JPS5898121A - Gas washing apparatus - Google Patents

Gas washing apparatus

Info

Publication number
JPS5898121A
JPS5898121A JP56195051A JP19505181A JPS5898121A JP S5898121 A JPS5898121 A JP S5898121A JP 56195051 A JP56195051 A JP 56195051A JP 19505181 A JP19505181 A JP 19505181A JP S5898121 A JPS5898121 A JP S5898121A
Authority
JP
Japan
Prior art keywords
liquid
tower bottom
cleaning
bottom liquid
specific gravity
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.)
Granted
Application number
JP56195051A
Other languages
Japanese (ja)
Other versions
JPS629366B2 (en
Inventor
Naotoshi Matsunaga
松永 直利
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.)
Mitsubishi Electric Corp
Original Assignee
Mitsubishi Electric Corp
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 Mitsubishi Electric Corp filed Critical Mitsubishi Electric Corp
Priority to JP56195051A priority Critical patent/JPS5898121A/en
Publication of JPS5898121A publication Critical patent/JPS5898121A/en
Publication of JPS629366B2 publication Critical patent/JPS629366B2/ja
Granted legal-status Critical Current

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  • Treating Waste Gases (AREA)
  • Separation Of Particles Using Liquids (AREA)

Abstract

PURPOSE:To provide the titled apparatus carrying out the renewal of a washing liquid easily and properly, by detecting that the specific gravity of a tower bottom liquid reaches a predetermined value or more by a densitometer for monitoring the specific gravity of the tower bottom liquid attached to a scrubbing tower to operate a washing liquid renewing apparatus. CONSTITUTION:When the specific gravity of a tower bottom liquid 3 reaches a set value or more, a densitometer 22 transmits the detected value to a scrubbing liquid renewing apparatus 16 through a line 23 and the apparatus 16 performs the renewal operation of the tower bottom liquid 3 by the input signal therefrom. That is, a solenoid valve 20 is closed through a power line 19 and a solenoid valve 18 is opened through a power line 17 to carry out the discharge of the tower bottom liquid 3. In this case, a level gauge 14 detects such a state that the level of the tower bottom liquid 3 is lowered to a definite level through a signal line 15 to close the valve 18. At this time, a valve 20 is opened to supply a replenishing water 12 through a liquid level controller 19 to return the liquid amount of the tower bottom liquid 3 to the original amount. The tower bottom liquid 3 is diluted by this operation and NaClO (purifying chemical agent) is injected corresponding to the diluted position of said chemical agent by operating a concn. controller 8 to raise the concn. of the chemical agent to set concn. and the renewal operation of the tower bottom liquid 3 is completed.

Description

【発明の詳細な説明】 この発明は、薬gを含む溶液を洗浄液として循環洗浄す
るガス洗浄装置、特にバッチ法にて洗浄液の更新を行う
ガス洗浄装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a gas cleaning device that circulates and cleans a solution containing a drug G as a cleaning liquid, and particularly to a gas cleaning device that renews the cleaning liquid by a batch method.

