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JP5751244B2 - Gas purification device - Google Patents
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JP5751244B2 - Gas purification device - Google Patents

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JP5751244B2
JP5751244B2 JP2012261297A JP2012261297A JP5751244B2 JP 5751244 B2 JP5751244 B2 JP 5751244B2 JP 2012261297 A JP2012261297 A JP 2012261297A JP 2012261297 A JP2012261297 A JP 2012261297A JP 5751244 B2 JP5751244 B2 JP 5751244B2
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activated carbon
carbon element
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JP2014104447A (en
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幸雄 佐橋
幸雄 佐橋
山脇 健
健 山脇
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Kurita Water Industries Ltd
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Description

本発明は、ガス浄化装置に係り、特に腐食性成分を吸着する活性炭エレメントを備えたガス浄化装置に関する。   The present invention relates to a gas purification device, and more particularly to a gas purification device including an activated carbon element that adsorbs corrosive components.

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(特開2003−10688)。また、硫化水素等の悪臭成分を除去するために、塩化銅や金属酸化物を担持させた活性炭を用いることが特開平9−262273に記載されている。   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 (Japanese Patent Laid-Open No. 2003-10688). Japanese Patent Application Laid-Open No. 9-262273 describes using activated carbon carrying copper chloride or a metal oxide in order to remove malodorous components such as hydrogen sulfide.

特開2004−89963には、臭気成分含有ガスを、相対湿度85%以上に調湿した後、活性炭含有ハニカム状吸着剤と接触させて臭気成分を吸着除去する方法が記載されている。   Japanese Patent Application Laid-Open No. 2004-89963 describes a method of adsorbing and removing an odor component by adjusting the humidity of the odor component-containing gas to a relative humidity of 85% or more and then bringing it into contact with an activated carbon-containing honeycomb adsorbent.

特開2000−157620には、硫化水素などを含有した排泄物臭気成分含有空気をファンによって活性炭充填床に通過させて脱臭する脱臭装置が記載されている。   Japanese Patent Application Laid-Open No. 2000-157620 describes a deodorizing device that deodorizes by passing a waste odor component-containing air containing hydrogen sulfide or the like through a bed filled with activated carbon by a fan.

特開2003−10688JP2003-10688 特開平9−262273JP-A-9-262273 特開2004−89963JP 2004-89963 A 特開2000−157620JP 2000-157620 A

腐食性成分含有被処理ガスを活性炭の成形体や充填床などの活性炭エレメントに通過させ続けると、次第に活性炭の吸着残存容量が減少し、遂には活性炭が破過(ブレーク)して腐食性成分がリークするようになる。   If the gas to be treated containing a corrosive component is continuously passed through an activated carbon element such as an activated carbon molded body or a packed bed, the adsorption capacity of the activated carbon gradually decreases, and finally the activated carbon breaks through and the corrosive component is formed. To leak.

従来、この腐食性成分のリークを検出するために、ガス分析を行うか、又は金属片よりなるテストピースを吸着装置の出口側に配置し、このテストピースの腐食状況からリークの有無を判断するようにしているが、判定に時間がかかると共に、実際にリークが発生した後でなければ検出することができないという短所があった。   Conventionally, in order to detect leakage of this corrosive component, gas analysis is performed, or a test piece made of a metal piece is arranged on the outlet side of the adsorption device, and the presence or absence of leakage is determined from the corrosion state of this test piece. However, there are disadvantages that it takes a long time to make a determination and can only be detected after a leak has actually occurred.

本発明は、腐食性成分が実際にリークが開始する前に、また過度に早期となることなく、適性時期に活性炭エレメントを交換することができるガス浄化装置を提供することを目的とする。   An object of the present invention is to provide a gas purifying apparatus capable of replacing an activated carbon element at an appropriate time before the leakage of corrosive components actually starts and without becoming too early.

