JP4357606B2 - Exhaust gas absorber - Google Patents

Exhaust gas absorber Download PDF

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Publication number
JP4357606B2
JP4357606B2 JP08796698A JP8796698A JP4357606B2 JP 4357606 B2 JP4357606 B2 JP 4357606B2 JP 08796698 A JP08796698 A JP 08796698A JP 8796698 A JP8796698 A JP 8796698A JP 4357606 B2 JP4357606 B2 JP 4357606B2
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gas
ion exchange
main body
ion
regeneration
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JPH11262619A (en
Inventor
光 西村
隆哉 奥田
直巳 加藤
進司 服部
直樹 入江
健 森本
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DAN-TAKUMA TECHNOLOGIES INC.
Toshiba Plant Systems and Services Corp
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DAN-TAKUMA TECHNOLOGIES INC.
Toshiba Plant Systems and Services Corp
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  • Separation Of Gases By Adsorption (AREA)
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Description

【0001】
【発明の属する技術分野】
本発明は気体中の被除去物質をイオン交換法により除去する排ガス吸収装置、および排ガス吸収装置を用いて気体中の被除去物質を除去する気体処理方法に関するものである。
【0002】
【従来の技術】
従来から、気体中に含まれる不純物質や汚染物質などの被除去物質を除去するためには、スクラバーが使用されている。このようなスクラバーとしては、装置の本体内を通過する気体に水などの液体を噴霧し、被除去物質を液体に吸収させて分離除去する湿式のスクラバーが一般的である。しかし近年になって、本体内に湿らせたイオン交換体を配置し、通過する気体中の被除去物質をイオン交換により除去する、いわゆるドライガススクラバー(排ガス吸収装置)が操作性や処理効率などの点から注目されている。
【0003】
従来のドライガススクラバー(排ガス吸収装置)は、本体内にイオン交換体を収容するイオン交換部を設けると共に、その上流側に処理すべき気体の気体供給部、下流側に処理された気体排出部を設けて構成される。そして平常運転時には、気体供給部から導入された気体がイオン交換部を通過する間に被除去物質とイオン交換体との間にイオン交換がなされ、被除去物質の除去された気体は気体排出部から本体外に排出される。一定期間運転を継続すると、イオン交換体の交換能力が低下するので、一旦装置を停止しイオン交換体の再生処理が行われる。再生処理はイオン交換体に再生液を流すことにより行われ、化学的に吸着(イオン結合)された被除去物質イオンが再生液とのイオン交換により取り除かれ、イオン交換体はもとのイオン交換基に再生される。
【0004】
【発明が解決しようとする課題】
しかしながら上記従来の方法では、イオン交換体の再生時に装置の運転を一時中断しなければならないという問題がある。それを回避するために従来から行われている方法として、交互運転方式がある。該方式は、装置を2台設置して一方の装置を運転している間に、他方の装置のイオン交換体を再生処理するものである。しかしこの方式では、装置を2台設けるために設置コストや運転コストが大きくなるという別の問題を生じる。
【0005】
次に装置を1台のみ設置し、運転を中断せずにイオン交換体の再生処理を行なう方法として、運転中に再生処理を並行して行なう方式が考えられる。しかしこの方式を採用する場合には、再生処理に伴い気体に同伴して下流側に飛散する再生液ミストを取り除く手段、例えばミストセパレータ(デミスター)などを設置する必要があるので、装置が大きくなる(特に高さが大きくなる)と共に、設置コストも大きいという問題がある。また、再生期間中は気体の流速を再生液ミストの捕捉ができる程度までに減少させて運転する必要がある。
そこで本発明は、これらの問題を解決する排ガス吸収装置およびそれを用いた気体処理方法を提供することを課題とするものである。
【0006】
【課題を解決するための手段】
前記課題を解決するための請求項1に記載の発明は、気体中の被除去物質をイオン交換により除去する排ガス吸収装置において、