従来この種の装置として第1図に示すものがあった。第
1図は従来のガス洗浄装置を示すフロー図であシ、図に
おいて、(1)は洗浄塔、(2)はこの洗浄塔内に設け
らnた気液液8!l!を行わせるための充填物層、(3
+はこの充填物層の底に貯留さnる塔底液、+41およ
び(5)は被処理ガスの流入方向および処理ガスの流出
方向を示す矢印、(6)はデミスタ−1(7)は塔底液
t3+を罰記充横物層(21上に循環させる循環ポンプ
、(8)は塔底液(3)の次亜塩素酸ナトリウムの濃度
全調節する濃度調節計、(9)は循環液に薬液を注入す
る薬注ポンプ、001は薬液タンク、01)は薬注ポン
プ(9)用の動力線、(121は洗浄塔(IIへ供給さ
扛る補給水、03)は塔底液(31のg量を一定に惺つ
ための液面調節側で、補給水02+の補給量を調節する
A conventional device of this type is shown in FIG. FIG. 1 is a flow diagram showing a conventional gas cleaning device. In the figure, (1) is a cleaning tower, and (2) is a gas-liquid-liquid 8! installed in this cleaning tower. l! A filling layer for carrying out (3
+ indicates the bottom liquid stored at the bottom of this packed layer, +41 and (5) indicate arrows indicating the inflow direction of the gas to be treated and the outflow direction of the process gas, (6) indicates the demister-1 (7). A circulation pump that circulates the bottom liquid t3+ over the horizontal layer (21), (8) a concentration controller that adjusts the total concentration of sodium hypochlorite in the bottom liquid (3), and (9) a circulation pump. A chemical dosing pump that injects a chemical into the liquid, 001 is a chemical tank, 01) is a power line for the chemical dosing pump (9), (121 is make-up water supplied to the washing tower (II), 03 is a bottom liquid (Adjust the amount of replenishment water 02+ on the liquid level adjustment side to maintain a constant g amount of 31.

(141は塔底液(31のレベルゲージ、(國は信号線
、(IQは洗浄液更新装置、aηはt磁弁QSの開閉を
制御するための動力線で、洗浄液更新装置(則よ)出力
する。
(141 is the tower bottom liquid (level gauge of 31), (country is the signal line, (IQ is the cleaning liquid renewal device, aη is the power line for controlling the opening and closing of the t magnetic valve QS, and the output of the cleaning liquid renewal device (as a rule) do.

C9は補給水(121用の電磁弁(20)の開閉を制御
するための動力線で、同じく洗浄液更新装#(IQよ多
出力する。(21)は洗浄塔(1)から排出さnるドレ
ンである。
C9 is a power line for controlling the opening and closing of the solenoid valve (20) for make-up water (121), which also outputs more than the cleaning fluid renewal unit # (IQ). It's a drain.

次に動作について説明する。洗浄塔(11内に圧送また
は吸引さnfc被処理ガスは、矢印+41の方向に充填
物層(2)内金通過する間に、循環ポンプ(71によシ
送ら扛噴霧さ扛、充填物層(2)を流下する洗浄液と気
液接触し、被処理ガス中の有害成分等は洗浄液中に吸収
除去さnる。
Next, the operation will be explained. The NFC gas to be treated is pumped or sucked into the cleaning tower (11) while passing through the inner layer of the packing layer (2) in the direction of arrow +41, while being sent to the circulation pump (71) and sprayed into the packing layer. (2) comes into gas-liquid contact with the flowing cleaning liquid, and harmful components in the gas to be treated are absorbed and removed by the cleaning liquid.

ここで塔底液(3)は被処理ガスを洗浄する過程で水分
の一部が蒸発し、徐々に液量が減少するので、こnを防
止するため、液面調節計(13)を介して補給水(12
1を注入し、常にg量を一定に保持している。
Here, part of the moisture in the tower bottom liquid (3) evaporates during the process of cleaning the gas to be treated, and the liquid volume gradually decreases. make-up water (12
1 was injected, and the g amount was always kept constant.

また塔底Q(3+中の薬剤も有害成分等を吸収除去する
過程で消失して行くので、循環ポンプ(7)で圧送さT
′した洗浄液の一部を濃度調節計(8)に導き、塔底液
(3+中の次亜塩素酸ナトリウムの濃度をモニターし、
薬液タンクQOI内の次亜塩素酸ナトリウム原液の注入
量を薬注ポンプ(9)の起動停止によ多制御して、塔底
液(3)の次亜塩素酸ナトリウムを一定濃度に保持する
In addition, the chemicals in the bottom Q (3+) also disappear during the process of absorbing and removing harmful components, so the circulation pump (7) pumps the chemicals into the T
A part of the washed washing liquid is led to the concentration controller (8), and the concentration of sodium hypochlorite in the tower bottom liquid (3+) is monitored.
The injection amount of the sodium hypochlorite stock solution in the chemical tank QOI is controlled by starting and stopping the chemical injection pump (9), and the sodium hypochlorite in the tower bottom liquid (3) is maintained at a constant concentration.

