JPH10230131A - Method for absorption removal of carbon dioxide in air - Google Patents

Method for absorption removal of carbon dioxide in air

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Publication number
JPH10230131A
JPH10230131A JP9072587A JP7258797A JPH10230131A JP H10230131 A JPH10230131 A JP H10230131A JP 9072587 A JP9072587 A JP 9072587A JP 7258797 A JP7258797 A JP 7258797A JP H10230131 A JPH10230131 A JP H10230131A
Authority
JP
Japan
Prior art keywords
air
lime
carbon dioxide
water
lime water
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
Application number
JP9072587A
Other languages
Japanese (ja)
Other versions
JP3421832B2 (en
Inventor
Tetsujiro Matsuhashi
鉄治郎 松橋
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Individual
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Individual
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Filing date
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Priority to JP07258797A priority Critical patent/JP3421832B2/en
Publication of JPH10230131A publication Critical patent/JPH10230131A/en
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Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02CCAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00Capture or disposal of greenhouse gases
    • Y02C20/40Capture or disposal of greenhouse gases of CO2

Landscapes

  • Gas Separation By Absorption (AREA)
  • Treating Waste Gases (AREA)

Abstract

PROBLEM TO BE SOLVED: To efficiently absorb and capture carbon dioxide in the air with lime water by a method wherein saturated lime aqueous solution or calcium hydroxide aqueous solution of a specific concentration is continuously made to flow down in a thin layer form of a specific film thickness bringing that in contact with the air, or sprayed by circulation. SOLUTION: In the case where carbon dioxide in the air is eliminated by absorption, saturated lime aqueous solution, or calcium hydroxide solution of at least 3×10<-4> N (normal) concentration (hereinafter, referred to as lime water) is continuously made to flow down in a thin film form of about 5-10mm or lower bringing that in contact with the air, or sprayed in circulation in a thin film form. Thereby, carbon dioxide in the air is effectively eliminated by absorption with a dynamic film surface of lime water. In that case, a concentration of the lime water is not limited to a saturated state, and about 9.5 or higher pH may suffice. For the lime to be used, both of slaked lime (calcium hydroxide) and quick lime (calcium oxide) may suffice.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、空気洗浄を含む空調・
換気、大気汚染防止・環境保全、用廃水処理などの産業
技術に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an air conditioner including air cleaning.
It is related to industrial technologies such as ventilation, air pollution prevention and environmental protection, and wastewater treatment.

【0002】[0002]

【従来の技術】従来一般の空調・換気の技術、装置は、
熱力学的な温湿度調整や循環空気の除塵、除菌に限定さ
れており、空気中の二酸化炭素の低減、除去の技術は不
可能視されていた。ちなみに、大きな会議室等において
眠気を催すことは日常よく体験されることであり、ま
た、その生理的現象の一因は空気中の酸素量に対する二
酸化炭素量の相対的増加によることも常識化している。
工場煙害や、いわゆる大気汚染の技術対策としては、悪
臭成分や硫黄酸化物の除去、あるいは発生源の制限とい
う消極的な措置に留まっており、二酸化炭素の人為的な
除去ということはほとんど省みられなかった。また、石
灰使用の用廃水処理に伴うアルカリ水の中和に大気中の
二酸化炭素を有効に利用する実用的技術はなかった。
2. Description of the Related Art Conventional air conditioning and ventilation technologies and devices
It is limited to thermodynamic temperature and humidity adjustment, dust removal and germicidal removal of circulating air, and it has been considered impossible to reduce or remove carbon dioxide in the air. By the way, drowsiness is often experienced in large conference rooms, etc., and it is common knowledge that the physiological phenomenon is caused by the relative increase in the amount of carbon dioxide relative to the amount of oxygen in the air. I have.
As technical measures against industrial smoke pollution and so-called air pollution, passive measures such as removal of odorous components and sulfur oxides or limitation of emission sources have been limited, and artificial removal of carbon dioxide has been largely omitted. I couldn't. In addition, there is no practical technique for effectively utilizing atmospheric carbon dioxide for neutralizing alkaline water in wastewater treatment using lime.

