JPH0614567B2 - Excited oxygen generator - Google Patents
Excited oxygen generatorInfo
- Publication number
- JPH0614567B2 JPH0614567B2 JP8072787A JP8072787A JPH0614567B2 JP H0614567 B2 JPH0614567 B2 JP H0614567B2 JP 8072787 A JP8072787 A JP 8072787A JP 8072787 A JP8072787 A JP 8072787A JP H0614567 B2 JPH0614567 B2 JP H0614567B2
- Authority
- JP
- Japan
- Prior art keywords
- solution
- oxygen generator
- hydrogen peroxide
- oxygen
- alkaline hydrogen
- 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 - Fee Related
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01S—DEVICES USING THE PROCESS OF LIGHT AMPLIFICATION BY STIMULATED EMISSION OF RADIATION [LASER] TO AMPLIFY OR GENERATE LIGHT; DEVICES USING STIMULATED EMISSION OF ELECTROMAGNETIC RADIATION IN WAVE RANGES OTHER THAN OPTICAL
- H01S3/00—Lasers, i.e. devices using stimulated emission of electromagnetic radiation in the infrared, visible or ultraviolet wave range
- H01S3/09—Processes or apparatus for excitation, e.g. pumping
- H01S3/095—Processes or apparatus for excitation, e.g. pumping using chemical or thermal pumping
Landscapes
- Physics & Mathematics (AREA)
- Electromagnetism (AREA)
- Lasers (AREA)
- Engineering & Computer Science (AREA)
- Plasma & Fusion (AREA)
- Optics & Photonics (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、アルカリ性過酸化水素水溶液と塩素ガスとの
化学反応により、励起酸素を効率よく発生させる装置に
関するものである。TECHNICAL FIELD The present invention relates to an apparatus for efficiently generating excited oxygen by a chemical reaction between an aqueous alkaline hydrogen peroxide solution and chlorine gas.
〔従来の技術〕 最近、化学励起ヨウ素レーザ(chemically pumpediodine
laser:CPIL)の研究がなされ、1.315μm波長の高出力
レーザ発振に成功している。このCPILはレーザ発振のた
めのポンピング源として電気エネルギを必要とせず、化
学燃料でレーザ発振でき比較的簡単な構造であるという
利点を有している。[Prior art] Recently, chemically pumped iodine laser
laser: CPIL) has been researched and succeeded in high power laser oscillation of 1.315 μm wavelength. This CPIL has an advantage that it does not require electric energy as a pumping source for laser oscillation and can relatively easily oscillate with a chemical fuel and has a relatively simple structure.
CPILの基本原理は次式によるエネルギ移乗反応である。The basic principle of CPIL is the energy transfer reaction according to the following equation.
O2 *(1Δ)+I(2P3/2)O2(3Σ)+I* 2P1/2) …(1) (1)式で左辺から右辺への反応が速いため、効率良くポ
ンピングが行われI*(2P1/2)が生成する。このI*(2P1/2)
がレーザ媒質となり、波長1.315μmのレーザ光を発生
する。ここで最も重要なことは、ポンピング源であるO2
*(1Δ)をいかに効率よく発生するかである。現在知られ
ている最も効率のよい方法は、次式で示す過酸化水素の
分解反応である。O 2 * ( 1 Δ) + I ( 2 P 3/2 ) O 2 ( 3 Σ) + I * 2 P 1/2 ) ... (1) Since the reaction from the left side to the right side is fast in equation (1), Pumping is performed efficiently and I * ( 2 P 1/2 ) is generated. This I * ( 2 P 1/2 )
Serves as a laser medium to generate laser light having a wavelength of 1.315 μm. The most important thing here is the pumping source O 2
* It is how efficiently ( 1 Δ) is generated. The most efficient method currently known is the decomposition reaction of hydrogen peroxide represented by the following formula.
