JPH04292402A - Air-conditioning system apparatus - Google Patents
Air-conditioning system apparatusInfo
- Publication number
- JPH04292402A JPH04292402A JP24634789A JP24634789A JPH04292402A JP H04292402 A JPH04292402 A JP H04292402A JP 24634789 A JP24634789 A JP 24634789A JP 24634789 A JP24634789 A JP 24634789A JP H04292402 A JPH04292402 A JP H04292402A
- Authority
- JP
- Japan
- Prior art keywords
- aqueous solution
- oxygen
- quicklime
- hydrogen
- pipe
- 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.)
- Pending
Links
- 238000004378 air conditioning Methods 0.000 title description 6
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims abstract description 46
- 239000007864 aqueous solution Substances 0.000 claims abstract description 33
- 239000000292 calcium oxide Substances 0.000 claims abstract description 23
- 235000012255 calcium oxide Nutrition 0.000 claims abstract description 23
- 238000006243 chemical reaction Methods 0.000 claims abstract description 13
- 229910052802 copper Inorganic materials 0.000 claims abstract description 13
- 239000010949 copper Substances 0.000 claims abstract description 13
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000000243 solution Substances 0.000 claims abstract description 6
- 238000001816 cooling Methods 0.000 claims abstract description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 48
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 28
- 239000001301 oxygen Substances 0.000 claims description 28
- 229910052760 oxygen Inorganic materials 0.000 claims description 28
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 24
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 claims description 20
- 239000007789 gas Substances 0.000 claims description 18
- 239000001569 carbon dioxide Substances 0.000 claims description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- 239000001103 potassium chloride Substances 0.000 claims description 10
- 235000011164 potassium chloride Nutrition 0.000 claims description 10
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 8
- 239000001257 hydrogen Substances 0.000 claims description 8
- 229910052739 hydrogen Inorganic materials 0.000 claims description 8
- 238000005868 electrolysis reaction Methods 0.000 claims description 4
- 239000000498 cooling water Substances 0.000 claims description 3
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims 1
- 238000007664 blowing Methods 0.000 claims 1
- 229910052799 carbon Inorganic materials 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 claims 1
- 230000008016 vaporization Effects 0.000 claims 1
- 238000009834 vaporization Methods 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 230000008929 regeneration Effects 0.000 abstract description 3
- 238000011069 regeneration method Methods 0.000 abstract description 3
- 238000005422 blasting Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 4
- 238000003860 storage Methods 0.000 description 4
- 238000009776 industrial production Methods 0.000 description 3
- 210000004072 lung Anatomy 0.000 description 3
- 230000029058 respiratory gaseous exchange Effects 0.000 description 3
- 150000001879 copper Chemical class 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000010792 warming Methods 0.000 description 2
- 241000282412 Homo Species 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 230000001364 causal effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical compound [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 description 1
- 239000012212 insulator Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- 230000005658 nuclear physics Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 235000019640 taste Nutrition 0.000 description 1
Landscapes
- Oxygen, Ozone, And Oxides In General (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
Description
【発明の詳細な説明】
(イ)産業上の利用分野
この発明は大気中における炭酸ガスを取り除き、地球の
温暖化の要因とされている炭酸ガスの濃度を下げること
とし、あわせて高温水蒸気のもとにイオン化された基体
を電気分解によって新らたに酸素分子O2を生成するこ
ととした空調システム装置に関する。[Detailed description of the invention] (a) Industrial application field This invention removes carbon dioxide from the atmosphere and lowers the concentration of carbon dioxide, which is considered to be a cause of global warming, and also removes high-temperature water vapor. The present invention relates to an air conditioning system device in which oxygen molecules O2 are newly generated by electrolysis of an originally ionized substrate.
(ロ)従来の技術
炭酸ガスCO2を除去する為には、高価な設備を必要と
し工業生産現場ではシステム化もできているが、ビル内
の事務所向きのシステム装置になると高価で負担が大き
かった。(b) Conventional technology In order to remove carbon dioxide gas CO2, expensive equipment is required, and although it is possible to systemize it at industrial production sites, it is expensive and burdensome to use system equipment for offices in buildings. Ta.