処理すべき気体が通過する本体(1) と、
該本体(1)内に互いに密接して連結された複数の枠体と、これら枠体の各々の上端ならびに下端に板状の仕切り体(10)(11)が突設形成されて、前記各枠体内にイオン交換体が配置された複数のイオン交換処理部(9)と、
前記イオン交換処理部(9)の上側の前記仕切り体(11)内にそれぞれ設けられた気体流路開閉手段(12)と、
前記本体(1)の底部に設けられた再生液の回収槽(5)と、
前記回収槽(5)にポンプ(17)を介して連結され、前記複数の各イオン交換処理部(9)に対応して設けられた複数の分岐配管(15)と、
前記分岐配管(15)の各々の途中に設けられた開閉弁(14)と、
前記各々の分岐配管(15)の先端であって、前記気体流路開閉手段(12)と前記イオン交換体間に設けられた再生液噴出用ノズル(13)と、
前記本体下部に設けられ被処理気体を供給する気体供給部(3)と、
前記本体上部に設けられ気体を排出する気体排出部(4)と、を具備することを特徴とする排ガス吸収装置である。
【0007】
上記排ガス吸収装置によれば、本体内に配置されるイオン交換処理部は互いに独立した複数部分に分割され並列配置される形態となる。そして各処理部は時間をずらせて順次再生処理をすることができるので、再生処理をしている以外のイオン交換処理部はそのまま運転を継続でき、再生処理中に装置の運転を中断する必要がない。さらに再生中のイオン交換処理部の気体流路開閉手段を閉じることができるので、下流側に再生液ミストが飛散するということはない。その結果、再生時に気体の流速を低下させる必要がなく、処理可能な最大設計流速で気体の処理をすることができる。そのため気体通過面積を小さく設計することもできるので、装置全体の寸法をコンパクトにできる。
【0008】
また分割された形態で密着配置されるイオン交換処理部の数を多くすることにより、1個あたりのイオン交換処理部とその気体通過面積が小さくなるので、再生液の回収槽や移送ポンプの容量も減少するこができる。
さらにイオン交換処理部の数をn個とすると、n−1個のイオン交換処理部の処理能力で装置を設計しておき、いずれのイオン交換処理部のイオン交換体も運転可能状態なときにおいてはn個を同時に運転することも可能となり、その場合には装置全体の処理能力が結果的に一時アップされた運転となる。
【0011】
【発明の実施の形態】
以下、本発明の実施の形態を図面に基づいて説明する。
図1は本発明の排ガス吸収装置を使用して気体の処理を行う説明図である。
図1において、装置の本体1の中央部にイオン交換部2が配置され、下部に処理すべき気体を供給する気体供給部3、上部に処理された気体を本体1から外部に排出する気体排出部4がそれぞれ設けられる。さらに本体1の底部には、再生液の回収槽5が配置される。気体供給部3には外部からの供給配管6が接続され、供給配管6には気体移送用のブロワー7が設けられる。気体排出部4には排出配管8が接続され、その排出配管8の先は図示しないが、例えば処理された気体を使用する装置、2次処理装置または大気放出部などに接続される。
【0012】
イオン交換部2は独立して並列に密着配置された複数(この例では4個)のイオン交換処理部9を備え、各イオン交換処理部9にそれぞれイオン交換体が収容される。それら各イオン交換処理部9における気体供給側(下側)の境界部分に複数の板状の仕切り体10、気体出口側(上側)の境界部分に複数の板状の仕切り体11がそれぞれ設けられ、さらに各イオン交換処理部9の気体出口側にはダンパ等の気体流路開閉手段12が個別に設けられる。なお、この気体流路開閉手段12は空気圧、油圧,電動もしくは電磁式などの駆動手段により遠隔駆動される。
各イオン交換処理部9の気体出口側には、再生液を噴出するノズル13がそれぞれ配置され、それらノズル13は途中に開閉弁14を設けた複数の分岐配管15の先端部と接続されている。これら開閉弁14も空気圧、油圧、電動もしくは電磁式などの駆動手段により遠隔駆動できるようになっている。そして各分岐配管15はポンプ17を設けた再生液配管18により前記回収槽5と接続されている。このノズル13,開閉弁14および分岐配管15により再生液供給手段16が構成される。
【0013】
イオン交換体を収容する各イオン交換処理部2は、例えば複数の枠体を互いに密着して連結し、それを本体1に取り付けたものとすることができる。そして各枠体の内部にイオン交換体を収容するイオン交換体ユニットを着脱可能に装着できるように構成することが望ましい。
イオン交換体としては、この分野で通常使用される繊維状のイオン交換繊維や粒状のイオン交換樹脂などが使用できる。イオン交換繊維は繊維体にイオン交換基を形成させたもので、単位容積あたりの表面積が大きく、イオン交換速度を大きくできるので好ましい。
【0014】
イオン交換体の種類としては、陽イオンとイオン交換作用をする陽イオン交換体と陰イオンとイオン交換作用をする陰イオン交換体があり、被除去物質のイオン形態によってイオン交換体の極性や好ましい交換基の選択が行われる。例えば、気体中に亜硫酸ガスが被除去物質として含まれている場合には、亜硫酸ガスのSO3 2-イオンを自己のOH- イオンと交換する陰イオン交換体が使用される。