さてここでし尿処理場や下水処理場の各処理工程から排
出される臭気成分の洗浄除去の場合について説明する。
Now, the case of cleaning and removing odor components discharged from each treatment process of a human waste treatment plant or a sewage treatment plant will be explained.

この場合、被処理ガス中の臭気成分、すなわちアンモニ
ア、硫化水素、メチルメルカプタン、硫化メチル、二硫
化メチル等の各臭気成分は、充填物層(2)内を通過す
る間に次亜塩素酸す) IJウム全含む洗浄液と気液接
触して吸収除去さrしるが、この時の化学反応は次式で
示さnる。
In this case, each odor component in the gas to be treated, that is, ammonia, hydrogen sulfide, methyl mercaptan, methyl sulfide, methyl disulfide, etc., is absorbed by hypochlorous acid while passing through the packed layer (2). ) It is absorbed and removed by contacting with a cleaning solution containing all IJium, and the chemical reaction at this time is shown by the following equation.

2NH3+3NaC40−+ N2+3NaCl+3H
203H2S +6N a CI O+、2N aOH
−+Na 2 Sot + 6Na C1l +2 S
 +4H20CH3SH+3Na(JO+NaOH−+
 CH35o3Na +3NaCA! 十H20(CH
s ) S +NaC,d O→(CHs ) So 
十NaC1(CH3)2S2 +5NaClO+ 2N
 aOH−+ 2CH3S O3N a+5Nacl十
H20このようにして被処理ガス中の臭気は充填物層(
2+内で洗浄除去され、さらにデミスタ−(61を通過
して同伴する洗浄液ミストを除去さ几た後、処理ガスと
して洗浄塔(11よシ矢印(51のように排出される。
2NH3+3NaC40-+ N2+3NaCl+3H
203H2S +6N a CI O+, 2N aOH
−+Na 2 Sot + 6Na C1l +2 S
+4H20CH3SH+3Na(JO+NaOH-+
CH35o3Na +3NaCA! 10H20 (CH
s ) S + NaC, d O → (CHs ) So
10NaCl(CH3)2S2 +5NaClO+ 2N
aOH-+ 2CH3S O3N a+5Nacl+H20 In this way, the odor in the gas to be treated is removed from the packing layer (
2+, and further passes through a demister (61) to remove the accompanying cleaning liquid mist, and then is discharged as a process gas through a cleaning tower (11) as shown by an arrow (51).

一方洗浄液による吸収除去で生成した硫酸ナトリウム、
メタンスルホン酸ナトリウム、ジメチルスルホキシドや
、上記臭気成分除去のために作用した次亜塩素酸す) 
IJウムの老廃化物賀である塩化ナトリウム等は洗浄液
中に残り、徐々に蓄積ζnることになる。ここで洗浄液
がアルカリ性であると、被処理ガス中の炭酸ガスも次式
に従って吸収さn1洗浄数中に炭酸塩類として蓄積さn
る。
On the other hand, sodium sulfate produced by absorption and removal by the cleaning solution,
Sodium methanesulfonate, dimethyl sulfoxide, and hypochlorous acid that acts to remove the above-mentioned odor components)
Sodium chloride and the like, which are waste products of IJ, remain in the cleaning solution and gradually accumulate. Here, if the cleaning liquid is alkaline, carbon dioxide gas in the gas to be treated is also absorbed according to the following formula, and is accumulated as carbonates during n1 cleanings n
Ru.