本発明のガス浄化装置は、被処理ガスが通過するハウジングと、該ハウジング内に設けられた、腐食性成分を吸着する活性炭エレメントと、該活性炭エレメントに被処理ガスを流通させるファン、該活性炭エレメントよりも上流側において該ハウジングを横断するように設けられたプレフィルタと、該活性炭エレメントよりも下流側において該ハウジングを横断するように設けられたアフターフィルタと、該活性炭エレメントのガス通過差圧の検出手段及びガス通過量検出手段と、該検出手段の検出値に基づいて前記活性炭エレメントの交換時期を判定する判定手段とを備えたガス浄化装置であって、前記判定手段は、ガス通過差圧の判定手段とガス通過量の判定手段とを有し、前記活性炭エレメントは、通気性の内筒及び外筒と、該内筒と外筒との間のスペースの一端側を閉鎖するリング状の第1のエンドプレートと、活性炭エレメントの他端側を全面的に閉鎖する第2のエンドプレートと、該内筒と外筒との間のスペースに充填された粒状活性炭とを有し、前記粒状活性炭は、ヨウ化カリウム添加量が0.01〜10wt%のヨウ化カリウム添着活性炭であることを特徴とする。 The gas purification device of the present invention includes a housing through which a gas to be treated passes, an activated carbon element that adsorbs a corrosive component, a fan that circulates the gas to be treated in the activated carbon element , and the activated carbon. A pre-filter provided across the housing upstream of the element; an after-filter provided across the housing downstream of the activated carbon element ; and a gas passage differential pressure of the activated carbon element detecting means for detecting means and the gas passage of, a gas purifying device provided with a determining means the replacement timing of the activated carbon element based on the detected value of the detection means, said determining means, the gas The activated carbon element includes a gas-permeable inner cylinder and an outer cylinder, and an inner portion of the activated carbon element. A ring-shaped first end plate that closes one end side of the space between the outer cylinder and the outer cylinder, a second end plate that entirely closes the other end side of the activated carbon element, the inner cylinder and the outer cylinder, The granular activated carbon is filled with potassium iodide, and the amount of potassium iodide added is 0.01 to 10 wt% of potassium iodide impregnated activated carbon.

本発明のガス浄化装置に腐食性成分含有被処理ガスを通過させると、腐食性成分が活性炭エレメントに吸着され、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、活性炭の圧密化等によって活性炭エレメントの圧損が増加し、風量が減少する。本発明では、活性炭エレメントのガス通過差圧及びガス通過量の少なくとも一方を検出し、これに基づいて活性炭エレメントの交換時期の判定を行う。例えば、通過差圧が所定値以上となるか、又は通過量が所定量以下となった場合に活性炭エレメントの交換時期と判定することにより、活性炭エレメントを適切な時期に交換することが可能となる。   When the gas to be treated containing the corrosive component is passed through the gas purification apparatus of the present invention, the corrosive component is adsorbed on the activated carbon element, and the purified gas is taken out. If the gas supply to the gas purifier is continued, the pressure loss of the activated carbon element increases due to the consolidation of the activated carbon and the air volume decreases. In the present invention, at least one of the gas passage differential pressure and the gas passage amount of the activated carbon element is detected, and the replacement timing of the activated carbon element is determined based on this. For example, it is possible to replace the activated carbon element at an appropriate time by determining the replacement timing of the activated carbon element when the passing differential pressure is equal to or higher than a predetermined value or the passing amount is equal to or lower than the predetermined amount. .

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. 吸着ユニットの断面図であり、(a)図は活性炭エレメントの軸心方向の断面図、(b)図は(a)図のB−B線断面図である。It is sectional drawing of an adsorption | suction unit, (a) A figure is sectional drawing of the axial center direction of an activated carbon element, (b) A figure is the BB sectional drawing of (a) figure.

以下、図面を参照して実施の形態について説明する。図1の通り、腐食性成分含有被処理ガスがダクト1から吸着ユニット2に導入され、浄化ガスがダクト3を通って流出する。   Hereinafter, embodiments will be described with reference to the drawings. As shown in FIG. 1, the gas to be treated containing corrosive components is introduced from the duct 1 to the adsorption unit 2, and the purified gas flows out through the duct 3.

吸着ユニット2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と活性炭エレメント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エレメント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HEPAフィルタなどよりなるアフターフィルタ8とを有する。   The adsorption unit 2 includes a cylindrical housing 4, a prefilter 5 made of a non-woven 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 element 7. After-arrangement comprising: a fan 6 arranged; the activated carbon element 7 provided so as to transmit air supplied from the fan 6; and a HEPA filter provided so as to cross the downstream end of the housing 4 And a filter 8.

活性炭エレメント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、活性炭エレメント7の他端側を全面的に閉鎖するリヤエンドプレート13と、内筒10と外筒11と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 element 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 perforated plate, a mesh or the like. A ring-shaped front end plate 12, a rear end plate 13 that completely closes the other end of the activated carbon element 7, and a granular activated carbon 14 filled in a space between the inner cylinder 10 and the outer cylinder 11. .

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。   In this embodiment, activated carbon is impregnated with potassium iodide. The amount of potassium iodide is preferably 0.01 to 10 wt%.

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。活性炭エレメント7のフロントエンドプレート12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。活性炭エレメント7のガス通過線速度は0.2m/s以上、特に0.3〜0.35m/s程度が好ましい。   A ring-shaped mounting seat 15 having a center hole 15 a is provided on the inner surface of the housing 4. The front end plate 12 of the activated carbon element 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 gas passage linear velocity of the activated carbon element 7 is preferably 0.2 m / s or more, particularly preferably about 0.3 to 0.35 m / s.