H2O3+ 2NaOH+ Cl2→O2 *+2H2O+2NaCl …(2) 過酸化水素水溶液に水酸化ナトリウム溶液を加えアルカ
リ性にした上で、この混合溶液中に塩素ガスをバブリン
グすることによりO2 *(1Δ)は容易に発生する。このとき
(2)式の反応熱により、液温が上昇するため、効率のよ
いO2 *(1Δ)の生成を行うためには、反応溶液を冷却する
必要がある。H 2 O 3 + 2NaOH + Cl 2 → O 2 * + 2H 2 O + 2NaCl (2) Sodium hydroxide solution is added to the aqueous hydrogen peroxide solution to make it alkaline, and chlorine gas is bubbled into this mixed solution to produce O 2 * ( 1 Δ) easily occurs. At this time
Since the liquid temperature rises due to the reaction heat of the equation (2), it is necessary to cool the reaction solution in order to efficiently generate O 2 * ( 1 Δ).
従来、励起酸素を発生させる酸素発生器は、1.4Torr
前後の真空雰囲気、 -20℃前後の低温で運転されるの
で、酸素発生器自身をジャケット構造として冷却してい
た。Conventionally, the oxygen generator that generates excited oxygen is 1.4 Torr
Since it is operated in a vacuum atmosphere around and at a low temperature of around -20 ° C, the oxygen generator itself was cooled with a jacket structure.
したがって、従来の酸素発生器においては、伝熱面積が
不十分であり、きわめて冷却効率が悪いという不都合点
があった。Therefore, the conventional oxygen generator has a disadvantage that the heat transfer area is insufficient and the cooling efficiency is extremely poor.
本発明は上記の点に鑑みなされたもので、反応溶液を酸
素発生器の外部で冷却することにより、大量の励起酸素
を長時間にわたって発生させることができる励起酸素発
生装置の提供を目的とするものである。The present invention has been made in view of the above points, and an object thereof is to provide an excited oxygen generator capable of generating a large amount of excited oxygen over a long period of time by cooling the reaction solution outside the oxygen generator. It is a thing.
本発明の励起酸素発生装置は、図面を参照して説明すれ
ば、アルカリ性過酸化水素水溶液と塩素ガスとの化学反
応により励起酸素を発生させる酸素発生器1において、
この酸素発生器の溶液抜出管3を酸素発生器の上部に接
続して溶液循環ライン6を形成し、この溶液循環ライン
に新アルカリ性過酸化水素水溶液供給管11を接続する
とともに、溶液循環ラインに反応溶液を酸素発生器外部
で冷却するための冷却器8を設けたことを特徴としてい
る。Explained with reference to the drawings, the excited oxygen generator of the present invention is an oxygen generator 1 that generates excited oxygen by a chemical reaction between an aqueous alkaline hydrogen peroxide solution and chlorine gas.
The solution withdrawal pipe 3 of this oxygen generator is connected to the upper part of the oxygen generator to form a solution circulation line 6, and a new alkaline hydrogen peroxide aqueous solution supply pipe 11 is connected to this solution circulation line and the solution circulation line is also connected. Further, a cooling device 8 for cooling the reaction solution outside the oxygen generator is provided.
酸素発生器1内に供給されたアルカリ性過酸化水素水溶
液と塩素ガスとが接触して、前述の反応式(2)により励
起酸素が発生する。酸素発生器1から抜き出された反応
溶液は冷却器8で冷媒により所定の温度に冷却された
後、温度調整されて酸素発生器1へ循環される。The alkaline hydrogen peroxide solution supplied into the oxygen generator 1 and chlorine gas come into contact with each other, and excited oxygen is generated according to the above reaction formula (2). The reaction solution extracted from the oxygen generator 1 is cooled to a predetermined temperature by the refrigerant in the cooler 8, and then the temperature is adjusted and circulated to the oxygen generator 1.
以下、図面を参照して本発明の好適な実施例を詳細に説
明する。ただしこの実施例に記載されている構成機器の
形状、その相対配置などは、とくに特定的な記載がない
限りは、本発明の範囲をそれらのみに限定する趣旨のも
のではなく、単なる説明例にすぎない。Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the drawings. However, the shape of the constituent devices described in this embodiment, the relative arrangement thereof, and the like, unless otherwise specified, are not intended to limit the scope of the present invention only to them, and are merely illustrative examples. Only.