CO2+ NaOH−+ NaHCO3CO2+2Na
OH−+ Na2CO3+H20第2図はこの種の洗1
’41塔のfk′、浄液中に見らnる代表的な反応生成
物の溶解度曲線を示したものである。各物餉により溶解
度が異なシー概にはいえないが、第2図より、’cnぞ
nの成分濃度が常温付近でFi8〜20(Wt係)、0
℃付近では4〜7(wt%〕を越えると、溶質が析出し
、各部で閉塞などのトラブルが発生することが予想式n
る。このため洗浄液の定期的な更新が必要となる。
CO2+ NaOH-+ NaHCO3CO2+2Na
OH-+ Na2CO3+H20 Figure 2 shows this type of washing 1
The fk' of the '41 column shows the solubility curve of typical reaction products found in the purified liquid. Although it is difficult to generalize that the solubility differs depending on each substance, from Figure 2, the concentration of the component of 'CNZON is around room temperature, Fi8~20 (Wt), 0.
If the concentration exceeds 4 to 7 (wt%) near ℃, the solute will precipitate and problems such as clogging will occur in various parts, according to the predicted formula n.
Ru. For this reason, it is necessary to periodically renew the cleaning liquid.

従来は洗浄液の更新を行うために洗浄液更新装置(16
)が定期的に作動しこfLを実行していた。すなわち予
めセットさnた時間に達した所で、洗浄液更新装置(1
6)より出力さnた動力が動力線0′7)を介して電磁
弁(国を開き塔底fi (31がドレンQυよシ排出さ
れる。そしてこfLを同時にそntで動力線a9に通じ
ていた動力が停止して電磁弁(20)を閉じ、補給水(
+21の給水が1筐す、塔底* (3+の排出を容易に
する。
Conventionally, a cleaning liquid renewal device (16
) was activated periodically to execute fL. In other words, when the preset time is reached, the cleaning fluid renewal device (1
6) The power output from the tower opens the solenoid valve (fi (31) through the power line 0'7) and is discharged through the drain Qυ.Then, this fL is simultaneously connected to the power line a9 by the The power that was flowing stopped, the solenoid valve (20) was closed, and the makeup water (
One case of +21 water supply at the bottom of the tower* (facilitates the discharge of 3+.

セして塔底W (31のレベルが一定の深さ1で下がっ
た所で、レベルゲージ04)によシこf′Lヲ検知し、
信号線(国により洗?¥Ig更新・装置α旬に伝えて、
電磁弁a樽を開いた動力が停止し、逆に電磁弁(20)
は再び動力が与えら汎て開かれる。そして再び液面調節
計Q31ffi介して給水が行わ扛、元のレベル筐で水
位が上昇した所で補給水圓が止する。このようにして、
従来は塔底液(3+を補給水(121で希釈して洗浄液
の更新を行っていた。
At the point where the level of the tower bottom W (31 has dropped to a certain depth 1), the level gauge 04 detects the bottom f'L,
Signal line (depending on the country?\Ig update/device α)
The power that opened the solenoid valve a barrel stops, and the solenoid valve (20)
is re-energized and unfolds. Then, water is supplied again via the liquid level controller Q31ffi, and the supply of water stops when the water level rises at the original level box. In this way,
Conventionally, the washing liquid was renewed by diluting the column bottom liquid (3+) with make-up water (121).

従来のガス洗浄装置は以上のように構成されているので
、塔底液(3+の更新間隔は予め机上計算によシ予測す
るとともに、試運転により確認した上で、なおかつよシ
安全側に設定し、更新間隔を短くする必要があった。こ
のため更新間隔の設定に手間どる上に、その設定をよシ
安全側にするため、不必要に薬液を排出し、薬液の浪費
を招くという欠点があった。
Conventional gas cleaning equipment is configured as described above, so the update interval for the tower bottom liquid (3+) can be predicted in advance through theoretical calculations, confirmed through trial runs, and set to be on the safe side. Therefore, it was necessary to shorten the update interval.As a result, it took time to set the update interval, and in order to set the update interval on the safer side, the chemical solution was discharged unnecessarily, resulting in wasted chemical solution. there were.