ダクト1,3にはそれぞれ圧力センサ20,21が設けられ、それらの検出信号が判定装置22に入力される。ダクト3には熱線流速計などの流量センサ23が設けられており、この流量センサの検出信号が判定装置22に入力される。   The ducts 1 and 3 are provided with pressure sensors 20 and 21, respectively, and their detection signals are input to the determination device 22. The duct 3 is provided with a flow rate sensor 23 such as a hot-wire anemometer, and a detection signal of the flow rate sensor is input to the determination device 22.

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、腐食性成分含有被処理ガスがダクト1からプレフィルタ5を透過して吸着ユニット2内に流入し、活性炭エレメント7の内筒10、活性炭14の充填部及び外筒11を透過し、浄化ガスがアフターフィルタ8を透過し、ダクト3へ流出する。ファン6を定速で回転させ、運転を継続する。そして、圧力センサ20,21の差(差圧)と、流量センサ23の検出流量とを判定装置22で経時的に判定する。   In the gas purification apparatus configured as described above, when the fan 6 is driven, the gas to be treated containing corrosive components passes through the prefilter 5 from the duct 1 and flows into the adsorption unit 2, and the inner cylinder 10 of the activated carbon element 7. Then, it passes through the filling portion of the activated carbon 14 and the outer cylinder 11, and the purified gas passes through the after filter 8 and flows out to the duct 3. The fan 6 is rotated at a constant speed and the operation is continued. Then, the determination device 22 determines the difference between the pressure sensors 20 and 21 (differential pressure) and the detected flow rate of the flow rate sensor 23 over time.

運転を継続すると、差圧が徐々に上昇し、通過流量が徐々に低下する。そこで、差圧が予め設定した所定値以上となるか、又は流量が所定流量以下となったときには、活性炭エレメント7を取付座15から取り外し、新品(又は活性炭再生済み)の活性炭エレメント7と交換する。   When the operation is continued, the differential pressure gradually increases and the passing flow rate gradually decreases. Therefore, when the differential pressure is equal to or higher than a predetermined value set in advance or the flow rate is lower than the predetermined flow rate, the activated carbon element 7 is removed from the mounting seat 15 and replaced with a new (or activated carbon regenerated) activated carbon element 7. .

活性炭エレメント7から腐食性成分のリークが開始するときの差圧又は流量を予め求めておき、これに安全率を勘案した値を上記の所定値又は所定流量として設定するのが好ましい。   It is preferable that a differential pressure or a flow rate when the leakage of the corrosive component starts from the activated carbon element 7 is obtained in advance, and a value in consideration of the safety factor is set as the predetermined value or the predetermined flow rate.

腐食性成分のリークが検出されたときには、活性炭の破過を通知する通知手段を作動させる。通知手段は警告ランプの点灯手段、警告音の発生手段、警告メールの送信手段などが挙げられるが、これに限定されない。   When the leak of the corrosive component is detected, the notification means for notifying the breakthrough of the activated carbon is activated. The notification means includes, but is not limited to, a warning lamp lighting means, a warning sound generation means, a warning mail transmission means, and the like.

これにより、腐食性成分がリークする前に、また過度に早期となることなく適切な時期に活性炭エレメント7を交換することができる。   Thereby, the activated carbon element 7 can be replaced at an appropriate time before the corrosive component leaks and without being excessively early.

なお、上記の差圧や流量センサの計測は連続的に行ってもよく、間欠的(例えば数時間〜数箇月に1回の頻度)に行ってもよい。   Note that the measurement of the differential pressure and the flow rate sensor may be performed continuously or intermittently (for example, once every several hours to several months).

ガスは一過式に流通させてもよく、循環流通させてもよい。   The gas may be circulated in a transient manner or circulated.

本発明の効果を確認するための実験を行った。   Experiments were conducted to confirm the effects of the present invention.

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エレメントを図1のハウジング内に設置し、ガス浄化装置を構成した。粒状活性炭は粒径2.4〜4.7mmのものが90wt%の粒度のものである。活性炭にはヨウ化カリウムを0.5wt%添着した。このガス浄化装置に硫化水素濃度100ppb程度に調整した空気を通風し、差圧及び風量を計測した。また、活性炭の破過の有無については、ハウジングの出口側ダクトで測定した硫化水素濃度の変化により判定した。結果を表1に示す。   An activated carbon element 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 a structure shown in FIG. 2 was installed in the housing of FIG. The granular activated carbon has a particle size of 90 wt% with a particle size of 2.4 to 4.7 mm. Activated carbon was impregnated with 0.5 wt% potassium iodide. Air adjusted to a hydrogen sulfide concentration of about 100 ppb was passed through the gas purification device, and the differential pressure and the air volume were measured. The presence or absence of breakthrough of the activated carbon was determined by the change in the hydrogen sulfide concentration measured in the outlet duct of the housing. The results are shown in Table 1.

