JPH04104813A - Adsorbing body for adsorption treatment of gas - Google Patents

Adsorbing body for adsorption treatment of gas

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Publication number
JPH04104813A
JPH04104813A JP2223633A JP22363390A JPH04104813A JP H04104813 A JPH04104813 A JP H04104813A JP 2223633 A JP2223633 A JP 2223633A JP 22363390 A JP22363390 A JP 22363390A JP H04104813 A JPH04104813 A JP H04104813A
Authority
JP
Japan
Prior art keywords
moisture
adsorbent
adsorption
activated carbon
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.)
Pending
Application number
JP2223633A
Other languages
Japanese (ja)
Inventor
Soichiro Tsujimoto
聡一郎 辻本
Yoshitaka Nakahigashi
中東 義貴
Susumu Fujita
進 藤田
Toshio Date
伊達 利夫
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Osaka Gas Co Ltd
Original Assignee
Osaka Gas Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Osaka Gas Co Ltd filed Critical Osaka Gas Co Ltd
Priority to JP2223633A priority Critical patent/JPH04104813A/en
Publication of JPH04104813A publication Critical patent/JPH04104813A/en
Pending legal-status Critical Current

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  • Drying Of Gases (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Treating Waste Gases (AREA)
  • Separation Of Gases By Adsorption (AREA)

Abstract

PURPOSE:To maintain high adsorbing power of an adsorbing body to a component to be adsorbed in gas to be treated even in the presence of moisture by forming the adsorbing body for adsorption treatment of gas with an adsorbing element contg. activated carbon and a hygroscopic element contg. a hygroscopic agent adhered to one side of the adsorbing element. CONSTITUTION:A hygroscopic element 2 contg. >=0.01g/cm<3> hygroscopic agent such as silica gel is adhered to one side of an adsorbing element 3 contg. activated carbon to form an adsorbing body 1 for adsorption treatment of gas. This adsorbing body 1 can maintain high adsorbing power to a component to be adsorbed in gas to be treated even in the presence of moisture.

Description

【発明の詳細な説明】 [産業上の利用分野コ 本発明は、溶剤回収装置、溶剤濃縮装置、脱臭装置など
に使用されるガス吸着処理用吸着体に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an adsorbent for gas adsorption treatment used in a solvent recovery device, a solvent concentrator, a deodorizing device, etc.

[従来の技術と発明か解決しようとする課題]カスを吸
着処理する吸6装置には、活性炭素を含む吸着体が使用
されている。この吸着体の活性炭素は、処理ガス中に含
まれ、かつ吸着処理すべき特定の成分に応して選択され
ている。また、般に、特定の成分の吸着効率を高めるた
め、一種類の活性炭素か使用されている。
[Prior Art and Problems to be Solved by the Invention] An adsorbent containing activated carbon is used in a suction device for adsorbing waste. The activated carbon of this adsorbent is selected depending on the specific component contained in the process gas and to be adsorbed. Additionally, one type of activated carbon is generally used to increase the adsorption efficiency of specific components.

しかしながら、前記処理ガス中に水分か共存する場合に
は、吸着体の活性炭素に水分か吸着するので、本来、吸
着処理すべき特定の成分に対する吸着性か低下し、吸着
装置の性能か大きく低下する。例えば、温度30℃、相
対湿度6〔]%の空気は、2. 5X 10’ ppm
もの水分を含んでいる。
However, if moisture coexists in the treated gas, the moisture will be adsorbed to the activated carbon of the adsorbent, which will reduce the adsorption ability for specific components that should be adsorbed, and the performance of the adsorption device will decrease significantly. do. For example, air with a temperature of 30°C and a relative humidity of 6% is 2. 5X 10' ppm
Contains water.

そして、高濃度の水分は、活性炭素の吸着性能を著しく
低下させる。第3図は、温度25℃で、水分が共存する
条件下でのトリクロロエチレンに対する活性炭素(BE
T表面積1000 m’ / g )の吸着特性を示す
グラフである。第3図より明らかなように、相対湿度、
水分濃度が高くなるにつれて、活性炭素のトリクロロエ
チレンに対する吸着能か著しく低下する。
Moreover, a high concentration of water significantly reduces the adsorption performance of activated carbon. Figure 3 shows activated carbon (BE) against trichlorethylene at a temperature of 25°C and in the presence of moisture.
It is a graph showing the adsorption characteristics of T surface area 1000 m'/g). As is clear from Figure 3, relative humidity,
As the water concentration increases, the adsorption ability of activated carbon for trichlorethylene decreases significantly.