この発明は上記のような従来のものの欠点を除去するた
めになさlt″したもので、洗浄塔に塔底液の比重全モ
ニターする比重計を取りつけ、この比重計によシ塔底液
比重が設定値以上になった所で洗浄液更新装置を働かせ
ることによシ、容易にかつ連接に洗浄液更新が行えるガ
ス洗浄装置を提供することを目的としている。
This invention was made in order to eliminate the above-mentioned drawbacks of the conventional ones.The washing tower is equipped with a hydrometer that monitors the total specific gravity of the bottom liquid, and this hydrometer measures the specific gravity of the bottom liquid. It is an object of the present invention to provide a gas cleaning device that can easily and continuously renew the cleaning fluid by operating the cleaning fluid renewal device when the gas exceeds a set value.

以下この発明の一実施例を図について説明する。An embodiment of the present invention will be described below with reference to the drawings.

第3図はこの発明の一実施例によるガス洗浄装置全示す
フロー図であシ、図において、(1)ないし帆は第1図
と同−寸たけ相当部分を示す。(221は塔底i +3
1の比重の変化全モニターするための比重計、(ハ)は
この比重計によシ塔底g(3+が予め設定さrした比重
以上になったことを検知して洗浄液更新装置06)へ伝
達するための信号線である。
FIG. 3 is a flowchart showing the entire gas cleaning apparatus according to an embodiment of the present invention. In the figure, (1) or sail indicates a portion corresponding to the same size as that in FIG. 1. (221 is the bottom i + 3
The hydrometer (c) is used to monitor all changes in the specific gravity of 1. (c) is sent to the bottom of the column g (when it detects that the specific gravity of 3+ has exceeded the preset r value, it is sent to the washing liquid renewal device 06). This is a signal line for transmission.

洗浄液中に生成する代表的な反応生成物のそnぞnの水
溶is:度とその溶液比重の関係を第4図に示す。第4
図よυ明らかなように、し尿処理場や下水処理場より排
出さ几る臭気を次亜塩素酸ナトリウム洗浄にて吸収除去
した際に、洗浄液中に生成する代表的な反応生成物の溶
液比重は、1〜10チの濃度範囲においてはそ扛ぞf′
L直線関係にあシ、また各成分の同一比重を示すそ九ぞ
nの水溶液濃度は、中間値に対して±20チ前後に収す
ることかわかる。例えば溶液比重1.04を示す水溶液
濃度の最小は炭酸ナトリウムの4.2チであシ、溶液比
重1.04を示す水溶fi濃度の最大は塩化ナトリウム
の6%である。従ってその中間値は5.1チとなシ、そ
れぞnの水溶液濃度はその中間値5.1優に対して±0
9%の濃度範囲にあることになる。
FIG. 4 shows the relationship between the aqueous solubility of typical reaction products produced in the cleaning solution and the specific gravity of the solution. Fourth
As is clear from the figure, when the odor discharged from human waste treatment plants and sewage treatment plants is absorbed and removed by sodium hypochlorite cleaning, the solution specific gravity of the typical reaction products generated in the cleaning solution. is so f' in the concentration range of 1 to 10.
It can be seen that the concentration of the aqueous solution, which has a linear relationship with L and shows the same specific gravity of each component, falls within ±20 degrees of the intermediate value. For example, the minimum aqueous solution concentration exhibiting a solution specific gravity of 1.04 is 4.2% of sodium carbonate, and the maximum aqueous solution concentration exhibiting a solution specific gravity of 1.04 is 6% of sodium chloride. Therefore, the intermediate value is 5.1, and the aqueous solution concentration of each n is ±0 with respect to the intermediate value of 5.1.
This results in a concentration range of 9%.

このように同−比重全示すそnぞnの水溶液濃度は中間
値5.1%に対して±20%の幅の中に収する。従って
これを利用Tnば、洗浄後の比重を計測することで浴液
中の各成分の平均濃度を知る仁とができ、それによシ洗
浄液の更新時期を的確に知ることができる。
In this way, the concentration of each aqueous solution exhibiting the same specific gravity falls within a range of ±20% with respect to the median value of 5.1%. Therefore, if this is utilized, it is possible to know the average concentration of each component in the bath liquid by measuring the specific gravity after cleaning, and it is thereby possible to accurately know when to renew the cleaning liquid.