Figure 0005751244
Figure 0005751244

表1より、活性炭破過と風量減少、差圧上昇に相関があることが確認された。また、表1より、風量が11m/minを下回った時点、風量が初期量の75%を下回った時点、差圧が190Paを上回った時点、または差圧が初期値の140%を上回った時点のいずれかの時点で活性炭が破過したと判定できることが認められた。従って、破過する前の例えば15ヶ月経過時の値を設定値とし、この設定値に達したならば活性炭エレメントを交換することにより、活性炭エレメントが適切時期に交換される。 From Table 1, it was confirmed that there was a correlation between activated carbon breakthrough, air volume reduction, and differential pressure increase. Also, from Table 1, when the air volume falls below 11 m 3 / min, when the air volume falls below 75% of the initial volume, when the differential pressure exceeds 190 Pa, or the differential pressure exceeds 140% of the initial value. It was found that it could be determined that the activated carbon broke through at any point in time. Therefore, for example, a value at the time of 15 months before breakthrough is set as a set value, and when this set value is reached, the activated carbon element is replaced at an appropriate time by replacing the activated carbon element.

1,3 ダクト
2 吸着ユニット
4 ハウジング
5 プレフィルタ
6 ファン
7 活性炭エレメント
8 アフターフィルタ
14 活性炭
20,21 圧力センサ
22 判定装置
23 流量センサ
DESCRIPTION OF SYMBOLS 1,3 Duct 2 Adsorption unit 4 Housing 5 Pre filter 6 Fan 7 Activated carbon element 8 After filter 14 Activated carbon 20, 21 Pressure sensor 22 Judgment device 23 Flow rate sensor

Claims (3)

被処理ガスが通過するハウジングと、
該ハウジング内に設けられた、腐食性成分を吸着する活性炭エレメントと、
該活性炭エレメントに被処理ガスを流通させるファン
該活性炭エレメントよりも上流側において該ハウジングを横断するように設けられたプレフィルタと、
該活性炭エレメントよりも下流側において該ハウジングを横断するように設けられたアフターフィルタと、
該活性炭エレメントのガス通過差圧の検出手段及びガス通過量検出手段と、
該検出手段の検出値に基づいて前記活性炭エレメントの交換時期を判定する判定手段と
を備えたガス浄化装置であって、
前記判定手段は、ガス通過差圧の判定手段とガス通過量の判定手段とを有し、
前記活性炭エレメントは、通気性の内筒及び外筒と、該内筒と外筒との間のスペースの一端側を閉鎖するリング状の第1のエンドプレートと、活性炭エレメントの他端側を全面的に閉鎖する第2のエンドプレートと、該内筒と外筒との間のスペースに充填された粒状活性炭とを有し、
前記粒状活性炭は、ヨウ化カリウム添加量が0.01〜10wt%のヨウ化カリウム添着活性炭であることを特徴とするガス浄化装置。
A housing through which the gas to be treated passes;
An activated carbon element that adsorbs corrosive components provided in the housing ;
A fan that distributes the gas to be treated to the activated carbon element ;
A pre-filter provided so as to cross the housing on the upstream side of the activated carbon element;
An after filter provided so as to cross the housing on the downstream side of the activated carbon element;
A means for detecting a gas passage differential pressure and a means for detecting a gas passage amount of the activated carbon element;
A gas purifying apparatus provided with a judging means for judging replacement time of the activated carbon element based on the detected value of the detection means,
The determination means includes a gas passage differential pressure determination means and a gas passage amount determination means,
The activated carbon element includes a breathable inner cylinder and outer cylinder, a ring-shaped first end plate that closes one end side of a space between the inner cylinder and the outer cylinder, and the other end side of the activated carbon element over the entire surface. A second end plate that is closed, and granular activated carbon filled in a space between the inner cylinder and the outer cylinder,
The granular activated carbon is a potassium iodide-impregnated activated carbon having a potassium iodide addition amount of 0.01 to 10 wt%.
請求項1において、前記プレフィルタは不織布よりなり、前記アフターフィルタはHEPAフィルタよりなることを特徴とするガス浄化装置。 2. The gas purification apparatus according to claim 1, wherein the pre-filter is made of a non-woven fabric, and the after-filter is made of a HEPA filter . 請求項1又は2において、前記ファンは、前記活性炭エレメントのガス通過線速度が0.2〜0.35m/secとなるように定速で回転することを特徴とするガス浄化装置。 3. The gas purification device according to claim 1, wherein the fan rotates at a constant speed so that a gas passage linear velocity of the activated carbon element is 0.2 to 0.35 m / sec .
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