JPS5815175B2 - Encasisogasnojiyokiyozai - Google Patents
EncasisogasnojiyokiyozaiInfo
- Publication number
- JPS5815175B2 JPS5815175B2 JP50036846A JP3684675A JPS5815175B2 JP S5815175 B2 JPS5815175 B2 JP S5815175B2 JP 50036846 A JP50036846 A JP 50036846A JP 3684675 A JP3684675 A JP 3684675A JP S5815175 B2 JPS5815175 B2 JP S5815175B2
- Authority
- JP
- Japan
- Prior art keywords
- hydrogen chloride
- chloride gas
- activated carbon
- allophane
- 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
Links
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 54
- 239000007789 gas Substances 0.000 claims description 51
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 claims description 48
- 229910000041 hydrogen chloride Inorganic materials 0.000 claims description 48
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 42
- 229910001583 allophane Inorganic materials 0.000 claims description 14
- 239000003795 chemical substances by application Substances 0.000 claims description 10
- 239000000203 mixture Substances 0.000 claims description 9
- 238000001035 drying Methods 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 description 12
- 238000001179 sorption measurement Methods 0.000 description 8
- 238000012360 testing method Methods 0.000 description 8
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 7
- 238000010586 diagram Methods 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 229910001873 dinitrogen Inorganic materials 0.000 description 3
- 239000008240 homogeneous mixture Substances 0.000 description 3
- 235000019645 odor Nutrition 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 238000003915 air pollution Methods 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 235000013162 Cocos nucifera Nutrition 0.000 description 1
- 244000060011 Cocos nucifera Species 0.000 description 1
- 241000238631 Hexapoda Species 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 229910052593 corundum Inorganic materials 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000499 gel Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 238000005554 pickling Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000001846 repelling effect Effects 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 238000003900 soil pollution Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
- 229910001845 yogo sapphire Inorganic materials 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Description
【発明の詳細な説明】
本発明は塩化水素ガスの除去剤、特に大気中に混在する
塩化水素ガスの除去剤に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an agent for removing hydrogen chloride gas, and particularly to an agent for removing hydrogen chloride gas mixed in the atmosphere.
我国の公害対策基本法によれば、代表的な公害として大
気汚染、悪臭、水質汚濁、土壌汚染、騒音、振動、地盤
沈下などを指定している。According to Japan's Basic Law on Pollution Control, representative pollution is specified as air pollution, bad odors, water pollution, soil pollution, noise, vibration, and ground subsidence.
上記の大気汚染および悪臭の発生の原因の一つである種
々の有害ガスの内、特に塩化水素ガスは忌むべき刺激臭
を有し、湿った空気中で激しく発煙し、水分の存在で腐
蝕性を有するので人体に悪影響を与えるばかりでなく、
機械器具および建築物などを腐蝕損傷させるもので、染
料製造、塩酸製造、塩化物の製造、鉄鋼の酸洗などの場
合において発生し大気中に混在するのである。Among the various harmful gases that are one of the causes of air pollution and bad odors mentioned above, hydrogen chloride gas in particular has an unpleasant pungent odor, smokes strongly in humid air, and is corrosive in the presence of moisture. It not only has a negative effect on the human body, but also
It corrodes and damages machinery, equipment, and buildings, and is generated during dye manufacturing, hydrochloric acid manufacturing, chloride manufacturing, pickling of steel, etc., and mixed in the atmosphere.
従来、塩化水素ガスの除去にはアルカリ中和洗滌法、水
洗滌法などが実施せられているが、これらの方法では大
規模な設備を使用する必要があり小規模にて環境の浄化
を行うには不向であるという難点がある。Traditionally, hydrogen chloride gas has been removed using alkali neutralization washing method, water washing method, etc., but these methods require the use of large-scale equipment, making it difficult to purify the environment on a small scale. The problem is that it is not suitable for
本発明はこのような難点を除くために塩化水素ガスの除
去剤として有効なものを求めるため種々研究を行った結
果これを完成したもので、その発明の要旨とするところ
はアロフェンを主成分とし、これに活性炭を混合した混
合物を成形、乾燥してなることを特徴とする塩化水素ガ
スの除去剤である。The present invention was completed as a result of various research conducted in order to find an effective remover for hydrogen chloride gas in order to eliminate these difficulties. This is a hydrogen chloride gas remover characterized by being made by molding and drying a mixture of the hydrogen chloride gas and activated carbon.
