JP2014104448A - Active carbon cartridge and gas purification device - Google Patents

Active carbon cartridge and gas purification device Download PDF

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JP2014104448A
JP2014104448A JP2012261298A JP2012261298A JP2014104448A JP 2014104448 A JP2014104448 A JP 2014104448A JP 2012261298 A JP2012261298 A JP 2012261298A JP 2012261298 A JP2012261298 A JP 2012261298A JP 2014104448 A JP2014104448 A JP 2014104448A
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activated carbon
carbon cartridge
filter
cartridge
inner cylinder
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JP5776672B2 (en
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Yukio Sahashi
幸雄 佐橋
Hisao Oshimizu
久夫 大清水
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Kurita Water Industries Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide an active carbon cartridge which inhibits outflow of dust coal and a gas purification device including the active carbon cartridge.SOLUTION: A gas purification device 1 includes: a cylindrical housing 4; a prefilter 5; a fan 6; an active carbon cartridge 7 which is provided so as to transmit air from the fan 6; and an after filter 8. The active carbon cartridge 7 includes: an inner cylinder 10 and an outer cylinder 11; a ring shaped front end plate 12; a discoid shaped rear end plate 13; a filter sheet 9 which is provided along an outer peripheral surface of the inner cylinder 10 and an inner peripheral surface of the outer cylinder 11; and granular active carbon 14 placed in a space between the inner cylinder 10 and the outer cylinder 11.

Description

本発明は、通気性の内筒と外筒との間に活性炭を充填した活性炭カートリッジと、この活性炭カートリッジを備えたガス浄化装置に関する。   The present invention relates to an activated carbon cartridge in which activated carbon is filled between a breathable inner cylinder and an outer cylinder, and a gas purification apparatus including the activated carbon cartridge.

活性炭の充填層に空気等のガスを通気すると、ガス中の腐食性成分や臭気成分等が吸着除去される。特許文献1の図5,6には、通気性の内筒と外筒との間に活性炭を充填し、内筒内に空気を送り込み、外筒の外周面から浄化空気を取り出すように構成した活性炭カートリッジが記載されている。特許文献2の図5〜8には、ファンによって空気を活性炭に通気してガス状不純物を除去する空気清浄機が記載されている。   When a gas such as air is passed through the packed bed of activated carbon, the corrosive components and odor components in the gas are adsorbed and removed. In FIGS. 5 and 6 of Patent Document 1, activated carbon is filled between the air-permeable inner cylinder and the outer cylinder, air is sent into the inner cylinder, and purified air is taken out from the outer peripheral surface of the outer cylinder. An activated carbon cartridge is described. 5 to 8 of Patent Document 2 describe an air cleaner that removes gaseous impurities by ventilating air through activated carbon with a fan.

近年、高精度の電気・電子機器の複合腐食性ガスに起因する腐食発生によって、工場内でさまざまなトラブル発生している。例えば電子部品製造工程で発生した極めて低濃度の硫化水素により、電気設備・電子機器・電子部品の表面に露出した銅などの金属が腐食することがある。   In recent years, various troubles have occurred in factories due to the occurrence of corrosion caused by the complex corrosive gas of high-precision electrical and electronic equipment. For example, a very low concentration of hydrogen sulfide generated in the electronic component manufacturing process may corrode metals such as copper exposed on the surfaces of electrical equipment, electronic devices, and electronic components.

精密基板などを採用した盤、制御部品等は、硫化水素などにより精密基板が腐食して短絡トラブルにより故障・破損すると、その修繕には多大な労力と時間を要するため、製造ライン休止による被害が甚大である。そのため、これらの精密基板などを採用した盤、制御部品等を設置した室内の空気から硫化水素などの腐食性成分を高度に除去することが求められている。   Panels and control parts that use precision substrates, etc., are corroded by hydrogen sulfide, etc., and if a precision substrate corrodes and breaks or breaks due to a short-circuit problem, the repair takes a lot of labor and time, so damage due to production line outages It is enormous. For this reason, it is required to highly remove corrosive components such as hydrogen sulfide from the air in the room in which the boards, control parts and the like employing these precision substrates are installed.

硫黄酸化物や硫化水素等を空気中から除去するために、ヨウ化カリウムを添着した活性炭を用いることが知られている(特許文献3)。   In order to remove sulfur oxide, hydrogen sulfide and the like from the air, it is known to use activated carbon impregnated with potassium iodide (Patent Document 3).