【0003】[0003]

【発明が解決しようとする課題】通常の空気の組成は次
のようである(岩波理化学辞典、第三版、1971)。
酸素23.01%,窒素75.51%,アルゴン1.2
86%,二酸化炭素0.04%,その他。(各重量
%)。これらの混合成分のなかで二酸化炭素の含有濃度
は人的な環境により変動しやすいから、健全な人間活動
のために適正な濃度を維持することが必要である。そし
て、地球規模での二酸化炭素の低減化の重要性が一般に
指摘されている。
The composition of ordinary air is as follows (Iwanami Dictionary of Physical and Chemical Sciences, Third Edition, 1971).
23.01% oxygen, 75.51% nitrogen, 1.2 argon
86%, carbon dioxide 0.04%, and others. (Each% by weight). Among these mixed components, the concentration of carbon dioxide tends to fluctuate depending on the human environment, so that it is necessary to maintain an appropriate concentration for healthy human activities. The importance of reducing carbon dioxide on a global scale is generally pointed out.

【0004】一方、二酸化炭素は水に溶けると炭酸とな
るが、硫酸や塩酸などの鉱酸に比べて、酸としての炭酸
の作用は温和である。そして中和生成物の炭酸塩は二次
的な分解を起こしたとしても硫黄化合物や塩素化合物の
ような危害はない。さらに、空気中の二酸化炭素の相対
的濃度は低いとしても資源量としては無限大に等しい。
従って未利用資源としての利用開発の意義も大きい。
[0004] On the other hand, carbon dioxide becomes carbonic acid when dissolved in water, and the action of carbonic acid as an acid is milder than that of mineral acids such as sulfuric acid and hydrochloric acid. And even if the carbonate of the neutralized product causes secondary decomposition, there is no harm like sulfur compounds and chlorine compounds. Furthermore, even though the relative concentration of carbon dioxide in the air is low, the amount of resources is infinite.
Therefore, the significance of utilization development as unused resources is significant.

【0005】[0005]

【課題を解決するための手段】本発明は、通常処理水と
して放流されている褐色工場廃水の脱色方法として別途
に発明された「石灰乳による廃水処理法」(特開平8−
294693)の後処理において、大気中二酸化炭素が
中和工程に有用なことを見出だした新たな実験事実に由
来する。すなわち、pH12.5程度の飽和石灰水の中
和は大気中二酸化炭素の捕集によっても達成されるが、
時間と水表面積の2条件が大きな支配要因であることが
初めに突き止められた。また、その中和が石灰水に捕集
された二酸化炭素によることの確証に加えて、石灰水へ
の二酸化炭素の溶け込み量は、pH約9.5以上のアル
カリ性領域において定常的なことが究明された。
SUMMARY OF THE INVENTION The present invention relates to a "method for treating wastewater with lime milk" which was separately invented as a method for decolorizing brown factory wastewater normally discharged as treated water (Japanese Unexamined Patent Publication No.
294 693) in a post-treatment, based on a new experimental finding that atmospheric carbon dioxide was found to be useful in the neutralization step. That is, the neutralization of the saturated lime water of about pH 12.5 is also achieved by trapping carbon dioxide in the atmosphere,
It was first identified that the two conditions, time and water surface area, were the major controlling factors. In addition to confirming that the neutralization is due to the carbon dioxide trapped in the lime water, it has been found that the amount of carbon dioxide dissolved in the lime water is steady in an alkaline region having a pH of about 9.5 or more. Was done.

【0006】大気中二酸化炭素の溶け込みによる「所要
中和日数;y〔d〕」と飽和石灰水の「相対的表面積;
x〔cm/l〕」との間に次の実験式が誘導された。 log y=a log x+b 〔式1〕 式1において、aおよびbは地理的条件等によって決定
される定数であり、aは常に負数の係数である。具体的
に、甲地点(海抜約360m)に関するa,b値は−
0.993および3.31、乙地点(海抜約590m)
に関するa,b値は−0.955および2.77であ
る。
"Necessary neutralization days; y [d]" due to the incorporation of atmospheric carbon dioxide and "relative surface area of saturated lime water;
x [cm 2 / l] ”, the following empirical formula was derived. log y = a log x + b [Formula 1] In Formula 1, a and b are constants determined by geographical conditions and the like, and a is always a negative coefficient. Specifically, the a and b values for the point A (about 360m above sea level) are-
0.993 and 3.31, Otsu (about 590m above sea level)
The a, b values for are -0.955 and 2.77.

