JPS61268342A - Method for controlling concentration of hydrogen chloride in exhaust gas - Google Patents

Method for controlling concentration of hydrogen chloride in exhaust gas

Info

Publication number
JPS61268342A
JPS61268342A JP60109250A JP10925085A JPS61268342A JP S61268342 A JPS61268342 A JP S61268342A JP 60109250 A JP60109250 A JP 60109250A JP 10925085 A JP10925085 A JP 10925085A JP S61268342 A JPS61268342 A JP S61268342A
Authority
JP
Japan
Prior art keywords
hydrogen chloride
exhaust gas
amount
concn
concentration
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP60109250A
Other languages
Japanese (ja)
Inventor
Shinseki Itaya
板谷 真積
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.)
Mitsui Engineering and Shipbuilding Co Ltd
Original Assignee
Mitsui Engineering and Shipbuilding Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsui Engineering and Shipbuilding Co Ltd filed Critical Mitsui Engineering and Shipbuilding Co Ltd
Priority to JP60109250A priority Critical patent/JPS61268342A/en
Publication of JPS61268342A publication Critical patent/JPS61268342A/en
Pending legal-status Critical Current

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  • Treating Waste Gases (AREA)

Abstract

PURPOSE:To rapidly control the concn. of hydrogen chloride in exhaust gas, by changing the amount of air for atomizing an alkali solution corresponding to the change in the concn. of residual hydrogen chloride after alkali spraying treatment to change the particle size of the liquid droplets of the alkali solution. CONSTITUTION:Exhaust gas containing hydrogen chloride supplied to a hydrogen chloride removing tower 1 from above is contacted with the alkali solution sprayed from nozzles 2 and taken out from an outlet 5 while hydrogen chloride therein is removed. The concn. of residual hydrogen chloride (a) in exhaust gas at the outlet is measured and, when said concn. rised so as to exceed the prescribed concn., a valve 4 is opened to increase the amount of air supplied to the nozzle 2 and liquid droplets are made minute to be increased in a surface area and the removal capacity of hydrogen chloride is enhanced. At this time, because the concn. and supply amount of the alkali solution 6 are always constant and only the amount of air is changed, correspondence is extremely rapid and operation is also simple.

Description

【発明の詳細な説明】 〔発明の技術分野〕 本発明は排ガス中の塩化水素濃度を制御する方法に関す
る。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to a method for controlling hydrogen chloride concentration in exhaust gas.

〔従来技術〕[Prior art]

近年、都市ゴミ中のプラスチック、特にポリ塩化ビニル
の増加につれて、都ゴミ焼却炉からの燃焼排ガス中の塩
化水素量の増加が問題になっている。
In recent years, as the amount of plastic, particularly polyvinyl chloride, in municipal garbage has increased, the amount of hydrogen chloride in the combustion exhaust gas from municipal garbage incinerators has become a problem.

そこで、かかる排ガス中の塩化水素濃度を低下させるた
めに、排ガス中にアルカリ溶液を噴霧する方法が一般に
採用されている。
Therefore, in order to reduce the hydrogen chloride concentration in the exhaust gas, a method of spraying an alkaline solution into the exhaust gas is generally adopted.

そして、従来のアルカリ溶液を噴霧する方法では、排ガ
ス中の塩化水素濃度、特にアルカリ処理後に塩化水素除
去塔から排出される排ガス中の塩化水素濃度の変化に対
応してアルカリ濃度または噴霧アルカリ溶液量を増減さ
せて、塩化水素除去塔出口の塩化水素濃度を制御してい
た。しかしながら、噴霧アルカリ溶液のアルカリ濃度を
変化させる方法は、操作が煩雑であるうえに、除去塔出
口における排ガス中の塩化水素濃度の変化に迅速に対応
できない欠点があった。また、噴霧アルカリ溶液量を増
減させる方法は、アルカリ溶液のスプレーパターンが変
化して安定した塩化水素除去が行なえず、更に除去塔出
口の排ガス温度も一定しない問題点があった。
In the conventional method of spraying an alkaline solution, the alkali concentration or the amount of atomized alkaline solution is adjusted depending on the hydrogen chloride concentration in the exhaust gas, especially the hydrogen chloride concentration in the exhaust gas discharged from the hydrogen chloride removal tower after the alkali treatment. The hydrogen chloride concentration at the outlet of the hydrogen chloride removal column was controlled by increasing or decreasing the amount of hydrogen chloride. However, the method of changing the alkali concentration of the atomized alkaline solution has the disadvantage that the operation is complicated and that it cannot quickly respond to changes in the hydrogen chloride concentration in the exhaust gas at the outlet of the removal tower. Further, the method of increasing or decreasing the amount of atomized alkaline solution has the problem that the spray pattern of the alkaline solution changes, making it impossible to perform stable hydrogen chloride removal, and furthermore, the temperature of the exhaust gas at the exit of the removal tower is not constant.