そこで、従来、吸着装置においては、水分の悪影響を低
減するため、処理ガスの温度を高め、相対湿度を下げる
ことか行なわれている。しかしなから、この方法は、吸
着処理すべき特定の成分の沸点か低い場合や、吸着特性
が元来劣る成分を吸着処理する場合には、適用するのが
困難である。
Therefore, conventionally, in adsorption apparatuses, in order to reduce the adverse effects of moisture, the temperature of the processing gas is increased and the relative humidity is lowered. However, this method is difficult to apply when the boiling point of a specific component to be adsorbed is low or when a component with inherently poor adsorption properties is to be adsorbed.

すなわち、処理ガスの温度を高めると、前記特定の成分
の吸着特性か低下し、本来の目的を達成できない。
That is, when the temperature of the processing gas is increased, the adsorption properties of the specific components are reduced, making it impossible to achieve the original purpose.

従って、本発明の「1的は、水分の共存下でも、処理ガ
ス中の被吸着成分に対して高い吸着能を保持するガス吸
着処理用吸着体を提供することにある。
Therefore, an object of the present invention is to provide an adsorbent for gas adsorption treatment that maintains a high adsorption capacity for adsorbed components in a processing gas even in the presence of moisture.

[発明の構成] 本発明は、活性炭素を含む吸着エレメントと、この吸着
エレメントの一方の面に配され、かつ吸湿剤を0.01
g/−以上含む吸湿エレメントとで構成されているガス
吸着処理用吸着体を提供する。
[Structure of the Invention] The present invention includes an adsorption element containing activated carbon, a moisture absorbent disposed on one surface of the adsorption element, and a moisture absorbent of 0.01%.
Provided is an adsorbent for gas adsorption processing, which is constituted by a moisture absorbing element containing more than 100 g/-g/- of moisture.

前記吸着エレメントの品性炭素としては、粒状炭、粉状
炭、繊維状活性炭のいずれてあってもよいが、吸着速度
及び吸着能の大きな繊維状活性炭が好ましい。活性炭素
の比表面積は、通常、500〜4000 m’ / g
 、好ましくは750〜4000 m’ / g、さら
に好まし、くは1000〜4000m’/g程度である
。繊維状活性炭の繊維径は、通常、40μm以下、好ま
しくは8〜20μm程度である。なお、繊維状活性炭は
、ピッチ系、ポリアクリロニトリル系、レーヨン系なと
の炭素繊維を賦活処理することにより得ることかできる
The quality carbon of the adsorption element may be granular carbon, powdered carbon, or fibrous activated carbon, but fibrous activated carbon is preferable because of its high adsorption rate and adsorption capacity. The specific surface area of activated carbon is usually 500 to 4000 m'/g
, preferably about 750 to 4000 m'/g, more preferably about 1000 to 4000 m'/g. The fiber diameter of the fibrous activated carbon is usually 40 μm or less, preferably about 8 to 20 μm. The fibrous activated carbon can be obtained by activating pitch-based, polyacrylonitrile-based, or rayon-based carbon fibers.

前記吸着エレメントはフェルト・状、ペーパー状に成形
されているのか好ましい。特に、ペーパ状に成形された
吸着エレメントは、ハニカム構造に形成されていたり、
エンボス加工されているのか好ましい。吸着エレメント
の活性炭素は、処理ガス中の特定の被吸着成分に対して
高い吸着能を何する。
Preferably, the adsorption element is shaped like felt or paper. In particular, paper-shaped adsorption elements have a honeycomb structure,
Preferably embossed. The activated carbon of the adsorption element has a high adsorption capacity for specific adsorbed components in the process gas.

吸湿エレメントは吸湿剤を含んでいる。また、吸湿エレ
メントは、通常、繊維と!−インダーとを含んでいる。
The hygroscopic element contains a hygroscopic agent. Also, moisture absorbing elements are usually made of fibers! - Contains an inder.