イオン交換体に吸着した被除去物質のイオンを離脱させ、イオン交換体を元のイオン形態に再生する再生液としては、吸着したイオンと同じ極性のイオンを有するものが使用される。例えば、イオン交換体に前述のようなSO3 2-イオンが吸着されているときは、カセイソーダ(NaOH)液などが使用される。
【0015】
次に、上記排ガス吸収装置を使用して気体処理を行う方法を説明する。
先ず、排ガス吸収装置の4個のイオン交換処理部9のうち、1個のイオン交換処理部9におけるイオン交換体が再生処理中で、他の3個のイオン交換処理部9で気体処理を行っているとする。この状態では、気体処理している3個のイオン交換処理部9の気体流路開閉手段12は開いた状態になっており、ブロワー7から気体供給部3に導入された気体は、これらイオン交換処理部9を通過する間に含まれる被除去物質がイオン交換体とのイオン交換により除去されて気体排出部4へ排出される。
【0016】
一方、イオン交換体の再生処理を行っているイオン交換処理部9は、その気体流路開閉手段12が閉状態とされ、そのため気体はそのイオン交換処理部9を通過しない。同様に該イオン交換処理部9用の開閉弁14は開状態とされるので、本体1の底部に配置した回収槽5から再生液がポンプ17によりノズル13に供給されて再生処理が行われている。その際、気体流路開閉手段12が上述のように閉状態になっているので、イオン交換体に供給された再生液のミストは下流側には飛散せず回収槽5に落下して回収される。
【0017】
このようにして1個のイオン交換処理部9の再生処理が終了したら、再生処理を必要とする次のイオン交換処理部9の再生処理に切り換える。この切換操作を行うには、先ず再生処理の終了したイオン交換処理部9における開閉弁14を閉じ、次にそこからの再生ミストの飛散のおそれがなくなった時点で気体流路開閉手段12を開ける。これらの操作により、再生の終了したイオン交換処理部9が気体処理状態(運転状態)に移行する。
次に再生処理をすべきイオン交換処理部9の気体流路開閉手段12を閉じ、開閉弁14を開ける。これらの操作により、新たなイオン交換処理部9のイオン交換体の再生処理が開始される。
【0018】
同様な方法により、さらに別のイオン交換処理部9におけるイオン交換体の再生処理を予め定められたスケジュールに従って行う。
このように複数のイオン交換処理部9について時間をずらせて逐次再生処理を行うには、気体流路開閉手段12や開閉弁14の開閉操作およびポンプ17の起動停止操作を手動により行うこともできるが、それらの操作を例えばシーケンサやコンピュータを使用して自動的にプログラム制御することもできる。
【0019】
【発明の効果】
以上のように請求項1に記載された排ガス吸収装置の発明は、処理すべき気体が通過する本体と、その本体内に並列に密着配置された複数のイオン交換処理部と、各イオン交換処理部にそれぞれ設けた気体流路開閉手段と、各イオン交換処理部に収容されるイオン交換体に再生液を個別に供給する複数の再生液供給手段を備えているので、本体内に配置されるイオン交換処理部は互いに独立した複数部分に分割され並列配置される形態となる。そして各処理部は時間をずらせて順次再生処理をすることができるので、再生処理をしている以外のイオン交換処理部はそのまま運転を継続でき、再生処理中に装置の運転を中断する必要がない。
【0020】
さらに再生中のイオン交換処理部の気体流路開閉手段を閉じることができるので、下流側に再生液ミストが飛散するということはない。その結果、再生時に気体の流速を低下させる必要がなく、処理可能な最大設計流速で気体の処理をすることができる。そのため気体通過面積を小さく設計することもできるので、装置全体の寸法をコンパクトにできる。
また、分割された形態で密着配置されるイオン交換処理部の数を多くすることにより、1個あたりのイオン交換処理部とその気体通過面積が小さくなるので、再生液の回収槽や移送ポンプの容量も減少することができる。
【0021】
さらに、本体の底部に再生液の回収槽、下部に処理すべき気体を供給する気体供給部、中間部に複数のイオン交換処理部および上部に処理された気体を排出する気体排出部がそれぞれ配置され、回収槽から各再生液供給手段に再生液を移送する移送手段が設けられるので、装置をよりコンパクトにできると共に、再生処理部分の構成を簡単にできる。
【図面の簡単な説明】
【図1】本発明の排ガス吸収装置を使用して気体の処理を行う説明図。
【符号の説明】
1 本体
2 イオン交換部
3 気体供給部
4 気体排出部
5 回収槽
6 供給配管
7 ブロワー
8 排出配管
9 イオン交換処理部
10 仕切り体
11 仕切り体
12 気体流路開閉手段
13 ノズル
14 開閉弁
15 分岐配管
16 再生液供給手段
17 ポンプ
18 再生液配管
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an exhaust gas absorber that removes a substance to be removed in a gas by an ion exchange method, and a gas treatment method that removes the substance to be removed in a gas using the exhaust gas absorber.