〔発明の目的〕[Purpose of the invention]

本発明は、塩化水素除去塔出口における排ガス中の塩化
水素濃度変化に対応する応答が早く、操作が簡単であり
、かつスプレーパターンがほぼ一定した、アルカリ溶液
の噴霧による排ガス中の塩化水素濃度を制御する方法を
提供することを目的とするものである。
The present invention has a quick response to changes in the concentration of hydrogen chloride in the exhaust gas at the outlet of the hydrogen chloride removal tower, is simple to operate, and has a nearly constant spray pattern. The purpose is to provide a method for controlling

〔発明の構成〕[Structure of the invention]

上記目的を達成する°本発明は、塩化水素を含む排ガス
にアルカリ溶液を噴霧して排ガス中の塩化水素濃度を制
御する方法において、前記アルカリ溶液噴霧後の排ガス
中に残存する塩化水素の濃度に対応して前記アルカリ溶
液を噴霧するノズルに供給する空気量を変化させること
を特徴とするものである。    、 以下、本発明を第1図に示す工程図にもとづき説明する
To achieve the above object, the present invention provides a method for controlling the concentration of hydrogen chloride in the exhaust gas by spraying an alkaline solution into the exhaust gas containing hydrogen chloride. The present invention is characterized in that the amount of air supplied to the nozzle that sprays the alkaline solution is changed accordingly. Hereinafter, the present invention will be explained based on the process diagram shown in FIG.

第1図において塩化水素除去塔1には、塩化水素を含む
排ガスが矢印Aに沿って塩化水素除去塔1の上方から供
給され、塩化水素除去塔1内を流下して矢印B方向に取
り出される。
In FIG. 1, exhaust gas containing hydrogen chloride is supplied to the hydrogen chloride removal column 1 from above the hydrogen chloride removal column 1 along arrow A, flows down inside the hydrogen chloride removal column 1, and is taken out in the direction of arrow B. .

塩化水素除去塔1内には、ノズル2が設けられており、
バルブ3を経て供給されたアルカリ溶液6は、このノズ
ル2から排ガスの流下する方向に沿って噴霧される。な
お本発明においては、塩化水素を含む排ガスを塩化水素
除去塔1の下方から上方に向って流し、一方、アルカリ
溶液を除去塔1の上方から下方に噴霧させて、排ガス流
とアルカリ溶液の流れを向流させることもできる。
A nozzle 2 is provided in the hydrogen chloride removal column 1,
The alkaline solution 6 supplied through the valve 3 is sprayed from this nozzle 2 along the direction in which the exhaust gas flows. In the present invention, the exhaust gas containing hydrogen chloride flows upward from the bottom of the hydrogen chloride removal tower 1, and the alkaline solution is sprayed downward from the top of the removal tower 1, thereby controlling the flow of the exhaust gas and the alkaline solution. It is also possible to countercurrent the flow.

ここで本発明においては、ノズル2からのアルカリ溶液
噴霧量は常に一定に保持され、かつアルカリ溶液に省け
るアルカリ濃度も一定に保たれる。なおアルカリとして
は、NaOH,Na2 CO3等が用いられる。
Here, in the present invention, the amount of alkaline solution sprayed from the nozzle 2 is always kept constant, and the alkali concentration that can be omitted from the alkaline solution is also kept constant. Note that NaOH, Na2 CO3, etc. are used as the alkali.

そして本発明においては、バルブ4から供給される霧化
空気量が、塩化水素除去塔1の出口5から排出される排
ガス中の塩化水素濃度の変化に対応して制御され、アル
カリ溶液と混合された後にバルブ2に供給される。
In the present invention, the amount of atomizing air supplied from the valve 4 is controlled in accordance with changes in the concentration of hydrogen chloride in the exhaust gas discharged from the outlet 5 of the hydrogen chloride removal tower 1, and the amount of atomizing air is After that, it is supplied to valve 2.