(ハ)発明が解決しようとする問題点
しかし、このようなエネルギーの変換のプロセスの中で
生成される炭酸ガスCO2は、工業生産的には一定の設
備を有することによって解決もされていたのだか、地球
温暖化現象のように生体維持における炭酸ガスCO2の
因果関係を指摘されると、各地域ごとの空間の単位量で
炭酸ガスCO2を除去してゆくしかない。加えて地球的
規模で緑の面積が減少し、炭酸ガス濃度を押し上げてい
るようになると、原子物理学的方法や化学における反応
方式によって、酸素の生成や炭酸ガスを再生してゆくし
かないことになる。(c) Problems to be solved by the invention However, the carbon dioxide gas CO2 produced in this energy conversion process has been solved by having certain equipment in industrial production. However, when it is pointed out that there is a causal relationship between carbon dioxide gas CO2 and the maintenance of living organisms, such as the phenomenon of global warming, we have no choice but to remove carbon dioxide gas CO2 by the unit amount of space in each region. In addition, as the amount of greenery decreases on a global scale, pushing up the concentration of carbon dioxide gas, we have no choice but to generate oxygen and regenerate carbon dioxide gas using nuclear physics methods and chemical reaction methods. become.
この発明は工業生産的規模というより、各居住地域の空
間単位量で炭酸ガスCO2を除去し、生体のエネルギー
変換の現象である酸素による酸化の問題を、化学的方式
で低価で容易に造り出しうる実用的な酸素生成機構で、
生体にとって必要な酸素の再生と生成を得ることを目的
としている。This invention removes carbon dioxide gas CO2 on a spatial unit basis in each residential area rather than on an industrial production scale, and easily solves the problem of oxidation caused by oxygen, which is a phenomenon of energy conversion in living organisms, at a low cost using a chemical method. With a practical oxygen generation mechanism,
The purpose is to obtain the regeneration and production of oxygen necessary for living organisms.
(ニ)問題を解決するための手段
この発明を図面に基づいて説明すると、第1図において
、酸素生成システムボックス23の内部の下部に塩化カ
リウム等の水溶液の入った反応槽1を設け、又槽の中に
はヒーターの電極2を設置し加熱している。反応槽と塩
化カリウム水溶液のタンク22はパイプ24によって連
結されている。反応槽の上部には格子状形電極3と、こ
の電極に反転層の形で電極4があり、生成された酸素分
子O2と水素分子H2の混合気体の通路5があり、塩化
カリウム水溶液の横転による流出を止めるストッパー6
がある。この気体通路は冷却部の下部に導かれ分子化さ
れた気体は、銅製パイプ9の内径を経て上昇する。又こ
の銅製パイプ9は上部に貯水槽10が設置されているの
で、パイプ9と貯水槽に造られたギャップ穴25によっ
て、この穴の隙間から生石灰の水溶液18を適量づつ、
パイプ9を軸に下方の生石灰の水溶液の槽に落下させる
。このようにして造られた多数の銅製パイプに対して直
角にモーター13を介したファン12によって送風する
と、風は送風口19から銅製パイプを経て送排風口20
に至る。生石灰の水溶液の上部はセンサー26によって
検知され、下部の生石灰の水溶液は送水管17を経てポ
ンプ16によって送水管11を通って汲みあげられる。(d) Means for solving the problem The present invention will be explained based on the drawings. In FIG. A heater electrode 2 is installed in the tank to heat it. The reaction tank and the potassium chloride aqueous solution tank 22 are connected by a pipe 24. At the top of the reaction tank, there is a lattice-shaped electrode 3 and an electrode 4 in the form of an inversion layer on this electrode, and there is a passage 5 for a mixed gas of generated oxygen molecules O2 and hydrogen molecules H2, and the potassium chloride aqueous solution is turned over. Stopper 6 to stop leakage due to
There is. This gas passage is led to the lower part of the cooling section, and the molecularized gas rises through the inner diameter of the copper pipe 9. Also, since this copper pipe 9 has a water storage tank 10 installed at the top, an appropriate amount of quicklime aqueous solution 18 is poured through the gap between the holes 25 made in the pipe 9 and the water tank.
It is dropped into a tank containing an aqueous solution of quicklime using the pipe 9 as its axis. When the fan 12 via the motor 13 blows air at right angles to the large number of copper pipes thus constructed, the air flows from the air outlet 19 through the copper pipes to the air outlet 20.
leading to. The upper part of the quicklime aqueous solution is detected by the sensor 26, and the lower part of the quicklime aqueous solution is pumped up through the water pipe 11 by the pump 16 via the water pipe 17.