【0007】また、式1に関する対数グラフにおいて
甲、乙にかかわる二つのx,y座標が同一点に重なる場
合の数値は、およそ130cm/l,16日であり、
これは実測の範囲内のデータであった。この相対的表面
積は、有効水深7.7m,直径12.9mの円形水槽の
場合に相当する。このことから、飽和石灰水の所要中和
日数を短縮すること、すなわち大気中二酸化炭素の捕集
能率を増大するためには、何らかの手段方法で相対的表
面積を格段に増大してやればよいことになる。
Further, in the logarithmic graph relating to the equation 1, when the two x, y coordinates relating to the insteps A and B overlap the same point, the numerical value is about 130 cm 2 / l, 16 days.
This was data within the range of the actual measurement. This relative surface area corresponds to a circular water tank having an effective water depth of 7.7 m and a diameter of 12.9 m. From this, in order to shorten the required neutralization days of saturated lime water, that is, to increase the trapping efficiency of atmospheric carbon dioxide, the relative surface area should be significantly increased by some means. .

【0008】一方、定常的[OH]減小期における、
飽和石灰水による大気中二酸化炭素の捕集・反応速度
は、1日1m当り 約5.6g(CO)になること
も見出だされた。これはまた、通常pH約9.5以上の
アルカリ性領域で同効果がある。
On the other hand, in the stationary [OH ] decrease period,
It has also been found that the rate of capture and reaction of atmospheric carbon dioxide by saturated lime water is about 5.6 g (CO 2 ) per 1 m 2 per day. It also has the same effect in the alkaline region, usually at a pH of about 9.5 or higher.

【0009】以上のことから、空気と接触する石灰水の
相対的表面積をできるだけ大きくすること、その手段と
して石灰水を例えば平均厚み1mm以下の薄膜状にして
空気中に噴出させ、かつ循環させることにより、空気中
の二酸化炭素を効率よく捕集、吸収することができる。
また、短時間に中和を達成することが出来る。その際の
石灰水膜の表面積は、技術的に可能な限り広くすること
が有用である。なお必ずしも中和を目的としない場合の
二酸化炭素吸収手段としては、石灰水を薄層状にして連
続流下する方法も効果的であり、その循環方式も有用で
ある。
In view of the above, it is necessary to increase the relative surface area of lime water in contact with air as much as possible. As a means for this, lime water is spouted into the air in the form of a thin film having an average thickness of 1 mm or less and circulated. Thereby, carbon dioxide in the air can be efficiently collected and absorbed.
Further, neutralization can be achieved in a short time. It is useful to make the surface area of the lime water film as large as technically possible. As a means of absorbing carbon dioxide when the purpose of neutralization is not always intended, a method in which lime water is continuously flowed in a thin layer form is effective, and its circulation system is also effective.

【0010】[0010]

【作用】空気中の二酸化炭素は、式2のように石灰水と
反応する。 Ca(OH)+CO→ CaCO+HO 〔式2〕 反応生成物である炭酸カルシウム(CaCO)は難溶
性の沈殿となるから、式2の反応は右の方向に進行す
る。また空気中に共存する酸素の水に対する溶解度は二
酸化炭素に比べてはるかに小さいことも、この式2の反
応促進に有利に作用する。
The carbon dioxide in the air reacts with the lime water as shown in equation (2). Ca (OH) 2 + CO 2 → CaCO 3 + H 2 O [Equation 2] Since calcium carbonate (CaCO 3 ), which is a reaction product, forms a sparingly soluble precipitate, the reaction of Equation 2 proceeds to the right. In addition, the fact that the solubility of oxygen coexisting in the air in water is much smaller than that of carbon dioxide, which also has an advantageous effect on accelerating the reaction of Formula 2.

【0011】石灰水面が静的状態の場合、飽和ないしは
飽和に近い濃厚な石灰水への大気中二酸化炭素の溶け込
みは、本発明者の研究結果によると、1日、相対的表面
積1cm/l当り、おおよそ1×10−5[OH
N(規定濃度)相当である。これをさらに換算すると、
石灰水表面における空気中二酸化炭素の捕集・吸収速度
は前記のとおり、約”5.6g(CO)/m・da
y”となる。
[0011] When the lime water surface is in a static state, the dissolution of atmospheric carbon dioxide into saturated or nearly saturated lime water, according to the results of the present inventors, shows that the relative surface area is 1 cm 2 / l per day. Approximately 1 × 10 −5 [OH ]
It is equivalent to N (specified density). Converting this further,
As described above, the rate of trapping and absorbing carbon dioxide in air on the surface of lime water is about “5.6 g (CO 2 ) / m 2 · da.
y ".