[0002]
[Prior art]
Conventionally, scrubbers have been used to remove substances to be removed such as impurities and contaminants contained in a gas. As such a scrubber, a wet scrubber that sprays a liquid such as water on a gas passing through the main body of the apparatus and absorbs a substance to be removed by the liquid to separate and remove is generally used. However, in recent years, a so-called dry gas scrubber (exhaust gas absorption device), in which a moistened ion exchanger is arranged in the main body and the substance to be removed in the passing gas is removed by ion exchange, has improved operability and processing efficiency. It is attracting attention from the point of.
[0003]
A conventional dry gas scrubber (exhaust gas absorption device) is provided with an ion exchange part that accommodates an ion exchanger in the main body, a gas supply part of a gas to be processed on the upstream side, and a gas discharge part processed on the downstream side Is provided. During normal operation, ion exchange is performed between the substance to be removed and the ion exchanger while the gas introduced from the gas supply part passes through the ion exchange part, and the gas from which the substance to be removed is removed is the gas discharge part. Is discharged from the main body. If the operation is continued for a certain period, the exchange capacity of the ion exchanger decreases, so that the apparatus is temporarily stopped and the regeneration process of the ion exchanger is performed. The regeneration process is performed by flowing the regeneration solution through the ion exchanger, and the ions to be removed that have been chemically adsorbed (ion-bonded) are removed by ion exchange with the regeneration solution. Regenerated based on.
[0004]
[Problems to be solved by the invention]
However, the conventional method has a problem that the operation of the apparatus must be temporarily interrupted when the ion exchanger is regenerated. In order to avoid this, there is an alternate operation method as a conventional method. In this system, while two apparatuses are installed and one apparatus is operating, the ion exchanger of the other apparatus is regenerated. However, this method causes another problem that the installation cost and the operation cost increase because two apparatuses are provided.
[0005]
Next, as a method of installing only one apparatus and performing the regeneration process of the ion exchanger without interrupting the operation, a method of performing the regeneration process in parallel during the operation can be considered. However, when this method is adopted, it is necessary to install a means for removing the regenerated liquid mist accompanying the gas accompanying the regeneration process and scattered downstream, for example, a mist separator (demister), etc., so that the apparatus becomes large. (In particular, the height is increased) and the installation cost is also high. Further, during the regeneration period, it is necessary to operate by reducing the gas flow rate to such an extent that the regeneration liquid mist can be captured.
Therefore, an object of the present invention is to provide an exhaust gas absorbing device that solves these problems and a gas treatment method using the same.
[0006]
[Means for Solving the Problems]
The invention according to claim 1 for solving the above-described problem is an exhaust gas absorption apparatus for removing a substance to be removed in a gas by ion exchange .
A body (1) through which the gas to be treated passes,
A plurality of frames closely connected to each other in the main body (1), and plate-like partition bodies (10) and (11) projectingly formed at the upper and lower ends of each of the frames, A plurality of ion exchange processing units (9) in which ion exchangers are arranged in the frame ;
The upper side of the partition member of the ion exchange treatment unit (9) respectively provided with gas passage opening and closing means in (11) (12),
A regeneration liquid recovery tank (5) provided at the bottom of the main body (1);
A plurality of branch pipes (15) connected to the recovery tank (5) via a pump (17) and provided corresponding to each of the plurality of ion exchange treatment units (9),
An on-off valve (14) provided in the middle of each of the branch pipes (15),
Regeneration liquid ejection nozzle (13) provided at the tip of each branch pipe (15), between the gas flow path opening / closing means (12) and the ion exchanger,
A gas supply section (3) for supplying a gas to be processed provided in the lower part of the main body;
An exhaust gas absorbing device comprising: a gas exhaust part (4) provided at an upper part of the main body and configured to exhaust gas .