吸湿剤としては、例えば、塩化リチウム、臭化リチウム
なとのリチウム塩、塩化力ルンウム、臭化カルシウムな
とのカルシウム塩、過マンガン酸塩、シリカゲルなどの
ケイ素の酸化物、チタンの酸化物、活性アルミナ、ゼオ
ライトなどが挙げられる。これらの吸湿剤の中で、シリ
カゲル、セオライト及び塩化リチウムか好ましい。吸湿
剤の含a量は、(1,01g/crA以上、好ましくは
0.03g/cm以」二である。
Examples of moisture absorbing agents include lithium salts such as lithium chloride and lithium bromide, calcium salts such as chloride and calcium bromide, permanganates, silicon oxides such as silica gel, titanium oxides, Examples include activated alumina and zeolite. Among these moisture absorbers, silica gel, theolite and lithium chloride are preferred. The content of the moisture absorbent is (1.01 g/crA or more, preferably 0.03 g/cm or more).

前記繊維としては、活性炭素繊維を除く、天然繊維、合
成繊維、無機繊維などが挙げられる。
Examples of the fibers include natural fibers, synthetic fibers, and inorganic fibers, excluding activated carbon fibers.

吸湿剤を含む吸湿エレメントは、低湿度で大きな吸湿能
を有するものが好ましく、前記吸湿剤は、相対湿度30
%で10重量%以上、特に相対湿度20%以上で10重
n%以上の吸湿量を有するのか好ましい。
The hygroscopic element containing a hygroscopic agent preferably has a large hygroscopic ability at low humidity, and the hygroscopic element has a relative humidity of 30
It is preferable that it has a moisture absorption amount of 10% by weight or more, particularly 10% by weight or more at a relative humidity of 20% or more.

吸湿剤を含む吸湿エレメントは、ペーパー状又はシート
状であるのか特に好ましい。このような吸湿エレメント
の製造方法としては、例えば、少なくとも吸湿剤、繊維
状活性炭を除く繊維およびバインダーを含むスラリーか
ら湿式で抄紙する方法、繊維状活性炭を除く無機繊維、
木材パルプ、合成バルブなどの少なくとも一種の繊維と
、バインダーからなるシートに吸湿剤を付着させる方法
It is particularly preferable that the moisture absorbing element containing the moisture absorbent is in the form of a paper or a sheet. Examples of methods for producing such moisture absorbing elements include, for example, a method of wet paper making from a slurry containing at least a moisture absorbent, fibers excluding fibrous activated carbon, and a binder, inorganic fibers excluding fibrous activated carbon,
A method of attaching a moisture absorbent to a sheet made of at least one type of fiber such as wood pulp or synthetic valve and a binder.

前記シート中に、化学合成により吸湿剤を生成させ結合
させる方法などが挙げられる。
Examples include a method of producing and bonding a moisture absorbent in the sheet through chemical synthesis.

特に、吸湿エレメントは、前記吸着エレメントと同しく
、ハニカム構造に形成されていたり、エンボス加工され
ているのか好ましい。
In particular, it is preferable that the moisture absorbing element is formed into a honeycomb structure or embossed like the adsorption element.

そして、前記吸着エレメントの一方の面には、前記吸湿
エレメントか配されている。吸湿エレメントを、吸着エ
レメントの一方の而のうち処理ガスの上流側、すなわち
流入側に配するのが好ましい。この場合、高濃度の水分
を含む処理ガスを吸着処理すると、吸湿エレメントによ
り、水分を除去できる。水分が除去された処理ガス中の
成分は、下流側、すなわち流出側の前記活性炭素を含む
吸着エレメントにより吸着処理できる。すなわち、吸湿
エレメントと吸着エレメントにより、水分の除去と、処
理ガス中の成分の吸着とを機能分担している。従って、
高濃度の水分を含む処理ガスであっても、前記水分によ
る吸着性能の低下を防止しつつ、前記吸着エレメントに
より本来の吸着性能を維持できる。
The moisture absorption element is disposed on one surface of the absorption element. Preferably, the moisture absorbing element is disposed on the upstream side of the process gas, that is, on the inflow side of one of the adsorption elements. In this case, when the processing gas containing a high concentration of moisture is adsorbed, the moisture can be removed by the moisture absorption element. Components in the processing gas from which water has been removed can be adsorbed by the adsorption element containing activated carbon on the downstream side, that is, on the outflow side. That is, the functions of removing moisture and adsorbing components in the processing gas are shared between the moisture absorption element and the adsorption element. Therefore,
Even if the process gas contains a high concentration of water, the adsorption element can maintain the original adsorption performance while preventing the adsorption performance from being lowered due to the water content.