【0012】石灰水を薄膜ないしは薄層状に噴出させる
動的状態の場合は、正確な数値を把握しがたいが、おお
むね式1の関係が成立し、従って空気中二酸化炭素の捕
集・吸収の時間的効率が格段に向上することは、以下の
実施例に示すとおりである。すなわち、石灰水の容積に
対する、薄膜状液面の累計面積の大きさが、その支配因
子となる。
In the case of a dynamic state in which lime water is ejected in a thin film or a thin layer, it is difficult to grasp an accurate numerical value. The time efficiency is remarkably improved, as shown in the following embodiments. That is, the size of the total area of the thin film liquid level with respect to the volume of the lime water is the controlling factor.

【0013】[0013]

【実施例1】内径276mm、容量約20リットルのバ
ケツに飽和石灰水14リットル(1)を収容し、極小水
中ポンプを用いて高さ50cmの位置で水平方向に薄膜
状に噴出させ、その前方約15cmに懸垂した平滑な金
属板に水流末端を緩衝突、流下させる方式により、循環
噴流させた。この場合、石灰水循環量は約5l/mi
n、噴出口から下の液面までの落差は約15cm、水平
方向の膜面の形状は少し湾曲したが、膜面の広さは大略
幅10cm,長さ10cm.厚み1mmであり、水温
(2月)は0〜3℃であった。pH測定に基ずく中和所
要時間によって、二酸化炭素の吸収の速さを間接的に評
価した。その結果、24時間以内に中和の完了が認めら
れた。
Example 1 A bucket of saturated lime water (14 liters (1)) was placed in a bucket having an inner diameter of 276 mm and a capacity of about 20 liters, and was spouted horizontally into a thin film at a height of 50 cm using a micro water pump. A circulating jet was made by a method in which the end of a water stream was buffered and flowed down onto a smooth metal plate suspended to about 15 cm. In this case, the amount of lime water circulation is about 5 l / mi.
n, the head from the spout to the lower liquid surface was about 15 cm, and the horizontal film surface was slightly curved, but the width of the film surface was approximately 10 cm in width and 10 cm in length. The thickness was 1 mm, and the water temperature (February) was 0 to 3 ° C. The speed of carbon dioxide absorption was indirectly evaluated by the time required for neutralization based on the pH measurement. As a result, the completion of neutralization was recognized within 24 hours.

【0014】試みに、この石灰水を静的に放置した場合
の所要中和日数の計算値は、甲地における式1により4
8日となる。つまり、上記の方式による二酸化炭素の吸
収は静的な場合に比べて、およそ、50倍の効率であっ
たと言える。ちなみに、動的な膜面の累計面積(相対的
表面積)は約3,571cm/lとなり、同式を当て
はめた場合の所要中和日数の計算値は0.60日、(約
15時間)と算出された。
In the trial, the calculated value of the required neutralization days when the lime water was left standing statically was 4
8 days. In other words, it can be said that the absorption of carbon dioxide by the above method was approximately 50 times as efficient as in the case of static. Incidentally, the cumulative total area (relative surface area) of the dynamic membrane surface is about 3,571 cm 2 / l, and the calculated value of the required neutralization days when the same equation is applied is 0.60 days (about 15 hours). It was calculated.

【0015】[0015]