[0007]
According to the exhaust gas absorbing device, the ion exchange processing unit arranged in the main body is divided into a plurality of parts independent of each other and arranged in parallel. Since each processing unit can sequentially perform regeneration processing at different times, the ion exchange processing units other than the regeneration processing can continue to operate as they are, and it is necessary to interrupt the operation of the apparatus during the regeneration processing. Absent. Furthermore, since the gas flow path opening / closing means of the ion exchange processing unit being regenerated can be closed, the regenerated liquid mist will not be scattered downstream. As a result, it is not necessary to reduce the gas flow rate during regeneration, and the gas can be processed at the maximum design flow rate that can be processed. Therefore, since the gas passage area can be designed to be small, the overall size of the apparatus can be made compact.
[0008]
Also, by increasing the number of ion exchange processing units arranged in close contact with each other in a divided form, the ion exchange processing unit and its gas passage area are reduced, so the capacity of the regeneration liquid recovery tank and transfer pump Can also be reduced.
Further, when the number of ion exchange processing units is n, the apparatus is designed with the processing capacity of n-1 ion exchange processing units, and the ion exchangers of any ion exchange processing units are in an operable state. It is also possible to operate n at the same time. In this case, the processing capacity of the entire apparatus is consequently temporarily increased.
[0011]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
FIG. 1 is an explanatory view for treating a gas using the exhaust gas absorbing device of the present invention.
In FIG. 1, the ion exchange part 2 is arrange | positioned in the center part of the main body 1 of the apparatus, the gas supply part 3 which supplies the gas which should be processed to the lower part, and the gas discharge which discharges the gas processed from the upper part to the exterior from the main body 1 Each part 4 is provided. Further, a recovery liquid recovery tank 5 is disposed at the bottom of the main body 1. An external supply pipe 6 is connected to the gas supply unit 3, and a gas transfer blower 7 is provided in the supply pipe 6. A discharge pipe 8 is connected to the gas discharge section 4, and the tip of the discharge pipe 8 is connected to, for example, a device that uses the processed gas, a secondary processing apparatus, or an atmospheric discharge section, although not shown.
[0012]
The ion exchange unit 2 includes a plurality of (in this example, four) ion exchange processing units 9 arranged in close contact independently, and each ion exchange processing unit 9 accommodates an ion exchanger. A plurality of plate-like partition bodies 10 are provided at the gas supply side (lower side) boundary portions of the respective ion exchange processing sections 9, and a plurality of plate-like partition bodies 11 are provided at the gas outlet side (upper side) boundary portions, respectively. Furthermore, gas flow path opening / closing means 12 such as a damper is individually provided on the gas outlet side of each ion exchange processing unit 9. The gas flow path opening / closing means 12 is remotely driven by pneumatic, hydraulic, electric or electromagnetic driving means.
On the gas outlet side of each ion exchange processing unit 9, nozzles 13 for ejecting the regenerating liquid are respectively arranged, and these nozzles 13 are connected to the front ends of a plurality of branch pipes 15 provided with on-off valves 14 in the middle. . These on-off valves 14 can also be remotely driven by a driving means such as pneumatic, hydraulic, electric or electromagnetic. Each branch pipe 15 is connected to the recovery tank 5 by a regenerating liquid pipe 18 provided with a pump 17. The nozzle 13, the on-off valve 14 and the branch pipe 15 constitute a regenerating liquid supply means 16.
[0013]
Each ion exchange processing unit 2 that accommodates the ion exchanger may be configured such that, for example, a plurality of frames are in close contact with each other and attached to the main body 1. And it is desirable to comprise so that the ion exchanger unit which accommodates an ion exchanger in each frame can be mounted | worn detachably.
As the ion exchanger, a fibrous ion exchange fiber or a granular ion exchange resin usually used in this field can be used. The ion exchange fiber is preferably formed by forming an ion exchange group on a fibrous body, has a large surface area per unit volume, and can increase the ion exchange rate.