前記吸湿エレメントは、吸着エレメントの内面又は外面
、特に、吸着エレメントの上流側に配設されているのが
好ましい。吸湿エレメントは、吸着エレメントの一方の
面に、積層されているのか好ましい。
The moisture absorbing element is preferably arranged on the inner or outer surface of the adsorption element, particularly on the upstream side of the adsorption element. Preferably, the moisture absorbing element is laminated on one side of the adsorption element.

前記吸着エレメントと吸湿エレメントとて構成された吸
着体は、シート状に限らず、筒状などの立体形状であっ
てもよい。
The adsorbent composed of the adsorption element and the moisture absorbing element is not limited to a sheet shape, but may have a three-dimensional shape such as a cylinder shape.

第1図及び第2図は、それぞれ、本発明の吸着体の一例
を示す一部切欠斜視図である。
FIG. 1 and FIG. 2 are partially cutaway perspective views showing an example of the adsorbent of the present invention, respectively.

第1図に示す例では、吸着体(1)は、処理ガスの上流
側に位置する円板状吸湿エレメント(2)と、この吸湿
エレメント(2)に積層され、下流側に位置する円筒状
吸着エレメント(3)とで構成されている。前記吸湿エ
レメント(2)は、吸湿剤を含むシート(2a)と、吸
湿剤を含む波形状シート(2b)とを交互に巻回して積
層したハニカム構造に形成され、前記吸着エレメント(
3)も、繊維状活性炭素からなるシート(図示せず)と
波形状シート(図示せず)とを交互に巻回して積層した
ハニカム構造に形成されている。また、吸着体(1)の
上流側の面には除塵シート(4)が取付けられている。
In the example shown in FIG. 1, the adsorbent (1) includes a disc-shaped hygroscopic element (2) located upstream of the process gas, and a cylindrical hygroscopic element (2) stacked on this hygroscopic element (2) and located downstream. It is composed of an adsorption element (3). The moisture absorbing element (2) is formed into a honeycomb structure in which a sheet (2a) containing a moisture absorbent and a corrugated sheet (2b) containing a moisture absorbent are alternately wound and laminated.
3) is also formed into a honeycomb structure in which sheets made of fibrous activated carbon (not shown) and corrugated sheets (not shown) are alternately wound and laminated. Further, a dust removal sheet (4) is attached to the upstream side surface of the adsorbent (1).

第2図に示す例では、吸着体(11)は直方体状に形成
されている。吸着体(11)の上流側に位置する吸湿エ
レメント(12)は、吸湿剤を含む平板状シート(12
a)と、吸湿剤を含む波形状シート(12b)とを交互
に積層することにより形成されている。また、下流側に
位置する吸着エレメント(13)も、繊維状活性炭素か
らなる平板状シート(図示せず)と、繊維状活性炭素か
らなる波形状シート(図示せず)とを交互に積層するこ
とにより形成されている。
In the example shown in FIG. 2, the adsorbent (11) is formed in the shape of a rectangular parallelepiped. A moisture absorbing element (12) located upstream of the adsorbent (11) is a flat sheet (12) containing a moisture absorbent.
a) and a corrugated sheet (12b) containing a moisture absorbent are alternately laminated. Further, the adsorption element (13) located on the downstream side also has flat sheets (not shown) made of fibrous activated carbon and corrugated sheets (not shown) made of fibrous activated carbon stacked alternately. It is formed by

そして、前記吸湿エレメント(12)と吸着エレメント
(13)は、通気可能に積層され一部いる。また、吸着
体(11)の上流側の面には除塵シー1−(+4)か取
付けられている。
The moisture absorption element (12) and the adsorption element (13) are partially laminated to allow ventilation. Further, a dust removal sheet 1-(+4) is attached to the upstream side surface of the adsorbent (11).