特開2001−225055JP 2001-225055 A 特開2002−170874JP 2002-170874 A 特開2003−10688JP2003-10688

粒径2.4〜4.7mm程度の粒状活性炭を用いる場合、孔径1〜2.5mmのカートリッジを用いれば活性炭の流失を防ぐことができる。しかしながら、被処理ガスを長時間にわたって粒状活性炭充填活性炭カートリッジに通気すると、粒状活性炭が次第に粉化し、微粉炭が活性炭カートリッジから流出し、該活性炭カートリッジ下流のアフターフィルタに目詰りが生じる。特に、比較的大型の活性炭カートリッジを用いた場合、活性炭カートリッジへの通気速度を大きくすると、活性炭の振動が大きくなり、活性炭が粉化し易くなり、アフターフィルタに目詰りが生じ易くなり、アフターフィルタの交換頻度が高くなる。   When granular activated carbon having a particle size of about 2.4 to 4.7 mm is used, it is possible to prevent the activated carbon from flowing out by using a cartridge having a pore size of 1 to 2.5 mm. However, when the gas to be treated is passed through the granular activated carbon filled activated carbon cartridge for a long time, the granular activated carbon is gradually pulverized, pulverized coal flows out of the activated carbon cartridge, and the after filter downstream of the activated carbon cartridge is clogged. In particular, when a relatively large activated carbon cartridge is used, if the ventilation rate to the activated carbon cartridge is increased, the vibration of the activated carbon increases, the activated carbon is easily pulverized, and the after filter is easily clogged. The exchange frequency increases.

本発明は、微粉炭の流出が抑制された比較的大型の活性炭カートリッジと、この活性炭カートリッジを備えたガス浄化装置とを提供することを目的とする。   An object of this invention is to provide the comparatively large sized activated carbon cartridge by which the outflow of pulverized coal was suppressed, and the gas purification apparatus provided with this activated carbon cartridge.

本発明の活性炭カートリッジは、通気孔を有した内筒及び外筒と、外筒の内周面及び内筒の外周面に設けられた不織布よりなるフィルタシートと、該フィルタシートの間に10〜20kg充填された粒状活性炭とを有する活性炭カートリッジであって、粒状活性炭は粒径2.4〜4.7mmが90wt%以上の粒度であり、外筒及び内筒の孔径は1〜2.5mmであることを特徴とするものである。   The activated carbon cartridge of the present invention includes an inner cylinder and an outer cylinder having vent holes, a filter sheet made of a nonwoven fabric provided on an inner peripheral surface of the outer cylinder and an outer peripheral surface of the inner cylinder, and 10 to 10 between the filter sheets. An activated carbon cartridge having 20 kg of granular activated carbon, wherein the granular activated carbon has a particle size of 2.4 to 4.7 mm and a particle size of 90 wt% or more, and the outer and inner cylinders have a hole diameter of 1 to 2.5 mm. It is characterized by being.

フィルタシートとしては静電フィルタシートが好ましい。   The filter sheet is preferably an electrostatic filter sheet.

本発明のガス浄化装置は、かかる本発明の活性炭カートリッジと、該活性炭カートリッジにガスを風量5〜25m/minで通気させる通気手段とを有する。 The gas purification apparatus of the present invention has the activated carbon cartridge of the present invention and a ventilation means for allowing gas to flow through the activated carbon cartridge at an air flow rate of 5 to 25 m 3 / min.

この通気手段は、前記活性炭カートリッジの内筒内にガスを供給し、外筒の外周面からガスを流出させるよう構成されていることが好ましい。   Preferably, the ventilation means is configured to supply gas into the inner cylinder of the activated carbon cartridge and to cause the gas to flow out from the outer peripheral surface of the outer cylinder.

本発明の活性炭カートリッジを備えたガス浄化装置に腐食性成分や臭気成分等を含有した被処理ガスを通過させると、腐食性成分や臭気成分等が活性炭に吸着され、浄化されたガスが取り出される。このガス浄化装置へのガス供給を継続すると、次第に活性炭に粉化が生じてくるが、不織布フィルタを設けているので、微粉炭が流出することが抑制され、アフターフィルタの交換頻度が減少する。   When a gas to be treated containing a corrosive component or odor component is passed through a gas purification apparatus equipped with the activated carbon cartridge of the present invention, the corrosive component or odor component is adsorbed on the activated carbon, and the purified gas is taken out. . If the gas supply to the gas purification device is continued, pulverization of the activated carbon gradually occurs. However, since the nonwoven fabric filter is provided, the outflow of pulverized coal is suppressed, and the replacement frequency of the after filter is reduced.