【実施例2】内径567mm、容量約200リットルの
ドラム缶に飽和石灰水160リットル(1)を収容し、
小型水中ポンプを用いて高さ約3mの位置から長四角の
薄層状に石灰水を放出し、水の落下途中から傾斜角約8
0度の板樋を経てドラム缶に流し込み、還流させる方式
により、石灰水を連続流下させた。この場合、石灰水流
量は約50l/min、放出口から下の液面までの落差
は約2m、空中に小滝状に落下する水膜部分の広さは、
大略、幅30cm、長さ40cm、厚み5mmであり、
水温(10〜11月)は7〜22℃であった。前記同
様、pH測定に基ずく中和所要時間によって、二酸化炭
素の吸収の速さを間接的に評価した。反復試行の結果、
中和所要日数は5〜9日、平均7日であった。
Embodiment 2 A drum having an inner diameter of 567 mm and a capacity of about 200 liters is filled with 160 liters (1) of saturated lime water,
Using a small submersible pump, lime water is discharged in a thin rectangular shape from a position about 3 m in height, and an inclination angle of about 8
The lime water was continuously flowed down by a method of flowing into a drum via a 0 ° sheet trough and refluxing. In this case, the lime water flow rate is about 50 l / min, the head from the discharge port to the lower liquid level is about 2 m, and the area of the water film that falls like a small waterfall in the air is:
Roughly 30 cm wide, 40 cm long and 5 mm thick,
The water temperature (October-November) was 7-22C. Similarly to the above, the speed of carbon dioxide absorption was indirectly evaluated based on the time required for neutralization based on the pH measurement. As a result of the repeated trials,
The number of days required for neutralization was 5 to 9 days, with an average of 7 days.

【0016】試みに、この石灰水を静的に放置した場合
の所要中和日数の計算値は、乙地における式1により7
3日となる。この方式の場合ても、およそ10倍の効率
が得られたことになる。ちなみに、動的な膜面の累計面
積(相対的表面積)は約625cm/lとなり、同式
を当てはめた場合の所要中和日数の計算値は5.1日と
算出された。
In the trial, the calculated value of the required number of neutralization days when this lime water was left standing statically was calculated as
3 days. Even in the case of this method, about ten times the efficiency is obtained. Incidentally, the cumulative area (relative surface area) of the dynamic membrane surface was about 625 cm 2 / l, and the calculated value of the required number of neutralization days when the same equation was applied was calculated to be 5.1 days.

【0017】[0017]

【発明の効果】本発明は、以上説明したように構成され
ているので、以下に記載されるような効果を奏する。
Since the present invention is configured as described above, it has the following effects.

【0018】空気中の二酸化炭素を石灰水の動的な膜面
により効果的に吸収することができる。その際、石灰水
の濃度は飽和状態であることに限定されず、およそpH
9.5以上であればよい。使用する石灰は、消石灰(水
酸化カルシウム)であっても、生石灰(酸かカルシウ
ム)であっても、同一の効果が得られる。
The carbon dioxide in the air can be effectively absorbed by the dynamic surface of the lime water. At that time, the concentration of the lime water is not limited to the saturated state,
What is necessary is just 9.5 or more. The same effect can be obtained regardless of whether the lime used is slaked lime (calcium hydroxide) or quick lime (acid or calcium).

【0019】静的な飽和石灰水表面における空気中二酸
化炭素の捕集・吸収速度は約5.6g(CO)/m
・dayと測定された。これに対して本発明において
は、薄膜状に循環噴出する石灰水により、静的な石灰水
表面からの二酸化炭素吸収に比べて少なくとも50倍以
上の効率で、空気中二酸化炭素を捕集・吸収できる。こ
の効率は、水膜面の面積を拡げ膜厚を薄くすることによ
り、さらに向上させることが可能である
The rate of capturing and absorbing carbon dioxide in the air on the surface of static saturated lime water is about 5.6 g (CO 2 ) / m 2.
Measured as day. On the other hand, in the present invention, lime water circulated and ejected in the form of a thin film captures and absorbs carbon dioxide in the air at least 50 times more efficiently than carbon dioxide absorption from a static lime water surface. it can. This efficiency can be further improved by increasing the area of the water film surface and reducing the film thickness.

【0020】本発明の方法により、アルカリ性の石灰水
を短時間で中和することができる。したがって、これを
容易に用廃水処理に適用することができる。
According to the method of the present invention, alkaline lime water can be neutralized in a short time. Therefore, this can be easily applied to wastewater treatment.

【0021】二酸化炭素の捕集・吸収の評価、その水質
管理や機能測定は、pH測定により簡便に行なうことが
できる。
The evaluation of the collection and absorption of carbon dioxide, the management of its water quality, and the measurement of its function can be easily performed by pH measurement.