このような吸着体は、水分含t−T量の如何に拘らず、
種々の処理ガスを吸着処理できる。処理ガス中の特定の
成分は特に限定されるものではなく、例えば、有機溶剤
、悪臭成分か挙げられる。本発明の吸着体は、特に、水
分の存rE下で吸着性か低下する成分を含む処理ガスに
好適に適用される。
Such an adsorbent, regardless of the water content t-T,
Various processing gases can be adsorbed and processed. The specific components in the processing gas are not particularly limited, and include, for example, organic solvents and malodorous components. The adsorbent of the present invention is particularly suitably applied to processing gases containing components whose adsorptivity decreases in the presence of moisture.

このような成分としては、例えば、フロン113.1.
1.1−トリクロロエタン、トリクロロエチレン、塩化
メチレンなどのハロゲン化炭化水素。
Examples of such components include Freon 113.1.
1.1-Halogenated hydrocarbons such as trichloroethane, trichloroethylene, methylene chloride.

アセト−・なとのケトン類:ヘキサンなとの炭化水素類
:酢酸メチル、酢酸エチルなとのエステル類なとか挙げ
られる。
Examples include ketones such as acetate, hydrocarbons such as hexane, and esters such as methyl acetate and ethyl acetate.

本発明の吸着体は、種々の吸着装置に適用でき、例えば
、溶剤回収装置、溶剤濃縮装置、脱臭装置なとに好適に
使用される。
The adsorbent of the present invention can be applied to various adsorption devices, and is suitably used, for example, in a solvent recovery device, a solvent concentrator, a deodorizing device, and the like.

本発明の吸着体は、洗浄装置、塗装工場、印刷工場、化
学上場、半導体工場、ドライクリー二ング工場なとから
発生する溶剤含a処理ガス中の溶剤や、悪臭成分を吸着
処理する上で好適である。
The adsorbent of the present invention is useful for adsorbing solvents and malodorous components in solvent-containing processing gases generated from cleaning equipment, painting plants, printing plants, chemical listing plants, semiconductor plants, dry cleaning plants, etc. suitable.

[発明の効果] 本発明の吸着体は、水分の共仔Fても、処理ガス中の被
吸着成分に対して高い吸着能を有する。
[Effects of the Invention] The adsorbent of the present invention has a high adsorption capacity for adsorbed components in the process gas, even if it contains moisture.

[実施例] 以下に、実施例にb(づいて本発明をより詳細に説明す
る。
[Example] The present invention will be described in more detail below with reference to Example (b).

実施例 BET表面積が約1500 m’ / gの石炭ピッチ
系活性炭素繊維(温度25℃、相対湿度20%での吸湿
量が約1重i 0i )からなるシートをハニカム構造
に成形し、吸着エレメントを形成した。また、温度25
℃、相対湿度20%での吸湿量が13重量%のシリカゲ
ルを0.05g/−含むシートをハニカム構造に成形し
、吸湿エレメントを形成した。そして、各ハニカム構造
の成層エレメントと吸湿エレメントとを第2図に示すよ
うに積層し、直方体状の吸着体(縦1 (’10 mm
 X横100mm×長さ500mm)を作製した。なお
、吸着エレメントの嵩密度は65 r / m 、長さ
380 mmであり、吸湿エレメントの嵩密度は120
 kg / m’、長さ120m+である。
Example BET A sheet made of coal pitch-based activated carbon fiber (moisture absorption of about 1 layer i 0i at a temperature of 25° C. and a relative humidity of 20%) with a surface area of about 1500 m'/g was formed into a honeycomb structure and used as an adsorption element. was formed. Also, temperature 25
A sheet containing 0.05 g/- of silica gel with a moisture absorption of 13% by weight at 20% relative humidity and 20% relative humidity was formed into a honeycomb structure to form a moisture absorbing element. Then, the stratified elements and moisture absorbing elements of each honeycomb structure were stacked as shown in Fig.
100 mm in width x 500 mm in length) was prepared. The bulk density of the adsorption element is 65 r/m and the length is 380 mm, and the bulk density of the moisture absorption element is 120 r/m.
kg/m', length 120m+.