実施の形態に係るガス浄化装置の長手方向の断面図である。It is sectional drawing of the longitudinal direction of the gas purification apparatus which concerns on embodiment. (a)図は活性炭カートリッジの軸心方向の断面図、(b)図は(a)図のB−B線断面図である。(A) The figure is sectional drawing of the axial center direction of an activated carbon cartridge, (b) The figure is a BB sectional drawing of (a) figure. 活性炭カートリッジへの活性炭の充填方法を示す断面図である。It is sectional drawing which shows the filling method of the activated carbon to an activated carbon cartridge.

以下、図面を参照して実施の形態について説明する。図1,2の通り、このガス浄化装置1は、活性炭カートリッジ7によって空気を浄化するように構成されたものである。   Hereinafter, embodiments will be described with reference to the drawings. As shown in FIGS. 1 and 2, the gas purification device 1 is configured to purify air with an activated carbon cartridge 7.

ガス浄化装置1は、円筒形のハウジング4と、該ハウジング4の上流側の端部を横断するように設けられた不織布等よりなるプレフィルタ5と、該プレフィルタ5と活性炭カートリッジ7との間に配置されたファン6と、該ファン6からの送気を透過させるように設けられた該活性炭カートリッジ7と、ハウジング4の下流側の端部を横断するように設けられたアフターフィルタ8とを有する。   The gas purification apparatus 1 includes a cylindrical housing 4, a prefilter 5 made of a nonwoven fabric or the like provided so as to cross the upstream end of the housing 4, and a space between the prefilter 5 and the activated carbon cartridge 7. , The activated carbon cartridge 7 provided so as to transmit the air supplied from the fan 6, and the after filter 8 provided so as to cross the downstream end of the housing 4. Have.

活性炭カートリッジ7は、図2に示すように、それぞれ多孔板、メッシュ等よりなる通気性の内筒10及び外筒11と、該内筒10と外筒11との間のスペースの一端側を閉鎖するリング状のフロントエンドプレート12と、活性炭カートリッジ7の他端側を全面的に閉鎖する円板状のリヤエンドプレート13と、外筒11の内周面に沿って設けられたフィルタシート9と、内筒10の外周面に沿って設けられたフィルタシート9と、各フィルタシート9の間のスペースに充填された粒状活性炭14とを有する。   As shown in FIG. 2, the activated carbon cartridge 7 closes one end side of a space between the inner cylinder 10 and the outer cylinder 11, and a breathable inner cylinder 10 and an outer cylinder 11 each made of a porous plate, a mesh or the like. A ring-shaped front end plate 12, a disc-shaped rear end plate 13 that completely closes the other end of the activated carbon cartridge 7, a filter sheet 9 provided along the inner peripheral surface of the outer cylinder 11, It has the filter sheet 9 provided along the outer peripheral surface of the inner cylinder 10, and the granular activated carbon 14 with which the space between each filter sheet 9 was filled.

この活性炭カートリッジ7は粒状活性炭10〜20kgを収容できる大型のものである。なお、活性炭の充填量が10kgを下回るとカートリッジ交換頻度が高くなる場合がある(例えば50〜400ppbの硫化水素を10ppb以下に低減するのが困難となる)。また、20kgを超えると搬送や交換の作業が困難になるので好ましくない。   The activated carbon cartridge 7 is a large cartridge capable of accommodating 10 to 20 kg of granular activated carbon. In addition, when the filling amount of activated carbon is less than 10 kg, the cartridge replacement frequency may increase (for example, it becomes difficult to reduce 50 to 400 ppb hydrogen sulfide to 10 ppb or less). On the other hand, if it exceeds 20 kg, it is not preferable because it is difficult to carry and exchange.