【0022】本発明の物理化学的、機械装置的な手段、
操作は原理的には簡明な方法であり、そのハードウェア
ーの規模の大小は任意に設定できる。また、石灰ないし
は石灰水はアルカリ性物質であることを除いては、人体
等への危害は考え難く、日常ハンドリングに支障のない
化学物質である。したがって、各種産業分野への応用が
容易である。
Physicochemical and mechanical means of the present invention,
The operation is a simple method in principle, and the size of the hardware can be set arbitrarily. Except for the fact that lime or lime water is an alkaline substance, it is unlikely to cause any harm to the human body and is a chemical substance that does not hinder daily handling. Therefore, application to various industrial fields is easy.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 飽和石灰水溶液、ないしは3x10−4
N(規定)以上の濃度の水酸化カルシウム水溶液(以下
総括しては、石灰水という)を空気に接触させつつ、5
〜10mm程度以下の薄層状にして連続流下するか、薄
膜状にして循環散水することにより、空気中の二酸化炭
素を能率的に吸収する方法。
1. A saturated lime solution or 3 × 10 -4
An aqueous solution of calcium hydroxide having a concentration of N (normative) or higher (hereinafter collectively referred to as lime water) is brought into contact with air while
A method of efficiently absorbing carbon dioxide in the air by forming a thin layer having a thickness of about 10 mm or less and continuously flowing down, or forming a thin film and circulating water sprinkling.
【請求項2】 pH12.5またはこれに近いアルカリ
性の石灰水を、薄膜状にして流水または循環散水・噴霧
する処理方法により、空気中の二酸化炭素を積極的に吸
収させ、中和する方法。
2. A method of actively absorbing and neutralizing carbon dioxide in the air by a treatment method in which alkaline lime water having a pH of 12.5 or close thereto is formed into a thin film, and is subjected to running water or circulating water spraying / spraying.
JP07258797A 1997-02-17 1997-02-17 Absorption and removal method of carbon dioxide in air Expired - Fee Related JP3421832B2 (en)

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Application Number Priority Date Filing Date Title
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Publications (2)

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JPH10230131A true JPH10230131A (en) 1998-09-02
JP3421832B2 JP3421832B2 (en) 2003-06-30

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006072753A1 (en) * 2005-01-07 2006-07-13 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Method for the pre-treatment of air prior to the introduction thereof into a cryogenic air separation unit, and corresponding apparatus
KR100866642B1 (en) 2007-03-19 2008-11-04 주식회사 엔버스 Method and cartridge for measuring carbon dioxide in atmosphere
JP2009136862A (en) * 2007-11-14 2009-06-25 Hokkaido Univ Treatment method of high alkaline water and treatment apparatus thereof
JP2016539004A (en) * 2013-11-21 2016-12-15 マフェット, ルースMuffett, Ruth Absorption of atmospheric carbon dioxide
JP7407317B1 (en) * 2023-02-27 2023-12-28 株式会社錢高組 environmental control system

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006072753A1 (en) * 2005-01-07 2006-07-13 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Method for the pre-treatment of air prior to the introduction thereof into a cryogenic air separation unit, and corresponding apparatus
FR2880677A1 (en) * 2005-01-07 2006-07-14 Air Liquide METHOD FOR PRETREATING FRONT AIR INTRODUCTION IN CRYOGENIC AIR SEPARATION UNIT AND CORRESPONDING APPARATUS
JP2008527295A (en) * 2005-01-07 2008-07-24 レール・リキード−ソシエテ・アノニム・プール・レテュード・エ・レクスプロワタシオン・デ・プロセデ・ジョルジュ・クロード Method for pretreating air prior to introduction into a cryogenic air separation device and corresponding device
KR100866642B1 (en) 2007-03-19 2008-11-04 주식회사 엔버스 Method and cartridge for measuring carbon dioxide in atmosphere
JP2009136862A (en) * 2007-11-14 2009-06-25 Hokkaido Univ Treatment method of high alkaline water and treatment apparatus thereof
JP2016539004A (en) * 2013-11-21 2016-12-15 マフェット, ルースMuffett, Ruth Absorption of atmospheric carbon dioxide
JP2020089892A (en) * 2013-11-21 2020-06-11 マフェット, ルースMuffett, Ruth Method and system for at least partially removing carbon dioxide present in air, and device
JP7407317B1 (en) * 2023-02-27 2023-12-28 株式会社錢高組 environmental control system

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