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JP3124081B2 - Dispersion method of packed tower spray - Google Patents

Dispersion method of packed tower spray

Info

Publication number
JP3124081B2
JP3124081B2 JP03297146A JP29714691A JP3124081B2 JP 3124081 B2 JP3124081 B2 JP 3124081B2 JP 03297146 A JP03297146 A JP 03297146A JP 29714691 A JP29714691 A JP 29714691A JP 3124081 B2 JP3124081 B2 JP 3124081B2
Authority
JP
Japan
Prior art keywords
nozzle
spray
packed tower
liquid
exhaust gas
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.)
Expired - Fee Related
Application number
JP03297146A
Other languages
Japanese (ja)
Other versions
JPH05137943A (en
Inventor
雅和 鬼塚
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 Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP03297146A priority Critical patent/JP3124081B2/en
Publication of JPH05137943A publication Critical patent/JPH05137943A/en
Application granted granted Critical
Publication of JP3124081B2 publication Critical patent/JP3124081B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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  • Treating Waste Gases (AREA)
  • Gas Separation By Absorption (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は湿式排煙脱硫装置などの
排ガス洗浄装置に関するもので、排ガスを洗浄する充填
塔における吸収液の散布方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an exhaust gas cleaning apparatus such as a wet flue gas desulfurization apparatus, and more particularly to a method of spraying an absorbing liquid in a packed tower for cleaning exhaust gas.

【0002】[0002]

【従来の技術】従来の充填塔におけるスプレーの散布方
法を図3によって説明する。図3において、液溜め10
6に貯留する吸収液Aをポンプ107で揚液し、スプレ
ヘッダ102からノズル101に流入した吸収液Aは上
向きに棒状の液柱としてノズル101先端から噴射さ
れ、噴射動圧に応じた高さまで到達した後、傘状に広が
り自由落下し、吸収塔104内で分散し、スプレヘッダ
102下部に設けられた充填物105を濡らしながら排
ガスBと気液接触して排ガスを洗浄するものである。な
お、図中、103は液溜め106内に設置された攪拌
機、B′は浄化排ガスを示す。
2. Description of the Related Art A conventional method of spraying a spray in a packed tower will be described with reference to FIG. In FIG.
Absorbent A stored in 6 is pumped up by a pump 107, and the absorbent A flowing into the nozzle 101 from the spray header 102 is ejected upward from the tip of the nozzle 101 as a rod-shaped liquid column, and reaches a height corresponding to the ejection dynamic pressure. after, which fall freely spread in an umbrella shape, and dispersed in the absorption tower 104. wash the exhaust gas with the exhaust gas B and gas-liquid contact while wetting the packing 105 provided spray headers <br/> 102 lower It is. In the drawing, reference numeral 103 denotes a stirrer installed in the liquid reservoir 106, and B 'denotes purified exhaust gas.

【0003】[0003]

【発明が解決しようとする課題】上記したように、液を
単に上向きに噴射させるだけでは液を微滴に分散させる
ことができず、また、噴射量を増やして噴射高さを高く
しても最高到達部での吸収効率が噴射液量に関係して上
昇するものの噴射上昇過程での効率は僅かであり、この
噴射上昇過程での吸収効率上昇は吸収液の自由落下量と
高さが増加した分若干上昇するものであり、投入した動
力からすると効率は低下したことになる。さらに、噴射
量の増加は吸収塔の高さの増加にも繋がるなどの欠点が
あり、この欠点を補うためにはノズル口径を大きくした
り数を増やしたりすると共に充填物を沢山充填する必要
があった。
As described above, it is not possible to disperse the liquid into fine droplets simply by ejecting the liquid upward, and even if the ejection height is increased by increasing the ejection amount. Although the absorption efficiency at the highest point rises in relation to the amount of liquid injected, the efficiency during the injection rise process is small, and the increase in absorption efficiency during the injection rise process increases the free fall amount and height of the absorbent. However, the efficiency is reduced in terms of the input power. In addition, an increase in the injection amount has a drawback such as an increase in the height of the absorption tower, and in order to compensate for this drawback, it is necessary to increase the nozzle diameter or increase the number and fill a lot of packing material. there were.

【0004】本発明は上記技術水準に鑑み、従来技術に
おけるような不具合のない充填塔スプレーの分散方法を
提供しようとするものである。
[0004] In view of the above-mentioned state of the art, the present invention aims to provide a method for dispersing a packed tower spray which does not have a problem as in the prior art.