粒状活性炭は粒径2.4〜4.7mmの活性炭が90wt%以上の粒度のものを用いる。この実施の形態では、活性炭にヨウ化カリウムが添着されている。ヨウ化カリウムの添着量は0.01〜10wt%であることが好ましい。内筒10、外筒11としては網状濾過体(目開き1〜2.5mm程度)が好適である。フィルタシート9としてはスポンジ状シート体でJIS11種(風速8.7cm/s)での捕集効率10〜40%程度のものが好適である。プレフィルタ5としては、一般的な除塵フィルターでありASHRAE平均質量法捕集率で70〜80%程度のものが好適である。アフターフィルタ8としては、一般的な中高性能フィルターでありJIS比色法捕集率で90%以上のものが好適である。ただし、これらは一例であって、本発明はこれに限定されるものではない。   As the granular activated carbon, activated carbon having a particle size of 2.4 to 4.7 mm and having a particle size of 90 wt% or more is used. In this embodiment, activated carbon is impregnated with potassium iodide. The amount of potassium iodide is preferably 0.01 to 10 wt%. As the inner cylinder 10 and the outer cylinder 11, a mesh filter (mesh size of about 1 to 2.5 mm) is preferable. The filter sheet 9 is preferably a sponge-like sheet having a collection efficiency of about 10 to 40% in JIS 11 species (wind speed 8.7 cm / s). The prefilter 5 is preferably a general dust removal filter having an ASHRAE average mass method collection rate of about 70 to 80%. As the after filter 8, a general medium-high performance filter having a JIS colorimetric collection rate of 90% or more is preferable. However, these are merely examples, and the present invention is not limited thereto.

前記ハウジング4の内面には中心孔15aを有したリング状の取付座15が設けられている。活性炭カートリッジ7が該取付座15にボルト等によって脱着自在に取り付けられている。中心孔15aと内筒10とは、略等径であり、同軸状に配置されている。外筒11の直径はハウジング4よりも小径である。外筒10はハウジング4と同軸状に設置されており、外筒10の外周面とハウジング4の内周面との間が通気空間となっている。活性炭カートリッジ7のガス通過の風量は5〜25m/min、特に6〜15m/minの大風量とする。 A ring-shaped mounting seat 15 having a center hole 15 a is provided on the inner surface of the housing 4. The activated carbon cartridge 7 is detachably attached to the attachment seat 15 with bolts or the like. The center hole 15a and the inner cylinder 10 have substantially the same diameter and are arranged coaxially. The diameter of the outer cylinder 11 is smaller than that of the housing 4. The outer cylinder 10 is installed coaxially with the housing 4, and a ventilation space is formed between the outer peripheral surface of the outer cylinder 10 and the inner peripheral surface of the housing 4. The amount of air passing through the activated carbon cartridge 7 is 5 to 25 m 3 / min, particularly 6 to 15 m 3 / min.

このように構成されたガス浄化装置において、ファン6を駆動すると、腐食性成分などを含有した被処理ガスがプレフィルタ5を透過して活性炭カートリッジ7内に流入し、活性炭カートリッジ7の内筒10、内筒10に重なるフィルタシート9、活性炭14の充填部、外筒11に重なるフィルタシート9及び外筒11を順次透過し、浄化ガスがアフターフィルタ8を透過して流出する。   In the gas purification apparatus configured as described above, when the fan 6 is driven, the gas to be treated containing a corrosive component or the like passes through the prefilter 5 and flows into the activated carbon cartridge 7, and the inner cylinder 10 of the activated carbon cartridge 7. The filter sheet 9 that overlaps the inner cylinder 10, the filling portion of the activated carbon 14, the filter sheet 9 that overlaps the outer cylinder 11, and the outer cylinder 11 sequentially pass through, and the purified gas passes through the after filter 8 and flows out.

本発明では風量が大きいためガス浄化装置の振動が大きくなり、運転を継続すると、活性炭14に徐々に粉化が生じてくるが、フィルタシート9を設けているので、微粉炭が活性炭カートリッジ7から流出することが抑制され、アフターフィルタ8の目詰りが抑制され、アフターフィルタ8の交換頻度が低下する。   In the present invention, since the air volume is large, the vibration of the gas purifier increases, and when the operation is continued, the activated carbon 14 is gradually pulverized. However, since the filter sheet 9 is provided, the pulverized coal is removed from the activated carbon cartridge 7. Outflow is suppressed, clogging of the after filter 8 is suppressed, and the replacement frequency of the after filter 8 is reduced.