第3図において比重計(221は塔底m (31の溶液
比重が設定値以上になれば、そnを信号線(23)を介
して洗浄液更新装置0句へ伝達する。その入力信号にょ
シ洗浄液更新装置06)は塔底ff (31の更新操作
を実行する。、すなわち動力線(1ωを介して電磁弁C
aを閉じるとともに動力線(1ηを介して電磁弁08)
を開いて塔底液(3,の排出を行う。そして塔底m (
3+面がある一定レベル1で下がったことをレベルゲー
ジ(14)により信号線Q51を介して検知し、電磁弁
[+8)を閉じるとともに電磁弁(20e開いて補給水
面の供給を液面調節計03)を介して行い、塔底液(3
+の液量は元にもどる。そして塔底g(3Jが希釈さ九
、次亜塩素酸ナトリウムの希薄となった分は濃度調節計
(8)の働きによシ楽注して、設定画度丑で次亜塩素酸
ナトリウム濃度を上昇させ、塔底wL(3iの更新操作
は完了する。
In Fig. 3, a hydrometer (221) indicates the specific gravity of the solution at the bottom of the tower (m). The cleaning liquid renewal device 06) executes the renewal operation of tower bottom ff (31), that is, the solenoid valve C is connected via the power line (1ω).
Close a and connect the power line (1η to solenoid valve 08)
Open the column bottom liquid (3,
The level gauge (14) detects via the signal line Q51 that the 3+ surface has dropped to a certain level 1, closes the solenoid valve [+8] and opens the solenoid valve (20e) to control the supply of makeup water to the liquid level controller. 03) and the bottom liquid (3
The + liquid level will return to its original level. Then, the tower bottom g (3J is diluted), the diluted amount of sodium hypochlorite is calculated by the action of the concentration controller (8), and the sodium hypochlorite concentration is adjusted to the set rate. The update operation of tower bottom wL (3i is completed.

洗浄液更新装置0ωは比m#(2わよシ信号線f23)
全弁して入力を一度得た債は、−通多更新操作が完了す
る時間を経過しなけnば、角度比重計(221よシの信
号を入力しないような保護回路を設けておき、補給水面
の供給がスムーズに行えるような回路構成を持たせるの
が望ましい。
The cleaning liquid renewal device 0ω is the ratio m# (2 way signal line f23)
Once the input has been obtained through full valve operation, a protection circuit must be installed to prevent the signal from the angular hydrometer (221) from being input until the time for completing the update operation has elapsed. It is desirable to have a circuit configuration that allows smooth supply of water.

なお上記実施例では洗浄液として次亜塩素酸ナトリウム
を用いる洗浄装置について説明したが、こnK限定ざn
るものではなく、他の薬液を用いるガス洗浄装置、例え
ば硫酸、塩酸、水酸化ナトリウム、過酸化水素、過マン
ガン酸カリウム、亜塩素酸ナトリウム、次亜臭素酸ナト
リウム、チオ硫酸ナトリウム等の薬剤を一種以上含む水
浴液を洗浄液とするガス洗浄装置に適用してもよく、上
記実施例と同様の効果を奏する。
In addition, in the above embodiment, a cleaning device using sodium hypochlorite as the cleaning liquid was explained, but this is limited to nK.
gas cleaning equipment that uses other chemical solutions, such as sulfuric acid, hydrochloric acid, sodium hydroxide, hydrogen peroxide, potassium permanganate, sodium chlorite, sodium hypobromite, and sodium thiosulfate. The present invention may be applied to a gas cleaning device that uses a water bath liquid containing one or more types of water bath liquid as a cleaning liquid, and the same effects as those of the above embodiments can be obtained.

また、上記実施例では塔底M (31の浴液比重を自動
計測する方式で説明したが、人手により溶液比重を計測
し、その結果によシ洗浄液更新装置α0を手動で働かせ
てもよく、上記と同様な効果を奏する。
Further, in the above embodiment, the method of automatically measuring the specific gravity of the bath liquid at the bottom of the column M (31) was explained, but the specific gravity of the solution may be measured manually, and based on the results, the washing liquid renewal device α0 may be operated manually. The same effect as above is achieved.