【0005】[0005]

【課題を解決するための手段】本発明は上向きに設けた
複数のスプレーノズルから吸収液を散布して排ガスを気
液接触処理させるにあたって、該ノズルから鉛直方向に
噴射された吸収液を該ノズルの上部に設けた衝突体に衝
突させることを特徴とする充填塔スプレーの分散方法で
ある。
SUMMARY OF THE INVENTION In the present invention, when the absorbing liquid is sprayed from a plurality of spray nozzles provided upward and the exhaust gas is subjected to gas-liquid contact treatment, the absorbing liquid jetted vertically from the nozzle is sprayed onto the nozzle. A method of dispersing a packed tower spray, characterized in that the packed tower spray is made to collide with a collision body provided on the upper part of the column.

【0006】[0006]

【作用】本発明は上記したように、ノズルから鉛直方向
に噴射された吸収液をノズルの上部に設けた衝突体に衝
突させ微滴化して分散させることにより、該衝突体の隙
間を通過する排ガスと前記微滴が激しく気液接触する。
According to the present invention, as described above, the absorbing liquid ejected from the nozzle in the vertical direction collides with the colliding body provided at the upper part of the nozzle, and is made into fine droplets and dispersed, thereby passing through the gap between the colliding bodies. Exhaust gas and the microdrops come into violent gas-liquid contact.

【0007】[0007]

【実施例】本発明をまず図1の実施態様例を用いて具体
的に説明する。図1において、液溜め6から循環ポンプ
7で揚液された吸収液AAは、スプレーヘッダ2に複数
個設けられたノズル1から鉛直方向に噴射され、該ノズ
ル1の噴射口の直上部に設けられた衝突体8に衝突し分
散され、吸収塔4に導入された未処理排ガスBBと激し
く気液接触し、排ガスを洗浄するものである。なお、図
1中、3は攪拌機、4は吸収塔、5は充填物、BB′は
浄化排ガスを示す。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will first be specifically described with reference to the embodiment shown in FIG. In FIG. 1, an absorbent AA pumped from a liquid reservoir 6 by a circulation pump 7 is jetted in a vertical direction from a plurality of nozzles 1 provided on a spray header 2, and is provided directly above an injection port of the nozzle 1. The colliding body 8 collides with the untreated exhaust gas BB introduced into the absorption tower 4, and vigorously comes into gas-liquid contact to wash the exhaust gas. In FIG. 1, 3 is a stirrer, 4 is an absorption tower, 5 is a packing, and BB 'is a purified exhaust gas.

【0008】図2に衝突体8の一実施態様の断面形状例
を示す。図2において、衝突体8の頂部9を鋭角に加工
し、底部10も尖らせた。底部10の角度は分散状況に
よって調整した。
FIG. 2 shows an example of a cross-sectional shape of one embodiment of the collision body 8. In FIG. 2, the top 9 of the collision body 8 was machined to an acute angle, and the bottom 10 was also sharpened. The angle of the bottom 10 was adjusted according to the dispersion condition.

【0009】以下、本発明を、図1の態様をなす装置で
行った実施例と、図3の従来態様をなす装置を用いた比
較例とを用いて具体的に説明する。
Hereinafter, the present invention will be described in detail with reference to an embodiment in which the apparatus according to the embodiment shown in FIG. 1 is used and a comparative example using the apparatus according to the conventional embodiment shown in FIG.

【0010】(実施例)SO2 を780ppm相当添加
した空気を毎時1400m3 N吸収塔頂部から導入し、
循環ポンプで炭酸カルシウムを45mmol/リットル
含有する石膏スラリを毎時250m3 吸収塔に散布し
た。この時、断面積1m2 の吸収塔への吸収液の散布に
は内径60mmのノズル4本を用い、1m角の吸収塔に
対し衝突体は厚み200mm、高さ1500mm、幅1
000mm、頂部角60°、底部角90°のもの2枚を
ノズルの噴射口から700mm上部に設けた。以上の条
件下でスプレーヘッダ下部でのSO2 濃度の測定は11
0ppmであった。また、ノズルから噴射された吸収液
は衝突体の上端を越して上部に飛散することはなかっ
た。
(Embodiment) Air to which 780 ppm of SO 2 was added was introduced from the top of the 1400 m 3 N absorption tower per hour,
A gypsum slurry containing 45 mmol / liter of calcium carbonate was sprayed to a 250 m 3 absorption tower per hour by a circulation pump. At this time, four nozzles having an inner diameter of 60 mm were used to spray the absorbing liquid onto the absorption tower having a cross section of 1 m 2 , and the collision body was 200 mm thick, 1500 mm high and 1 width wide with respect to the 1 m square absorption tower.
Two pieces having a size of 000 mm, a top angle of 60 °, and a bottom angle of 90 ° were provided 700 mm above the injection port of the nozzle. Under the above conditions, the measurement of the SO 2 concentration under the spray header is 11
It was 0 ppm. Further, the absorbing liquid jetted from the nozzle did not scatter above the upper end of the collision body.