活性炭カートリッジ7に活性炭を充填するには、図3のようにフロントエンドプレート12が底面となるように活性炭カートリッジ7のカートリッジ本体を縦とし、フィルタシート9を装着した後、活性炭を充填し、リヤエンドプレート13を装着すればよい。活性炭を充填するに際しては、内筒10にキャップを被せておき、内筒10の内側に活性炭が入り込まないようにするのが好ましい。また、活性炭の全量を一度に投入するのではなく、全量の2/3ほどを充填した後、バイブレータ等によって加振し、活性炭層を締める(充填密度を高くする)ようにした後、残部の活性炭を充填し、再度振動締め固めし、次いで必要に応じて活性炭を追加充填し、リヤエンドプレート13を装着するのが好ましい。フィルタシート9としては不織布が好ましく、特に不織布静電フィルタシートが好ましい。   In order to fill the activated carbon cartridge 7 with activated carbon, as shown in FIG. 3, the cartridge main body of the activated carbon cartridge 7 is placed vertically so that the front end plate 12 is the bottom, and after the filter sheet 9 is mounted, the activated carbon is filled and the rear end. The plate 13 may be attached. When filling the activated carbon, it is preferable to cover the inner cylinder 10 with a cap so that the activated carbon does not enter the inner cylinder 10. Also, instead of charging the entire amount of activated carbon at once, after filling about 2/3 of the total amount, vibrate with a vibrator, etc., and tighten the activated carbon layer (increase the packing density), then the remainder It is preferable that the activated carbon is filled and vibrationally compacted again, and then the activated carbon is additionally filled as necessary, and the rear end plate 13 is mounted. As the filter sheet 9, a nonwoven fabric is preferable, and a nonwoven fabric electrostatic filter sheet is particularly preferable.

なお、ガスを外筒外周面から内筒に向って流すことも可能である。本発明は硫化水素(50〜400ppb程度)など腐食性ガスが発生する工場内で電気・電子機器の金属腐食による故障を防止するために用いることができる。   It is also possible to flow the gas from the outer peripheral surface of the outer cylinder toward the inner cylinder. The present invention can be used in a factory where corrosive gas such as hydrogen sulfide (about 50 to 400 ppb) is generated to prevent a failure due to metal corrosion of an electric / electronic device.

[実施例1]
内径200mm、外径350mm、長さ500mmであり、粒状活性炭充填量15kgの図2に示す構造の活性炭カートリッジを図1のハウジング内に設置し、ガス浄化装置を構成した。粒状活性炭として粒径2.4〜4.7mmが90wt%以上の粒度のものを用いた。活性炭にはヨウ化カリウムを0.5wt%添着した。
[Example 1]
An activated carbon cartridge having an inner diameter of 200 mm, an outer diameter of 350 mm, and a length of 500 mm and having a granular activated carbon filling amount of 15 kg and having the structure shown in FIG. 2 was installed in the housing of FIG. A granular activated carbon having a particle size of 2.4 to 4.7 mm and a particle size of 90 wt% or more was used. Activated carbon was impregnated with 0.5 wt% potassium iodide.

プレフィルター5としては日本バイリーン製のフィレドン(登録商標)エアフィルタPS(捕集効率76%)を用い、アフターフィルタ8としては日本バイリーン製のフィロプリーツ(登録商標)VM(捕集効率90%)を用いた。内筒10、外筒11としては塩化ビニル製の円筒型カートリッジ(目開き2mm程度)を用いた。不織布静電フィルタシート9として東洋紡製のエリトロン(登録商標)EF(捕集効率20〜35%)を用いた。なお、長方形状の1115mm×500mmのシートを筒状に巻回して保形し、内筒10の外周面及び外筒11の内周面に沿ってそれぞれ設置し、粘着テープで仮留めし、その後、活性炭を充填した。   The Viledon (registered trademark) air filter PS manufactured by Japan Vilene (collection efficiency 76%) is used as the pre-filter 5, and the Filopleat (registered trademark) VM (collection efficiency 90%) manufactured by Vilene Japan is used as the after filter 8. Was used. As the inner cylinder 10 and the outer cylinder 11, a vinyl chloride cylindrical cartridge (mesh size of about 2 mm) was used. Erytron (registered trademark) EF (collection efficiency: 20 to 35%) manufactured by Toyobo was used as the nonwoven fabric electrostatic filter sheet 9. In addition, a rectangular 1115 mm × 500 mm sheet is wound into a cylindrical shape and retained, installed along the outer peripheral surface of the inner cylinder 10 and the inner peripheral surface of the outer cylinder 11, and temporarily fixed with an adhesive tape. Filled with activated carbon.

このガス浄化装置1に対して、硫化水素を100ppb含むガスを活性炭カートリッジを透過する風量が6m/minとなるように通気して1年間連続運転したところ、硫化水素は10ppb以下に低減された状態を維持した。アフターフィルタ8の差圧が初期差圧から100〜200Pa程度上昇したときにアフターフィルタ8を交換するようにメンテナンスした。その結果、アフターフィルタ8は途中で1回交換するだけで足りた。 When this gas purifying apparatus 1 was continuously operated for one year by passing a gas containing 100 ppb of hydrogen sulfide so that the amount of air passing through the activated carbon cartridge was 6 m 3 / min, the hydrogen sulfide was reduced to 10 ppb or less. The state was maintained. Maintenance was performed so that the afterfilter 8 was replaced when the differential pressure of the afterfilter 8 increased by about 100 to 200 Pa from the initial differential pressure. As a result, it was sufficient to replace the after-filter 8 once in the middle.