[0014]
The types of ion exchangers include cation exchangers that exchange ions with cations and anion exchangers that exchange ions with anions. Depending on the ion form of the substance to be removed, the polarity of the ion exchanger is preferable. Exchange group selection is made. For example, when sulfurous acid gas is contained as a substance to be removed in the gas, an anion exchanger that exchanges SO 3 2− ions of sulfurous acid gas with its own OH ions is used.
As a regenerating liquid that desorbs ions of the substance to be removed adsorbed on the ion exchanger and regenerates the ion exchanger to the original ion form, a regenerating liquid having the same polarity as the adsorbed ions is used. For example, when SO 3 2- ions as described above are adsorbed on the ion exchanger, a caustic soda (NaOH) solution or the like is used.
[0015]
Next, a method for performing gas treatment using the exhaust gas absorber will be described.
First, among the four ion exchange treatment units 9 of the exhaust gas absorption device, the ion exchanger in one ion exchange treatment unit 9 is in the regeneration process, and the other three ion exchange treatment units 9 perform gas treatment. Suppose that In this state, the gas flow path opening / closing means 12 of the three ion exchange processing units 9 that are performing gas processing are in an open state, and the gas introduced from the blower 7 into the gas supply unit 3 The substance to be removed while passing through the processing unit 9 is removed by ion exchange with the ion exchanger and is discharged to the gas discharge unit 4.
[0016]
On the other hand, in the ion exchange processing unit 9 performing the regeneration process of the ion exchanger, the gas flow path opening / closing means 12 is closed, so that the gas does not pass through the ion exchange processing unit 9. Similarly, since the on-off valve 14 for the ion exchange processing unit 9 is opened, the regeneration liquid is supplied from the recovery tank 5 arranged at the bottom of the main body 1 to the nozzle 13 by the pump 17 to perform the regeneration process. Yes. At that time, since the gas flow path opening / closing means 12 is closed as described above, the mist of the regenerated liquid supplied to the ion exchanger does not scatter to the downstream side and falls into the recovery tank 5 and is recovered. The
[0017]
When the regeneration process of one ion exchange processing unit 9 is completed in this way, the process is switched to the regeneration process of the next ion exchange processing unit 9 that requires the regeneration process. In order to perform this switching operation, first, the opening / closing valve 14 in the ion exchange processing unit 9 after the regeneration process is closed, and then the gas flow path opening / closing means 12 is opened when there is no possibility of the regeneration mist scattering from there. . By these operations, the ion exchange processing unit 9 that has been regenerated moves to the gas processing state (operating state).
Next, the gas flow path opening / closing means 12 of the ion exchange processing section 9 to be regenerated is closed, and the opening / closing valve 14 is opened. By these operations, the regeneration process of the ion exchanger of the new ion exchange processing unit 9 is started.
[0018]
By the same method, the regeneration process of the ion exchanger in still another ion exchange processing unit 9 is performed according to a predetermined schedule.
As described above, in order to sequentially perform the regeneration process by shifting the time for the plurality of ion exchange processing units 9, the gas channel opening / closing means 12 and the opening / closing valve 14 can be manually opened and closed and the pump 17 can be started and stopped manually. However, these operations can be automatically program-controlled using, for example, a sequencer or a computer.
[0019]
【The invention's effect】
As described above, the invention of the exhaust gas absorbing device described in claim 1 includes a main body through which a gas to be processed passes, a plurality of ion exchange treatment units arranged in close contact in parallel within the main body, and each ion exchange treatment. Gas passage opening / closing means provided in each part and a plurality of regenerative liquid supply means for individually supplying regenerative liquids to the ion exchangers accommodated in each ion exchange processing part. The ion exchange processing unit is divided into a plurality of parts independent of each other and arranged in parallel. Since each processing unit can sequentially perform regeneration processing at different times, the ion exchange processing units other than the regeneration processing can continue to operate as they are, and it is necessary to interrupt the operation of the apparatus during the regeneration processing. Absent.
[0020]
Furthermore, since the gas flow path opening / closing means of the ion exchange processing unit being regenerated can be closed, the regenerated liquid mist will not be scattered downstream. As a result, it is not necessary to reduce the gas flow rate during regeneration, and the gas can be processed at the maximum design flow rate that can be processed. Therefore, since the gas passage area can be designed to be small, the overall size of the apparatus can be made compact.
In addition, by increasing the number of ion exchange processing units arranged in close contact with each other in a divided form, the ion exchange processing unit and its gas passage area are reduced, so that the regeneration liquid recovery tank and transfer pump Capacity can also be reduced.