以上のように、この発明によnば、洗浄液の比重を計測
して洗浄液更新を行うようにしたので、従来装置のよう
に不必要に洗浄液を排出することがなくなシ、また洗浄
除去対象成分が予期以上に濃厚となって、反応生成物が
蓄積し、結晶析出によシトラブルを引き起こすようなこ
とがなくなる。
As described above, according to the present invention, since the specific gravity of the cleaning liquid is measured and the cleaning liquid is renewed, the cleaning liquid is not discharged unnecessarily as in the conventional device, and the cleaning liquid is removed by cleaning. This prevents the components from becoming more concentrated than expected, resulting in reaction products accumulating and causing trouble due to crystal precipitation.

さらに補給水も最少量に維持できるため省エネルギーに
も役立つなどの効果がある。
Additionally, the amount of supplementary water can be kept to a minimum, which helps save energy.

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

第1図は従来のガス洗浄装置を示すフロー図、第2図は
し尿臭や下水具を次亜塩素酸ナトリウム洗浄した場合に
洗浄液中に蓄積する反応生成物の溶解度曲線図、第3図
はこの発明の一実施例によるガス洗浄装置を示すフロー
図、第4図は上記洗浄液中に蓄積する反応生成物の水浴
g濃度と溶液比重の関係曲線図である。 図中、(I)は洗浄塔、(2+は充填物層、+31は塔
底液、(4)は被処理ガスの流入方向を示す矢印、(5
Jは処理ガスの流出方向を示す矢印、(6)はデミスタ
−1(711Wは循環ポンプ、(8)は濃度調節計、(
9)は薬注ポンプ、は信号線、(16)は洗浄液更新装
置、(18) 、 (20)は電磁弁、CDはドレン、
(22)は比重計である。 なお、図中、同一符号は同一またけ相当部分を示す。 代理人 為 野 信 −(外1名) (Ill 第2図
Figure 1 is a flow diagram showing a conventional gas cleaning device, Figure 2 is a solubility curve diagram of the reaction products that accumulate in the cleaning solution when sodium hypochlorite is used to clean sewage equipment, and Figure 3 is FIG. 4 is a flowchart showing a gas cleaning apparatus according to an embodiment of the present invention, and is a relationship curve diagram between the water bath g concentration of the reaction product accumulated in the cleaning liquid and the solution specific gravity. In the figure, (I) is a cleaning tower, (2+ is a packed layer, +31 is a bottom liquid, (4) is an arrow indicating the inflow direction of the gas to be treated, (5)
J is an arrow indicating the outflow direction of the processing gas, (6) is demister-1 (711W is a circulation pump, (8) is a concentration controller, (
9) is the chemical injection pump, is the signal line, (16) is the cleaning fluid renewal device, (18) and (20) are the solenoid valves, CD is the drain,
(22) is a hydrometer. In the drawings, the same reference numerals indicate parts corresponding to the same straddle. Agent Shin Tameno - (1 other person) (Ill Figure 2)

Claims (2)