[比較例1]
実施例1において、活性炭カートリッジ7に内筒側及び外筒側の各フィルタシート9を用いないこと以外は同一のガス浄化装置を同一条件で運転した。その結果、アフターフィルタ8は1年間で3回交換する必要があった。
[Comparative Example 1]
In Example 1, the same gas purification apparatus was operated under the same conditions except that the activated carbon cartridge 7 did not use the filter sheets 9 on the inner cylinder side and the outer cylinder side. As a result, the after filter 8 had to be replaced three times in one year.

[比較例2]
比較例1において、風量を3m/minとしたこと以外は同一条件で運転した。その結果、アフターフィルタは1年間に1回交換するだけで足りた。
[Comparative Example 2]
In the comparative example 1, it drive | operated on the same conditions except having set the air volume to 3 m < 3 > / min. As a result, the after-filter has only to be changed once a year.

従って、これらの実験により次の事項が確認された。
(1) フィルタシートにより微粉炭の流出が抑制され、装置後段のアフターフィルタの目詰まりが減り、消耗品であるアフターフィルタの交換頻度が著しく減少する。
(2) ガス浄化装置の差圧が低減し、消耗品交換目安も明確にでき、安定して連続運転することができる。
(3) 風量が小さければ微粉炭発生の課題は生じない。
Therefore, the following items were confirmed by these experiments.
(1) The outflow of pulverized coal is suppressed by the filter sheet, the clogging of the after-filter after the apparatus is reduced, and the replacement frequency of the after-filter, which is a consumable item, is significantly reduced.
(2) The differential pressure of the gas purifier can be reduced, the consumable replacement standard can be clarified, and stable and continuous operation can be achieved.
(3) If the air volume is small, the problem of pulverized coal generation does not occur.

1 ガス浄化装置
4 ハウジング
5 プレフィルタ
6 ファン
7 活性炭カートリッジ
8 アフターフィルタ
9 フィルタシート
14 活性炭
DESCRIPTION OF SYMBOLS 1 Gas purification apparatus 4 Housing 5 Pre filter 6 Fan 7 Activated carbon cartridge 8 After filter 9 Filter sheet 14 Activated carbon

Claims (4)

通気孔を有した内筒及び外筒と、外筒の内周面及び内筒の外周面に設けられた不織布よりなるフィルタシートと、該フィルタシートの間に10〜20kg充填された粒状活性炭とを有する活性炭カートリッジであって、
粒状活性炭は粒径2.4〜4.7mmが90wt%以上の粒度であり、外筒及び内筒の孔径は1〜2.5mmであることを特徴とする活性炭カートリッジ。
An inner cylinder and an outer cylinder having vent holes, a filter sheet made of a non-woven fabric provided on the inner peripheral surface of the outer cylinder and the outer peripheral surface of the inner cylinder, and granular activated carbon filled with 10 to 20 kg between the filter sheets; An activated carbon cartridge having
The activated carbon cartridge is characterized in that the granular activated carbon has a particle size of 2.4 to 4.7 mm and a particle size of 90 wt% or more, and the hole diameter of the outer cylinder and the inner cylinder is 1 to 2.5 mm.
請求項1において、該フィルタシートは静電フィルタシートであることを特徴とする活性炭カートリッジ。   2. The activated carbon cartridge according to claim 1, wherein the filter sheet is an electrostatic filter sheet. 請求項1又は2の活性炭カートリッジと、該活性炭カートリッジにガスを風量5〜25m/minで通気させる通気手段とを有するガス浄化装置。 A gas purification apparatus comprising: the activated carbon cartridge according to claim 1 or 2; and a ventilation means for allowing gas to flow through the activated carbon cartridge at an air volume of 5 to 25 m 3 / min. 請求項3において、該通気手段は前記活性炭カートリッジの内筒内にガスを供給し、外筒の外周面からガスを流出させるよう構成されていることを特徴とするガス浄化装置。   4. The gas purifier according to claim 3, wherein the ventilation means is configured to supply gas into the inner cylinder of the activated carbon cartridge and to cause the gas to flow out from the outer peripheral surface of the outer cylinder.
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