又横転による塩化カリウム水溶液と生石灰水溶液の混合
を防止する為に、耐需センサー27を介してゲート7、
8によって遮断している。In addition, in order to prevent mixing of potassium chloride aqueous solution and quicklime aqueous solution due to rollover, gate 7,
It is blocked by 8.
(ホ)作用
上記のように構成された空調システム装置の反応槽に、
塩化カリウム等の水溶液にヒーターを介して熱を加えて
やると、酸素O2の分子結合の割合が多くなり、水素原
子のH+イオン化が効率良くなる。触媒に適量のマンガ
ンMnOを入れると酸素の生成量は多くなる。酸素O2
と水素イオンの気体を電極を介して電気分解してやると
、酸素分子O2と水素分子H2になる。(e) Action In the reaction tank of the air conditioning system configured as above,
When heat is applied to an aqueous solution of potassium chloride or the like via a heater, the proportion of molecular bonds of oxygen O2 increases, and H+ ionization of hydrogen atoms becomes more efficient. When an appropriate amount of manganese MnO is added to the catalyst, the amount of oxygen produced increases. oxygen O2
When the hydrogen ion gas is electrolyzed through an electrode, it becomes oxygen molecules O2 and hydrogen molecules H2.
この高温で不安定な気体を銅製パイプの内径を通過させ
ることによって、高温気体は冷却されて冷たい酸素分子
O2と水素分子H2になる。By passing this hot and unstable gas through the inner diameter of the copper pipe, the hot gas is cooled into cold oxygen molecules O2 and hydrogen molecules H2.
冷たい酸素の方が人間にとっておいしく感じるのは、酸
素O2の分子運動量が小さい為に呼吸に容易であること
、高温の酸素分子は冷たいO2より分子が膨らんで肺呼
吸に適さない為である。又この銅製パイプの外周に生石
灰の水溶液を冷却水として使用することによって、ファ
ンから送風される大気の中に含む炭酸ガスCO2が冷却
水の生石灰の水溶液と反応して酸素が再生される。The reason why cold oxygen tastes better to humans is because the molecular momentum of oxygen O2 is small, making it easier to breathe, and because hot oxygen molecules expand more than cold O2, making them unsuitable for lung breathing. Furthermore, by using an aqueous solution of quicklime as cooling water around the outer periphery of this copper pipe, carbon dioxide gas CO2 contained in the atmosphere blown by the fan reacts with the aqueous solution of quicklime in the cooling water, and oxygen is regenerated.
以上の理由から酸素O2の温度は低い方が人間の肺呼吸
にとっては有効であり、上記のように構成されたシステ
ムは酸素の再生と生成に実用的に作用する。For the above reasons, a lower temperature of oxygen O2 is more effective for human lung respiration, and the system configured as described above works practically for the regeneration and production of oxygen.
(ヘ)実施例
第3図は金網型電極の実施態様を示し、電極3、4であ
り4は反転極性電極を構成し、金網型3に絶縁子30を
はさんでボルト28を通してナット29で固定し、間欠
的に電気的に接続してプラス極とマイナス極にしている
。第4図はゲート機構の実施態様を示し、ゲート7に対
してゲート受け8であり、スプリング31によって水路
の遮断をし、弾性体32によって水漏れを防ぐ。第5図
は貯水槽に銅製パイプをセットした場合の実施態様を示
すものであり、生石灰水溶液の貯水槽10と銅製パイプ
を軸にして落下する生石灰の水溶液にファン12からの
大気を吹きつけると、生石灰水溶液は反応して白く濁り
、炭酸ガスの酸素が再生されてくる。第6図は耐震セン
サー27を取付けた場合の実施態様を示し、横転の場合
による溶液の漏れと、塩化カリウムと生石灰の水溶液の
混合を防ぐものである。(F) Embodiment FIG. 3 shows an embodiment of a wire mesh type electrode, in which electrodes 3 and 4 constitute an inverted polarity electrode, an insulator 30 is sandwiched between the wire mesh type 3, a bolt 28 is passed through a nut 29, and a wire mesh type electrode is used. It is fixed and electrically connected intermittently to create positive and negative terminals. FIG. 4 shows an embodiment of the gate mechanism, in which a gate receiver 8 is provided for the gate 7, a spring 31 blocks a waterway, and an elastic body 32 prevents water leakage. FIG. 5 shows an embodiment in which a copper pipe is set in a water storage tank, and air from a fan 12 is blown onto the water storage tank 10 containing a quicklime aqueous solution and the quicklime aqueous solution falling around the copper pipe as an axis. The quicklime aqueous solution reacts and becomes cloudy white, and oxygen from carbon dioxide gas is regenerated. FIG. 6 shows an embodiment in which a seismic sensor 27 is installed, which prevents leakage of the solution in the event of a rollover and mixing of the aqueous solution of potassium chloride and quicklime.