すなわち、塩化水素除去塔出口5における排ガス中の塩
化水素濃度が測定され、この濃度が規定濃度よりも上昇
したときにはバルブ4が開かれてノズル2に供給される
空気量が増大し、一方、出口5における排ガス中の塩化
水素濃度が低下したときには、バルブ4が閉ざされてバ
ルブ2への供給空気量が削減される。
That is, the concentration of hydrogen chloride in the exhaust gas at the outlet 5 of the hydrogen chloride removal tower is measured, and when this concentration rises above the specified concentration, the valve 4 is opened to increase the amount of air supplied to the nozzle 2, while at the outlet When the hydrogen chloride concentration in the exhaust gas at step 5 decreases, valve 4 is closed and the amount of air supplied to valve 2 is reduced.

このようにノズル2に供給される空気量を変化させるこ
とによって、ノズル2における気液比が変化し、液滴は
微小化される。
By changing the amount of air supplied to the nozzle 2 in this manner, the gas-liquid ratio in the nozzle 2 is changed, and the droplets are miniaturized.

すなわち、空気量が増大するにつれて液滴は径が小さく
なり、空気量の減少によって液滴径は増大する。そして
液滴が小さくなれば、噴霧アルカリ溶液量が一定でも液
滴の表面積が増大し、排ガス中の塩化水素除去性能が高
められる。
That is, as the amount of air increases, the diameter of the droplet decreases, and as the amount of air decreases, the diameter of the droplet increases. If the droplets become smaller, the surface area of the droplets will increase even if the amount of atomized alkaline solution is constant, and the performance of removing hydrogen chloride from exhaust gas will be improved.

逆に塩化水素除去塔出口5における塩化水素濃度が低い
場合には、霧化空気量が少なく、アルカリ溶液液滴の径
は大きくても良いことになる。
Conversely, when the hydrogen chloride concentration at the hydrogen chloride removal tower outlet 5 is low, the amount of atomizing air is small and the diameter of the alkaline solution droplets may be large.

なお、出口5における排ガス中の塩化水素濃度は、自動
的に測定され、この値に対応してバルブ4の開閉も自動
的に行なわれる。
Note that the hydrogen chloride concentration in the exhaust gas at the outlet 5 is automatically measured, and the valve 4 is automatically opened and closed in accordance with this value.

かかる本発明の方法は、噴霧溶液の種類を適宜選択する
ことによって、塩化水素以外の有毒ガス除去にも利用す
ることができる。またスラリー噴霧にも応用出来る。
The method of the present invention can also be used to remove toxic gases other than hydrogen chloride by appropriately selecting the type of spray solution. It can also be applied to slurry spraying.

〔発明の効果〕〔Effect of the invention〕

以上述べたように本発明によれば、アルカリ溶液を噴霧
するノズルに供給される空気量を変化させるだけなので
、アルカリ噴霧処理後に排ガス中に残存する塩化水素濃
度の変化に対応して迅速に霧化アルカリ溶液液滴の粒径
を変化させることができる。
As described above, according to the present invention, since the amount of air supplied to the nozzle that sprays the alkaline solution is simply changed, the atomization can be performed quickly in response to changes in the concentration of hydrogen chloride remaining in the exhaust gas after the alkaline spray treatment. The particle size of the alkali solution droplets can be varied.

従来のように、アルカリ溶液の噴霧量やアルカリ濃度を
変化させる方法に比較して除去塔出口5における塩化水
素濃度の変化に対する応答が著るしく早い。
The response to changes in the hydrogen chloride concentration at the outlet 5 of the removal tower is significantly faster than the conventional method of changing the amount of alkaline solution sprayed or the alkali concentration.

また操作も極めて簡単であり、塩化水素除去率70〜9
0%(Na/cl比−2,0の場合)の範囲内で容易に
調整することができる。
In addition, the operation is extremely simple, and the hydrogen chloride removal rate is 70 to 9.
It can be easily adjusted within the range of 0% (in case of Na/Cl ratio -2.0).

更に、噴霧アルカリ液量の液化がないので、霧化空気量
が変化してもスプレーパターンははとんど変化せず、安
定した気液接触を行なうことができる。
Furthermore, since the amount of atomized alkaline liquid does not liquefy, the spray pattern hardly changes even if the amount of atomized air changes, and stable gas-liquid contact can be achieved.