[0021]
Furthermore, a regenerative liquid recovery tank is provided at the bottom of the main body, a gas supply unit for supplying gas to be processed at the lower part, a plurality of ion exchange processing parts at the intermediate part, and a gas discharge part for discharging the processed gas at the upper part In addition, since the transfer means for transferring the regeneration liquid from the recovery tank to each regeneration liquid supply means is provided, the apparatus can be made more compact and the configuration of the regeneration processing part can be simplified.
[Brief description of the drawings]
BRIEF DESCRIPTION OF DRAWINGS FIG. 1 is an explanatory diagram for performing gas treatment using an exhaust gas absorption apparatus of the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Main body 2 Ion exchange part 3 Gas supply part 4 Gas discharge part 5 Recovery tank 6 Supply pipe 7 Blower 8 Discharge pipe 9 Ion exchange processing part 10 Partition body 11 Partition body 12 Gas flow path opening / closing means 13 Nozzle 14 On-off valve 15 Branch pipe 16 Regenerating liquid supply means 17 Pump 18 Regenerating liquid piping

Claims (1)

気体中の被除去物質をイオン交換により除去する排ガス吸収装置において、
処理すべき気体が通過する本体(1) と、
該本体(1)内に互いに密接して連結された複数の枠体と、これら枠体の各々の上端ならびに下端に板状の仕切り体(10)(11)が突設形成されて、前記各枠体内にイオン交換体が配置された複数のイオン交換処理部(9)と、
前記イオン交換処理部(9)の上側の前記仕切り体(11)内にそれぞれ設けられた気体流路開閉手段(12)と、
前記本体(1)の底部に設けられた再生液の回収槽(5)と、
前記回収槽(5)にポンプ(17)を介して連結され、前記複数の各イオン交換処理部(9)に対応して設けられた複数の分岐配管(15)と、
前記分岐配管(15)の各々の途中に設けられた開閉弁(14)と、
前記各々の分岐配管(15)の先端であって、前記気体流路開閉手段(12)と前記イオン交換体間に設けられた再生液噴出用ノズル(13)と、
前記本体下部に設けられ被処理気体を供給する気体供給部(3)と、
前記本体上部に設けられ気体を排出する気体排出部(4)と、を具備することを特徴とする排ガス吸収装置。
In the exhaust gas absorption device that removes the substance to be removed in the gas by ion exchange,
A body (1) through which the gas to be treated passes,
A plurality of frames closely connected to each other in the main body (1), and plate-like partition bodies (10) and (11) projectingly formed at the upper and lower ends of each of the frames, A plurality of ion exchange processing units (9) in which ion exchangers are arranged in the frame ;
The upper side of the partition member of the ion exchange treatment unit (9) respectively provided with gas passage opening and closing means in (11) (12),
A regeneration liquid recovery tank (5) provided at the bottom of the main body (1);
A plurality of branch pipes (15) connected to the recovery tank (5) via a pump (17) and provided corresponding to each of the plurality of ion exchange treatment units (9),
An on-off valve (14) provided in the middle of each of the branch pipes (15),
Regeneration liquid ejection nozzle (13) provided at the tip of each branch pipe (15), between the gas flow path opening / closing means (12) and the ion exchanger,
A gas supply section (3) for supplying a gas to be processed provided in the lower part of the main body;
An exhaust gas absorbing device , comprising: a gas discharge unit (4) provided at an upper portion of the main body and configured to discharge gas .
JP08796698A 1998-03-17 1998-03-17 Exhaust gas absorber Expired - Fee Related JP4357606B2 (en)

Priority Applications (1)

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JP08796698A JP4357606B2 (en) 1998-03-17 1998-03-17 Exhaust gas absorber

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Application Number Priority Date Filing Date Title
JP08796698A JP4357606B2 (en) 1998-03-17 1998-03-17 Exhaust gas absorber

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JP4357606B2 true JP4357606B2 (en) 2009-11-04

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Publication number Priority date Publication date Assignee Title
TWI253951B (en) * 2002-05-14 2006-05-01 Korea M A T Co Ltd Gas scrubber with a device for using ion exchange fiber
CN113713585B (en) * 2021-09-15 2023-10-24 安徽紫朔环境工程技术有限公司 Flue gas desulfurization and denitrification device and desulfurization and denitrification method thereof

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