本発明の塩化水素ガスの除去剤において使用するアロフ
ェンとは膠質上とも呼称せられ、nSiO2゜Al20
A1203O〔n=1〜2〕の組成を有し、例えばSi
O2約40重量%、Al2O3約40重量%。The allophane used in the hydrogen chloride gas remover of the present invention is also called colloid, and is composed of nSiO2゜Al20
It has a composition of A1203O [n=1-2], for example, Si
About 40% by weight of O2, about 40% by weight of Al2O3.
H20約17重量%を・含有し、比表面積約300m/
gおよび真比重約2.7を有するものである。Contains about 17% by weight of H20 and has a specific surface area of about 300m/
g and true specific gravity of about 2.7.
このアロフェンは例えば水簸法その他の精製法によって
精製して使用するのが好ましい。This allophane is preferably purified and used, for example, by elutriation or other purification methods.
使用する場合のアロフェンの粉末の大きさは一般に20
0乃至500メツシユ特に300乃至400メツシユの
範囲であるのが好ましい。The size of allophane powder when used is generally 20
A range of 0 to 500 meshes, particularly 300 to 400 meshes is preferred.
本発明の塩化水素ガスの除去剤に使用する活性炭は市販
の活性炭、例えばヤシガラ炭、炭化水素燃焼の除虫する
油性活性炭などを使用することができる。The activated carbon used in the hydrogen chloride gas remover of the present invention may be commercially available activated carbon, such as coconut shell charcoal or oil-based activated carbon for repelling insects that burn hydrocarbons.
使用する場合の活性炭の粒の大きさは一般に300乃至
500メツシユ、特に30Dメツシユ以下の範囲である
のが好ましい。The particle size of activated carbon when used is generally in the range of 300 to 500 mesh, particularly preferably 30D mesh or less.
アロフェンと活性炭との使用割合は一般に80:20.
60:40.特に70:30とするのが好ましい。The ratio of allophane to activated carbon is generally 80:20.
60:40. In particular, it is preferable to set the ratio to 70:30.
本発明の塩化水素ガスの除去剤を製造するにはアロフェ
ンと活性炭とを混合し、その混合物をほぼ0.3〜6龍
のはゞ球状の大きさに成形し、約150乃至160℃の
温度で約2乃至3時間乾燥すればよい。To produce the hydrogen chloride gas remover of the present invention, allophane and activated carbon are mixed, the mixture is formed into a spherical size of approximately 0.3 to 6 mm, and heated at a temperature of approximately 150 to 160°C. It is sufficient to dry it for about 2 to 3 hours.
本発明の塩化水素ガスの除去剤においては、アロフエン
と活性炭のほかに従来公知の吸着剤例えばシリカゲル、
アルミナゲル、活性白土などを混合することができるが
、少量を使用することが肝要である。In the hydrogen chloride gas remover of the present invention, in addition to allofene and activated carbon, conventionally known adsorbents such as silica gel,
Alumina gel, activated clay, etc. can be mixed, but it is important to use small amounts.
本発明による塩化水素ガスの除去剤は、一定の容器、例
えば鉄製の容器に充填し、この容器にダクトを設け、そ
の充填層に塩化水素ガスを混在する空気を強制的に通過
させて塩化水素ガスの除去に使用する。The hydrogen chloride gas remover according to the present invention is filled in a certain container, for example, an iron container, a duct is provided in this container, and air mixed with hydrogen chloride gas is forced to pass through the filled bed to remove hydrogen chloride gas. Used for gas removal.