【0011】(比較例)上記装置から衝突体を撤去して
同一条件で試験を実施し、上記同様スプレーヘッダ下で
のSO2 濃度の測定の結果232ppmであった。ま
た、この時、ノズルから噴射された吸収液の噴出高さは
4本で若干ばらつきはあったが2〜2.3m程度であっ
た。
(Comparative Example) A test was carried out under the same conditions by removing the collision body from the above apparatus, and the result of measurement of the SO 2 concentration under the spray header was 232 ppm as in the above. Also, at this time, the ejection height of the absorbing liquid ejected from the nozzles was about 2 to 2.3 m although there were some variations in the ejection height of the nozzles.

【0012】[0012]

【発明の効果】本発明によれば、上記したようにノズル
からの噴射吸収液を該ノズルの上部に設けた衝突体に衝
突させて微滴に分散させることにより脱硫性能の向上及
び吸収塔高さの低減が可能である。
According to the present invention, as described above, the jetting / absorbing liquid from the nozzle is made to collide with the collision body provided above the nozzle to be dispersed into fine droplets, thereby improving the desulfurization performance and increasing the height of the absorption tower. It is possible to reduce the size.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の実施態様例の説明図。FIG. 1 is an explanatory diagram of an embodiment example of the present invention.

【図2】図1における衝突体の断面図。FIG. 2 is a sectional view of the collision body in FIG. 1;

【図3】従来の実施態様例の説明図。FIG. 3 is an explanatory view of a conventional embodiment.

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) B01D 53/18 B01D 53/34 B01D 53/77 - 53/79 B01J 19/26 ──────────────────────────────────────────────────の Continued on the front page (58) Field surveyed (Int.Cl. 7 , DB name) B01D 53/18 B01D 53/34 B01D 53/77-53/79 B01J 19/26

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 上向きに設けた複数のスプレーノズルか
ら吸収液を散布して排ガスを気液接触処理させるにあた
って、該ノズルから鉛直方向に噴射された吸収液を該ノ
ズルの上部に設けた衝突体に衝突させることを特徴とす
る充填塔スプレーの分散方法。
1. A when to gas-liquid contact process the spraying to exhaust the absorbed liquid from a plurality of spray nozzles provided in the upward, 該No the absorption liquid which is injected in a vertical direction from the nozzle
A method for dispersing a spray in a packed tower, which comprises colliding with an colliding body provided on top of a chirle .
JP03297146A 1991-11-13 1991-11-13 Dispersion method of packed tower spray Expired - Fee Related JP3124081B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP03297146A JP3124081B2 (en) 1991-11-13 1991-11-13 Dispersion method of packed tower spray

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP03297146A JP3124081B2 (en) 1991-11-13 1991-11-13 Dispersion method of packed tower spray

Publications (2)

Publication Number Publication Date
JPH05137943A JPH05137943A (en) 1993-06-01
JP3124081B2 true JP3124081B2 (en) 2001-01-15

Family

ID=17842799

Family Applications (1)

Application Number Title Priority Date Filing Date
JP03297146A Expired - Fee Related JP3124081B2 (en) 1991-11-13 1991-11-13 Dispersion method of packed tower spray

Country Status (1)

Country Link
JP (1) JP3124081B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2716346A3 (en) * 2004-11-01 2014-08-20 Mitsubishi Heavy Industries, Ltd. Exhaust gas treatment apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2716346A3 (en) * 2004-11-01 2014-08-20 Mitsubishi Heavy Industries, Ltd. Exhaust gas treatment apparatus

Also Published As

Publication number Publication date
JPH05137943A (en) 1993-06-01

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Effective date: 20000919

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