【特許請求の範囲】[Claims] (1)被処理ガス中の有害成分除去用の薬液を含む溶液
を洗浄液として循環洗浄するガス洗浄装置において、前
記洗浄液の比重の変化を検知して洗浄液の更新を行う洗
浄液更新装置を備えたことを特徴とするガス洗浄装置。
(1) A gas cleaning device that circulates and cleans a solution containing a chemical solution for removing harmful components from a gas to be treated as a cleaning liquid, including a cleaning liquid renewal device that detects a change in the specific gravity of the cleaning liquid and updates the cleaning liquid. A gas cleaning device featuring:
(2)洗浄液の比重の変化を検知する比重計と、比重の
変化の検知により自動的に洗浄液の更新を行う洗浄液更
新装置を備えたことを特徴とする特許請求の範囲第1項
記載のガス洗浄装置。 (3+洗浄液は次亜塩素酸ナトリウム、硫酸、塩酸、水
酸化ナトリウム、過酸化水素、過マンガン酸カリウム、
亜塩素酸ナトリウム、次亜臭素酸ナトリウム、およびチ
オ硫酸ナトリウムから選ばnる薬剤を一種以上含む水溶
液であることを特徴とする特許請求の範囲第1項または
第2項記載のガス洗浄装置。
(2) The gas according to claim 1, which is equipped with a hydrometer that detects a change in the specific gravity of the cleaning liquid, and a cleaning liquid renewal device that automatically updates the cleaning liquid by detecting the change in the specific gravity. cleaning equipment. (3+ cleaning solutions include sodium hypochlorite, sulfuric acid, hydrochloric acid, sodium hydroxide, hydrogen peroxide, potassium permanganate,
3. The gas cleaning device according to claim 1 or 2, which is an aqueous solution containing one or more agents selected from sodium chlorite, sodium hypobromite, and sodium thiosulfate.
JP56195051A 1981-12-03 1981-12-03 Gas washing apparatus Granted JPS5898121A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56195051A JPS5898121A (en) 1981-12-03 1981-12-03 Gas washing apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56195051A JPS5898121A (en) 1981-12-03 1981-12-03 Gas washing apparatus

Publications (2)

Publication Number Publication Date
JPS5898121A true JPS5898121A (en) 1983-06-10
JPS629366B2 JPS629366B2 (en) 1987-02-27

Family

ID=16334725

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56195051A Granted JPS5898121A (en) 1981-12-03 1981-12-03 Gas washing apparatus

Country Status (1)

Country Link
JP (1) JPS5898121A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008105141A1 (en) * 2007-02-26 2008-09-04 Mitsubishi Chemical Corporation Method for neutralization of carbonyl chloride
NL2001538C2 (en) * 2008-04-29 2009-10-30 Haaring Beheer B V H Air washer for removing ammonia from ammonia contaminated air produced in intensive livestock stables, has controller to open valve for supplying washing fluid if current value of mass-related parameter exceeds predetermined limit
WO2012117585A1 (en) * 2011-02-28 2012-09-07 三菱重工業株式会社 Co2 recovery device and operation control method of co2 recovery device
WO2019138885A1 (en) * 2018-01-10 2019-07-18 株式会社ジャパンエンジンコーポレーション Water treatment apparatus

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008105141A1 (en) * 2007-02-26 2008-09-04 Mitsubishi Chemical Corporation Method for neutralization of carbonyl chloride
CN102702502A (en) * 2007-02-26 2012-10-03 三菱化学株式会社 Method for neutralization of carbonyl chloride
NL2001538C2 (en) * 2008-04-29 2009-10-30 Haaring Beheer B V H Air washer for removing ammonia from ammonia contaminated air produced in intensive livestock stables, has controller to open valve for supplying washing fluid if current value of mass-related parameter exceeds predetermined limit
WO2012117585A1 (en) * 2011-02-28 2012-09-07 三菱重工業株式会社 Co2 recovery device and operation control method of co2 recovery device
JP2012179520A (en) * 2011-02-28 2012-09-20 Mitsubishi Heavy Ind Ltd Co2 recovery apparatus and method for controlling operation of co2 recovery apparatus
US9084959B2 (en) 2011-02-28 2015-07-21 Mitsubishi Heavy Industries, Ltd. CO2 recovering apparatus and operation control method of CO2 recovering apparatus
WO2019138885A1 (en) * 2018-01-10 2019-07-18 株式会社ジャパンエンジンコーポレーション Water treatment apparatus
JP2019118903A (en) * 2018-01-10 2019-07-22 株式会社ジャパンエンジンコーポレーション Water treatment apparatus
CN111566053A (en) * 2018-01-10 2020-08-21 日本发动机股份有限公司 Water treatment device

Also Published As

Publication number Publication date
JPS629366B2 (en) 1987-02-27

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