次に、本発明を製造例および実施例を挙げて具体的に説
明する。Next, the present invention will be specifically described with reference to production examples and examples.
を有する300〜400メツシユの大きさのアロフェン
70重量%と300メツシユ以下の大きさの活性炭(市
販の油性活性炭)30重量%とを混合して均質な混合物
となし、この混合物を0.3〜6mmのほぼ球状に造粒
し、160℃にて2時間乾燥して製品(塩化水素ガス除
去剤)とする。70% by weight of allophane with a size of 300 to 400 meshes and 30% by weight of activated carbon (commercially available oil-based activated carbon) with a size of 300 meshes or less are mixed to form a homogeneous mixture, and this mixture is The pellets are granulated into approximately spherical shapes of 6 mm and dried at 160° C. for 2 hours to obtain a product (hydrogen chloride gas removal agent).
製造例 2
製造例1で使用したアロフェンと活性炭とをそれぞれ6
0重量%および40重量%の割合で混合して均質な混合
物となし、この混合物を製造例1と同様に造粒乾燥して
製品(塩化水素ガス除去剤)とする。Production Example 2 Allophane and activated carbon used in Production Example 1 were each
A homogeneous mixture is obtained by mixing 0% by weight and 40% by weight, and this mixture is granulated and dried in the same manner as in Production Example 1 to obtain a product (hydrogen chloride gas removing agent).
製造例 3
製造例1で使用したアロフェンと活性炭とをそれぞれ8
0重量%および20重量%の割合で混合して均質な混合
物となし、この混合物を製造例1と同様に造粒乾燥して
製品(塩化水素除去剤)とする。Production Example 3 Allophane and activated carbon used in Production Example 1 were each
A homogeneous mixture is obtained by mixing 0% by weight and 20% by weight, and this mixture is granulated and dried in the same manner as in Production Example 1 to obtain a product (hydrogen chloride removal agent).
実施例
製造例1および2に示した製品(塩化水素ガス除去剤)
を第1図に示した試験装置により次の如く試験した。Examples Products shown in Production Examples 1 and 2 (hydrogen chloride gas removal agent)
was tested as follows using the testing apparatus shown in FIG.
その試験結果を第2図に記載する。試験装置の要部は、
塩化水素ガス発生装置1、湿度調節装置2および塩化水
素ガス吸着装置3からなる。The test results are shown in Figure 2. The main parts of the test equipment are:
It consists of a hydrogen chloride gas generator 1, a humidity control device 2, and a hydrogen chloride gas adsorption device 3.
試験に当っては、塩化水素ガス発生装置1はガラス容器
中に濃塩酸溶液4を入れ加熱装置5により加温できるよ
うにしてあり、湿度調節装置2には水6を入れ加熱装置
7により保温できるようにしである。In the test, the hydrogen chloride gas generator 1 was configured such that a concentrated hydrochloric acid solution 4 was placed in a glass container and heated by a heating device 5, and water 6 was placed in a humidity control device 2 and kept warm by a heating device 7. It is possible to do so.
窒素ボンベ8のコック9を開いて窒素ガスを取り出し、
これを二つの部分に分は一つは流量計10を経て塩化水
素ガス発生装置1を通り塩化水素ガスを伴ってガス溜1
1に入り、他の一つは流量計12を経て湿度調節装置2
を通りそこで加熱装置7により適当に加温加湿され、両
者の流れは三方管13にて合流し、適当に加湿された塩
化水素ガスと窒素ガスの混合気体となる。Open the cock 9 of the nitrogen cylinder 8 and take out the nitrogen gas.
This is divided into two parts: one passes through a flow meter 10 and then a hydrogen chloride gas generator 1, with hydrogen chloride gas flowing through a gas reservoir 1;
1, and the other one goes through the flow meter 12 to the humidity controller 2.
There, the gas is appropriately heated and humidified by the heating device 7, and the two flows are combined at the three-way pipe 13 to form an appropriately humidified mixed gas of hydrogen chloride gas and nitrogen gas.