(ト)発明の効果
この発明は以上説明したように、塩化カリウム等の水溶
液にヒーターを直入したものであり、酸素O2の生成を
容易にしている。低温の酸素O2は安定性があるので、
人間の肺呼吸には効率が良くなる。生石灰の水溶液の表
面積が大きくなっているので炭酸ガス濃度の上昇を低減
し、簡単な構造で再生するという効果がある。(G) Effects of the Invention As explained above, in this invention, a heater is placed directly into an aqueous solution of potassium chloride or the like, thereby facilitating the production of oxygen O2. Since low temperature oxygen O2 is stable,
Human lung breathing becomes more efficient. Since the surface area of the quicklime aqueous solution is large, it has the effect of reducing the increase in carbon dioxide concentration and regenerating with a simple structure.
又、水H2Oに対して水タンク22にメジャー33によ
って塩化カリウムを適切な濃度に作り、生石灰水溶液も
水溶液タンク21に入れることによってジョイント14
と水溶液通路15によって、溶液の落差によって補給す
ることができ、水量を定量として循環させることができ
る。In addition, potassium chloride is made to an appropriate concentration using a measure 33 in the water tank 22 for water H2O, and a quicklime aqueous solution is also put in the aqueous solution tank 21 to prepare the joint 14.
With the aqueous solution passage 15, the solution can be replenished by the drop of the solution, and the amount of water can be circulated at a constant rate.
更にこのような空調のシステム化をすると、単にコスト
が安いだけでなく、1年中使用できることになる。即ち
寒い冬には反応槽の上部の蓋34を開き、酸素O2を冷
却せずに高温のままにし、暑い夏には銅製パイプを通過
させて冷却する。時雨どきには開孔を開いて大気を取り
入れて湿気を電気分解させることになり、空調の効果が
良くなる。使用済み生石灰水溶液はホース35を使用し
て排水する。Furthermore, by creating an air conditioning system like this, not only is the cost low, but it can also be used all year round. That is, in the cold winter, the lid 34 at the top of the reaction tank is opened and the oxygen O2 remains at a high temperature without being cooled, and in the hot summer, it is cooled by passing it through a copper pipe. When it rains, the holes are opened to let in air and electrolyze the moisture, improving the effectiveness of air conditioning. The used quicklime aqueous solution is drained using a hose 35.
第1図は、第2図は空調システム機器の縦断面図、第3
図は電気分解における電極の実施態様を示す正面図3、
反転極性図4と側面図、第4図は横転防止の実施態様を
示す縦断側面と正面図、第5図は生石灰水溶液の貯水槽
と銅製パイプの取付部の実施態様を示す縦断面図、第6
図は耐震センサーの実施態様を示す縦断面図、第7図は
塩化カリウム等のタンクとメジャーの実施態様を示す縦
断面図である。
1…反応槽、3…格子状形電極、
6…ストッパー、7…ゲート、9…銅製パイプ、10…
貯水槽、12…ファン、13…モータ、14…生石灰水
溶液の供給機構、
22…KCl水溶液のタンク、25…ギップ穴、27…
耐震センサー、35…ホース、
36…湿気の開孔、37…生石灰水溶液の流し台、38
…使用済み生石灰水溶液の外部取出蓋。Figure 1 is a vertical cross-sectional view of air conditioning system equipment;
The figure is a front view 3 showing an embodiment of an electrode in electrolysis;
Reversed polarity Figure 4 and side view, Figure 4 is a longitudinal side view and front view showing an embodiment of rollover prevention, Figure 5 is a longitudinal sectional view showing an embodiment of a quicklime aqueous solution storage tank and a copper pipe attachment part, 6
The figure is a vertical cross-sectional view showing an embodiment of an earthquake-resistant sensor, and FIG. 7 is a vertical cross-sectional view showing an embodiment of a tank for potassium chloride, etc., and a measure. DESCRIPTION OF SYMBOLS 1... Reaction tank, 3... Grid-shaped electrode, 6... Stopper, 7... Gate, 9... Copper pipe, 10...