そして、400pp■のキシレンを含み、温度30℃、
相対湿度70%の空気からなる処理ガスを、吸湿エレメ
ント側から空塔速度1.6m/秒の条件で供給し、5%
破過、すなわち吸着エレメント側の出口濃度が20 p
pmとなるまでの時間を調べたところ、5%破過時間は
26分てあった。
It contains 400pp■ xylene, the temperature is 30℃,
A processing gas consisting of air with a relative humidity of 70% is supplied from the moisture absorption element side at a superficial velocity of 1.6 m/sec, and the relative humidity is 5%.
Breakthrough, that is, the outlet concentration on the adsorption element side is 20 p
When the time taken to reach pm was investigated, the 5% breakthrough time was 26 minutes.

比較例1 実施例1の吸湿エレメントを積層することなく、実施例
で用いた石炭ピッチ系活性炭素繊維(相対湿度30%で
の吸湿量が約1重量%)からなるシートをハニカム構造
に成形し、直方体状の吸着体(縦1. OOmm X横
100mmX長さ500mm)を作製した。なお、吸着
体の嵩密度は65 kl / m″である。
Comparative Example 1 A sheet made of the coal pitch-based activated carbon fiber used in the example (moisture absorption of about 1% by weight at 30% relative humidity) was formed into a honeycomb structure without laminating the moisture absorbing element of Example 1. A rectangular parallelepiped adsorbent (length 1.00 mm x width 100 mm x length 500 mm) was prepared. Note that the bulk density of the adsorbent is 65 kl/m''.

そして、実施例1と同様にして、596破過時間を測定
したところ、14分てあった。
Then, when the 596 breakthrough time was measured in the same manner as in Example 1, it was 14 minutes.

比較例2 実施例1の吸湿エレメントに代えて、シリカゲル含有量
0 、 005 g /−のシートを/%ニカム構造に
成形した吸湿エレメント(縦100 mm X FR1
00mm X長さ120mm)を用いる以外、実施例と
同様にして、5%破過時間を測定したところ、11分て
あった。
Comparative Example 2 In place of the moisture absorbing element of Example 1, a moisture absorbing element (length 100 mm
When the 5% breakthrough time was measured in the same manner as in Example except that the length was 120 mm (00 mm x length 120 mm), it was 11 minutes.

【図面の簡単な説明】[Brief explanation of drawings]

第1図及び第2図は、それぞれ、本発明の吸着体の一例
を示す一部切欠斜視図、 第3図は、温度25℃で、水分か共存する条件下でのト
リクロロエチレンに対する活性炭素(BET表面積10
00 m’ / g )の吸着特性を示すグラフである
。 (+)(11)・・・吸着体、(2)(+2)・・・吸
湿エレメント、(3)(+3)・・吸着エレメント 特許出願人 大阪瓦斯株式会+1
1 and 2 are partially cutaway perspective views showing an example of the adsorbent of the present invention, respectively. surface area 10
00 m'/g) is a graph showing the adsorption characteristics. (+) (11)... Adsorbent, (2) (+2)... Moisture absorption element, (3) (+3)... Adsorption element patent applicant Osaka Gas Co., Ltd. +1

Claims (1)

