples in which iodine was added at a -F-le ratio of 6 showed similar thermal loss curves, with almost all of the iodine evaporated by about 200°C, and the same <3 Mg(OH) at about 280°C. M,9I,
produced a composition of
この塩基性ヨウ化物は、常圧のアルゴンW囲気中、約3
20℃から分解を開始し、380℃で終了して固形分と
して酸化マグネシウムのみを残した。This basic iodide is dissolved in an argon W atmosphere at normal pressure at about 3
Decomposition started at 20°C and ended at 380°C, leaving only magnesium oxide as a solid content.
実施例2゜
ヨウ化マグネシウム水溶液、およびこれにヨウ素を溶解
した溶液の蒸気圧を硬質ガラス製ブルドン管を用いて測
定した。濃度50.7及び60.7%ヨウ化マグネシウ
ム溶液の沸点(1気圧)は夫々115℃及び136.5
℃であった。一方60.71溶液に12/Mg■2モル
比4のヨウ素を添加すると、沸点、134℃を示した。Example 2 The vapor pressure of an aqueous magnesium iodide solution and a solution in which iodine was dissolved was measured using a hard glass Bourdon tube. The boiling points (1 atm) of magnesium iodide solutions with concentrations of 50.7% and 60.7% are 115°C and 136.5°C, respectively.
It was ℃. On the other hand, when iodine in a 12/Mg2 molar ratio of 4 was added to the 60.71 solution, the boiling point was 134°C.
Claims (1)
水・ど過剰ヨウ素の存在下、酸化マグネシウムとヨウ素
の反応(第1段反応)で生成し、かつヨウ素酸マグネシ
ウムを炉別して得られるヨウ化マグネシウム水溶譚を2
分割し、一方ニハ、ヨウ化マグネシウム1モル当93モ
ルの酸化マグネシウムを添加し、得られる混合物を加熱
蒸発してマグネシウムヒドロキシヨウ化物(3M、?
(o)i)、・Ml、)を生成させ、この際発生する水
蒸気とヨウ素蒸気を、分割された他方のヨウ化マグネシ
ウム水溶液に吸収させて蒸気熱量を回収し、かくして稀
釈されたヨウ化マグネシウム水溶液は再び第1段反応用
として戻すものとし、また該マグネシウムヒドロキシヨ
ウ化物は加熱によりヨウ化水素、水蒸気および酸化マグ
ネシウムに分解させるこ・とを特徴とするマグネシウム
−ヨウ素系サイクルによる水の熱化学分解法。(1) In the magnesium iodine cycle,
An aqueous solution of magnesium iodide, which is produced by the reaction of magnesium oxide and iodine (first stage reaction) in the presence of excess iodine in water and water, and which is obtained by separating magnesium iodate in a furnace, is
93 moles of magnesium oxide per mole of magnesium iodide were added, and the resulting mixture was heated and evaporated to produce magnesium hydroxyiodide (3M, ?).
(o) i), ・Ml, ) is produced, and the water vapor and iodine vapor generated at this time are absorbed into the other divided magnesium iodide aqueous solution to recover the vapor heat, and thus the diluted magnesium iodide The aqueous solution is returned for the first stage reaction, and the magnesium hydroxyiodide is decomposed into hydrogen iodide, water vapor and magnesium oxide by heating. Water thermochemistry using a magnesium-iodine cycle. Decomposition method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56140696A JPS5841701A (en) | 1981-09-07 | 1981-09-07 | Thermochemical decomposition of water by magnesium- iodine system cycle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56140696A JPS5841701A (en) | 1981-09-07 | 1981-09-07 | Thermochemical decomposition of water by magnesium- iodine system cycle |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5841701A true JPS5841701A (en) | 1983-03-11 |
| JPS6116721B2 JPS6116721B2 (en) | 1986-05-01 |
Family
ID=15274612
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56140696A Granted JPS5841701A (en) | 1981-09-07 | 1981-09-07 | Thermochemical decomposition of water by magnesium- iodine system cycle |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5841701A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6372017B1 (en) * | 2000-02-07 | 2002-04-16 | Orville Lee Maddan | Method for producing magnesium |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6355220U (en) * | 1986-09-26 | 1988-04-13 |
-
1981
- 1981-09-07 JP JP56140696A patent/JPS5841701A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6372017B1 (en) * | 2000-02-07 | 2002-04-16 | Orville Lee Maddan | Method for producing magnesium |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6116721B2 (en) | 1986-05-01 |
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