Water tank, 12... Fan, 13... Motor, 14... Quicklime aqueous solution supply mechanism, 22... KCl aqueous solution tank, 25... Gip hole, 27...
Seismic sensor, 35...hose, 36...humidity hole, 37...sink for quicklime aqueous solution, 38
...External removal lid for used quicklime aqueous solution.
Claims (4)
リウム等を水溶液にし、槽の内部にヒーターで加熱する
ことによって、水蒸気H2Oを酸素分子O2と水素原子
をイオン化させる反応槽の装置。Claim 1: A reaction tank device that ionizes water vapor H2O into oxygen molecules O2 and hydrogen atoms by making potassium chloride or the like into an aqueous solution in the reaction tank, which is an oxygen generating device, and heating it with a heater inside the tank. .
とによって、酸素分子O2と水素分子H2の分子結合を
させる電気分解装置を取り付けた特許請求の範囲第1項
記載の高温水蒸気の電気分解装置。2. The high-temperature steam electrolysis device according to claim 1, which is equipped with an electrolysis device that causes molecular bonds between oxygen molecules O2 and hydrogen molecules H2 by electrolyzing the ionized high-temperature steam.
を通過させて、この銅製パイプを生石灰水溶液で冷却さ
せて、酸素O2と水素H2の温度を冷却することができ
るようにして生石灰水溶液を冷却水として使用した特許
請求の範囲第2項記載の生石灰水の冷却溶液。Claim 3: High-temperature oxygen and hydrogen are passed through a number of thin pipes, and the copper pipes are cooled with a quicklime aqueous solution to cool the temperature of oxygen O2 and hydrogen H2. A cooling solution of quicklime water according to claim 2, wherein the aqueous solution is used as cooling water.
気をファンをもって吹き付けることによって、大気中の
炭酸ガスCO2の炭素Cを化学反応させながら生石灰の
水溶液の気化熱によって、酸素と水素の温度も下げるこ
とになり、炭酸ガスCO2の清浄化と高温に電気分解さ
れた酸素O2と水素H2を冷却することができるように
した、特許請求の範囲第2項記載の炭酸ガスCO2の化
学反応システム装置。[Claim 4] By blowing air taken in from the outside into the cooling solution of quicklime using a fan, the temperature of oxygen and hydrogen is also increased by the heat of vaporization of the aqueous solution of quicklime while causing a chemical reaction with the carbon C of carbon dioxide gas CO2 in the atmosphere. The chemical reaction system device for carbon dioxide gas CO2 according to claim 2, which is capable of lowering the carbon dioxide gas CO2 and cooling the electrolyzed oxygen O2 and hydrogen H2 to a high temperature. .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24634789A JPH04292402A (en) | 1989-09-25 | 1989-09-25 | Air-conditioning system apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24634789A JPH04292402A (en) | 1989-09-25 | 1989-09-25 | Air-conditioning system apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH04292402A true JPH04292402A (en) | 1992-10-16 |
Family
ID=17147209
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24634789A Pending JPH04292402A (en) | 1989-09-25 | 1989-09-25 | Air-conditioning system apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH04292402A (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5118295A (en) * | 1974-08-07 | 1976-02-13 | Hosoda Haruji | |
| JPS5141085U (en) * | 1974-09-20 | 1976-03-26 | ||
| JPS5420956A (en) * | 1977-07-18 | 1979-02-16 | Kimimichi Monma | Method and apparatus for purifying indoor air |
| JPS5522335A (en) * | 1978-08-04 | 1980-02-18 | Sumitomo Chem Co Ltd | Dispersion of supply gas in multitubular wetted wall tower |
-
1989
- 1989-09-25 JP JP24634789A patent/JPH04292402A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5118295A (en) * | 1974-08-07 | 1976-02-13 | Hosoda Haruji | |
| JPS5141085U (en) * | 1974-09-20 | 1976-03-26 | ||
| JPS5420956A (en) * | 1977-07-18 | 1979-02-16 | Kimimichi Monma | Method and apparatus for purifying indoor air |
| JPS5522335A (en) * | 1978-08-04 | 1980-02-18 | Sumitomo Chem Co Ltd | Dispersion of supply gas in multitubular wetted wall tower |
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