このことは通常実際の塩化水素ガス混合気体はある程度
の湿度を伴っているので試験はこの自然条件に合せるた
め混合気体を調製したのである。This is because actual hydrogen chloride gas mixtures usually involve a certain degree of humidity, so the test was conducted by preparing a gas mixture to match this natural condition.
このようにして適当に加湿された塩化水素ガスと窒素ガ
スとの混合ガスを塩化水素ガス吸着装置3に送り、この
塩化水素吸着装置3は16mm内径のガラス管でこれに
前記の塩化水素ガス除去剤14の5gを入れる。The mixed gas of hydrogen chloride gas and nitrogen gas that has been appropriately humidified in this manner is sent to the hydrogen chloride gas adsorption device 3, which uses a glass tube with an inner diameter of 16 mm to remove the hydrogen chloride gas. Add 5g of Agent 14.
しかして塩化水素ガス吸着装置3へ導入する塩化水素ガ
スの濃度は15〜30ppmとし、流量は2.41/分
とし、湿度は関係湿度40〜50%として試験した。The concentration of hydrogen chloride gas introduced into the hydrogen chloride gas adsorption device 3 was 15 to 30 ppm, the flow rate was 2.41/min, and the relative humidity was 40 to 50%.
塩化水素ガスの除去率は塩化水素ガス吸着装置3と三方
管13との間に設けたサンプル採取管15から採取した
サンプル(吸着前)の塩化水素の濃度と、塩化水素ガス
吸着装置3の流出側に設けたサンプル採取管16から採
取したサンプル(吸着後)の塩化水素の濃度を測定しそ
の塩化水素の濃度の差によって求めた。The removal rate of hydrogen chloride gas is determined by the concentration of hydrogen chloride in the sample (before adsorption) taken from the sample collection tube 15 installed between the hydrogen chloride gas adsorption device 3 and the three-way pipe 13, and the outflow from the hydrogen chloride gas adsorption device 3. The concentration of hydrogen chloride in the sample (after adsorption) taken from the sample collection tube 16 provided on the side was measured and determined from the difference in the concentration of hydrogen chloride.
試験結果は第2図の曲線図(横軸は時で示した時間を表
わし、縦軸は塩化水素ガスの除去率を表わす)に示した
通りである。The test results are shown in the curve diagram of FIG. 2 (the horizontal axis represents time in hours, and the vertical axis represents hydrogen chloride gas removal rate).
第2図の曲線図には製造例1及び2に示した塩化水素除
去剤14の代りに活性炭単独(100%)またはアロフ
ェン単独(100%)のそれぞれ5gずつを充填して上
記と同一条件(すなわち塩化水素ガス濃度15〜30p
pm、流量2.41/分及び関係湿度40〜50%)と
して試験した場合の塩化水素ガスの除去率も併せて示し
た。In the curve diagram of FIG. 2, 5 g each of activated carbon alone (100%) or allophane alone (100%) was filled in place of the hydrogen chloride removing agent 14 shown in Production Examples 1 and 2, and under the same conditions as above ( That is, hydrogen chloride gas concentration 15-30p
pm, flow rate 2.41/min, and relative humidity 40-50%). The removal rate of hydrogen chloride gas is also shown.
第2図の曲線図から明らかな如く、アロフェン100%
のものも高率の除去性能を示すが活性炭100%のもの
は可成り低い性能しか示さない。As is clear from the curve diagram in Figure 2, allophane 100%
Those made of 100% activated carbon also show a high removal performance, but those made of 100% activated carbon only show a considerably low performance.
しかるにアロフェンに活性炭を加えると相乗効果を現出
しアロフェン100%のものよりも除去性能及び性能持
続につき大巾の向上を示すようになる。However, when activated carbon is added to allophane, a synergistic effect appears, and the removal performance and performance duration are greatly improved compared to those containing 100% allophane.