【特許請求の範囲】 1、活性炭素を含む吸着エレメントと、この吸着エレメ
ントの一方の面に配され、かつ吸湿剤を0.01g/c
m^3以上含む吸湿エレメントとで構成されているガス
吸着処理用吸着体。 2、吸湿剤が、シリカゲル、ゼオライト又は塩化リチウ
ムである請求項1記載のガス吸着処理用吸着体。 3、吸湿エレメントが、吸湿剤、活性炭素繊維を除く繊
維、およびバインダーで形成されている請求項1記載の
ガス吸着処理用吸着体。 4、吸湿エレメントの吸湿剤の吸湿量が、相対湿度30
%で10重量%以上である請求項1記載のガス吸着処理
用吸着体。 5、活性炭素が、繊維状である請求項1記載のガス吸着
処理用吸着体。
[Claims] 1. An adsorption element containing activated carbon, disposed on one side of this adsorption element, and containing 0.01 g/c of a moisture absorbent.
An adsorbent for gas adsorption processing, which is composed of a moisture absorption element containing m^3 or more. 2. The adsorbent for gas adsorption treatment according to claim 1, wherein the moisture absorbent is silica gel, zeolite, or lithium chloride. 3. The adsorbent for gas adsorption treatment according to claim 1, wherein the hygroscopic element is formed of a hygroscopic agent, fibers other than activated carbon fibers, and a binder. 4. The amount of moisture absorbed by the moisture absorbing agent in the moisture absorption element is 30% relative humidity.
The adsorbent for gas adsorption treatment according to claim 1, wherein the amount is 10% by weight or more. 5. The adsorbent for gas adsorption treatment according to claim 1, wherein the activated carbon is fibrous.
JP2223633A 1990-08-23 1990-08-23 Adsorbing body for adsorption treatment of gas Pending JPH04104813A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2223633A JPH04104813A (en) 1990-08-23 1990-08-23 Adsorbing body for adsorption treatment of gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2223633A JPH04104813A (en) 1990-08-23 1990-08-23 Adsorbing body for adsorption treatment of gas

Publications (1)

Publication Number Publication Date
JPH04104813A true JPH04104813A (en) 1992-04-07

Family

ID=16801257

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2223633A Pending JPH04104813A (en) 1990-08-23 1990-08-23 Adsorbing body for adsorption treatment of gas

Country Status (1)

Country Link
JP (1) JPH04104813A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06343823A (en) * 1993-06-08 1994-12-20 Nec Corp Intake and exhaust treatment system for clean chamber
US6120584A (en) * 1997-01-31 2000-09-19 Takasago Thermal Engineering Co., Ltd. Air cleaning apparatus, air filter and method for manufacturing the same
JP2005021851A (en) * 2003-07-01 2005-01-27 Kuraray Chem Corp Method for recovering mixed solvent
JP2008012432A (en) * 2006-07-05 2008-01-24 Mitsubishi Paper Mills Ltd Dispersion, sheet-like object and sheet-like object for humidity control
JP2009512911A (en) * 2005-09-08 2009-03-26 スイスコム・モバイル・アクチエンゲゼルシヤフト Communication apparatus, system, and method
JP2011105545A (en) * 2009-11-17 2011-06-02 Toyobo Co Ltd Activated carbon fiber
CN103406003A (en) * 2013-05-17 2013-11-27 江苏同康特种活性炭纤维面料有限公司 High-efficiency moisture-absorbing active carbon fiber composite material and preparation method thereof
CN104057758B (en) * 2014-06-17 2017-01-04 长沙怡家环保工艺品有限公司 A kind of production method of activated carbon carving stereo product

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06343823A (en) * 1993-06-08 1994-12-20 Nec Corp Intake and exhaust treatment system for clean chamber
US6120584A (en) * 1997-01-31 2000-09-19 Takasago Thermal Engineering Co., Ltd. Air cleaning apparatus, air filter and method for manufacturing the same
JP2005021851A (en) * 2003-07-01 2005-01-27 Kuraray Chem Corp Method for recovering mixed solvent
JP4509502B2 (en) * 2003-07-01 2010-07-21 クラレケミカル株式会社 Recovery method of mixed solvent
JP2009512911A (en) * 2005-09-08 2009-03-26 スイスコム・モバイル・アクチエンゲゼルシヤフト Communication apparatus, system, and method
JP2008012432A (en) * 2006-07-05 2008-01-24 Mitsubishi Paper Mills Ltd Dispersion, sheet-like object and sheet-like object for humidity control
JP2011105545A (en) * 2009-11-17 2011-06-02 Toyobo Co Ltd Activated carbon fiber
CN103406003A (en) * 2013-05-17 2013-11-27 江苏同康特种活性炭纤维面料有限公司 High-efficiency moisture-absorbing active carbon fiber composite material and preparation method thereof
CN103406003B (en) * 2013-05-17 2016-08-10 江苏同康特种活性炭纤维面料有限公司 A kind of efficient absorbent activated carbon fibrous composite and preparation method thereof
CN104057758B (en) * 2014-06-17 2017-01-04 长沙怡家环保工艺品有限公司 A kind of production method of activated carbon carving stereo product

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