更にまた、塩化水素除去塔出口における塩化水素濃度が
変化しても、アルカリ溶液のアルカリ濃度を一定に保持
することができる利点もある。
Furthermore, even if the hydrogen chloride concentration at the outlet of the hydrogen chloride removal column changes, there is also the advantage that the alkaline concentration of the alkaline solution can be kept constant.

以下、本発明の実施例を述べる。Examples of the present invention will be described below.

〔実施例〕〔Example〕

噴霧アルカリ溶液量が一定の場合、塩化水素除去塔入口
における塩化水素濃度が450ppmの排ガスについて
、霧化空気量の変化と塩化水素除去率との関係を検討し
た。
When the amount of atomized alkaline solution is constant, the relationship between changes in the amount of atomized air and the hydrogen chloride removal rate was investigated for exhaust gas with a hydrogen chloride concentration of 450 ppm at the inlet of the hydrogen chloride removal tower.

結果を第2図に示す。The results are shown in Figure 2.

なお第2図において、曲線AはNa/cl比3.0゜曲
線Bは2.01曲曲線は1.0の場合を夫々示す。
In FIG. 2, curve A shows the case where the Na/Cl ratio is 3.0°, curve B shows the case where the Na/Cl ratio is 2.0°, and curved curve shows the case where the Na/Cl ratio is 1.0.

第2図から霧化空気量の増大につれてかつ、塩化水素に
対してアルカリが過剰に存在する程、塩化水素除去率が
増大することが明らかである。
It is clear from FIG. 2 that as the amount of atomizing air increases and as the alkali is present in excess of hydrogen chloride, the hydrogen chloride removal rate increases.

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

第1図は本発明の工程図、第2図は霧化空気量の変化に
対する塩化水素除去率の変化を示す図である。 l・・・塩化水素除去塔、2・・・ノズル、4・・・空
気バルブ、5・・・塩化水素除去塔出口、6・・・アル
カリ溶液。
FIG. 1 is a process diagram of the present invention, and FIG. 2 is a diagram showing changes in the hydrogen chloride removal rate with respect to changes in the amount of atomizing air. 1... Hydrogen chloride removal column, 2... Nozzle, 4... Air valve, 5... Hydrogen chloride removal column outlet, 6... Alkaline solution.

Claims (1)

【特許請求の範囲】[Claims] 塩化水素を含む排ガスにアルカリ溶液を噴霧して排ガス
中の塩化水素濃度を制御する方法において、前記アルカ
リ溶液噴霧後の排ガス中に残存する塩化水素の濃度に対
応して前記アルカリ溶液を噴霧するノズルに供給する空
気量を変化させることを特徴とする排ガス中の塩化水素
濃度を制御する方法。
In a method for controlling the hydrogen chloride concentration in exhaust gas by spraying an alkaline solution into exhaust gas containing hydrogen chloride, a nozzle that sprays the alkaline solution in accordance with the concentration of hydrogen chloride remaining in the exhaust gas after the alkaline solution is sprayed. A method for controlling hydrogen chloride concentration in exhaust gas, characterized by changing the amount of air supplied to the exhaust gas.
JP60109250A 1985-05-23 1985-05-23 Method for controlling concentration of hydrogen chloride in exhaust gas Pending JPS61268342A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60109250A JPS61268342A (en) 1985-05-23 1985-05-23 Method for controlling concentration of hydrogen chloride in exhaust gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60109250A JPS61268342A (en) 1985-05-23 1985-05-23 Method for controlling concentration of hydrogen chloride in exhaust gas

Publications (1)

Publication Number Publication Date
JPS61268342A true JPS61268342A (en) 1986-11-27

Family

ID=14505416

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60109250A Pending JPS61268342A (en) 1985-05-23 1985-05-23 Method for controlling concentration of hydrogen chloride in exhaust gas

Country Status (1)

Country Link
JP (1) JPS61268342A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02131121A (en) * 1988-09-27 1990-05-18 Von Roll Ag Method and apparatus for removing nitrogen oxides from flue gas
JPH0884909A (en) * 1994-09-14 1996-04-02 Nippon Puraiburiko Kk Hydrogen chloride removing apparatus for small-sized incinerator

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02131121A (en) * 1988-09-27 1990-05-18 Von Roll Ag Method and apparatus for removing nitrogen oxides from flue gas
JPH0884909A (en) * 1994-09-14 1996-04-02 Nippon Puraiburiko Kk Hydrogen chloride removing apparatus for small-sized incinerator

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