即ち活性炭自身は塩化水素ガスを除去する性能は低いが
活性炭のもっている大きな比表面積が塩化水素ガスの分
子をアロフェンの活性表面に近づけるのに有効な作用を
示すものと推定される。That is, although activated carbon itself has a low ability to remove hydrogen chloride gas, it is presumed that the large specific surface area of activated carbon has an effective effect in bringing hydrogen chloride gas molecules closer to the active surface of allophane.
実験によれば活性炭の添加率を30重量%から40重量
%に増加させると除去率及び除去継続時間を向上させる
ようであるが、その差は僅かであって実用上の性能では
殆んど差を認めるまでには至らない。According to experiments, increasing the addition rate of activated carbon from 30% to 40% by weight seems to improve the removal rate and removal duration, but the difference is small and there is almost no difference in practical performance. I cannot go so far as to admit that.
即ち各時間毎の平均値の誤差は±5%(自由度32)程
度である。That is, the error in the average value for each time is about ±5% (32 degrees of freedom).
また活性炭を30重量%から40重量%に増加させるど
造粒物の粉化の程度が上昇するために実用的には30重
量%程度が適当と推定される。Furthermore, as the amount of activated carbon is increased from 30% by weight to 40% by weight, the degree of pulverization of the granulated material increases, so it is estimated that approximately 30% by weight is practically appropriate.
第1図は本発明の塩化水素ガスの除去剤の性能の試験装
置の要領を示す図式図であり、第2図は本発明の塩化水
素ガスの除去剤の性能の試験結果を示す曲線図である。
1・・・・・・塩化水素ガス発生装置、2・・・・・・
湿度調節装置、3・・・・・・塩化水素ガス吸着装置、
4・・・・・・濃塩酸溶液、5・・・・・・加熱装置、
6・・・・・・水、7・・・・・・加熱装置、8・・・
・・・窒素ボンベ、9・・・・・・コック、10・・・
・・・流量計、11・・・・・・ガス溜、12・・・・
・・流量計、13・・・・・・三方管、14・・・・・
・塩化水素ガス除去剤、15・・・・・・サンプル採取
管、16・・・・・・サンプル採取管、17・・・・・
・流量計、18,19,20,21および22・・・・
・・コック。Fig. 1 is a schematic diagram showing the outline of a test device for the performance of the hydrogen chloride gas remover of the present invention, and Fig. 2 is a curve diagram showing the test results of the performance of the hydrogen chloride gas remover of the present invention. be. 1... Hydrogen chloride gas generator, 2...
Humidity control device, 3...Hydrogen chloride gas adsorption device,
4... Concentrated hydrochloric acid solution, 5... Heating device,
6...Water, 7...Heating device, 8...
...Nitrogen cylinder, 9...Cock, 10...
...Flowmeter, 11...Gas reservoir, 12...
...Flowmeter, 13...Three-way pipe, 14...
・Hydrogen chloride gas removal agent, 15... Sample collection tube, 16... Sample collection tube, 17...
・Flowmeter, 18, 19, 20, 21 and 22...
··cock.
Claims (1)
混合物を成形、乾燥してなることを特徴とする塩化水素
ガスの除去剤。1. A hydrogen chloride gas removal agent characterized by forming and drying a mixture containing allophane as a main component and mixed with activated carbon.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP50036846A JPS5815175B2 (en) | 1975-03-28 | 1975-03-28 | Encasisogasnojiyokiyozai |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP50036846A JPS5815175B2 (en) | 1975-03-28 | 1975-03-28 | Encasisogasnojiyokiyozai |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS51112492A JPS51112492A (en) | 1976-10-04 |
JPS5815175B2 true JPS5815175B2 (en) | 1983-03-24 |
Family
ID=12481114
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP50036846A Expired JPS5815175B2 (en) | 1975-03-28 | 1975-03-28 | Encasisogasnojiyokiyozai |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5815175B2 (en) |
-
1975
- 1975-03-28 JP JP50036846A patent/JPS5815175B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS51112492A (en) | 1976-10-04 |
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