1は酸素発生器で、前述の反応式(2)を行わせるための
ものである。この酸素発生器1は、上部にアルカリ性過
酸化水素水溶液導入管2が、下部に溶液抜出管3が、液
相部に塩素ガス噴出管4(バブラー)が、気相部に励起
酸素取出口5が接続されている。Reference numeral 1 is an oxygen generator for carrying out the above reaction formula (2). This oxygen generator 1 has an alkaline hydrogen peroxide aqueous solution introduction pipe 2 in the upper part, a solution withdrawal pipe 3 in the lower part, a chlorine gas ejection pipe 4 (bubbler) in the liquid phase part, and an excited oxygen outlet in the gas phase part. 5 is connected.
溶液抜出管3の他端は酸素発生器1の上部のアルカリ性
過酸化水素水溶液導入管2に接続されて溶液循環ライン
6が形成されている。7は循環ポンプである。この溶液
循環ライン6に冷却器8を配設して、酸素発生器1を出
た反応溶液をフレオンなどの冷媒で冷却できるように構
成している。The other end of the solution withdrawal pipe 3 is connected to the alkaline hydrogen peroxide solution introducing pipe 2 above the oxygen generator 1 to form a solution circulation line 6. 7 is a circulation pump. A cooler 8 is arranged in the solution circulation line 6 so that the reaction solution discharged from the oxygen generator 1 can be cooled by a refrigerant such as Freon.
また溶液循環ライン6の酸素発生器入口に近い個所にク
ッションタンク10を設け、このタンク10に新アルカ
リ性過酸化水素水溶液供給管11を接続して、常に一定
濃度のアルカリ性過酸化水素水溶液が酸素発生器1に供
給できるようにしている。なおクッションタンク10は
必ずしも必要ではなく、新アルカリ性過酸化水素水溶液
供給管11を直接、溶液循環ライン6に接続することも
可能である。また新アルカリ性過酸化水素水溶液供給管
11の代りに、過酸化水素供給管、NaOH、KOH などのア
ルカリを供給するアルカリ供給管、水供給管を接続して
もよい。Further, a cushion tank 10 is provided at a position near the oxygen generator inlet of the solution circulation line 6, and a new alkaline hydrogen peroxide aqueous solution supply pipe 11 is connected to this tank 10 so that the alkaline hydrogen peroxide aqueous solution having a constant concentration always generates oxygen. It can be supplied to the vessel 1. The cushion tank 10 is not always necessary, and the fresh alkaline hydrogen peroxide solution supply pipe 11 can be directly connected to the solution circulation line 6. Further, instead of the new alkaline hydrogen peroxide solution supply pipe 11, a hydrogen peroxide supply pipe, an alkali supply pipe for supplying alkali such as NaOH and KOH, and a water supply pipe may be connected.
上記のように構成された励起酸素発生装置において、酸
素発生器1内に供給されたアルカリ性過酸化水素水溶液
と塩素ガスとが接触して、前述の反応式(2)により励起
酸素発生し、レーザ共振器(図示せず)へ送られる。酸
素発生器1から抜き出された反応溶液は冷却器8でフレ
オンなどの冷媒により-10〜 -30℃に冷却された後、新
アルカリ性過酸化水素水溶液を供給し濃度調整されて酸
素発生器1へ循環される。In the excited oxygen generator configured as described above, the alkaline hydrogen peroxide solution supplied into the oxygen generator 1 and chlorine gas come into contact with each other to generate excited oxygen according to the above-mentioned reaction formula (2), and the laser is generated. It is sent to a resonator (not shown). The reaction solution extracted from the oxygen generator 1 is cooled to −10 to −30 ° C. by a cooling medium such as Freon in the cooler 8, and then the concentration of the oxygen generator 1 is adjusted by supplying a new alkaline hydrogen peroxide aqueous solution. Is circulated to.
なお上記の実施例では、酸素発生器がバブリング型の場
合について説明したが、他の型式、たとえばアルカリ性
過酸化水素水溶液を霧化し、塩素ガスと接触させるよう
な構造などとすることも可能である。In the above embodiment, the case where the oxygen generator is a bubbling type has been described, but it is also possible to adopt another type, for example, a structure in which an alkaline hydrogen peroxide aqueous solution is atomized and brought into contact with chlorine gas. .
(発明の効果〕 本発明は上記のように、反応溶液を酸素発生器の外部で
冷却するように構成されているので、溶液抜出管をコイ
ル状などとして伝熱面積を十分にとることができ、この
ため反応溶液の冷却温度制御が容易となり、大量の励起
酸素を長時間にわたって発生させることができるという
優れた効果を有している。(Effects of the Invention) Since the present invention is configured to cool the reaction solution outside the oxygen generator as described above, it is possible to take a sufficient heat transfer area by forming the solution withdrawal pipe into a coil shape or the like. Therefore, the cooling temperature of the reaction solution can be easily controlled, and a large amount of excited oxygen can be generated for a long time, which is an excellent effect.
図面は本発明の励起酸素発生装置の一例を示す説明図で
ある。 1……酸素発生器、2……アルカリ性過酸化水素水溶液
導入管、3……溶液抜出管、4……塩素ガス噴出管、5
……励起酸素取出口、6……溶液循環ライン、7……循
環ポンプ、8……冷却器、10……クッションタンク、
11……新アルカリ性過酸化水素水溶液供給管The drawings are explanatory views showing an example of the excited oxygen generator of the present invention. 1 ... Oxygen generator, 2 ... Alkaline hydrogen peroxide aqueous solution introduction pipe, 3 ... Solution extraction pipe, 4 ... Chlorine gas ejection pipe, 5
...... Excited oxygen outlet, 6 …… Solution circulation line, 7 …… Circulation pump, 8 …… Cooler, 10 …… Cushion tank,
11 …… New alkaline hydrogen peroxide solution supply pipe
───────────────────────────────────────────────────── フロントページの続き (72)発明者 藤井 洋郎 兵庫県神戸市中央区東川崎町3丁目1番1 号 川崎重工業株式会社神戸工場内 (56)参考文献 米国特許4342116(US,A) 米国特許4653062(US,A) ─────────────────────────────────────────────────── ─── Continuation of front page (72) Hiroo Fujii Inventor Hiroo Fujii 3-1-1 Higashikawasaki-cho, Chuo-ku, Kobe-shi, Hyogo Kawasaki Heavy Industries Ltd. Kobe factory (56) Reference US Patent 4342116 (US, A) USA Patent 4653062 (US, A)
Claims (1)
の化学反応により励起酸素を発生させる酸素発生器にお
いて、この酸素発生器の溶液抜出管を酸素発生器の上部
に接続して溶液循環ラインを形成し、この溶液循環ライ
ンに新アルカリ性過酸化水素水溶液供給管を接続すると
ともに、溶液循環ラインに反応溶液を酸素発生器外部で
冷却するための冷却器を設けたことを特徴とする励起酸
素発生装置。1. An oxygen generator for generating excited oxygen by a chemical reaction between an aqueous alkaline hydrogen peroxide solution and chlorine gas, wherein a solution withdrawal pipe of the oxygen generator is connected to an upper part of the oxygen generator. And a new alkaline hydrogen peroxide aqueous solution supply pipe is connected to this solution circulation line, and a cooler for cooling the reaction solution outside the oxygen generator is provided in the solution circulation line. Generator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8072787A JPH0614567B2 (en) | 1987-03-31 | 1987-03-31 | Excited oxygen generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8072787A JPH0614567B2 (en) | 1987-03-31 | 1987-03-31 | Excited oxygen generator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63245980A JPS63245980A (en) | 1988-10-13 |
| JPH0614567B2 true JPH0614567B2 (en) | 1994-02-23 |
Family
ID=13726401
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8072787A Expired - Fee Related JPH0614567B2 (en) | 1987-03-31 | 1987-03-31 | Excited oxygen generator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0614567B2 (en) |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4342116A (en) | 1980-03-11 | 1982-07-27 | The Garrett Corporation | Dry excited singlet delta oxygen generator |
| US4653062A (en) | 1985-06-18 | 1987-03-24 | The United States Of America As Represented By The Secretary Of The Air Force | Chemical oxygen-iodine laser |
-
1987
- 1987-03-31 JP JP8072787A patent/JPH0614567B2/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4342116A (en) | 1980-03-11 | 1982-07-27 | The Garrett Corporation | Dry excited singlet delta oxygen generator |
| US4653062A (en) | 1985-06-18 | 1987-03-24 | The United States Of America As Represented By The Secretary Of The Air Force | Chemical oxygen-iodine laser |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63245980A (en) | 1988-10-13 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |