TW438619B - Wet gas processing method and the apparatus using the same - Google Patents

Wet gas processing method and the apparatus using the same Download PDF

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Publication number
TW438619B
TW438619B TW87118702A TW87118702A TW438619B TW 438619 B TW438619 B TW 438619B TW 87118702 A TW87118702 A TW 87118702A TW 87118702 A TW87118702 A TW 87118702A TW 438619 B TW438619 B TW 438619B
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Taiwan
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liquid
absorption
exhaust gas
gas
absorption liquid
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TW87118702A
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Chinese (zh)
Inventor
Toru Takashina
Masakazu Onizuka
Koichiro Iwashita
Satoshi Nakamura
Kenji Inoue
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Mitsubishi Heavy Ind Ltd
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  • Treating Waste Gases (AREA)
  • Gas Separation By Absorption (AREA)

Abstract

This invention is related to a wet gas process which would not require a spray pump, and which would allow the absorption liquid to be recovered smoothly even if the flow velocity of the gases entrained to the liquid should decrease, and a wet gas processing apparatus in which the absorption liquid collected in the liquid storage tank is sprayed in a specified direction by a liquid discharge unit consisting of spray nozzles or the like in the absorption tower. The sprayed liquid is brought into contact with the exhaust gases which are conducted into the tower, and the targeted components of the gases are absorbed and removed. This processing apparatus is distinguished by the following. The liquid storage tank for the absorption liquid comprises a pressure tank which generates a pressurized gas in the space above the surface of the collected liquid. The increased pressure of the pressurized gas is employed to spray the liquid collected in the pressurized tank from the spray nozzle unit in the absorption tower. The spray nozzle unit forms as required the overflowed or gushed absorption liquid discharge unit facing the orthogonal direction of a plurality of absorption pipes arranged in parallel crossing to said gas paths. The absorption liquid propelled by the discharge unit makes orthogonal contact with the flow of exhaust gases, which results in both atomization of the liquid and liquid-vapor contact.

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經濟部中央橾率局貝工消费合作杜印製 4386 1 9 at _____B7__ 五、發明説明（t ) 〔發明之技術領域〕 本發明是有關可從廢氣中除去有害成份之其他目的成份的 濕式氣體處理方法及其裝置，尤其是關於可有效進行與吸收液 及煤炭或重油等然燒廢氣之氣液接觸的濕式氣體處理方法及其 裝置。 〔習知技術〕 以往，例如從煤炭燃燒鍋爐等的排煙除去亞二氧化硫氣體 等有害物質之濕式排煙脫硫裝置中是使用各種形態的氣液接觸 裝置，其中氣液接觸裝置之一形態是例如本發明人所提出之曰 本專利實開昭5 9 — 5 3 8 2 8號之所謂液柱式裝置。 該裝置是從配設在吸收塔內的複數個噴嘴朝著上方噴出如 石灰懸浮液之吸收液，而出現如柱狀的形態，對此噴流之中予 以排煙通氣可吸收含排煙之二氧化硫氣體的同時，可有效地除 去煙灰等粉塵。 並且，其基本之構成係如第2 4 (A)圖表示之模式圖， 在’吸收塔2上方設置排煙導出部8，在下部設置形成廢氣1的 入口之排煙導入部3 *同時在吸收塔2內的下部呈複數列狀配 設總管190，在該管190上例如形成矩陣配設同圖（B) 表示之複數個向上噴嘴4。 又，將吸收塔2內的下部構成可在漏斗狀液體儲存部5 6 儲存石灰懸浮液等的吸收液，經回收泵2 1 a回流至吸收液儲 存槽5 7內》使回流後的吸收液5再度經由噴出泵2 1 b流量 開關閥6 0及總管1 9 0而連通導入向上噴嘴4 » 本紙張尺度適用中國國家標準（CNS ) A4規格（210X297公釐） I I I n u n K ^ 線 (請先閲讀背面之注意事項真、·寫本頁) 經濟部中央樣準局Μβζ工消t合作社印装 4386 1 9 A7 A/ __B7五、發明説明) 此外，配設形成上述矩陣形之複數個向上噴嘴4所構成的 噴嘴群可將吸收液5形成朝上方之液柱狀噴流5·同時與此同 時從上述排煙導入部3導入而朝著塔上部通氣之廢氣1是根據 其流速而隨著上述噴流狀吸收液5上升，且藉其通過頂部呈傘 狀散開之噴流5 a中得以氣液接觸者。隨後，藉設於上述噴流 頂點附近之吸收塔2上部的消霧器6而隨廢氣1分離之吸收液 5，可回收於吸收液儲存槽5 7內。又，直接落下至液體儲存 部5 6之吸收液5是藉著回收泵2 1 a送至吸收液儲存槽5 7 內。 上述構成之氣液接觸裝置中，使泵2 1 b動作經由流量開 關閥6 0及總管1 9 0，而從向上噴嘴4將吸收液5朝著上方 噴射，使排煙導入部3側導入之廢氣1通過噴流5 a中得以氣 液接觸，將除去二氧化硫氣體等處理後的廢氣（淨化氣體）7 從上方側的排煙導出部8導出。’ 並且，如上述將吸收液5朝上方噴出的技術中，不僅吸收 液5需要長的往返（上升、下降）時間|獲得氣液接觸之外， 到達頂點呈傘狀開啓而流下時，由於吸收液5形成液滴狀1因 此可增加氣液接觸效果，又，當含於廢氣中的二氧化硫氣體等 較少時，只須改變液柱高度即可進行經濟運轉，另外例如使吸 收液流下至塡充格子狀柵格之塔內，與接觸氣體之所謂塡充方 式等比較，具有不易造成流體通路的阻塞等多數優點。 此外，上述之技術的場合係使噴射用泵2 1 b動作，使儲 存在液體儲存部5 6或吸收液儲存槽5 7的吸收液5在總管 1 9 0側循環的同時，利用噴嘴4設定噴出壓將吸收液5噴出 I I I I I I 訂 I I 1 (1 f ^ (請先閲讀背面之注意事項莽：為本頁) 本紙張尺度通用中國國家標準（CNS ) A4规格（2丨〇X297公釐） -5 * 經濟部中央橾準局負工消费合作社印製 4 386 1 9 at _.____B7五、發明説明) 至預定高度》 再者，本圖中噴射用泵2 1 b是爲了簡化說明而以單一構 件表示之*但實際上是使用複數個，因此會有裝置小巧化及設 備費用、運轉費用刪減等各観點上的問題。 又，爲了提高廢氣與吸收液之間氣液接觸的效率，必須設 置多數使接觸廢氣之吸收液微粒化的噴嘴，因此存在有必須配 設如第2 4 ( B )圇所示矩陣狀複數個吸收液噴出用噴嘴群等 而增大設備負擔等的問題。 因此，例如德國專利第D E — A — 1 7 6 9 9 4 5號或者 日本專利特表平9 — 50779 2號中，設置儲存供應循環上 述噴嘴之懸浮液的槽，將該槽之液面位準設定高於噴嘴噴出位 置，使隨噴嘴噴出的吸收液隨著氣體在吸收塔的上部分離成吸 收液與氣體，可將分離後的吸收液保持在槽內而利用該槽液面 的重力差藉著噴嘴將懸浮液噴出，不須使用噴射泵而可利用重 力差進行噴嘴之懸浮液的噴出及循環。 但是，上述相關之技術中，儲存吸收液之槽的液面雖是以 高於吸收塔內噴嘴噴出位置的位置爲條件，但是一般吸收塔具 有相當的高度，而設定高於該高度位置的液面時，會有必須增 加槽的高度等缺點。 另外，如排煙脫硫裝置的氣體淸洗裝置中，鍋爐等的氣體 產生源一般會有載荷變動，因此上述任意的裝置中*當氣體流 量減少時，會因爲氣體流速的降低而不能吸引吸收液·因此不 能順利進行吸收液與氣流間的氣液接觸，不僅不能有效地除去 排煙中$含有的二氧化硫氣體或粉塵’更無法在吸收塔上回收 I — ^ n I ^ 11 H ] ^ (請先W讀背面之注意事項真 寫本頁) 本紙浪尺度適用中國國家標率（CNS ) A4規格（210X297公釐） -6- 438619 A7 B7 五、發明説明6 ) * 吸收液，換言之，於槽內之吸收液的循環困難，其結果會使槽 內液面逐漸降低|最後會導致利用其本身重量進行吸收液困難 0 此外*在上述任意的裝置中，吸收液的噴出速度，換言之 噴出高度是與廢氣的流速成比例而增減•因此如第13圖所示 吸收塔內上升時的T1以至下降時的T2·燃燒機側的燃燒容量 小時，會使廢氣流速降低，而不可能使噴嘴噴出的吸收液噴出 高度提高至基準位準以上，其結果，上述噴流的大致全量無法 到達設於塔頂部的消霧氣而在腰折的狀態下落至液體儲存部， 使儲存在上述液體儲存部的吸收液大多無法加以利用。 因此，以往的裝置中，由於吸收液可連續循環使用，而必 須增大液體儲存部5 6的尺寸，或者僅回流用回收泵2 1 a對 應吸收塔2升高及降下時，準備大容量之物，但隨之會產生設 備成本不必要的增加。 另外，上述的任意裝置同樣隨廢氣而吸收二氧化硫氣體等 的目的成份之噴霧（液滴）係衝擊於吸收塔上部之噴霧淨化器 的彎曲板而落至吸收塔內可使吸收液連續循環，但是如上述之 習知裝置中，塔內的氣體流速爲一般的4〜5m/s時，可以 消霧器加以補足，但是近年來由於處理能力的提升與空間的節 省，具有必須提高塔內氣體流速至例如5.5m/s以上之高速 化的要求》 + , 氣體速度一旦提升至5 .5 m / s以上時+，消霧器中該部份 的液滴不能瀝除，而隨著氣體同時與吸收液滴被排出塔外，放 出至大氣中1且被送至後段的處理設備內等並非理想。 本紙張尺度適用中國國家標準（CNS > A4规格（2丨0X297公釐） ------------裝------訂------線 {請先閲讀背面之注^^項声卜寫本頁) 經濟部中央揉準局貝工消费合作社印装 4 3 8 6 1 9 經濟部中央標準局月工消费合作社印製 A7 B7五、發明説明) 又，5.5m/s以上的氣體流速會隨著氣體而大幅地增加 到達消霧器的吸收液液量，因此應從消霧器落下的液體不能有 效地落下，在消霧器的入口部形成螺旋狀液滴而發生滯留現象 (飛散吸收液儲存區域），使噴霧除去性能顯著降低該噴霧 除去性能的降低是從飛散吸收液儲存區域隨著廢氣而使噴霧（ 液滴）再度飛散所產生，因此會使來自排氣用煙道噴霧的溢散 增加。 〔發明之說明〕 本發明有鑑於上述習知技術之缺點，提供不須使用噴射泵 |或即使隨吸收液而降低氣體流速時仍可順利地回收吸收液之 濕式氣體處理的發明爲目的者。 本發明之其他目的爲提供不須使用習知之向上噴嘴，或不 須要大的動力的節省能源方式•且可解除噴嘴設備負擔的增加 等而可實現低成本化，並可有效地使氣液接觸之濕式氣體處理 的發明爲目的者。 本發明之其他目的爲提供不須無謂地加大液體儲存部的尺 寸及容量|並可有效地解決當上述廢氣流速降低時所產生的問 題之濕式廢氣處理的發明爲目的者。 本發明之其他目的爲提供即使當吸收塔上升時乃至關閉時 低容量燃燒所產生的導入廢氣流速降低時，仍可將吸收液的液 柱高度維持在基準位準以上之廢氣處理的發明爲目的》 本發明之其他目的爲提供即使當吸收塔內廢氣在塔內速度 (載流速度）形成高度化時，使含於淸淨後之廢氣而自吸收塔 (请先聞讀背面之注意^項#朱寫本頁) 本紙張尺度適用中國國家標準（CNS ) A4規格U10X297公釐） _ 8 _ 經濟部中央桴率局貝工消费合作社印製 3 86 1 9 A7 _B7___五、發明説明（6 ) . 所排出吸收液之噴霧（液滴）量儘可能地少之濕式廢氣處理有 關之發明爲目的者。 爲解決上述問題，本發明係如申請專利範圍第1項所記載 *將儲存在吸收液儲存部的吸收液從吸收塔內的噴嘴等吸收液 流出部朝著預定方向（不僅朝著上方·同時包含橫向、朝下） 噴流，使該噴流與通氣於上述吸收塔內的廢氣氣液接觸，而吸 收/除去廢氣中的目的成份之濕式氣體處理裝置中•其特徵爲 藉產生加壓氣體之加壓槽將上述吸收液儲存部形成在儲存 液面上方空間，利用該加壓氣體的壓力|構成可從吸收塔內的 噴嘴部噴出儲存在上述加壓槽內的吸收液· 因此，根據相關之發明可藉著加壓槽的受壓面積與加壓氣 體的壓力決定噴嘴的吸收液噴出量|並且藉著鍋爐等燃燒裝置 的荷載變動等，即使當吸收塔內的氣體流速變動時，仍可控制 使加壓槽內的壓力朝著校正此一變動方向I藉此可大致維持一 定之噴嘴吸收液的噴出高度，其結果即使隨吸收液使氣體流速 降低時仍可順利地回收吸收液者。 再者，加壓槽內的氣體壓力可平均來自該槽的吸收液排出 量，及對於該槽之吸收液供應量與對於該槽內之氣體噴吹置而 可控制在預定壓》 又根據本發明*並非如噴射泵直接壓送吸收液，而是以壓 縮空氣等加壓氣體加屋於加壓槽內，換言之可不須使用複數個 泵，只須以加壓泵及供應加壓氣體於其中之空氣壓縮機等的氣 體壓縮源即已足夠，因此可實現裝置之小巧化及設備費用、運 (請先閲讀背面之注$項一本頁) 裝. 訂 本紙張尺度適用中固國家標準（CNS )六4此格（210X297公嫠） -9 - 經濟部中央樣準局貝工消费合作社印製 4 3 8 6 1 9 A7 B7五、發明説明& ) 轉費用的刪減等。 此外.，吸收液供應噴嘴即使是使用向上的向上裝置時，可 不須將此向上噴嘴定位在加壓槽液面的上部，即可設定低的加 壓槽而可予以自由配置者。 又本發明係如申請專利範圍第2項所記載，當吸收/除去 的上述吸收液中之一目的成份爲二氧化硫（S〇2)時，上述加 壓氣體爲含氧氣體，將此含氧氣體噴入加壓槽內底部之儲存液 即可。 藉此從噴嘴噴出而與廢氣的氣液接觸|將吸收S 0 2之含石 灰的懸浮液吸收液儲存在加壓槽內時•由於與上述含氧氣體的 接觸使SO 2氧化而可以產生硫酸鈣二水物（石膏）^ 另外本發明具備將上述吸收液噴流至吸收塔內噴嘴部上方 的向上噴嘴之濕式氣體處理裝置中，如申請專利範圍第3項所 記載，以產生加壓空氣之加壓槽將上述吸收液儲存部形成於儲 存液面上方空間，一方面將可回收吸收上述目的成份之吸收液 的回收部配置在高於上述加壓槽內儲存液面高之吸收塔內的預 定位置，或使上述回收部吸收液回流至加壓側之連通管的出口 端開口而定位在上述加壓槽內的儲存液內亦可。 根據本發明，吸收/除去目的成份之吸收液是經由回收部 回收至加壓槽側•形成可循環再使用吸收液者。 此外，於上述回收部朝加壓槽內部之上部封閉空間開設回 收吸收液之連通管時，該空間內的氣體壓力係經由連通管而溢 散於吸收塔內不能維持加壓槽的功能。 因此，本發明係將上述回收部使吸收液回流至加壓槽側之 * 裝 訂 線 (請先閏讀背面之注意事項寫本頁) 本紙張尺度遑用中國國家揉率（CNS ) A4規格{ 210Χ297公釐） -10- 43 86 1 9 A7 B7_____ 五、發明説明fe ) 連通管出口端開口定位在上述加壓槽內的儲存液內，藉此可利 用連通管內的吸收液形成加壓槽之氣體壓力密封，同時將回收 部配置在高於上述加壓槽內的儲存液面之吸收塔內的預定位置 ，因此可經由回收部的連通管使連通管內的液面上升至壓力槽 內部壓力平衡的位置。並且，設定連通管高低差、回收部的位 置及槽內壓使上述連通管內的液面低於回收部的位置，藉此可 進行自回收器至加壓槽內之吸收液的循還而可利用連通管內的 吸收液進行加壓槽之氣體壓力密封* 再者，根據本發明於吸收塔內向上噴流吸收液而利用設於 吸收塔上部的回收部回收吸收液時，由於其部份落下至吸收塔 底部，因此僅上述回收部並不能1 0 0%回收，因此當儲存在 吸收塔底部的液體位準達到預定量以上時*構成可利用低壓泵 朝加壓槽回送。又液體的一部份會與氣體同時排出，因此可以 原料供應管進行其補充。 此外，申請專利範圍第4項所記載之發明係將儲存於吸收 液儲存槽之吸收液導入吸收塔內，使該吸收液隨著沿上述吸收 塔內的排氣通路而通氣之排氣流速與該排氣流氣液接觸，吸收 /除去上述排氣中的目的成份之濕式氣體處理裝置，其特徵爲 於大致横斷上述排氣通路內的方向並設之複數吸收液管上 •使該吸收液與上述排氣通氣方向交叉的方向*更具體而言朝 著大致橫向方向形成呈溢流或噴出流之吸收液流出部，使該流 出部流出之吸收液與上述排氣流的交叉接觸而加以微粒化進行 氣液接觸。 I I (請先閲讀背面之注$項寫本頁) 經濟部中央樣準局员工消费合作社印裝 本紙張尺度適用中國國家橾準（CNS > Α4洗格（210X297公釐） -11 - 438619 A7 經濟部中央標準局—工消費合作杜印製 B7___五、發明説明) 即|本發明之吸收液的供應係朝著大致橫向方向形成呈溢 流或噴出流的吸收液來代替以往所使用之呈多數矩陣形配設之 噴嘴（參閱第2 4(B)圖），使該流出部流出之吸收液藉著 與上述排氣流的交叉接觸予以微粒化而進行氣液接觸者。 上述之發明係例如申請專利範圍第5項所記載，沿著大致 橫斷上述排氣通路內之一或複數面內列設一段或複數段（包含 上下鋸齒狀配置）上述吸收液管群，最好構成可於該列設之管 群的鄰接管互相間之空隙部導通上述排氣流者。 另外，上述吸收液管之構成係如申請專利範圍第6項所記 載，以上部開放式導水管狀構件構成上述吸收液管的同時，也 可以在該導水管狀構件上設置朝著與通氣方向交叉之大致水平 方向的溢流形成手段，又如申請專利範圍第7項所記載，以上 部封閉式管狀構件構成上述吸收液管的同時，也可以在與導通 該吸收液管之上述排氣流的空隙部相對之周圍面上，沿著管軸 線方向設置縫隙狀開口或多數小孔列之構成。 根據上述發明|只須使上述吸收液朝著上述鄰接之管彼此 間的空隙部側呈大致水平方向溢流或者流出即可可獲得設備 費用降低的效果。 此外，更如申請專利範圍第8項所記載，對上述吸收液管 之吸收液供應也可以構成利用重力之上述吸收液供應源，具體 而言以稍具高低差將吸收液供應源配置在吸收液管上方。 當然，本發明也可以採利用吸收液供應泵之構成，此時可 形成小型的上述供應泵，，除了可降低設備費用之外，同時可降 低動力 I n ! I I 訂 線 (請先聞讀背面之注意事項声ί寫本頁) 本紙張尺度適用中國國家標準（CNS ) Λ4洗格（210X297公釐） -12- 經濟部中央樣準局貝工消费合作社印裝 4 3 86 1 9 A7 B7_五、發明説明) 又，本發明係配設有以預定空隙多數條列設上述排氣通路 之吸收液管，因此其結果可以上述空隙部增加排氣流速度而可 以形成高速化。 本發明係將吸收液流出至使上述排氣流高速化之上述空隙 部而交叉狀接觸於其高速上升排氣流，因此吸收液爲廢氣所產 生高速度能源所擾亂而形成微粒化。又，藉著廢氣之上述空隙 部廢氣的急剌壓縮與膨脹所導致負壓化可同時使上述吸收液之 微小液滴於廢氣中急速分散，促進該吸收流霧化等有效的氣液 接觸與吸收液的供應|習知液柱式之液柱在頂部散開爲止與隨 排氣而流出完成之氣液接觸比較，可更爲有效地在短時間大幅 度地氣液接觸而可高效率地吸收/除去上述排氣中的目的成份 0 又，以鄰接之吸收液彼此間的空隙部進行氣液接觸，且構 成使吸收液的流出液膜或線狀液流噴出於上述空隙部，因此不 需如習知裝置配設高密度之噴嘴·於成本的降低上顯具貢獻。 再者，藉導水管狀構件構成上述吸收液管，尤其是配設上 述鋸齒狀之導水管構件時，排氣通路係穿設於排水管狀構件之 間，因此該通路之排氣係經過壓縮、膨脹等步驟I可促進排水 管構件之開放面的有效霧化及微小液滴化。 此外·本發明係如申請專利範圍第9項所記載，使儲存在 吸收液儲存部的吸收液從吸收塔內的噴嘴部朝著預定方向（除 向上方向並且包含橫向、向下）噴流|使該噴流與上述吸收塔 內通氣之排氣氣液接觸，而吸收/除去排氣中的目的成份之濕 式氣體處理方法中，其特徵爲： (請先閲讀背面之注項#4寫本頁) 本紙張尺度適用中國困家梯準（CNS ) Μ规格（210X2?7公釐） -13- 經濟部中央標準局貝工消費合作社印製 43 86 1 9 A7 B7五、發明説明纟1 ) 使上述吸收塔內通氣之廢氣通路對應上述排出量進行寬度 領域控制，可進行上述廢氣通路之氣體通路領域的調節。 因此根據本發明，可藉著鍋爐等燃燒裝置的負載變動，降 低吸收塔內的氣體流量，根據此一比例降低廢氣通路流動的流 速時，對應上述流量的降低控制氣體流入領域的氣體通過面積 使氣體流速形成一定*藉此可維持大致一定之噴嘴的吸收液噴 出高度，其結果•吸收液隨著氣體的流速可順利地使吸收液與 氣流氣液接觸，不僅可有效地除去排煙中所包含的二氧化硫氣 體或粉塵，可在吸收塔上部順利地回收吸收液*換言之，即可 使對於槽中之吸收液循環的順利· 此時，如申請專利範圍第1 0項所記載，停止來自上述氣 體流入所阻止區域的噴嘴部之吸收液的噴流，可節省無請的泵 驅動動力等，同時可阻止無謂的吸收液循環。 申請專利範圍第1 1項所記載之發明是有關可順利實施申 請專利範圍第9項所記載發明之濕式氣體處理裝置的發明，將 上述吸收塔內通氣之廢氣通路*以沿著廢氣流動方向延伸設置 至噴嘴噴流領域之分割板分割成複數個氣體流域|設置可對應 上述廢氣量進行上述所分割之氣體流域的氣體流入之流量控制 或開關控制的通路控制手段。 根據上述之發明，可降低吸收塔內的氣體流量，而根據此 一比例降低廢氣通路流動的流速時，封閉上述分割板所間隔的 複數個氣體流域一側或形成狹窄的氣體通過面積，藉此對應上 述流量的降低，可控制氣體通過面積形成一定的氣體流速。 申請專利範圍第1 2項所記載之發明係將申請專利範圍第 ---------^------ir-------^ (請先閲讀背面之注$項異.夂寫本頁) 本紙張尺度逍用中國國家標準（CNS ) A4規格（2〗0X297公嫠） -14- 經濟部中央標準局貝工消费合作社印装 4 3 8 6 19 A7 B7五、發明説明（12 ) * 1 1項所記載之裝置*於吸收塔下部配置吸收液儲存部，將噴 嘴部定位於其上方吸收塔內，顯示在該噴嘴部上方特定噴流吸 收液所成之濕式氣體處理裝置時的有效特徵，使沿著排氣流動 方向延伸垂直設置至噴嘴噴流領域爲止之至少一分割板的下端 延伸設置於吸收液儲存部爲止，藉該儲存部內吸收液之液位位 準的調節，可選擇性地使分割板下端沒入吸收液內*而構成可 選擇性地開關該分割板所分割之氣體通路》 即•更具體而言，形成不同之分割板下端的高度位置而藉 吸收液之液位位準的調節，構成可選擇性地將對應之分割板下 端沒入吸收液內。 又*不採取上述之構成，而是如申請專利範圍第1 3項所 記載，在吸收液儲存部側構成可自由升降之沿著排氣流動方向 垂直延伸設置至噴嘴噴流領域的至少一分割板下端側，選擇性 地使該分割板下端下降而沒入吸收液內，構成可選擇性地開關 該分割板所分割之氣體流域的通路亦可= 根據該等構成，藉著吸收液之液位位準的調節或選擇性地 使分割板下端下降使其沒入吸收液內•可選擇性地簡單開關氣 體流域的通路》 再者•其他之控制手段有如申請專利範圍第14項所記載 ，沿著排氣流動方向構成可自由擺動地延伸設置至噴嘴流域爲 止之至少1分割板的下端側，藉著該下端部的擺動轉向，構成 可進行以分割板分割之氣體流域的的氣體流入流量控制或開關 控制。 即，也可以擺動上述分割板之下端側封閉或使鄰接的通路 I n n n i ^ ^ {請先閲讀背面之注意事項寫本頁) 本紙張尺度逋用中國困家揉準（CNS > A4规格（210X297公釐） -15- 經濟部中央樣隼局負工消费合作杜印製 4386 1 9 a7 B7五、發明説明（13 ) 入口開口狹窄化，或也可以使分割板下端側向下傾倒而沒入吸 收液內。 於上述相關之構成中，藉著分割板下端側的擺動轉向，可 簡單地進行氣體流域之氣體流入流量的控制或開關控制。 申請專利範圔第1 5項所記載之發明，其特徵爲：構成使 上述分割板下端可朝著導入吸收塔內之廢氣導入部側轉向者* 從上述導入部導入吸收塔內的廢氣是沿著上述轉向部整流逆引 導至噴嘴噴流方向。 根據上述之發明，上述分割板也具有廢氣整流板的功能， 可更爲順利地進行氣液接觸。_ 另外|申請專利範圍第1 6項所記載之發明，其特徵爲： 構成可相對於廢氣流動方向大致朝著垂直方向移動之上述分割 板，藉著該分割板的移動構成可調節分割氣體流域之通路剖面 積者。 根據上述之發明，對應廢氣流量的變動而移動分割板•可 藉此自由地調節氣體流域之通路剖面積者。 申請專利範圍第1 7項所記載之發明，其特徵爲：利用從 吸收塔下部朝頂部通氣的廢氣而隨著吸收液的氣液接觸，使上 述廢氣中的目的成份吸收於吸收液所成之濕式廢氣處理方法中 ，其特徵爲： 上述廢氣的流速在預定流速以下時，使落下至設於上述吸 收塔底部之吸收塔底部液體儲存槽的吸收液經由第2液體儲存 槽，回流於供應吸收液至吸收塔內的吸收液儲存槽內。 此外，第2之液體儲存槽可使用維修用吹槽，或者經由第 I 111 裝 I 1 1 ^ (請先聞讀背面之注意事項-?坎寫本頁) 本紙張尺度適用中國國家橾準（CNS ) A4規格（210X297公釐） -16- 4386 19 經濟部中央榉準局兵工消资合作社印製 A7_____B7_五、發明説明（14 ) 2液體儲存槽，於回流吸收液儲存槽內循環系中使用維修用吹 .槽、吹槽泵所成吸收液之維修用循環系亦可》 即，上述維修用吹槽、吹槽泵所成之吸收液的維修用循環 系是在進行上述吸收塔淸掃等之時，以往即已安裝有可暫時儲 存吸收塔內的吸收液之用，且維修用吹槽的容積僅具有使存在 設於上述吸收塔底部的液體儲存部之吸收液全部暫時地退出而 與液體儲存部相同以上的容積。 因此無吸收塔上升乃至關閉時，使噴嘴噴出吸收液之大致 全部的量不會到達消霧器而在斷腰狀態下落至液體儲存部，當 儲存於上述液體儲存部的吸收液過多時，使用容積大的維修用 吹槽時’即可有效地退出，同時可不須要大的液體儲存部尺寸 0 又’退出至維修用吹槽等的第2液體儲存槽之吸收液如未 能回流至吸收液儲存槽側時，即無法期待隨後的順暢運轉。 另一方面，以維修用吹槽形成第2液體儲存槽時，在上述 維修動作完成後，或者淸掃後，由於附設有使退至第2液體儲 存槽之吸收液回流至吸收液儲存槽側的泵，因此本發明可使用 上述既設的泵（吹槽泵）使退至第2液體儲存槽的吸收液可一 邊回流至吸收液儲存槽側而持續地運轉。 因此，根據本發明不致造成液體儲存部尺寸無謂地增大及 新設乃至形成大型化之迴流泵，即使吸收塔上升時或者關閉時 皆可使吸收液順利地連續循環。 又’經由第2液體儲存槽而迴流至吸收液儲存槽的循環系 在使用維修用吹槽、吹槽泵所的之吸收液維修用循環系時，經 裝 訂 線 (请先Μ讀背面之注意事項#4寫本頁) 本紙張尺度適用中國國家標準（CNS > Α4现格（210X297公釐） -17- 438619 A7 經濟部中央輮準局貝工消费合作社印装 B7五、發明説明（15 ) 由上述維修用循環系之儲存槽的回流在吸收塔上升時及關閉時 進行即可。 藉此，於吸收塔上升時及關閉時，當廢氣的流速到達加載 流速爲止，使上述吸收液的噴流全量落下至液體儲存部，但是 該落下之吸收液會經由吸收塔下部液體儲存部而退避排出第2 液體儲存槽，可經由吸收液回流通道而緩慢地回流至吸收液儲 存槽，可從吸收塔上升時連續運轉至關閉爲止。 又，申請專利範圍第1 8項所記載之發明是關於最適當實 施申請專利範圍第i 7項發明之裝置的發明，藉由吸收塔下部 朝著頂部通氣的廢氣而隨吸收液予以氣液接觸，藉此構成可將 上述廢氣中之目的成份吸收於吸收液內之濕式廢氣處理裝置中 ，其特徵爲： 具備：吸收塔底部液體儲放槽：接受來自該吸收塔底部液 體儲存槽的第2液體儲存槽：供應吸收液於吸收塔內之吸收液 儲存槽；經由上述吸收塔底部液體儲存槽及第2液體儲存槽而 與吸收液儲存槽連結之吸收液回流通道：及，上述廢氣的流速 在預定速度以下時，使上述吸收塔底部液體儲存槽的吸收液經 由上述第2液體儲存槽而回流至吸收液儲存槽之控制手段。 此時*如申請專利範圍第1 9項所記載，爲實施上述申請 專利範圍第1 8項之更適當的發明，可具備使吸收液儲存槽內 部加壓之加壓手段，及控制使上述加壓手段朝著對吸收塔之吸 收液供應壓力形成一定方向的控制手段。 即，例如藉第2液.體儲存槽回流至吸收液儲存槽的循環系 中使用i隹修用吹槽、吹槽泵所成吸收液之維修用循環系時，經 I I II - u It「 . I (請先閲讀背面之注意事項1W寫本頁) 本紙張尺度逍用中國國家橾準（CNS ) A4規格（2Ι0Χ297公釐） -18- 經濟部中央搮隼局貝工消费合作社印製 '4386 1 9 A7 B7五、發明説明（16 ) '由上述維修用循環系對儲存槽的回流是當吸收塔上升時及關閉 時，上述吸收液的噴流全量會落下至液體儲存部，使其吸收液 經由吹槽回流至吸收液儲存槽時*上述吸收液儲存槽的液面與 一般運轉時比較爲高，換言之由於供應至供應手段之吸收液的 重力加成量爲變動量，因此會使供應手段之噴流液量變動。 如上述，本發明係以可加壓控制儲存槽之儲存液面上部空 間的構成，可對應上述吸收液之重力加成量的變動而控制作用 於其液面上方空間的壓力，而可不論該儲存部的液面上下皆可 供應一定的吸收液。 又，申請專利範圍第2 0項所記載的發明是在連接鍋爐或 燃燒機等燃燒廢氣排出源與煙囪等之該排氣大氣放出部的主通 道上|利用廢氣的流速而在廢氣中隨著吸收液之兩者的氣液接 觸|藉吸收廢氣中目的成份之吸收液的濕式吸收塔所成的廢氣 處理方法中|其特徵爲： ’ 上述廢氣之吸收塔內的流速在預定速度以下時，從上述吸 收塔所排出之處理後的廢氣是利用旁通通道而回流至吸收塔入 口側。 又|有效實施申請專利範圍第2 0項的發明之廢氣處理裝 置是如申請專利範圍第2 1項所記載，具備： 使上述吸收塔所排出之處理後的廢氣回流至吸收塔入口側 之旁通通道； 上述廢氣的吸收塔內流速在預定速度以下時，開放上述旁 通通道控制使處理後廢氣回流至吸收塔入口側之控制手段。 根據上述之發明•當吸收塔上升及關閉時之廢氣的塔內流 ----------^------1T------.^ (請先聞讀背面之注意事項灰4寫本頁) 本紙張尺度逍用中國國家標準（CNS > A4規格（210X297公釐） -19 - 438619 A7 B7 五、發明説明(17 ) 經濟部中央標準局男工消费合作社印製 速爲加載流速以下時，開放上述旁通通道使處理後的廢氣回流 至吸收塔入口側*藉此使用鍋爐或燃燒機等廢氣排出源之廢氣 的增速，補充氣體流量而可維持塔內流速至加載流速以上。 另外又如申請專利範圍第2 2項所記載，於上述吸收塔內 設置可變之廢氣通過面積的通過面積可變手段，使上述廢氣的 塔內流速在預定速度以下時，可藉上述通過面積可變手段縮小 吸收塔內的廢氣通過面積，且與其不能對應的場合，開放旁通 通道使處理後的廢氣回流吸收塔入口側，可藉此使導入上述吸 收塔內之廢氣的塔內流速更加增速，並且可刪減不必要的風扇 動力。 另外，通過面積可變手段係於吸收塔內沿著廢氣流動方向 垂直延伸設置至噴嘴噴流領域爲止，構成可調節廢氣的通道寬 度使廢氣的流速維持在加載流速以上的分割板，藉此減少循環 風量而可大幅地使廢氣在塔內的流速增加。 此外，申請專利範圍第23項所記載之發明中，於吸收塔 內使儲存在吸收塔之儲存槽的吸收液從噴射噴嘴噴出，同時使 其噴射流與廢氣於吸收塔內自下方朝著上方運轉流動而氣液接 觸，吸收除去廢氣中的目的成分*同時以設於吸收塔上部之消 霧器捕捉隨廢氣而產生霧狀吸收液之濕式廢氣處理裝置中•其 特徵爲： 在上述消霧器下部設置接受從該消霧器流下之吸收液的收 容器，其收容器上連通朝下方延伸設置預定長度之回流液配管 的上端部，同時在該配管下端部設置可以吸收塔內的預定位置 放出上述回流液之開口。 婧 先 閾 讀 背 面 之 注 訂 線 本紙張尺度適用中國國家標準（CNS ) A4規格（210X297公釐） _ 2〇 _ 438619 經濟部中央橾率局貝工消费合作社印製 A7 B7__五、發明説明68 ) . 根據上述之發明，即使使吸收塔內的廢氣流動速度高速化 ，隨著該廢氣而大幅增加到達消霧器之吸收液的液量時|可藉 由收容器將消霧器落下的液體利用回流液配管流下至消霧器的 預定長度下方而回流至塔內，因此隨淸洗處理後的廢氣從吸收 塔排出的吸收液噴霧僅有極少量的殘留，即使形成高速化之吸 收塔內廢氣的塔內速度（載流速度）*仍可盡可能形成少量之 含於淸洗後排氣內吸收塔所排出的吸收液噴霧，其結果可獲得 廢氣處理操作效率的提高，運用上極爲有利》 再者，後述之實施形態中，圖式例之噴射噴嘴係向上設置 •雖是使柱狀噴射流向上噴出•但是本發明之噴射噴嘴的方向 不僅限於向上者。但是，申請專利範圍第2 4項之噴射噴嘴的 方向是以向上的裝置爲前提。 申請專利範圍第2 4項的發明之上述噴射噴嘴係以向上者 ，在較此向上噴嘴所噴射之液柱高度的上方位置，最好是在消 霧器正下方飛散吸收液儲存區域的下方，且從向上噴嘴噴射之 液柱高度的上方位置上，使上述回流液配管的下端開口定位， 並且最好是如申請專利範圍第2 5項所記載，將上述回流液配 管的下端開口形成噴嘴狀，構成可從該下端開口朝著液柱噴出 回流液· 根據上述之發明，在噴射流的正上方（液柱高度頂部）附 近的吸收部上•使回流液配管所回流的吸收液與噴射噴嘴所噴 射之吸收液的噴射流同時，並可再次對於廢氣達到吸收作用， 因此除上述效果之外，並可保持高水準的廢氣處理性能。 申請專利範圍第2 6項記載之發明係構成可將上述回流液 裝—— I I I 訂 I I i 線 (請先W讀背面之注意事項"_〜寫本頁) 本纸張尺度適用中國围家標準（CNS ) A4規格（210X297公釐） -21 - 438619 經濟部中央樣隼局貝工消费合作社印裂 A7 ΒΊ_五、發明説明¢19 ) 配管之下端開口定位於液體儲存部內者。 根據上述之發明，即使大幅增加到達消霧器之吸收液的液 量時，也可以將其順利地回送至液體儲存部形成可再利用者。 〔圖示之簡軍說明〕 第1圖是表示本發明第1實施形態之濕式氣體處理裝置之 槪略圖。 第2圖係於第1圖之氣體處理裝置中，表示取得氣體流速 與S 0 2之除去率的關係例之圖表。 第3圖爲本發明第2實施形態之吸收液重力供應方式的濕 式氣體處理裝置之槪略構成圖。 第4圖是表示第3圖之導水管狀吸收液管的配設例，（A )是表示一段水平配列時的流線圖* ( B )是表示兩段鋸齒狀 配設時的流線圖。 第5圖是表示第4 (A)圖之導水管狀吸收液管的配設狀 態與吸收液的流通狀態之部份透視圖，（A)係表示未在導水 管狀吸收液管側壁上面設置缺口者，（B)是表示在導水管狀 吸收液管側壁上面設置缺口者。 第6圖是與上述實施形態表示之導水管狀吸收液管不同， 是表示以上部封閉式管狀構件構成上述吸收液管之實施例，（ A)爲吸收液管的下面呈剖面圓形之半圓管狀構件，（B)係 使用剖面爲中空圓形的管狀構件1， （C)是使用剖面橢圓形 管狀構件，（D)是在與其兩側側壁之空隙部的對面側上沿著 軸線方向穿設多數個小孔，（E)是在與其兩側側壁之空隙部 I 裝 n ϋ ^ ί II ^ (請先閎讀背面之注意事項产4-寫本頁) 本紙張尺度適用中國國家橾準（CNS ) A4洗格（210X297公釐} -22- 438619 經濟部中央標準局負工消费合作社印製 A7 B7五、發明説明紅） 的對面側上沿著軸線方向斷續地穿設縫隙開口所構成者。 第7圖是表示本發明第3實施形態之濕式氣體處理裝置的 槪略圖。 第8圇是表示第7圖分割板之第1變形例之濕式氣體處理 裝置的要部槪略圖。 第9圖是表示第7圖分割板之第2變形例之濕式氣體處理 裝置的要部槪略圖。 第10圖是表示第7圖分割板之第3變形例之濕式氣體處 理裝置的要部槪略圖。 第11圖是表示第7圖分割板之第4變形例之濕式氣體處 理裝置的要部槪略圖。 第12圖是表示本發明第4實施形態之濕式氣體處理裝置 的構成槪略圖》 第13圖是表示相對於鍋爐運轉時間之廢氣塔速的變化圖 表。 第14圖是表示連接廢氣排出源與大氣放出部的主通道上 間隔有濕式吸收塔所成之本發明第5實施形態之廢氣處理系統 (A)爲吸收塔上升前之檔板的開關狀態及廢氣的流動，（B )爲來自鍋爐對於吸收塔之導入廢氣的塔內流速在加載流速以 上時之檔板的開關狀況及廢氣的流動圖。 第15圖是表示吸收塔內設置限制廢氣通路寬度之分割板 的第14圖發明之變形例之廢氣處理系統的槪略圖。 第16圖是表示吸收塔內設置限制廢氣通路寬度之分割板 的第14圖發明之其他變形例的廢氣處理系統之槪略圖。 ---------¾------ΐτ------^. (請先聞讀背面之注意事項^'--从寫本頁) 本紙張尺度適用中國國家標準（CNS ) A4規格（210X297公瘦） -23- 4386 19 at B7 五、發明説明fel ) 第1 7圖是表示連接廢氣排出源與大氣放出部的主通道上 間隔有濕式吸收塔所成之習知廢氣吸收系統的槪略構成圖。 第1 8圇是表示本發明第6實施形態之濕式廢氣處理裝置 的槪要之前視圖β 第19圖爲第18圖之側視圖。 第2 0圖爲裝著於第1 8圖裝置之消霧器之擴大部份透視 圖。 第2 1圖是表示第1 8圖發明之變彤例之濕式廢氣處理裝 置的槪要圖。 第2 2圖是爲說明第1 8圖之發明，而表示對於塔內氣體 流速與消霧器出口之噴霧濃度的關係之試驗結果對數圖表。 第2 3圖是爲說明第1 8圖之發明，而表示對於塔內氣體 流速與消霧器入口之噴霧飛散率的關係之試驗結果對數圖表。 第24圖之（Α)是表示習知濕式氣體吸收塔的槪略構成 圖，（Β)是表示使用於（Α)之向上噴嘴群及其配管狀況的 透視圖。 ----------^------1T----.--0 (請先閱讀背面之注意事項声1¼本頁) 經濟部中央橾準局Μ工消费合作杜印製The Central Government Bureau of the Ministry of Economic Affairs, Shellfish Consumer Cooperation, Du printed 4386 1 9 at _____B7__ 5. Description of the Invention (t) [Technical Field of the Invention] The present invention is a wet gas that can remove harmful components and other components from the exhaust gas. The treatment method and the device thereof, in particular, relates to a wet gas treatment method and a device thereof which can effectively perform gas-liquid contact with the absorption liquid and coal or heavy oil and other burned exhaust gas. [Conventional Technology] In the past, various types of gas-liquid contact devices have been used in wet type flue gas desulfurization devices that remove harmful substances such as sulfur dioxide from the exhaust gas of coal-fired boilers. Among them, one of the gas-liquid contact devices It is, for example, a so-called liquid column type device disclosed by the present inventor in Japanese Patent Laid-Open No. 5 9-5 3 8 2 8. The device sprays an absorption liquid such as a lime suspension upward from a plurality of nozzles arranged in the absorption tower, and appears as a columnar shape. The smoke is vented in the jet to absorb sulfur dioxide containing exhaust smoke. At the same time, it can effectively remove dust such as soot. In addition, its basic structure is a schematic diagram as shown in FIG. 24 (A). A smoke exhausting section 8 is provided above the 'absorption tower 2', and a smoke exhaust introducing section 3 forming an inlet of the exhaust gas 1 is provided at the lower section. A header 190 is arranged in a plurality of rows in the lower part of the absorption tower 2. For example, a plurality of upward nozzles 4 shown in FIG. In addition, the lower part of the absorption tower 2 is configured so that the absorption liquid such as a lime suspension can be stored in the funnel-shaped liquid storage section 5 6 and returned to the absorption liquid storage tank 5 7 through the recovery pump 2 1 a. 5 Once again through the discharge pump 2 1 b flow switch valve 6 0 and the main pipe 1 9 0 to communicate with the upward nozzle 4 »This paper size applies the Chinese National Standard (CNS) A4 size (210X297 mm) III nun K ^ line (please first Read the notes on the back of this page, and write this page) Central Samples Bureau of the Ministry of Economic Affairs, Mβζ Industrial Consumer Cooperative Cooperative, printed 4386 1 9 A7 A / __B7 V. Description of the invention) In addition, a plurality of upward nozzles are formed to form the above matrix The nozzle group composed of 4 can form the absorption liquid 5 into a liquid columnar jet 5 upward. At the same time, the exhaust gas 1 introduced from the smoke exhaust introduction part 3 and vented toward the upper part of the tower follows the flow rate according to the flow rate. The jet-shaped absorption liquid 5 rises, and contacts the gas-liquid by passing through the jet 5a spreading in an umbrella shape at the top. Subsequently, the absorption liquid 5 separated with the exhaust gas 1 by the mist eliminator 6 provided on the upper part of the absorption tower 2 near the apex of the jet stream can be recovered in the absorption liquid storage tank 57. The absorption liquid 5 dropped directly to the liquid storage portion 56 is sent to the absorption liquid storage tank 57 by the recovery pump 21a. In the gas-liquid contact device configured as described above, the pump 2 1 b is operated through the flow switch valve 60 and the main pipe 19 0, and the absorption liquid 5 is sprayed upward from the upward nozzle 4 to cause the smoke exhaust introduction portion 3 side to be introduced. The exhaust gas 1 is brought into gas-liquid contact through the jet 5a, and the exhaust gas (purified gas) 7 after the treatment such as the removal of sulfur dioxide gas is led out from the smoke exhaust duct 8 on the upper side. 'Furthermore, in the above-mentioned technique of spraying the absorption liquid 5 upward, not only does the absorption liquid 5 require a long round-trip (rise, fall) time The liquid 5 forms a droplet 1 so that the gas-liquid contact effect can be increased. When the sulfur dioxide gas contained in the exhaust gas is small, only the height of the liquid column can be changed to perform economic operation. In addition, the absorption liquid flows down to 下Compared with the so-called filling method in which a gas is contacted, the tower filled with a grid has many advantages, such as preventing the fluid passage from being blocked. In the case of the above-mentioned technology, the injection pump 2 1 b is operated, and the absorption liquid 5 stored in the liquid storage portion 56 or the absorption liquid storage tank 57 is circulated on the main pipe 1 90 side, and is set by the nozzle 4 The spray pressure will spray the absorption liquid 5 IIIIII Order II 1 (1 f ^ (Please read the note on the back first: this page) The paper size is in accordance with the Chinese National Standard (CNS) A4 specification (2 丨 〇297mm)- 5 * Printed by the Consumers' Cooperative of the Central Bureau of Standards, Ministry of Economic Affairs 4 386 1 9 at _. ____B7 V. Description of the invention) To a predetermined height》 Furthermore, the injection pump 2 1 b in this figure is shown as a single component to simplify the description. * However, a plurality of pumps are actually used, so there will be compact equipment and equipment costs. , Reduction of running costs and other issues. In addition, in order to improve the efficiency of gas-liquid contact between the exhaust gas and the absorption liquid, it is necessary to provide a plurality of nozzles for atomizing the absorption liquid that contacts the exhaust gas. Therefore, there must be a plurality of matrix-shaped nozzles as shown in No. 2 4 (B) 囵. There is a problem that the nozzle group for absorbing liquid is discharged, etc., and the load on the equipment is increased. Therefore, for example, in German Patent No. DE 1-1 7 6 9 9 4 5 or Japanese Patent No. Hei 9-50779 No. 2, a tank for storing and supplying the suspension liquid for circulating the nozzle is provided, and the liquid level of the tank is set. It is set higher than the nozzle ejection position, so that the absorption liquid ejected by the nozzle is separated into absorption liquid and gas with the gas in the upper part of the absorption tower. The separated absorption liquid can be kept in the tank and the gravity difference of the liquid level of the tank can be used. The suspension is sprayed out through the nozzle, and the suspension of the nozzle can be sprayed and circulated by using the difference in gravity without using a jet pump. However, in the related art described above, although the liquid level of the tank storing the absorption liquid is based on the condition that the position is higher than the ejection position of the nozzle in the absorption tower, the absorption tower generally has a considerable height, and the liquid at a position higher than the height is set. When facing the surface, there are disadvantages such as that the height of the groove must be increased. In addition, in the gas scrubbing device of the flue gas desulfurization device, the gas generation source of the boiler and the like generally have load fluctuations. Therefore, in any of the above devices *, when the gas flow rate is reduced, the gas flow rate will not be able to attract and absorb Liquid · Therefore, the gas-liquid contact between the absorption liquid and the gas stream cannot be smoothly performed, and not only the sulfur dioxide gas or dust contained in the exhaust gas can not be effectively removed, but also I — ^ n I ^ 11 H] ^ ( Please read the precautions on the reverse side of this page before writing this page.) The paper scale is applicable to China National Standard (CNS) A4 specifications (210X297 mm) -6- 438619 A7 B7 V. Description of the invention 6) * Absorbent liquid, in other words, in The circulation of the absorption liquid in the tank is difficult, and as a result, the liquid level in the tank is gradually lowered. Finally, it will be difficult to absorb the liquid with its own weight. 0 In addition, in any of the above-mentioned devices, the discharge speed of the absorption liquid, in other words, the discharge height It increases and decreases in proportion to the flow rate of the exhaust gas. Therefore, as shown in Figure 13, T1 when the inside of the absorption tower rises to T2 when it falls. When the combustion capacity on the burner side is small, the exhaust gas is reduced. It is not possible to increase the spraying height of the absorption liquid sprayed from the nozzle to a level higher than the reference level. As a result, almost the entire amount of the spray flow cannot reach the defogging gas provided at the top of the tower and falls to the liquid storage part in a waist-folded state. In many cases, the absorption liquid stored in the liquid storage unit cannot be used. Therefore, in the conventional device, since the absorption liquid can be continuously circulated, the size of the liquid storage portion 56 must be increased, or only the recovery pump 2 1 a for the return flow should be prepared for a large capacity when the absorption tower 2 is raised and lowered. Material, but it will cause unnecessary increase in equipment costs. In addition, the spray (liquid droplets) of any of the above-mentioned devices that also absorb the target components such as sulfur dioxide gas with the exhaust gas impacts the curved plate of the spray purifier on the upper part of the absorption tower and falls into the absorption tower to continuously circulate the absorption liquid, but As in the conventional device described above, when the gas flow rate in the tower is generally 4 to 5 m / s, the mist eliminator can be used to supplement it. However, in recent years, due to the improvement of processing capacity and space saving, it is necessary to increase the gas flow rate in the tower. To e.g. 5. Requirement for high speed above 5m / s》 +, once the gas speed is increased to 5. Above 5 m / s +, the droplets in this part of the mist eliminator cannot be drained out, but with the gas and the absorbed droplets are discharged out of the tower at the same time, released into the atmosphere 1 and sent to the processing equipment in the later stage Waiting is not ideal. This paper size applies to Chinese national standards (CNS > A4 size (2 丨 0X297 mm) ------------ installation ------ order ------ line {please first Read the note on the back ^^ Xiang Shengbu write this page) Printed by the Central Government Bureau of the Ministry of Economic Affairs, printed by the Shellfish Consumer Cooperative 4 3 8 6 1 9 , 5. The flow velocity of gas above 5m / s will greatly increase the amount of absorbed liquid reaching the mist eliminator with the gas. Therefore, the liquid that should fall from the mist eliminator cannot effectively fall, and a spiral droplet is formed at the entrance of the mist eliminator. The retention phenomenon (scattered absorption liquid storage area) occurs, which significantly reduces the spray removal performance. The reduction of the spray removal performance is caused by the spray (liquid droplets) being scattered again with the exhaust gas from the scattered absorption liquid storage area, so the Exhaust from the flue spray for exhaust is increased. [Explanation of the Invention] The present invention has been made in view of the shortcomings of the above-mentioned conventional technology, and provides an invention for a wet gas treatment that does not require the use of a jet pump or can smoothly recover the absorption liquid even when the gas flow rate is reduced with the absorption liquid. . Another object of the present invention is to provide an energy-saving method that does not require the use of a conventional upward nozzle, or does not require a large amount of power. It can reduce the burden on the nozzle equipment, etc., can achieve low cost, and can effectively make gas-liquid contact. The invention of wet gas treatment is aimed at. Another object of the present invention is to provide a wet exhaust gas treatment invention that does not needlessly increase the size and capacity of the liquid storage section and can effectively solve the problems caused when the above-mentioned exhaust gas flow rate is reduced. Another object of the present invention is to provide an exhaust gas treatment invention that can maintain the liquid column height of the absorption liquid above the reference level even when the flow rate of the exhaust gas introduced by the low-capacity combustion decreases when the absorption tower rises or is closed. 》 Another object of the present invention is to provide the exhaust gas contained in the absorption tower from the absorption tower even when the exhaust gas in the absorption tower has a high internal velocity (current-carrying velocity) (please read the note on the back first ^ # 朱 写 页) This paper size applies to Chinese National Standard (CNS) A4 specification U10X297 mm) _ 8 _ Printed by the Bayer Consumer Cooperative of the Central Bureau of the Ministry of Economic Affairs 3 86 1 9 A7 _B7___ V. Description of the invention (6 ).  It is an object of the invention related to wet exhaust gas treatment that the amount of spray (liquid) to be discharged is as small as possible. In order to solve the above-mentioned problems, the present invention is described in item 1 of the scope of the patent application. * The absorption liquid stored in the absorption liquid storage portion is directed from the absorption liquid outflow portion such as a nozzle in the absorption tower toward a predetermined direction (not only upwards and at the same time). Including a horizontal, downward) jet stream, which makes the jet stream contact the exhaust gas gas-liquid ventilated in the absorption tower, and absorbs / removes the target component in the exhaust gas in a wet gas treatment device. It is characterized by generating pressurized gas. The pressure tank forms the absorption liquid storage portion above the storage liquid surface, and uses the pressure of the pressurized gas to form the absorption liquid stored in the pressure tank from the nozzle portion in the absorption tower. According to the invention, the discharge volume of the absorption liquid of the nozzle can be determined by the pressured area of the pressure tank and the pressure of the pressurized gas. Moreover, the load of the combustion device such as a boiler can be changed, even when the gas flow rate in the absorption tower is changed. The pressure in the pressure tank can be controlled to correct this fluctuation direction I, so that a certain nozzle spraying liquid can be maintained at a substantially constant height. If the body flow rate is decreased, the absorbent can be recovered smoothly. In addition, the pressure of the gas in the pressurized tank can be averaged from the discharge amount of the absorption liquid from the tank, and the supply amount of the absorption liquid to the tank and the gas injection in the tank can be controlled to a predetermined pressure. Invention * Instead of directly absorbing the absorption liquid with a jet pump, pressurized gas such as compressed air is added to the pressurized tank. In other words, it is not necessary to use multiple pumps, only the pressurized pump and the supply of pressurized gas in it A gas compression source such as an air compressor is sufficient, so the device can be miniaturized and the equipment cost can be realized (please read the note on the back page of the first page).  The paper size of the edition is applicable to the National Solid Standard (CNS) 6 4 this grid (210X297 gong) -9-Printed by the Shell Consumer Cooperative of the Central Samples Bureau of the Ministry of Economic Affairs 4 3 8 6 1 9 A7 B7 V. Description of the invention & ) Reduction of transfer costs, etc. Also. Even if the absorption liquid supply nozzle is an upward upward device, it is not necessary to locate the upward nozzle at the upper part of the liquid surface of the pressure tank, and a low pressure tank can be set and can be freely arranged. In addition, as described in item 2 of the scope of the patent application, when the target component in the absorption liquid to be absorbed / removed is sulfur dioxide (S02), the pressurized gas is an oxygen-containing gas, and this oxygen-containing gas Spray into the storage liquid at the bottom of the pressure tank. It is sprayed from the nozzle to make contact with the gas-liquid of the exhaust gas. When the lime-containing suspension absorbent that absorbs S 0 2 is stored in the pressurized tank. • The sulfur dioxide can be oxidized due to the contact with the oxygen-containing gas. Calcium dihydrate (gypsum) ^ In addition, the present invention is a wet gas processing apparatus provided with an upward nozzle that sprays the absorption liquid above the nozzle portion in the absorption tower, as described in item 3 of the patent application scope, to generate pressurized air. The pressure tank forms the absorption liquid storage part in the space above the storage liquid surface. On the one hand, the recovery liquid part that can recover and absorb the above-mentioned target component is arranged in an absorption tower higher than the storage liquid level in the pressure tank. It is also possible to return the absorption liquid of the recovery unit to the outlet end of the communication pipe on the pressurizing side, and position the liquid in the storage liquid in the pressurizing tank. According to the present invention, the absorption liquid for absorbing / removing the target component is recovered to the side of the pressurized tank through the recovery unit, and a reusable absorption liquid is formed. In addition, when a communication pipe for recovering the absorption liquid is opened in the recovery section toward the closed space inside the pressurized tank, the gas pressure in the space is diffused through the communication pipe into the absorption tower, and the function of the pressurized tank cannot be maintained. Therefore, the present invention refers to the * binding line for returning the absorption liquid to the pressure tank side by the recovery part (please read the precautions on the back first to write this page) This paper uses China National Kneading Ratio (CNS) A4 specifications { 210 × 297 mm) -10- 43 86 1 9 A7 B7_____ V. Description of the invention fe) The opening of the outlet end of the communication tube is positioned in the storage liquid in the above pressure tank, so that the pressure tank can be formed by using the absorption liquid in the communication tube. The gas pressure is sealed, and the recovery part is arranged at a predetermined position in the absorption tower higher than the storage liquid level in the pressure tank. Therefore, the liquid level in the communication tube can be raised to the inside of the pressure tank through the communication tube of the recovery part. Position of pressure balance. In addition, by setting the height difference of the communication pipe, the position of the recovery section and the pressure in the tank so that the liquid level in the communication pipe is lower than the position of the recovery section, the circulation of the absorption liquid from the recovery device to the pressure tank can be performed. The gas pressure sealing of the pressure tank can be performed by using the absorption liquid in the communication pipe. Furthermore, according to the present invention, when the absorption liquid is sprayed upward in the absorption tower and the absorption liquid is recovered by the recovery part provided in the upper part of the absorption tower, It falls to the bottom of the absorption tower, so only the above recovery part cannot recover 100%. Therefore, when the liquid level stored in the bottom of the absorption tower reaches a predetermined amount or more, it can be returned to the pressure tank by a low pressure pump. A part of the liquid is discharged simultaneously with the gas, so it can be replenished by the raw material supply pipe. In addition, the invention described in item 4 of the scope of patent application is to introduce the absorption liquid stored in the absorption liquid storage tank into the absorption tower, and make the absorption liquid flow with the exhaust gas flow rate along the exhaust passage in the absorption tower and The exhaust gas is in a gas-liquid contact and absorbs / removes the target component in the exhaust gas. The wet gas processing device is characterized in that it is provided on a plurality of absorption liquid pipes arranged substantially across the direction of the exhaust passage. The direction in which the liquid intersects with the above-mentioned exhaust gas venting direction * More specifically, an absorption liquid outflow portion in the form of an overflow or a discharge flow is formed in a substantially lateral direction, and the absorption liquid flowing out of the outflow portion contacts the exhaust gas flow in a cross-contact manner. Micronization is performed for gas-liquid contact. II (Please read the note on the back to write this page first) The printed paper size of the Consumer Cooperatives of the Central Procurement Bureau of the Ministry of Economic Affairs is applicable to the Chinese National Standard (CNS > Α4 wash grid (210X297 mm) -11-438619 A7 Central Standards Bureau of the Ministry of Economic Affairs-Industrial-Consumer Cooperation Du printed B7___ 5. Description of the invention) That is, the supply of the absorbent liquid of the present invention is to form an absorbent liquid that overflows or spouts in a generally transverse direction instead of the conventional one. Most nozzles are arranged in a matrix shape (see Figure 24 (B)), and the absorption liquid flowing out of the outflow part is atomized by the cross-contact with the above-mentioned exhaust gas stream to make gas-liquid contact. The above-mentioned invention is, for example, as described in item 5 of the scope of patent application, one or more sections (including the upper and lower zigzag arrangement) of the absorption liquid pipe group are arranged along one or more planes that substantially cross the exhaust path. It is preferable that the above-mentioned exhaust gas flow can be conducted in a gap portion between adjacent pipes of the pipe group arranged in the row. In addition, the structure of the absorbent pipe is as described in item 6 of the scope of patent application. At the same time as the above-mentioned open water-conducting tubular member constitutes the absorbent pipe, the water-conducting tubular member may be provided in a direction that intersects the ventilation direction. The means for forming the overflow in the substantially horizontal direction is also described in item 7 of the scope of the patent application. The upper closed tubular member constitutes the absorption liquid pipe, and can also be connected with the exhaust gas flow through the absorption liquid pipe. A slit-like opening or a plurality of small hole rows are provided along the tube axis direction on the surrounding surface of the part. According to the above-mentioned invention, it is only necessary to make the absorption liquid overflow or flow out in a substantially horizontal direction toward the gap portion side between the adjacent pipes, and the effect of reducing the equipment cost can be obtained. In addition, as described in item 8 of the scope of the patent application, the absorption liquid supply to the absorption liquid tube may also constitute the absorption liquid supply source using gravity. Specifically, the absorption liquid supply source is arranged in the absorption at a slightly different level. Above the liquid tube. Of course, the present invention can also adopt the configuration of the absorption liquid supply pump. At this time, the above-mentioned small supply pump can be formed. In addition to reducing the equipment cost, it can also reduce the power I n! II. (Please read the back first Note on this page) This paper size applies Chinese National Standard (CNS) Λ4 Washing (210X297 mm) -12- Printed by the Bayer Consumer Cooperative of the Central Sample Bureau of the Ministry of Economic Affairs 4 3 86 1 9 A7 B7_ 5. Description of the invention) In addition, the present invention is provided with absorption liquid pipes in which the exhaust passages are arranged in a plurality of predetermined gaps. As a result, the velocity of the exhaust gas can be increased at the gaps, and the speed can be increased. In the present invention, the absorption liquid flows out to the above-mentioned space portion where the exhaust flow is accelerated, and contacts the high-speed rising exhaust flow in a cross shape. Therefore, the absorption liquid is disturbed by the high-speed energy generated by the exhaust gas, and is formed into particles. In addition, the negative pressure caused by the rapid compression and expansion of the exhaust gas in the gap portion of the exhaust gas can simultaneously rapidly disperse the tiny droplets of the absorption liquid in the exhaust gas, and promote effective gas-liquid contact such as atomization of the absorption flow and the like. Supply of absorption liquid | The liquid column of the conventional liquid column type can be more effectively and efficiently absorbed in a short period of time, compared with the gas-liquid contact completed when the liquid column is spread out at the top, and it is discharged with the exhaust gas. / Remove the target component 0 in the exhaust gas, and make gas-liquid contact with the gaps between adjacent absorption liquids, and the outflow liquid film or linear flow of absorption liquid is sprayed out of the gaps, so it is not necessary For example, the conventional device is equipped with high-density nozzles, which significantly contributes to cost reduction. Furthermore, the above-mentioned liquid absorption pipe is constituted by a water-conducting tubular member. Especially when the above-mentioned serrated water-conducting pipe member is arranged, the exhaust passage is interposed between the drainage tubular members, so the exhaust system of the passage is compressed and expanded. Waiting for step I can promote effective atomization and minute droplet formation of the open surface of the drainage pipe member. In addition, as described in item 9 of the scope of the patent application, the present invention sprays the absorption liquid stored in the absorption liquid storage portion from a nozzle portion in the absorption tower in a predetermined direction (except for the upward direction and includes the lateral direction and the downward direction). The jet flow is in contact with the exhaust gas-liquid ventilated in the absorption tower, and the wet gas treatment method that absorbs / removes the target component in the exhaust gas is characterized by: (Please read the note item # 4 on the back first to write this page ) This paper size is applicable to China ’s Standards for Household Standards (CNS) M (210X2? 7mm) -13- Printed by the Shellfish Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 43 86 1 9 A7 B7 The exhaust gas passage ventilated in the absorption tower is controlled in a width region corresponding to the discharge amount, and the gas passage region of the exhaust gas passage can be adjusted. Therefore, according to the present invention, it is possible to reduce the gas flow in the absorption tower by changing the load of a combustion device such as a boiler. When the flow rate of the exhaust gas passage is reduced according to this ratio, the gas passage area of the controlled gas inflow area is controlled in accordance with the decrease in the flow rate. The gas flow rate is constant * As a result, the absorption liquid spraying height of the nozzle can be maintained at a substantially constant level. As a result, the absorption liquid can smoothly contact the absorption liquid with the gas and liquid of the gas with the flow velocity of the gas, which can not only effectively remove the smoke in the exhaust. The contained sulfur dioxide gas or dust can smoothly recover the absorption liquid in the upper part of the absorption tower * In other words, the circulation of the absorption liquid in the tank can be smoothly performed. At this time, as described in item 10 of the scope of patent application, stop from the above The jet of the absorption liquid from the nozzle portion where the gas flows into the blocked area can save unnecessary pump driving power, etc., and at the same time, prevent unnecessary absorption liquid circulation. The invention described in item 11 of the scope of patent application is an invention related to a wet gas treatment device that can smoothly implement the invention described in item 9 of the scope of patent application. The partition plate extended to the nozzle flow area is divided into a plurality of gas flow areas | It is provided with a path control means that can perform flow control or switch control of the gas inflow of the divided gas flow areas according to the above-mentioned exhaust gas amount. According to the above-mentioned invention, the gas flow rate in the absorption tower can be reduced, and when the flow velocity of the exhaust gas passage flow is reduced according to this ratio, one side of the plurality of gas basins spaced by the partition plate is closed or a narrow gas passage area is formed, thereby Corresponding to the decrease in the above flow rate, the gas passing area can be controlled to form a constant gas flow rate. The invention described in item 12 of the scope of patent application is the scope of the scope of patent application --------- ^ ------ ir ------- ^ (Please read the note on the back first Item difference. (This page is written on the page.) This paper is in accordance with the Chinese National Standard (CNS) A4 specification (2〗 0X297). -14- Printed by the Bayer Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 4 3 8 6 19 A7 B7 V. Description of the invention (12) * 11 The device described in item 1 * An absorption liquid storage section is arranged below the absorption tower, and the nozzle section is positioned in the absorption tower above it, and the wet gas treatment by a specific jet of absorption liquid above the nozzle section is displayed. An effective feature of the device is that the lower end of at least one of the dividing plates extending vertically along the flow direction of the exhaust gas to the nozzle jet flow area is extended to the absorption liquid storage section, and the liquid level of the absorption liquid is adjusted in the storage section. Can selectively make the lower end of the dividing plate submerged into the absorption liquid * to form a switch that can selectively open and close the gas path divided by the dividing plate ", that is, more specifically, forming different height positions of the lower ends of the dividing plates to absorb The adjustment of the liquid level of the liquid constitutes that the lower end of the corresponding dividing plate can be selectively submerged into the absorption liquid. Also * instead of adopting the above-mentioned structure, as described in Item 13 of the scope of patent application, at least one dividing plate which is vertically extendable along the flow direction of the exhaust gas to the nozzle flow area is formed on the side of the absorption liquid storage section, which can be raised and lowered freely. On the lower end side, the lower end of the partition plate is selectively lowered and submerged into the absorption liquid, and a path for selectively opening and closing the gas flow area divided by the partition plate may also be formed. Adjusting the level or selectively lowering the lower end of the dividing plate to submerge it into the absorption liquid. • It is possible to selectively open and close the path of the gas flow area. Furthermore, other control methods are as described in item 14 of the scope of patent application. The lower end side of at least one partition plate extending freely to the nozzle flow area is formed in the direction of the exhaust gas flow, and the gas inflow flow rate control of the gas flow area divided by the partition plate is configured by the swing turning of the lower end portion. Or switch control. That is, you can also swing the lower end of the above-mentioned dividing plate to close or make the adjacent passageway I nnni ^ {Please read the precautions on the back first to write this page) This paper is based on Chinese standards (CNS > A4 specifications ( 210X297mm) -15- Duty printing cooperation of the Central Bureau of Procurement of the Ministry of Economic Affairs 4386 1 9 a7 B7 V. Description of the invention (13) The entrance opening can be narrowed, or the lower end of the partition plate can be tilted down without falling In the above-mentioned related structure, by the swing steering at the lower end side of the partition plate, it is possible to easily control or switch the gas inflow gas flow rate in the gas basin. The invention described in the 15th item of the patent application It is characterized in that it constitutes a person who can turn the lower end of the dividing plate toward the exhaust gas introduction part side leading into the absorption tower * The exhaust gas introduced into the absorption tower from the introduction part is rectified and guided in the direction of the nozzle jet along the turning part. According to the above-mentioned invention, the above-mentioned dividing plate also has the function of an exhaust gas rectifying plate, which can make gas-liquid contact more smoothly. _ In addition | The invention described in the 16th aspect of the patent application, its characteristics The above-mentioned division plate is configured to be able to move substantially vertically with respect to the flow direction of the exhaust gas, and the passage cross-sectional area of the divided gas flow area can be adjusted by the movement of the division plate. According to the above-mentioned invention, corresponding to the fluctuation of the exhaust gas flow rate, Mobile partition plate • The person who can freely adjust the cross-sectional area of the channel of the gas basin. The invention described in item 17 of the patent application scope is characterized in that the exhaust gas that is ventilated from the lower part of the absorption tower to the top is used to follow the absorption liquid. In a wet-type exhaust gas treatment method in which the target component in the exhaust gas is absorbed by the gas-liquid contact, the exhaust gas is characterized in that when the flow velocity of the exhaust gas is below a predetermined flow rate, the absorption is dropped to the absorption provided at the bottom of the absorption tower. The absorption liquid in the liquid storage tank at the bottom of the tower is returned to the absorption liquid storage tank that supplies the absorption liquid to the absorption tower through the second liquid storage tank. In addition, the second liquid storage tank can use a maintenance blower or the first I 111 Pack I 1 1 ^ (Please read the precautions on the back-write this page first) This paper size is applicable to China National Standard (CNS) A4 (210X297 mm) -16- 4386 19 Printed by the Central Beef Associate Bureau, Ministry of Economic Affairs, Military Industry Consumer Cooperatives, A7_____B7_ V. Description of the invention (14) 2 Liquid storage tank, used for maintenance in the circulation system in the storage tank of reflux absorption liquid To blow. The maintenance circulation system of the absorption liquid formed by the tank and the blower pump is also possible. That is, the maintenance circulation system of the absorption liquid formed by the maintenance blower and the blower pump is performed when the absorption tower is cleaned. In the past, it has been installed to temporarily store the absorption liquid in the absorption tower, and the volume of the maintenance blow tank has only the capacity to temporarily withdraw all the absorption liquid existing in the liquid storage portion provided at the bottom of the absorption tower, and the liquid storage portion The same volume as above. Therefore, when the non-absorption tower rises or even closes, almost the entire amount of the absorption liquid ejected by the nozzle will not reach the mist eliminator and will fall to the liquid storage section in the state of broken waist. When there is too much absorption liquid stored in the liquid storage section, use When the maintenance tank with a large volume is used, it can be withdrawn efficiently. At the same time, a large liquid storage section size of 0 is not required. Also, if the absorption liquid from the second liquid storage tank such as the maintenance tank is not returned to the absorption liquid, With the storage tank side, the subsequent smooth operation cannot be expected. On the other hand, when the second liquid storage tank is formed by a maintenance blower, after the maintenance operation is completed or after cleaning, the absorption liquid returned to the second liquid storage tank is returned to the absorption liquid storage tank side. Therefore, according to the present invention, the existing pump (blow tank pump) can be used to continuously operate the absorption liquid returned to the second liquid storage tank while returning to the side of the absorption liquid storage tank. Therefore, according to the present invention, the size of the liquid storage unit is not increased unnecessarily, and a new size or even a large-sized return pump is formed. Even when the absorption tower is raised or closed, the absorption liquid can be continuously circulated smoothly. Also, the circulation system that flows back to the absorption liquid storage tank through the second liquid storage tank is the gutter (please read the note on the back side first) when using the maintenance liquid circulation system of the maintenance blow tank and blow tank pump. Item # 4 write this page) This paper size is in accordance with Chinese national standards (CNS > Α4 now (210X297 mm) -17- 438619 A7 Printed by the Brigade Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs. ) The recirculation of the storage tank of the maintenance circulation system may be performed when the absorption tower is raised or closed. Thus, when the absorption tower is raised or closed, when the flow rate of the exhaust gas reaches the loading flow rate, The jet is dropped to the liquid storage part in full, but the dropped absorption liquid will escape through the liquid storage part in the lower part of the absorption tower and be discharged to the second liquid storage tank, which can be slowly returned to the absorption liquid storage tank through the absorption liquid return channel, and can be absorbed from When the tower rises, it continues to operate until it is closed. In addition, the invention described in the 18th scope of the patent application is the invention of the device that best implements the 7th invention in the patent scope. The exhaust gas vented from the lower part of the absorption tower toward the top is brought into gas-liquid contact with the absorption liquid, thereby constituting a wet-type exhaust gas treatment device capable of absorbing the target components in the exhaust gas into the absorption liquid, which is characterized by: Liquid storage tank at the bottom of the absorption tower: A second liquid storage tank that receives liquid storage tanks at the bottom of the absorption tower: an absorption liquid storage tank that supplies absorption liquid in the absorption tower; through the liquid storage tank at the bottom of the absorption tower and the second liquid storage An absorption liquid return channel connected to the absorption liquid storage tank; and when the flow rate of the exhaust gas is below a predetermined speed, the absorption liquid in the liquid storage tank at the bottom of the absorption tower is returned to the absorption liquid storage through the second liquid storage tank Means for controlling the tank at this time * As described in item 19 of the scope of patent application, in order to implement a more appropriate invention in item 18 of the scope of patent application, pressure means for pressurizing the inside of the absorption liquid storage tank may be provided, And control so that the above-mentioned pressurizing means toward a certain direction of the pressure of the absorption liquid supply tower control means. That is, for example, by the second liquid. In the circulation system for returning the bulk storage tank to the absorption liquid storage tank, when the maintenance circulation system of the absorption liquid formed by the repair tank and the blower pump is used, I I II-u It``.  I (Please read the note on the back 1W first to write this page) This paper size is in accordance with China National Standard (CNS) A4 specification (2Ι0 × 297 mm) -18- Printed by the Shellfish Consumer Cooperative of the Central Government Bureau of the Ministry of Economic Affairs' 4386 1 9 A7 B7 V. Description of the invention (16) 'The reflux of the storage tank by the above-mentioned maintenance circulation system is that when the absorption tower rises and closes, the entire amount of the jet of the absorption liquid will fall to the liquid storage part to make the absorption liquid When returning to the absorption liquid storage tank through the blowing tank * The liquid level of the absorption liquid storage tank is higher than during normal operation. In other words, the gravity added amount of the absorption liquid supplied to the supply means is a variable amount, so the supply means will be changed. The fluid flow of the jet fluctuates. As described above, the present invention has a structure capable of controlling the upper space of the storage liquid surface of the storage tank under pressure, and can control the pressure acting on the space above the liquid surface in response to the change in the gravity addition amount of the absorption liquid, regardless of the A certain amount of absorbing liquid can be supplied on the liquid surface of the storage section. In addition, the invention described in the scope of patent application No. 20 is a main passage connecting the exhaust gas emission source such as a boiler or a burner with a chimney and the exhaust air emission portion. Gas-liquid contact of both absorption liquids | In an exhaust gas treatment method by a wet absorption tower that absorbs an absorption liquid of a target component in the exhaust gas, it is characterized by: 'When the flow velocity in the above-mentioned exhaust gas absorption tower is below a predetermined speed The treated exhaust gas discharged from the absorption tower is returned to the absorption tower inlet side by using a bypass passage. Also | The exhaust gas treatment device for effectively implementing the invention in the scope of patent application No. 20 is as described in the scope of patent application No. 21, and is provided with: the treated exhaust gas discharged from the absorption tower is returned to the side of the inlet of the absorption tower When the flow velocity in the absorption tower of the exhaust gas is below a predetermined speed, the above-mentioned bypass passage is opened to control the control means for returning the treated exhaust gas to the inlet side of the absorption tower. According to the invention described above, the internal flow of exhaust gas when the absorption tower rises and closes ---------- ^ ------ 1T ------. ^ (Please read the notes on the back of this article before writing this page.) This paper size is not in accordance with the Chinese national standard (CNS > A4 size (210X297mm) -19-438619 A7 B7 V. Description of invention (17) Ministry of Economy When the printing speed of the Male Standards Consumer Cooperative of the Central Bureau of Standards is below the loading flow rate, the above bypass channel is opened to return the treated exhaust gas to the entrance side of the absorption tower *, thereby using the exhaust gas exhaustion sources such as boilers or burners to increase the exhaust gas. The flow rate of the gas can be replenished to maintain the flow velocity in the tower above the loading flow rate. In addition, as described in item 22 of the scope of the patent application, a variable exhaust gas passage area in the absorption tower is provided with a variable passage area method to make the exhaust gas When the flow velocity in the tower is lower than the predetermined speed, the exhaust gas passage area in the absorption tower can be reduced by the above-mentioned variable area method, and if it cannot correspond to it, open the bypass channel to return the treated exhaust gas to the inlet side of the absorption tower. This makes the flow velocity of the exhaust gas introduced into the absorption tower faster, and eliminates unnecessary fan power. In addition, it is tied to the area by means of variable area. The receiving tower is vertically extended along the flow direction of the exhaust gas to the nozzle jet flow area, and a partition plate can be configured to adjust the width of the exhaust gas channel to maintain the flow velocity of the exhaust gas above the loading flow rate, thereby reducing the circulating air volume and greatly allowing the exhaust gas to pass through the tower. In addition, in the invention described in claim 23 of the scope of patent application, the absorption liquid stored in the storage tank of the absorption tower is ejected from the injection nozzle in the absorption tower, and the jet stream and the exhaust gas are caused to flow in the absorption tower. It flows from the bottom to the top and comes into contact with gas-liquid, absorbs and removes the target components in the exhaust gas * At the same time, it uses a mist eliminator installed on the upper part of the absorption tower to capture the wet exhaust gas treatment device that generates mist-like absorption liquid with the exhaust gas. For: The lower part of the mist eliminator is provided with a receiving container for receiving the absorbing liquid flowing down from the mist eliminator, and the upper end of the receiving container communicates with a predetermined length of return liquid pipe extending downward, and at the same time, a lower end of the pipe can be provided. The opening of the above-mentioned return liquid is released at a predetermined position in the absorption tower. Printed with the Chinese National Standard (CNS) A4 specification (210X297 mm) _ 2〇 _ 438619 The Central Government Bureau of the Ministry of Economic Affairs, Shellfish Consumer Cooperative, printed A7 B7__ V. Invention Description 68).  According to the above-mentioned invention, even if the exhaust gas flow rate in the absorption tower is increased at a high speed, the amount of the absorption liquid reaching the mist eliminator is greatly increased with the exhaust gas. The liquid falling from the mist eliminator can be recycled by the container. The liquid piping flows down to a predetermined length of the mist eliminator and returns to the tower. Therefore, the absorption liquid spray discharged from the absorption tower with the exhaust gas after the scrubbing treatment has only a small amount of residue, even if the exhaust gas in the absorption tower with a high speed is formed. The speed in the tower (current-carrying speed) * can still form a small amount of the absorption liquid spray contained in the absorption tower exhausted in the exhaust after the scrubbing. As a result, the efficiency of the exhaust gas treatment operation can be improved, which is extremely advantageous in use. In the embodiment to be described later, the spray nozzle of the drawing example is provided upwards. Although the columnar jet is ejected upward, the direction of the spray nozzle of the present invention is not limited to the upward direction. However, the direction of the spray nozzle of the 24th patent application is based on the upward device. The above-mentioned spray nozzle of the invention in the 24th aspect of the patent application is the upward one, and it is preferably located above the height of the liquid column sprayed by the upward nozzle, and is preferably scattered below the absorbing liquid storage area directly below the mist eliminator. And from a position above the height of the liquid column sprayed from the upward nozzle, the lower end of the return liquid pipe is positioned, and the lower end of the return liquid pipe is preferably formed into a nozzle shape as described in item 25 of the patent application scope. According to the above-mentioned invention, the return liquid can be ejected toward the liquid column from the lower opening. According to the above-mentioned invention, on the absorption portion near the jet stream (the top of the liquid column height). The jets of the sprayed absorption liquid can simultaneously absorb the exhaust gas again, so in addition to the above effects, a high level of exhaust gas treatment performance can be maintained. The invention described in item 26 of the scope of patent application is composed of the above-mentioned recirculation liquid-III order II i line (please read the precautions on the back first " _ ~ write this page) This paper is applicable to Chinese homes Standard (CNS) A4 specification (210X297 mm) -21-438619 The central sample bureau of the Ministry of Economic Affairs, Shellfish Consumer Cooperative Co., Ltd. printed A7 ΒΊ_V. Description of the invention ¢ 19) The lower end of the pipe is positioned in the liquid storage department. According to the invention described above, even when the amount of the absorption liquid reaching the mist eliminator is greatly increased, it can be smoothly returned to the liquid storage section to be reusable. [Brief Description of the Army] Fig. 1 is a schematic view showing a wet gas processing apparatus according to a first embodiment of the present invention. Fig. 2 is a graph showing an example of the relationship between the obtained gas flow rate and the removal rate of S 0 2 in the gas processing apparatus of Fig. 1. Fig. 3 is a schematic configuration diagram of a wet gas processing apparatus using a gravity supply method of an absorption liquid according to a second embodiment of the present invention. Fig. 4 shows an example of the arrangement of the water-conducting tubular absorbent pipe shown in Fig. 3. (A) is a streamline diagram when one stage is arranged horizontally. (B) is a streamline diagram when two stages are arranged in a zigzag arrangement. Fig. 5 is a partial perspective view showing the arrangement state of the water-conducting tubular absorbent tube and the state of circulation of the absorbent liquid in Fig. 4 (A). (A) shows a person who has not provided a gap on the side wall of the water-conducting tubular absorbent tube. (B) indicates that a notch is provided on the side wall of the water-conducting tubular absorption liquid pipe. Fig. 6 is a different embodiment from the water-conducting tubular absorbent tube shown in the above embodiment, and shows an example in which the above closed tubular member constitutes the absorbent tube. (A) is a semicircular tube with a circular cross section on the lower surface of the absorbent tube. (B) is a tubular member 1 with a hollow circular cross-section, (C) is an oval-shaped tubular member with a cross-section, and (D) is provided along the axial direction on the side opposite to the gap between the side wall on both sides For many small holes, (E) is the gap I on the side wall on both sides of the hole. Ϋ ^ ί II ^ (Please read the precautions on the back side first-write this page) This paper size is applicable to Chinese national standards ( CNS) A4 (210X297 mm) -22- 438619 printed by the Central Standards Bureau of the Ministry of Economic Affairs and Consumer Cooperatives printed A7 B7 5. Invention Description Red) The gap opening is formed intermittently along the axis direction By. Fig. 7 is a schematic diagram showing a wet gas processing apparatus according to a third embodiment of the present invention. Fig. 8 is a schematic view of a main part of a wet-type gas processing apparatus showing a first modification of the division plate of Fig. 7; Fig. 9 is a schematic view of a main part of a wet-type gas processing apparatus showing a second modification of the division plate of Fig. 7; Fig. 10 is a schematic view of a main part of a wet-type gas processing apparatus according to a third modification of the division plate of Fig. 7; Fig. 11 is a schematic view of a main part of a wet-type gas processing apparatus showing a fourth modification of the division plate of Fig. 7; Fig. 12 is a schematic diagram showing the structure of a wet gas processing apparatus according to a fourth embodiment of the present invention. Fig. 13 is a graph showing changes in the exhaust gas tower speed with respect to the boiler operation time. Fig. 14 is a diagram showing a state in which the exhaust gas treatment system (A) according to the fifth embodiment of the present invention, which is formed by a wet absorption tower with a wet absorption tower spaced between the main passages connecting the exhaust gas exhaust source and the atmospheric emission portion, is a switch state of the baffle plate before the absorption tower rises; And the flow of the exhaust gas, (B) is the opening and closing conditions of the baffle plate and the flow chart of the exhaust gas when the flow rate of the exhaust gas introduced from the boiler to the absorption tower is above the loading flow rate. Fig. 15 is a schematic diagram showing an exhaust gas treatment system according to a modification of the invention of Fig. 14 in which a partition plate for limiting the width of the exhaust gas passage is provided in the absorption tower. Fig. 16 is a schematic diagram showing an exhaust gas treatment system according to another modification of the invention of Fig. 14 in which a partition plate for restricting the width of the exhaust gas passage is provided in the absorption tower. --------- ¾ ------ ΐτ ------ ^.  (Please read the precautions on the back ^ '-From the time of writing this page) The paper size is applicable to the Chinese National Standard (CNS) A4 specification (210X297 male thin) -23- 4386 19 at B7 V. Description of the invention fel) 1 FIG. 7 is a schematic configuration diagram showing a conventional exhaust gas absorption system formed by a wet absorption tower spaced on a main channel connecting an exhaust gas exhaust source and an atmospheric emission portion. Fig. 18 is a front view showing a wet exhaust gas treatment apparatus according to a sixth embodiment of the present invention. Fig. 19 is a side view of Fig. 18. Figure 20 is a perspective view of the enlarged part of the mist eliminator installed in the device of Figure 18. Fig. 21 is a schematic diagram showing a wet type exhaust gas treating apparatus according to a modification of the invention of Fig. 18; Figure 22 is a logarithmic graph of the test results showing the relationship between the gas flow rate in the tower and the spray concentration at the outlet of the mist eliminator to illustrate the invention of Figure 18. Fig. 23 is a logarithmic graph of the test results showing the relationship between the gas flow rate in the tower and the spray scattering rate at the inlet of the mist eliminator to explain the invention of Fig. 18. (A) of FIG. 24 is a schematic configuration diagram showing a conventional wet gas absorption tower, and (B) is a perspective view showing an upward nozzle group used in (A) and a piping condition thereof. ---------- ^ ------ 1T ----. --0 (Please read the note on the back of this page 1¼ this page) Printed by the Ministry of Economic Affairs, Central Bureau of Standards, M Industry and Consumer Cooperation

元件對照說明 1 2 2 AComponent comparison description 1 2 2 A

4 4 A4 4 A

4 C 廢氣 吸收塔 廢氣通道 》 排煙導入部 吸收液供應噴嘴 吸收液供應噴嘴群 本紙張尺度遑用中國國家榇準（CNS ) Α4規格（210X297公釐） •24- 經濟部中央橾準局貝工消费合作社印製 ! 4386 19 五、發明説明έ2 ) 5 5 a 6 6 a > 6 b 8 9 10 11 12 13 14 1 5 16 17 17a 18 19 2 0 2 1 2 2 2 3 2 4 2 4a > 24b 2 7 A7 B7 本紙張尺度適用中國®家標準（CNS > A4規格（2I0X297公釐> 吸收液 吸收液噴流 消霧器 板材列 排煙導出部 回收器 連通管. 槽 上部封閉空間 氣體噴吹管 吸收液供應管 流量控制閥 壓力控制閥 大氣開放管 加壓用壓縮機 原料供應管 抽取管 排水回收管 排水回收閥 緩衝槽 噴嘴閥 弧形管 回收管 吸收液儲存槽 I I n ,_ 訂 II 線 {請先閲讀背面之注意事項具本頁) -25- 438619 A7 B7 經濟部中央標準局貝工消費合作杜印装 五、 發明説明έ3 ) 2 7 a 液面 2 9 吸收液導入管 3 0 » 3 0 A，3 0 B 空隙部 3 1 3 1 A 吸收液管 3 1 c 半圓管狀構件 3 1 d 蓋體 3 2 廢氣流 3 4 中空圓形管狀構件 3 5 橢圓形管狀構件 3 6 小孔 3 7 縫隙開口 3 9 溢流 4 0 4 0 A，4 0 B 分割板 4 1 A 4 IB， 4 1C 廢氣流域 4 3 開關閥 4 3 A 4 3 C 流量開關閥 4 6 轉動板 4 8 支點 4 9 導管 5 6 液體儲存部 6 0 6 0 a 噴槽 6 1 回收管 6 2 壓力感測器 6 5 廢氣流速檢測感測器 本紙張尺度適用中國國家標準（CNS > A4规格（210X297公釐） 26- 經濟部中央標準局工消费合作社印装 控制電路 電磁開關閥 通道 控制電路 升壓風扇 旁通通道 楢板 主通道 檔板 收容器 回收液配管 噴嘴狀開口 垂直管路部 水平管路部 總管 側面開口 43 86 1 9 a? ___B7 五、發明説明“） 6 6 6 7 6 8 6 9 7 1 7 2 7 3 7 4 7 7 > 7 84 C Exhaust gas exhaust tower exhaust channel Absorption liquid supply nozzle of the smoke exhaust introduction section Absorption liquid supply nozzle group Paper size (using China National Standard (CNS) A4 size (210X297 mm) • 24- Central Ministry of Economic Affairs Printed by the Industrial and Consumer Cooperatives! 4386 19 V. Invention Description 2) 5 5 a 6 6 a > 6 b 8 9 10 11 12 13 14 1 5 16 17 17a 18 19 2 0 2 1 2 2 2 3 2 4 2 4a > 24b 2 7 A7 B7 This paper size is in accordance with China® standards (CNS > A4 size (2I0X297 mm) > Absorbent liquid Absorbent liquid jet mist eliminator sheet row smoke exhaust outlet recovery pipe connecting pipe. Closed space above the tank Gas injection pipe Absorption liquid supply pipe Flow control valve Pressure control valve Atmosphere open pipe Pressurization Compressor Raw material supply pipe Extraction pipe Drainage recovery pipe Drainage recovery valve Buffer tank Nozzle valve Arc tube Recovery pipe Absorption liquid storage tank II n, _ Order Line II (Please read the precautions on the back page first) -25- 438619 A7 B7 Printed by the Central Bureau of Standards of the Ministry of Economic Affairs of the People's Republic of China, Du Yinzhuang 5. Description of the invention 3) 2 7 a Liquid level 2 9 Absorption liquid introduction tube 3 0 »3 0 A, 3 0 B void portion 3 1 3 1 A absorber tube 3 1 c semi-circular tubular member 3 1 d cover 3 2 exhaust gas flow 3 4 hollow circular tubular member 3 5 oval tubular member 3 6 small hole 3 7 Gap opening 3 9 Overflow 4 0 4 0 A, 4 0 B Partition plate 4 1 A 4 IB, 4 1C Exhaust gas basin 4 3 On-off valve 4 3 A 4 3 C Flow on-off valve 4 6 Rotating plate 4 8 Pivot point 4 9 Duct 5 6 Liquid storage section 6 0 6 0 a Nozzle 6 1 Recovery tube 6 2 Pressure sensor 6 5 Exhaust gas flow velocity detection sensor The paper size applies to Chinese national standards (CNS > A4 specification (210X297 mm) 26- Printed control circuit of the Central Standards Bureau of the Ministry of Economic Affairs, Industrial and Consumer Cooperatives, solenoid switch valve, channel control circuit, boost fan, bypass channel, main plate, baffle, receiving container, piping, nozzle-shaped opening, vertical pipe section, horizontal pipe section, side opening 43 86 1 9 a? ___B7 V. Description of the invention ") 6 6 6 7 6 8 6 9 7 1 7 2 7 3 7 4 7 7 > 7 8

8 0 A，8 Ο B 8 1 A，8 1 B8 0 A, 8 Ο B 8 1 A, 8 1 B

8 2 A 9 0 9 1 19 0 19 0a 〔實施發明用之最佳狀態] 根據圖式以例示詳細說明本發明之實施例如下。但是，該 實施例中所記載之構成構件的尺寸、材質、形狀、其相對配置 等，如未予以特定記載之限定，則本發明之範圍即不僅限於此 一趣旨，而僅止於說明例而已· 第1圖是表示本發明第i實施形態之濕式氣體處理裝匱之 槪略圖。. ----.-----I------1T------0 (請先閲讀背面之注意事項本頁) 本紙张尺度遴用中國國家標率（CNS > Α4规格（210X297公釐） -27- 經濟部中央樣準局貝工消费合作杜印製 4 3 8 6 19 A7 ___B7_____五、發明説明) 第1圖中，來自鍋爐等燃燒裝置的排氣1係導入於設置在 吸收塔2下部之排煙導入部3內。導入之廢氣1是與設於吸收 塔2內下部之吸收液供應噴嘴4所供應的吸收液5接觸|使氣 體中的目的成份從氣體移動至吸收液5。 此時，氣體中的目的成份與吸收液的組合係指目的成份中 可溶於吸收液之物及粉塵等。例如本實施形態中，吸收液可溶 之目的成份爲二氧化硫（S〇2)，吸收液是使用含吸收劑的石 灰石之懸浮液。 並且，上述噴嘴在本實施形態中爲向上噴嘴4 *從該向上 噴嘴4將吸收液5朝著上方噴射，藉此使上述排煙導入部3導 入的廢氣1隨著上述噴嘴4所噴出的吸收液噴流5 a ，而通過 吸收液5的噴流中得以氣液接觸。 又上述噴流頂點附近之吸收塔2上部配設有消霧器6，藉 著該消霧器6將隨著氣體1的吸收液5除去。 在吸收塔2內從將目的成份從吸收液5除去，使隨消霧器 6而去除吸收液5之後的淨化氣體7，最後從排煙導出部8排 出於大氣中或必要未圖示的後流機器中。 另一方面，在消霧器6下方的吸收塔2側壁內周圍配設上 側開口之回收器9，以上述消霧器6所捕捉的吸收液5是以回 收器9回收而經由連通管1 0落下至加壓槽1 1。 因此，從上述吸收液供應噴嘴4所噴出之吸收液5的高度 是藉著廢氣1的流速推壓，設定可使其上升至高於上述回收器 9位置之加壓槽11的加壓力· 連通管10其上端係開口於回收器9底面，該連通管10 II ί ί ί I n i— I I 線 (請先閲讀背面之注意事項声 <寫本頁) 本紙伕尺度適用中國國家橾準（CNS )八4規<格（210X297公釐） -28· 438619 A7 B7 經濟部中央揉準局負工消费合作社印製 五、發明説明έβ ) 的下端則是從加壓槽11上面開設於經常沒入該槽11內的吸 收液中的位置，藉該連通管10進行加壓槽11之氣體密封。 即，利用回收器9所回收的吸收液5是從連通管1 0朝著 加壓槽1 1流動，但此時在加壓槽1 1內部的上部封閉空間 1 1 a產生壓縮空氣所成的氣體壓力，因此會使加壓槽1 1內 的吸收液5逆流，使連通管1 0內的液面上升至與加壓槽1 1 內部壓力平衡的位置•並且設定連通管10的高低差、回收器 9位置及槽11內壓使上述連通管10內的液面低於回收器9 的位置，藉此可利用回收器9朝著加壓槽1 1內持續進行吸收 液的循環而可藉著連通管10內的吸收液5使加壓槽11氣壓 密封。 加壓槽11內底部設置與空氣壓縮機12連結之氣體噴管 1 3，可噴入儲存放液所加壓的空氣，換言之含氧氣體。 該加壓氣體具有兩個功能》第1是可維持加壓槽11內上 部封閉空間I i a的壓力，第2是含有上述氣液接觸而吸收 S 〇2之石灰石的懸浮吸收液5是藉著與上述含氧氣體的接觸使 S〇2氧化而產生硫酸鈣二水物（石膏）· 儲存在加壓槽11內的吸收液5是藉著加壓槽11內上部 封閉空間1 1 a的壓力，經由控制吸收液供應管1 4及吸收液 5的供應流量之流量控制閥15循環於吸收塔2內的吸收液供 應噴嘴4 * 其次•說明上述加壓槽1 1的構成如下。 於加壓槽11頂部控制大氣開放管17及該槽11內壓力 之壓力控制閥1 6，或於槽側壁供應中和劑等原料之原料供應 - --------^-- (請先閲讀背面之注意事項声...窍本頁) ,ιτ 線 本纸張尺度速用中困繭家標率（CNS >Α4規格（210X297公釐） -29 · 經濟部中央樣準局貝工消費合作杜印装 4386 1 9 a? ._B7__五、發明説明) 管1 8分別安裝可藉排水回收泵2 1從設置於吸收塔2底部之 液體儲存部5 6回收吸收液5用之排水回收管2 0。 另一方面，在槽11底部安裝可拔出上述S〇2氧化時所產 生之石膏等的抽出管19» 說明構成上述加壓槽11的理由如下。 根據本實施形態，即使於吸收塔2內使吸收液5向上噴流 而藉設於吸收塔2上部的回收器9回收吸收液5時，吸收液5 的一部份會隨著氣體同時漏出，一部份會朝著吸收塔部2底部 落下|因此僅上述回收器9'並不能1 0 0%回收•因此*滞留 在吸收塔2底部液體的位準一旦形成預定量以上時|構成可以 泵2 1回壓至加壓槽1 1內者》 又，從原料供應管1 8將中和劑供應於加壓槽1 1的同時 •利用抽出管1 9抽出其一部份而回到石音回收步驟》因此本 實施形態中，可平衡原料供應管1 8之吸收液供應及未圖示之 石膏回收步驟的脫除液量及與氣體同時脫除的液體量等•維持 加壓槽11的液體位準。 從空氣壓縮機12供應加壓槽I1內的空氣量是對應廢氣 1中的3〇2量而噴入β因此，加壓槽1 1內的空氣壓是控制預 定壓力使吸收液供應管14及抽出管19的吸收液排出量；連 通管1 0、原料供應管1 8、排水回收管2 0的吸收液排出量 ;及，空氣壓縮機1 2的氣體噴出量達到平衡。 此外，破壞上述平衡使槽內壓力高於預定壓力時，可自動 開啓壓力控制閥1 6，將其中的壓力排出恢復至預定壓力，可 使槽內ή力維持在預定壓力· 本紙張尺度適用中圉國家揉準（CNS > Α4洗格（2Ι0Χ297公釐） -30- 438619 經濟部中央橾準局貝工消费合作社印製 A7 B7_五、發明説明如） 其次，以下述實驗確認上述實施形態表示裝置所產生的效 果。 第2圖是表示，本發明的氣體處理裝置中’以吸收液作爲 含碳酸鈣的懸浮液，使吸收液的循環流量一定而可取得氣體流 速與S 〇2除去率關係之一例的圖表。 藉此一實驗獲知可於寬廣之範圍內獲得一般二氧化硫除去 率所求得之90%以上的性能。 因此*使鍋爐等氣體產生源的負載變動降低其流量時，仍 可以9 0%以上的效率除去二氧化硫。 又，此一實驗中•吸收液可大致以第1圖表示之向上開口 的回收器9予以全量回收，而可順利地運轉。又，即使在降低 氣流之通氣速度的條件下|使加壓槽1 1的壓力上升，可促進 吸收液5到達上部，此時同樣可利用回收器9大致全量回收吸 收液5 β 因此，根據上述之實施形態可不須使用噴射泵，或即使隨 吸收液而降低其流速時•仍可順利地進行吸收液的回收。 尤其是根據本實施形態，可藉壓縮空氣等的加壓氣體使加 壓槽內的加壓，使加壓槽的液面不須位於吸收液供應噴嘴上部 的位置，除了可降低加壓槽之外，並可予以自由配置。此外如 上述，藉著負載變動等可降低吸收塔2內的氣體流速•即使不 隨著吸收液時仍可增加加壓槽內的壓力，使吸收液上升至消霧 器附近爲止，可回收吸收液· 第3圖是表示如本發明第2實施形態的上述實施形態之未 使用向上噴嘴之吸收液重力供應方式的濕式氣體處理裝置之槪 I ϋ I I n I ^ n 11 n I I n 線 (請先閲讀背面之注f項产V寫本頁) 本紙張尺度逋用中國國家揉準（CNS ) A4规格（210X297公t ) -31 - 經濟部中央樣準局負工消费合作杜印製 4 3 861 9 at ________B7_五、發明説明b ) 略構成。 如圖所示I利用設於吸收塔2下部的排煙導入部3導入來 自鍋爐等燃燒裝置的廢氣1 ，導通延伸設置在塔內上方的廢氣 通路2 A，形成上升廢氣流而構成藉消霧器6排出吸收塔頂部 的排煙導出部8。 又，在吸收塔2下部設有液體儲存部5 6，可儲存從塔2 上部落下之石灰懸浮液等的吸收液5藉回收泵21回流至吸收 液儲存槽2 7內。 另一方面，在排煙導入部3正上方的廢氣通道2 A入口部 ，使大致水平之多數上部開放式導水管狀吸收液管31呈複數 條平行剖面並設而形成水平配管列之構成，同時供應吸收液於 該導水管狀吸收液管3 1之儲存槽2 7的液面是設定僅稍微高 於上述導水管狀吸收液管3 1液面高度，可利用其適當落差的 重力作用使吸收液5經由吸收液導管2 9及閥6 0導入塔內總 管190 (參閱第5圖）之後，經由該總管190使導入導水 管狀吸收液管31的吸收液5構成較導水管狀吸收液管31側 壁上面更薄膜狀，而朝著夾持鄰接導水管狀吸收液管3 1彼此 間的空隙部30溢流（參閱第4圖、第5圖）。 再者，由於設定使吸收液儲存槽2 7的液面僅稍微高於上 述導水管狀吸收液管3 1液面高度*因此可對應吸收液供應閥 6 0供應的吸收童而調節回收泵2 1及回收管2 4 a的回收量 及新的吸收液5供應量· 第4圖中，雖是表示上述導水管狀吸收液管3 1的配設形 態*但是第4 (A)圖中，是將上述廢氣通道2A入口部沿著 裝 訂 線 {請先聞讀背面之注意事項真丨，容本頁) 本紙張尺度適用中國國家搮率（CNS > A4規格（2丨0X297公釐） -32- 1 4386 19 A7 B7 五、發明説明) 大致剖面之一水平面內而平行配列設置呈一段式，使該列設管 群鄰接的管彼此間的空隙部3 0構成可導通廢氣流3 2，同時 可回收從塔2內壁垂落之石灰懸浮液等的吸收液5，因此在其 左右兩壁的塔內壁設置9 0°弧形管2 4。 根據上述之構成，將上述廢氣通道2 A入口部經由預定的 空隙部3 0配設有呈多數根列設之導水管狀吸收液管3 1 ，因 此，其結果在上述空隙部3 0減少廢氣流3 2的通過面積而可 使其速度增加形成高速化·並且|使吸收液3 0溢流出上述廢 氣流3 2形成高速化之上述空隙部3 0，形成交叉狀接觸其高 速上升廢氣流3 2，因此吸收液5可隨著廢氣流3 2所引起之 高速度能源形成擾亂之微粒化。 又90°弧形管24回收的吸收液5會再度因氣體而上升 ，因此可減少回收泵21的動力。 於第4 (B)中列設使上述廢氣通道2 A入口部大致橫斷 之水平面內呈上下鋸齒狀的上述導水管狀吸收液管31 A、 經濟部中央標率局貞工消费合作社印氧 (請先聞讀背面之注意事項再衿本頁) 3 1 B，使該列設之管群所鄰接的管3 1A、3 1 B彼此間的 空隙部30A、30B可通過上述廢氣流32，因此，此時係 以一段側之導水管狀吸收液管3 1 A彼此的空隙部3 Ο A減少 廢氣流3 2的通過面積而增加其速度形成高速化者。並且，上 述廢氣流3 2形成高速化之上述空隙部3 0A中流出吸收液5 ，而其高速上升廢氣流3 2形成交叉接觸爲止是與第4 (A) 圖相同，但是在上述一段側導水管狀吸收液管3 1 A與二段側 之導水管狀吸收液管3 1 B之間的開放位置•利用上述高速化 廢氣流3 2的低速化與膨脹使廢氣1的高速流體形成負壓，並 本紙張尺度適用中固國家揉準（CNS ) A4规格（210X297公釐） -33- 經濟部中央樣率局員工消费合作杜印装 4386 19 A7 _B7_五、發明説明h ) 且在一側段的導水管狀吸收液管31A的開放面上引起吸收液 5的微粒子狀霧化，且再度以二段側之導水管狀吸收液管 3 1 B彼此的空隙部3 Ο B使廢氣流3 2的通過面積減少增加 其速度而形成高速化之與上述相同的作用，可更爲提高氣液接 觸的效率。當然，其段數也可以在3段以上。 第5圖中是揭示上述第4(A)圖之導水管狀吸收液管 31的吸收液5的流動狀態。 同圖中，連設在吸收液導管2 9的總管1 9 0是沿著塔內 例如裏側內壁而配設，該總管1 9 0的側面開口 1 9 0 a上開 設連設有沿著與管軸線正交方向而平行並設之導水管狀吸收液 管3 1的一端· 另外該導水管狀吸收液管3 1係構成如第5 (A)圖所示 •水平設定其兩側壁上面，經過導水管狀吸收液管3 1之側壁 上面全長而可使吸收液5溢流流出空隙部3 0側。 將導水管狀吸收液管31的側壁上面設定爲水平時較爲困 難，因此如第5 (B)圖所示，在導水管狀吸收液管3 1的左 右兩側壁上緣以預定間隔軸向設置複數個缺口 3 1 a，經由該 缺口 3 1 a可於空隙部3 0側斷續地形成溢流3 9，構成與高 速排氣流3 2交叉接觸。 根據上述之實施形態•相對於上述橫向之薄膜狀溢流而導 入吸收塔2內的上述廢氣1是通過多數根列設之導水管狀吸收 液管31間的空隙部30，藉此形成高速上升氣流（廢氣的塔 速大約爲10m/s)，如上述與吸收液5交叉接觸之後，藉 此接觸而交叉接觸之吸收液5是利用廢氣1的接觸能源使其微 I I H ^ li H I 線 {諳先閲讀背面之注意事項真為本頁) 本紙張尺度適用中國固家標率（CNS ) A4规格（210X25»7公釐） • 34- 經濟部中央樣準局貝工消费合作社印裝 43 86 1 9 a? _B7_五、發明説明) 小液滴化，且分散於導水管狀吸收液管3 1的上部而呈亂流狀 .膨脹之上述上升氣流中，同時從導水管狀吸收液管31的開放 面同樣以負壓使導水管上面的吸收液5霧化’分散混入而有效 地氣液接觸後形成氣液分散氣體。 上述氣液分散氣體係於其上方一邊形成氣液接觸區空域 2A而到達吸收塔上方的消霧器6，但是其間之排氣中的目的 成分是從廢氣1吸收吸收液5。 此外|氣體中的目的成份與吸收液5的組合是在實施形態 中爲可溶於吸收液5中的目的成份爲二氧化硫（S〇2)，吸收 液5是使用含有形成吸收劑之石灰石的懸浮液。 另一方面，經過上述氣液接觸區空域2 A的廢氣1可藉著 消霧器6回收隨之產生分散的吸收液5，又經由回收管2 4 a 回流至吸收液儲存槽2 7。所回收的吸收液5是利用設於塔內 壁的回收用半截狀弧形管2 4經由回收管2 4 b回流至吸收液 儲存槽2 7內。 吸收塔2內的目的成份爲吸收液所吸收，並以消霧器6分 離所伴隨之吸收液，最後將形成淨化氣體的廢氣1藉著排煙導 出部8送至大氣或者未圖示之下游機器。 第6圖中是表示與顯示上述實施形態之導水管狀吸收液管 的不同之其他實施例，以上部封閉式管狀構件構成上述吸收液 管3 1的同時|在與該吸收液管3 1的上述廢氣流體3 2通氣 之空隙部3 0相對的周圍面上，沿著管軸線方向設置縫隙狀開 口或多數個小孔列。此時，如圖所示爲了抑制流體的阻力，吸 收液管3 1下面側的剖面最好形成曲線形（例如圓形、流線形 ----------裝-------訂^------線 (請先閲讀背面之注意事項弄本頁) 本紙張尺度通用中國Η家橾準（CNS >六4现格（210X297公藿> -35- 經濟部中央橾準局貝工消費合作社印製 438619 at _._B7五、發明说明) 、紡滴形等）或者楔形或三角形，例如第6 (A)圖是表示吸 收液管31的下面是以平板狀蓋體31d封閉剖面圓形的半圓 管狀構件3 1 c的上面，與其兩側側壁的空隙部3 0相對側上 沿著軸線方向斷續地穿設多數個小孔3 6以致縫隙開口 3 7 ( 參閱第6 (D) 、（E)圖）所構成。 又，第6 ( B )圖表示的實施形態是使用剖面呈中空圓形 管狀構件3 4，在包含軸心的水平剖面的左右母線上·沿著軸 線方向斷續地穿設多數個小孔3 6以致縫隙開口 3 7 (參閱第 6 (D) ， （E)圖）所構成。 又，第6 ( C )圖表示的實施形態是使用剖面呈中空橢圓 形管狀構件3 4，在包含軸心的水平剖面的左右母線上，沿著 軸線方向斷續地穿設多數個小孔3 6以致縫隙開口 3 7 (參閱 第6(D) 、 （E)圖）所構成。此外，小孔36,或縫隙開 口 3 7不一定是設於包含軸心的水平剖面形左右母線上|也可 以設置在其上方或下方》 因此，根據本發明實施形態，與習知之向上噴嘴不同，上 述吸收液5只須朝著上述鄰接管之彼此間的空隙部側形成大致 水平方向溢流或流出•因而可降低設備費用及獲得能源降低的 效果。 又本實施形態最好是以利用重力的上述吸收液供應源構成 對上述吸收液管的吸收液供應，但是本發明也可以採利用吸收 液供應泵的構成|此時也可以小型的上述供應泵，同樣可獲得 設備費用的降低效果。. 又¥實施形態是在上述廢氣通道2 A入口部經由預定的空 裝 訂 _ 線 (請先W讀背面之注意事項务卷寫本頁) 本紙張尺度適用中國鬮家標率（cns>A4規格（uoxw公釐） .36- 438619 A7 B7 五、發明説明) 經濟部中央橾率局負工消费合作社印製 隙部3 0配設複數根列設之吸收液管，因此，其結果可以上述 空隙部同時進行廢氣流3 2與吸收液5的有效氣液接觸及吸收 液的供應，與以往液柱式之液柱在頂部散開爲止所伴隨的溝流 始完成之氣液接觸比較，可更有效地在短時間內進行大幅度地 氣液接觸，因此可高效率地吸收/除去上述廢氣中的目的成份 ，同時可進行更短時間之吸收液5的微粒化與分散，進而可降 低其設備費用。 第7圖是表示本發明第3實施形態之濕式氣體處理裝置的 槪路圖。 第7圖中，來自鍋爐等燃燒裝置的廢氣1係導入設置於吸 收塔2下部的排煙導入部3內。所導入之廢氣1是與設於吸收 塔2內下部的吸收液供應噴嘴群4A〜4 C所供應的吸收液5 接觸，可使廢氣1中的目的成份從氣體1移至吸收液5 · 此時，廢氣1中的目的成份與吸收液5的組合於本實施形 態中之可溶於吸收液5的目的成份爲二氧化硫（S〇2)，吸收 液5是使用包含吸收劑之石灰石的懸浮液。 又，在吸收塔2內的下部形成液體儲存部5 6，可儲存石 灰懸浮液等的吸收液5，並經由回收用泵2 1及再生用緩衝槽 22、噴嘴泵23及流童開關閥43A〜43C，而與該液體 儲存部5 6及上述各噴嘴4A〜4 C的導入管4 9連通。 並且|上述噴嘴群爲向上之噴嘴群4A〜4 C，從向上噴 嘴群4A〜4 C將吸收液5朝著上方噴射，藉此使上述排煙導 入部3導入之廢氣1隨著上述噴嘴群4A〜4 C所噴出的吸收 液5，可通過吸收液5 a中而藉此獲得氣液接觸。 請 先 閲 讀 背 面 項 4, 寫 本 頁 本紙乐尺度速用中囷國家標準（CNS)A4規格（2丨0X297公釐） _ _ A7 43 86 1 9 ____B7_ 五、發明説明&5 ) 此外’在上述噴嘴頂點附近的吸收塔2上部配設消霧器6 ’以該消霧器6除去回收隨氣體1產生的吸收液5。 在吸收塔2內將目的成分從吸收液5中除去，使隨著消霧 器6而除去吸收液5的淨化氣體7最後藉由排煙導出部8送出 至大氣中或必要之未圖示的後流機.器》 另一方面，在消霧器6下方之吸收塔2側壁內周圍配設上 側開口之回收器9，上述消霧器6所捕捉之吸收液5是藉回收 器9回收，並經由緩衝槽2 2等因應其需要而循環再使用。因 此，從上述向上噴嘴群4A〜4 C所噴出之吸收液5的高度是 利用廢氣1的流速上推，可設定上升至高於上述回收器9位置 之廢氣1的流速，但是鍋爐等氣體產生源一般皆會產生負載變 動，因此當氣體流量降低時，可藉著氣體流速降低並不會隨之 產生吸收液5係如上述。 因此1在本實施形態中，以圖上左、中央、右的三群構成 上述向上噴嘴4Α〜4C，在各個噴嘴群4Α〜4C的每個吸 收液導管4 9上設置開關閥4 3Α〜4 3 C，分別可在獨立的 噴嘴群4Α〜4 C進行吸收液5的噴出/停止。此外，噴嘴群 4Α〜4 C在圖中雖僅形成1個噴嘴|但實際上是在前後方向 列狀連設有複數個噴嘴。 又，上述左噴嘴群4Α與中央噴嘴群4 Β之間，及中央噴 嘴群4 Β與右噴嘴群4 C之間垂設有垂直方向延伸設置之分割 板 4 0 A、4 Ο Β » 並且上述分割板4 0A、4 Ο B之其上端是延伸設置至高 於上述回收器9的消霧器6安裝位置附近爲止，但是其下端的 ---------^------,π.------0 (請先Η讀背面之注意事項再.為本萸) 經濟部中央樣準局員工消费合作社印製 本紙張尺度適用中國國家標率（CMS ) Α4规格（210Χ297公釐） -38- 經濟部中央橾準局工消费合作社印製 4386 19_B7_五、發明説明^ ) . 高度位置係與其不同，其中之一分割板4 0 A是下垂至吸收液 5的液體儲存部5 6之A的液位位準的位置爲止’其.他分割板 4 Ο B則是下垂至高於上述A的液位位準之B的液位位準位置 ，在上述分割板4 0A、4 Ο B上形成分割之3個氣體流域 41A、41B、41C。 根據上述之實施例1藉著泵驅動控制使上述液體儲存部 5 6內之吸收液5的液位位準上升，在使上述液位位準提升至 A的液位位準位置之前，首先將一分割板4 0A的下端沒入吸 收液5內，藉此封閉左側之氣體流域4 1 A的氣體導入開口， 其結果可使排煙導入部3所導入之廢氣1的流域僅形成中央 4 1 B及右側4 1 C。並且在此狀態下關閉左側噴嘴群4A的 開關閥4 3A，藉此可使氣體流通面積僅形成中央及右側排氣 流域41B，41A之2/3的面積。 其結果，即使降低排氣1之導入流量的2/3時，可維持 一定的氣體流速，因此吸收液5隨著氣體流速而可維持噴嘴群 4 B、4 C之吸收液5的噴出高度，可順利地進行吸收液5與 氣流3 2間的氣液接觸。 此外將上述液位位準提升至B的液位位準位置，可使2片 分割板40A、40B的任一下端可同樣沒入吸收液5內，藉 此可封閉左側及中央氣體流域4 1 A、4 1 B的氣體導入開口 |其結果可使排煙導入部3所導入之廢氣1的流域僅彤成右側 4 1 C。並且在此狀態下，封閉左側與中央部噴嘴群4A、 4 B之開關閥4 3A、4 3 B，藉此使氣流通過面積僅形成氣 體流域4 1 C的1/3面積。其結果，可降低廢氣1之導入流 (請先閲讀背面之注意事項再：^本頁) 裝- 訂 本紙張尺度適用中國國家揉準（CNS ) Α4規格（210Χ297公釐） -39- 438619 經濟部中夹標準局Λ工消费合作社印製 A7 B7五、發明説明) 量的1/3而維持一定的氣體流速。 因此根據本實施例|降低吸收塔2內的氣體流量，而與此 比例降低流動於廢氣通道的流速時1封閉上述分割板4 0A 1 4 Ο B所隔開之複數個氣體流域4 1 A〜4 1 C之其中一側時 •對應上述流量的降低可控制流速使其形成一定的氣體通過面 積。 第8圖爲第7圖之實施形態的變形例，上述分割板4 0A 、40B的下端是構成可朝著導入吸收塔2內的排煙導入部3 側而呈「J」字形彎曲部4 5。 根據上述實施形態，從上述排煙導入部3導入吸收塔2內 呈向下傾斜方向的廢氣1是沿著上述「〗j字形彎曲部4 5 — 邊整流於噴嘴群4A〜4C噴流方向而被垂直向上引導，其結 果，上述分割板40A、40B同樣具有排氣整流板的功能， 可更爲順利地進行氣液接觸· 第9圖是本發明之其他實施形態，以上述向上噴嘴群4A 、4B作爲圖上左、右兩群構成，在各噴嘴群4A、4B的各 導入管49上設置開關閥43A、43B |可分別在獨立的噴 嘴群4A * 4B上噴出/停止吸收液5。 並且在上述左噴嘴群4A與右噴嘴群4 B之間垂直設置朝 垂直方向延伸之一分割板4 0A。 又，上述分割板4 0A係將支點4 8設於噴嘴群4A、 4 B安裝位置的更下方|而安裝以該支點4 8爲中心而朝著排 煙導入部3側轉動之轉動板4 6。 根據上述本實施例，使上述轉動板4 6朝著排煙導入部3 (請先閲讀背面之注$項再未頁) 訂 本紙張尺度適用中國國家摞準（CNS > Α4规格（2丨0X297公釐） -40· 經濟部中央橾準局员工消費合作社印11 4386 1 9 A7 A7 _B7五、發明説明ί8 ) 側轉動而保持至梢微低於水平的向下位置，藉此可同時開放右 .側與左側任一側氣體流域4 1 A、4 1 B的氣體導入開□，形 成可進行一般之氣液接觸。 其次，使上述轉動板4 6從排煙導入部3側朝著液體儲存 部向垂直下方轉動，可將轉動板4 6下端沒入吸收液5內·藉 此可封閉左側之氣體流域4 1 Α的氣體導入開口，其結果使排 煙導入部3所導入的廢氣流域僅形成右側4 1 B。並且在此狀 態下，封閉左側噴嘴群4A的開關閥43A，藉此使氣體流通 過面積僅彤成右側的1/2面積。 第1 0圖爲第7圖之其他變形例，說明與第9圖的變形例 不同的是上述分割板4 Ο A係於噴嘴群4 A、4 B安裝位置下 方，設置可垂直方向自由升降之升降板4 7。根據上述之實施 例，使上述升降板4 7上升至液體儲存部5 6的上方，可同時 開放左側及右側之任一側氣體流域4 1 A、4 1 B的氣體導入 開口，形成可進行一般之氣液接觸者。 其次，使上述升降板4 7在垂直下方降下移動•將升降板 4 7下端沒入吸收液5內，藉此封閉左側之氣體流域4 1 A的 氣體導入開口，其結果可使排煙導入部3所導入的廢氣流域僅 形成右側4 1 B。並且，在此狀態下封閉左側噴嘴群4A的開 關閥4 3A，可使氣體流通過面積僅形成右側的1/2面積》 又上述分割板4 Ο A也可以構成朝著與廢氣流動方向垂直 的水平方向移動。 第1 1圖爲可動分割板4 0A之其他變形例，使上述分割 板4 0A構成可相對於廢氣流動方向的大致正交方向，而從吸 1· I I n n I ^1 ^1— n «I n (請先閱讀背面之注意事項具..Λ本頁) 本纸張尺度逍用中國國家標牟（CNS Μ財i格（210Χ297公釐） -41 - 經濟部中央樣率局貝工消费合作杜印裝 438619 A7 _._B7 五、發明説明fo ) 收塔2左側壁面移動至中央位置，朝著中央位置的移動可在上 述左噴嘴群4 A及右噴嘴群4 B之間，垂直設置朝著垂直方向 延伸之一分割板40A。 又上述分割板4 0A的下端是沒入液體儲存部5 6的吸收 液5內。 其結果，僅上述分割板4 0A的右側廢氣流域4 1 B開放 氣體導入開口，該右側廢氣流域4 1 B係隨著將分割板40A 從吸收塔2左側壁面移動至中央位置，可形成廢氣1所導入之 右側氣體流域4 1 B的通道狹窄剖面積。 根據上述實施例，隨著廢氣流量的降低使分割板4 0A移 至中央側*可自由地形成狹窄之氣體流域4 1A、4 1 B的通 道剖面積。 因此•根據上述之實施形態，由於鍋爐等燃燒裝置的負載 變動等，降低吸收塔內的氣體流量•即使與此比例而降低流動 於廢氣通道的通路時，可控制氣體流入域的氣體通過面稹使氣 體流速形成一定，藉此可大致維持一定之噴嘴群的吸收液噴出 高度，其結果不僅可順利地進行吸收液與氣流間的氣液接觸， 可在吸收塔上部順利地回收吸收液。 又根據本實施形態 > 可節省不必要之泵驅動動力等，同時 可阻止吸收液無請的循環。 再者，可藉著上述分割板所間隔之複數個氣體流域的一方 或使其氣體通過面積的狹窄化，可對應上述流量的降低而控 制氣體通過面稹使氣體流速形成一定。 另外^，並藉著吸收液之液位位準的調節或選擇性地使分割 (請先聞讀背面之注意事項禽本頁) 本紙浪尺度適用中國闺家標準（CNS ) 格（210X297公釐） -42- 4 3 8 6 19 A7 B7 經濟部中央橾丰局貝工消費合作社印11 五、發明説明釦） 板下端下降而沒入吸收液內，可簡單地選擇開關氣體流域的通 道。 此外，根據本實施形態，藉著分割板下端側的擺動轉向· 可簡單地對氣體流域進行氣體流入的流量控制或開關控制。 又|根據第8圖的裝置，上述分割板同樣具有廢氣整流板 的功能，更可顧利地形成氣液接觸》 並且根據第9圖〜第1 1圖之裝置，可對應廢氣流量的變 動而移動分割板，可自由地調節氣體流域的通道剖面積。 第1 2圖是表示本發明第4實施形態之濕式廢氣處理裝置 的槪略構成，省略上述實施形態說明之裝置構成的重複部份之 說明。 如第1 2圇所示，在吸收塔2下部之吸收槽的液體儲存部 5 6下部設置既設之維修用吹槽6 0及吹槽泵6 0 a。 又，從液體儲存部5 6至吹槽6 0的通道6 8中設有電磁 開關閥6 7，可以控制電路6 6檢測來自設於排煙導入部3之 廢氣流速檢測感測器6 5的廢氣流速（塔速），於吸收塔2上 升時及下降時，可開放電磁開關閥6 7使廢氣1的流速到達加 載流速•形成液體儲存部5 6·*吹槽6 0 —吹槽泵6 0 a -加 壓槽1 1回流之迂迴回流通道> 又，設於吸收塔2外部之加壓槽11的儲存液面上部空間 是經由加壓用壓縮機1 7 a及壓力調節器1 6而可藉控制電路 6 9加壓控制於任意的壓力。 控制電路6 9是藉著壓力感測器6 2檢測吸收液供應管 1 4入口側的壓力，而朝著對噴嘴4提供一定吸收液供應壓力 ^!^lnllJ n n ^ (請先W讀背面之注$項/i..寫本頁) 本紙張尺度適用中囷國家標準（CNS ) A4規格（2丨0X297公t > · 43 · 438619 A7 B7 經濟部中央樣準局貝工消费合作社印裝 五、發明説明h ) 的方向，藉壓力調節器1 6控制加壓槽1 1液面上方空間 1 1 a的加壓力· 因此，即使槽1 1儲存液面上下變動時|可對應該吸收液 5的重力變動以壓力調節器16控制作用其液面上方空間的壓 力1藉此不論該槽1 1的液面上下.，皆可供應一定的吸收液5 又，利用設於吸收塔2上部的消霧器6分離之吸收液5的 回收管61是形成插入加壓槽11液面下的構造。 其結果 > 構成以加壓槽1 1—吸收液供應管1 4 —噴嘴4 —廢氣1等氣液接觸，吸收目的成分之載流步驟—消霧器6分 離而回流至回收管—加壓槽1 1的循環系（以下稱主循環系） 0 上述之實施形態中，廢氣流速爲8m/ S以上的加載速度 時，從噴嘴4噴出之吸收液5的噴流5 a爲廢氣1提升至消霧 器6爲止，因此吸收液5可利用上述主循環系循環· 即，利用壓力調節器1 6控制加壓槽1 1之液面上方空間 1 1 a的加壓力所獲得該加壓槽1 1的作用壓力，經由吸收液 供應管1 4而藉噴嘴4噴出之吸收液5的噴流5 a是控制使其 噴流速度形成預定値，而與上升至吸收塔2之上升廢氣氣液接 觸，在接觸的過程吸收廢氣1的目的成分到達消霧器6。到達 載流之吸收液係藉消霧器6分離而經由回收管回流至加壓槽 11· 其次，吸收塔2上升時以至關閉時，如第1 3圖所示廢氣 流速形成上述加載速度以下，因此從噴嘴4噴出之吸收液5的 — ；---V------^-- (請先閲讀背面之注意事項幕ί寫本頁) 訂 線 本紙張尺度適用中國困家標率（CNS) A4規格（210X297公釐） .44 · 438619 A7 B7 五、發明説明& ) (請先《讀背面之注意事項声/丨疼本頁) 噴流5 a並未能藉著廢氣1上升至吸收塔上部爲止，噴出之吸 收液5的全量幾乎落下至下方的液體儲存部5 6 (以符號5 b 表示）。 - 藉控制電路6 6檢測與此平行設於排煙導入部3之廢氣流 速檢測感測器6 5的廢氣流速，開放電磁開醑閥6 7使廢氣的 流速達到上述加載流速爲止*經由液體儲存部5 6 —吹槽6 0 —吹槽泵6 0 a—加壓槽1 1的迂迴回流通道，使儲存在液體 儲存部5 6的吸收液5回流至槽1 1。 即，落下至液體儲存部5 6的吸收液5 b係導入於下部既 設之吹槽6 0，可不需特別提升液體儲存部5 6的尺寸即可收 容於吹槽6 0內，其次收容之吸收液5可藉著吹槽泵6 0 a回 流至逐次加壓槽1 1內。 此外，即使以上述迂迴循環使槽1 1的儲存液面上下變動 時•控制電路6 9可利用壓力感測器6 2檢測吸收液供應管 1 4入口側的壓力，而利用壓力調節器1 6控制使噴嘴4的吸 收供應壓力形成一定的方向，因此可不論該槽1 1液面的上下 爲何皆可供應一定的吸收液5。 經濟部中央搮準局员工消费合作社印裝 因此，本實施形態是可利用壓縮機1 7 a將加壓槽1 1之 液面上部空間加壓至預定壓力，因此不須從噴嘴4設置噴出吸 收液5的循環泵。但是，回收管6 1的前端係插入於加壓槽 1 1，必須防止空氣的漏洩· 因此，根據本實施形態，即使隨著燃燒機側的負載變動而 導致廢氣速度的降低時，仍可經由上述吸收塔底部液體儲存槽 與第2液體儲存槽，利用連結於加壓槽的吸收液回流通道，最 -45- 本紙張尺度適用中國國家標準（CNS ) A4規格（210X297公釐） 經濟部中央標準局貝工消费合作社印装 438619 A7 B7五、發明説明幻） 好是有效利用維修用循環系可使吸收液連續循環，並且上述維 修用循環系可使用既設之吹槽及吹槽泵|因此對於相關機器可 不須要特別增大其尺寸或增加驅動力，可負擔以低成本低設備 費用》 又，根據本實施形態，吸收液噴流壓的控制是可利用加壓 槽的加壓所獲得的作用壓力任意控制，因此不僅不須噴出泵的 加壓，同時可不論加壓槽的液面上下爲何皆可供應一定的吸收 液。 此外，吸收塔2上升時乃至關閉時，如第13圖所示，廢 氣流速會形成上述負載速度以下，因此從噴嘴4噴出之吸收液 5的噴流5 a並未被廢氣1提升至吸收塔上部，噴出之吸收液 5的全量幾乎全量落下至下方的液體儲存部56 (符號5b表 示）。爲了解決上述的缺點，以往是在吸收塔上升及關閉時， 不使燃燒機或鍋爐等所排出的廢氣通過上述吸收塔，而是通過 迂迴該吸收塔的旁通通道排出煙囪側之後，使廢氣流速形成將 吸收液提升至基準位準以上之加載流速以上後《始讓廢氣通過 上述吸收塔時所存在的廢氣迂迴系統。 並且，上述之排氣迂迴系統係如第1 7圖所示，在連結鍋 爐或燃燒機等廢氣排出源與煙囪等廢氣之大量放出部的主通道 7 4上，間隔使鍋爐等的廢氣1升壓而可增速之升壓風扇7 1 及上述濕式吸收塔2的同時，設置連接升壓風扇7 1入口側與 吸收塔2的出口側，具備連接煙囪之檔板7 3的旁通通道7 2 ，在吸收塔2的上升及關閉時*可停止上述升壓風扇7 1的同 時，可開放檔板73並關閉檔板77、78 *使燃燒機或鍋爐 本紙張尺度通用中國國家標準（CNS ) A4規格（210X297公釐） _ aq _ n 裝 訂 線 {請先閲讀背面之注意事項^本頁) 經濟部中央樣準局貝工消費合作社印裴 4386 1 9 at B7五、發明説明W ) 等所排出的廢氣1不通過上述吸收塔2而是通過迂迴該吸收塔 2的旁通通道71排出至煙囪側之後，當廢氣流速形成使吸收 液5上升至基準位準以上的加載流速以上時•可驅動升壓風扇 71的同時，關閉檔板73，開放檔板77、7 8而關閉上述 旁通通道7 2，使廢氣1從鍋爐側通過箭頭表示的主通道7 4 *經由升壓風扇7 1並經過吸收塔2所用的脫硫處理而排出煙 囪側。 但是上述的習知技術中，在吸收塔上升及關閉時，廢氣並 未通過吸收塔，因此會有不進行廢氣處理即不能除去廢氣中所 含的二氧化硫氣體或粉塵等問題。又•未避免上述問題而燃燒 S〇2或煤塵等排出少的輕油時，會產生燃料費高等問題。 第1 4圖是表示有效利用習知旁通通路7 2，可提高與上 述第4實施形態相同效果之第5實施形態者，在連接鍋爐或燃 燒機等廢氣之排氣源及煙囪等廢氣之大氣放出部的主通道7 4 上，利用廢氣的流速而藉著隨吸收液5之兩者的氣液接觸•間 隔設置將廢氣中目的成份吸收於吸收液5之濕式吸收塔所成的 廢氣處理系統· （A)是表示吸收塔上升前之各檔板的關閉狀 態及廢氣的流動，（B)是表示從鍋嫿進入吸收塔之導入廢氣 的塔內流速在加載流速以上時之檔板的開關狀況及廢氣的流動 圖。 如第1 4圖所示|在連結鍋爐或燃燒機等的廢氣排出源與 煙囪等廢氣之大氣放出部的主通道7 4上，藉著鍋逋等使廢氣 i升壓而間隔可獲得增速之升壓風扇71與上述濕式吸收塔2 ，同時連接升壓風扇7 1入口側與吸收塔2出口側1設置具備 {請先聞讀背面之注意事項寫本頁) 本紙張尺度適用中國國家標準（CNS ) A4规格（210X297公釐） -47- 經濟部中央標隼局負工消费合作杜印«. 4386 19 A7 A/ _B7_五、發明説明（15 ) 與煙囪連接之檔板7 3的旁通通道7 2 » 上述之實施形態中，在進行對吸收塔2之廢氣導入前的上 升時，如第14 (A)圖所示開啓檔板73，以旁通通道72 與主通道7 4形成升屋循環通道*使鍋爐的廢氣1並非排出於 排出通道7 6，而是將循環通道內的氣體流速利用升壓泵7 1 持續增速使吸收塔2的塔內流速形成加載流速以上爲止。 並且在維持塔內流速形成加載流速以上時，如第1 4 (B )所示|關閉旁通通道7 2的檔板7 3，進行廢氣1的吸收處 理。 藉第1 3圖表示之相對於鍋爐運轉時間的吐出廢氣量的變 化圖說明上述升壓循環通路的使用狀況如下。 即*如第1 3圖所示，運轉開始後的上升時丁，與運轉完成 前之下降時T2會降低廢氣量，爲了使處理廢氣1之吸收塔2的 塔內流速形成液體落下速度（加載速度）V,以下，如第1 4 ( A)圖所示進行檔板73的開關控制使塔內流速形成加載流速 以上爲止•當塔內流速形成加載流速以上時，如第14 (B) 圖所示進行檔板7 3的開關控制而可使吸收塔2的動作完全作 用者。 第15圖是在吸收塔2內設置限制廢氣通道寬度之分割板 的第2實施例，在氣液接觸區空域4 1上設置朝垂直方向延伸 之分割板4 0，構成可使該分割板4 0朝著水平方向移動之可 變氣液接觸區空域4 1之廢氣通過面積* 第1 6圖是對應吸收塔2內設置限制廢氣通道寬度之分割 板的第Ϋ圖之第3實施例，在氣液接觸區空域4 1上呈階梯式 ---------^------tr.-------^ {请先閲讀背面之注意事項本頁) 本紙張尺度遢用中國困家標準（CMS ) Α4規格（210X297公釐） -48- 經濟部中央橾隼局貝工消费合作社印裝 4386 1 9 at __B7_五、發明説明&6 ) 複數片設置朝垂直方向之下端具不同高度位置的分割板40， 藉著下部液面位準的控制構成可變之廢氣通過面積。 並且，導入上述吸收塔2之廢氣1的塔內流速在加載流速 以下時，利用上述分割板4 0縮小吸收塔2內的廢氣通過面積 ，藉檔板7 3開放旁通通道7 2使處理後廢氣經由升壓泵7 1 回到吸收塔2入口側，藉此可迅速地增加導入上述吸收塔2內 之廢氣1的塔內流速。 因此根據本實施形態，可經常將塔內流速維持在加載流速 以上，因此設備的上升及下降時可完全維持著吸收塔的性能， 同時可不須增大吸收塔下部的液體儲存部及回收泵的容量。 第18圖及第19圖是表示本發明第6實施形態之濕式廢 氣處理裝置槪要之前視圖及側視圖，同圖中省略與上述實施形 態相同構成之說明。吸收塔2高度方向的中間部配置具有複設 個向上噴嘴4之任意數的總管1 90。在該總管1 9 0與上述 液體儲存部5 6之間，連通連接有於中途間設循環用回收泵 2 1的吸收液供應管1 4，以此將吸收液5散佈在吸收塔2內 ，其中吸收除去二氧化硫氣體或粉塵等的目的成份係與上述同 4 吸收塔2內的上部之排煙導出部8的下方位置上設置消霧 器6。 安裝於此之消霧器6的最佳例係舉例如第2 0圖所明示者 。該消霧器6係隔開間隔而形成橫剖面爲山形（扁平V字型） 之複數片板材6 a後重疊列設而以固定桿9 2固定所成，且其 整體是使上述一列狀板材列6 a以其下端位置朝著右向及左向 I — I m I n I ^ (诗先閲讀背面之注意事項再〆氣本頁) 本紙張尺度適用中國困家標準（CNS ) A4规格（210X297公釐） •49· A7 B7 438619 五、發明説明ο ) [---.—：---^— (請先M讀背面之注意事項再，'.vr本頁) 互相交叉傾斜，與其他板材列6 b收束所成而安裝於吸收塔2 β但是，消霧器6的形狀及配列型式不僅限於第2 0圇之例， 但是如後述爲了減少承接消霧器.6所流下之吸收液5的收容器 8 0Α的數量，也可以使鄰接的一對板材列6 a、6 b在其下 端側位置交互傾斜而收束，並且也可以在橫斷板材列6 a、 6 b的方向上配設收容器8 0A，但是爲使載流廢氣1之吸收 液5的噴霧可有效地爲消霧器6所捕獲*必須可導通載流的間 隙。 其次，根據本發明之要部構成說明如下。上述消霧器6的 下部設置任意個可承接其消霧器6所流下之如吸收液5捕集導 水管（參閱第2 0圖）的收容器8 0A。本實施形態爲3個收 容器8 0A的數量，但是也可適當設定消霧器6的配列狀態或 設置台數等。 此外I各收容器8 0A係連設於回送液配管8 1 A的上端 ，該回送液配管8 1 A具有朝下方延伸預定長度之垂直管路部 線. 經濟部中央樣率局貝工消费合作社印製 9 0 |可藉該垂直管路部9 0使回送吸收液5 c具有位能（重 力能源），同時延伸至第5圖之飛散吸收液儲存區域的下方位 置|在其下端設置噴嘴狀開口 8 2A。 再者•上述返送液配管8 1 A之垂直管路9 0的長度會因 爲向上噴嘴4上的噴出液柱高度而變動，但是例如也可以設定 與消霧器6相等左右或其以上之高度。 根據第1 9圖詳細說明上述收容器8 0及回送液配管 8 1A之具體構成如下。設於一對板材列6a、6b之下端收 束位置的收容器8 0A係橫斷其多數之消霧器下端收束位置而 本紙張尺度逍用中國困家揉準（CNS ) A4此格（210X297公釐） • 50 經濟部中央樣準局貝工消费合作社印裂 4 3 8 6 19 A7 _B7_五、發明説明) . 水平延伸設置於塔2內，同時使該收容器8 Ο A的底面僅微向 下方傾斜|可設定使回送液5 c朝著一方向流動。 並且於上述收容器8 Ο A之傾斜下游端位置的吸收塔2側 壁連設回送液配管8 1 A的上端部，可與收容器8 0A的傾斜 下游端連通。 此外，該回送液配管8 1A是形成「3」字型，將垂直管 路部9 0沿著塔外側壁朝著與消霧器6同等高度下方下垂之後 ，再度水平貫入塔內|並在水平貫入塔內的水平管路部9 1的 下面側上，軸向間隔預定距離設置複數個噴嘴狀開口 8 2A -更具體而言是在向上噴嘴4的上方位置，大致液柱的垂直上方 附近，且在消霧器6正下方之飛散吸收液儲存區域下方開口的 位置上分別設置噴嘴狀開口 8 2A，該噴嘴狀開口 8 2A噴出 的回送液5 c是利用（重力作用）垂直管路部9 0流下的位能 使之持續噴霧而與噴出液柱衝突形成微滴化，可更有效地構成 氣液接觸。 本實施形態中，避開向上噴嘴4所噴射之吸收液5的液柱 頂部上方位置，且容易產生飛散吸收液儲存區域之消霧器6的 正下部（入口部）設定配管8 1 A的向下長度位於其下方位置 〇 又，回送液配管8 1A也可以如第1 9圖所示，將其一部 份通過吸收塔2外側，也可以設置使包含垂直管路部9 0的全 部通過吸收塔2內。 其次，說明第2 1圚表示之本發明其他實施例如下。 該例中，僅針對與上述第1 9圖表示之實施例不同的構成 (請先閱讀背面之注$項声，¾本頁) 本纸張尺度適用中國國家樣準（CNS > A4规格（21〇χπ7公釐） -51 - 經濟部中央橾準局貝工消费合作社印装 438619 A7 _____B7__五、發明説明以） 說明。第2 1圖中，以相同於第1 8圖〜第20圖之符號表示 的構件或位置是表示相互等效之構件或位置，因此爲避免重覆 而省略其說明。 第2實施例係與第1 8圖相同，在一對消霧器6的下端收_ 束位置分別設置收容器8 Ο B，但是該等分別的收容器8 0 B 彼此之間，是利用集合管8 0集合爲一之後，將該集合管8 0 連通於下垂之回送液配管8 1 B的上端部。此外|該回送液配 管8 1 B是使塔2內朝著下方下垂，設定使其下端開口 8 2 B 位在液體儲存部5 6內，該開口 8 2 B與上述實施例不同並未 呈噴嘴狀而僅是形成開口。 因此，本實施形態係與第1 8圖及第1 9圖之實施例的有 關裝置不同，並非將收容器8 Ο B集中的回送液朝著液柱狀噴 射流的上方位置噴霧，而是採取回送至液體儲存部5 6的構成 其次•綜合上述第1 8圖至第2 1圖分別之實施形態的作 用說明如下。 在各個實施例的裝置中設定向上通過吸收塔2內之廢氣1 的流速爲5.5m/s以上的高度時，隨著廢氣1的液滴會附著 在消霧器6上，從其下方部份流出多量的吸收液5。其吸收液 5並非從消霧器6直接落至塔內|而是直接爲收容器8 0A、 80B所捕集|爲收容器80A、80B所捕集的回送液5c 是藉著重力流至回送液配管81A、81B內，在第18圖及 第1 9圖的實施彤態中，更非消霧器6正下方，而是在該回送 液配管81A垂直方向量的下方位置上利用來自噴嘴狀開口 -----.-----^------1T------^ (請先閲讀背面之注意事項""本頁) 本紙張尺度適用中國國家標率（CNS ) A4規格（210X297公釐） -52- 經濟部中央橾準局貝工消ik合作杜印製 43 86 1 9 A7 A7 _B7____五、發明説明fco ) 8 2 A的重力能源，噴出至吸收塔2內之向上噴嘴4的噴出液 柱（吸收液）上1並且從該噴嘴狀開口 8 2A噴出的回送液 5 c與噴出液柱衝突形成微滴化，.可更有效地構成氣液接觸。 另一方面，第2 1圖中是將收容器8 OB聚集的回送液 5 c回送至液體儲存部5 6 |再度經由總管1 9 0及噴出噴嘴 4而向上方噴出》 因此，在上述任意的實施形態中.，不致於在容易形成飛散 液體儲存區域的消霧器6正下方附近增加液滴的量，可阻止隨 其部份的廢氣1所造成之吸收液5的再飛散· 第2 2圓是表示以實驗確認之塔內氣體流速及消霧器出口 之噴霧濃度關係的對數圓表，爲排除吸收液（本發明裝置）與 未排除吸收液者（習知裝置）成對比。 例如液柱高度爲1.7m之習知裝置〇中，塔內氣體流速超 過5.5m時，會使噴霧出口濃度急劇地上升，但是液柱高度爲 1.8m之發明裝置♦中，即使超過5.8m也不致提高噴霧出口 濃度。 又，例如液柱高度爲3.4m的習知裝置△與液柱高度爲 3.3m的發明裝置▲中，本發明的裝置側爲5.8m時的噴霧出 口濃度與習知裝置比較獲知可大幅度地降低至1/5 0以下。 因此，根據本圖可獲知本發明裝置較習知裝置在氣體流速 約5.5m/s以上領域時，對於塔外具有極優異的噴霧放出阻 止力。 該試驗之本發明裝置係使用第2 1圖之實施例者》其他條 件係如下述·（並且•圖中之液柱高度係形成吸收液的柱狀噴 {請先閱讀背面之注意事項再从寫本頁) 本紙張尺度適用中國國家橾準（CNS ) A4规格（210X297公釐） -53- 經濟部中央樣準局5工消费合作社印製 1 43 86 19 A7 _._B7五、發明説明h ) 射流高度。） 使用之消霧器：彎板式係使用45度傾斜 消霧器與向上噴嘴間的距離：.8m 第2 3圖是表示以試驗確認塔內氣體流速與消霧器入口之 噴霧飛散率的關係圖表，本發明裝置之消霧器入口部的噴霧飛 散率（噴霧重量/噴射吸收液的全重量X 1 0 0 )其液柱高度 爲2.4 m之習知裝置〇與液柱高度爲1.9 m的發明裝置•中， 並未見有大的變化，其皆呈現低率値，但是液柱高度爲2.8m 之習知裝置△與液柱高度爲3.3m的發明裝置▲中，相對於本 發明噴霧飛散率之低率値，可獲知習知裝置會大幅度增加。其 結果即使使液柱高度提高至3.3m左右，氣體流速爲5.5m/ s左右的高速領域時，可獲知噴霧飛散率仍呈現充分之低率値 此一試驗使用裝置與第2 1圖的實施例相同。其他的條件 則如下述。（並且，圖中之液柱高度係形成吸收液的柱狀噴射 流商度。） 使用之消霧器：彎板式係使用4 5度傾斜 消霧器與向上噴嘴間的距離：8m 因此，根據本實施形態，即使使吸收塔內的廢氣流動速度 高速化，會隨著淸洗處理後的廢氣從吸收塔排出的吸收液噴霧 會殘留有極少量，因此隨著通過塔內之廢氣的高速化可提高廢 氣處理的操作效率，極爲有利》 又’根據第1 8圖及第1 9圖之實施形態，從回送液配管 回流至^射流正上方附近吸收部的吸收液係與向上噴嘴所噴射 (请先閲請背面之注意事項寫本頁) 本紙張尺度通用中國國家標率< CNS > A4規格（210X297公釐） -54 - 4386 19 a7 B7 五、發明説明fe2 ) 之吸收液的噴射流同時再度對廢氣產生吸收作用，因此除了上 述的效果之外，並可保持高水準的廢氣處理性能。 又根據第2 1圖之實施形態，.到達消霧器之吸收液的液量 即使大幅度地增加時，仍可順利地回送至液體儲存部而可進行 再利用者《 I n d 訂 * I H 線 (請先閲讀背面之注意事項且.¾本頁) 經濟部中央橾準扃員工消费合作社印装 本紙張尺度適用中國國家標準（CNS ) A4規格（210X297公董） -55-8 2 A 9 0 9 1 19 0 19 0a [Best state for carrying out the invention] An example of the present invention will be described in detail with reference to the drawings. However, if the dimensions, materials, shapes, and relative arrangement of the constituent members described in this embodiment are not specifically described, the scope of the present invention is not limited to this purpose, but only to the illustrative examples. Fig. 1 is a schematic view showing a wet gas treatment apparatus according to an i-th embodiment of the present invention. . ----.----- I ------ 1T ------ 0 (Please read the note on the back page first) This paper adopts China National Standard (CNS > Α4 specifications (210X297 mm) -27- Printed by the Shell Consumer Consumption Cooperation Department of the Central Sample Bureau of the Ministry of Economic Affairs 4 3 8 6 19 A7 ___B7_____V. Description of the Invention) In the first picture, the exhaust gas from a combustion device such as a boiler 1 It is introduced into the smoke exhaust introduction part 3 provided in the lower part of the absorption tower 2. The introduced exhaust gas 1 is in contact with the absorption liquid 5 supplied by the absorption liquid supply nozzle 4 provided in the lower part of the absorption tower 2 to move the target component in the gas from the gas to the absorption liquid 5. In this case, the combination of the target component in the gas and the absorbing solution means that the target component is soluble in the absorbing solution and dust. For example, in this embodiment, the soluble target component of the absorbing liquid is sulfur dioxide (SO2), and the absorbing liquid is a suspension of limestone containing an absorbing agent. In addition, the nozzle is an upward nozzle 4 in the present embodiment. * The absorption liquid 5 is sprayed upward from the upward nozzle 4 so that the exhaust gas 1 introduced by the smoke exhaust introduction unit 3 is absorbed by the nozzle 4. The liquid jet 5 a is in gas-liquid contact with the jet passing through the absorption liquid 5. A mist eliminator 6 is arranged on the upper part of the absorption tower 2 near the apex of the jet stream, and the absorption liquid 5 accompanying the gas 1 is removed by the mist eliminator 6. In the absorption tower 2, the target component is removed from the absorption liquid 5, and the purified gas 7 after the absorption liquid 5 is removed by the mist eliminator 6 is finally discharged into the atmosphere from the smoke exhausting section 8 or, if necessary, not shown in the figure. Streaming machine. On the other hand, a recoverer 9 with an upper opening is arranged around the side wall of the absorption tower 2 below the mist eliminator 6, and the absorption liquid 5 captured by the mist eliminator 6 is recovered by the recoverer 9 and passed through the communication pipe 10 Drop into the pressure tank 1 1. Therefore, the height of the absorption liquid 5 sprayed from the absorption liquid supply nozzle 4 is pushed by the flow rate of the exhaust gas 1 to set the pressure and communication pipe of the pressure tank 11 that can rise above the position of the recovery device 9 10 its upper end is open at the bottom of the recycler 9, the connecting pipe 10 II ί ί I ni— II line (please read the precautionary note on the back first < write this page) This paper's standard is applicable to China National Standards (CNS) Regulation 8 < Grid (210X297 mm) -28 · 438619 A7 B7 Printed by the Central Consumers Bureau of the Ministry of Economic Affairs, Printed by the Consumers Cooperative Cooperative, V. Description of the invention β) is opened from the top of the pressure tank 11 and is often submerged into the tank 11 The position in the absorption liquid inside is sealed by the communication pipe 10 with the gas of the pressure tank 11. That is, the absorption liquid 5 recovered by the recoverer 9 flows from the communication pipe 10 toward the pressure tank 11, but at this time, compressed air is generated in the upper closed space 1 1 a inside the pressure tank 11. The pressure of the gas will cause the absorption liquid 5 in the pressure tank 11 to flow back, and raise the liquid level in the communication pipe 10 to a position that is in equilibrium with the pressure in the pressure tank 1 1. And set the level difference of the communication pipe 10, The position of the recoverer 9 and the internal pressure of the tank 11 make the liquid level in the communication pipe 10 lower than the position of the recoverer 9 so that the recoverer 9 can continue to circulate the absorption liquid into the pressure tank 11 and can borrow the liquid. The pressure tank 11 is hermetically sealed against the absorption liquid 5 in the communication tube 10. The bottom of the pressure tank 11 is provided with a gas nozzle 13 connected to the air compressor 12, which can inject air pressurized by the storage and discharge liquid, in other words, an oxygen-containing gas. This pressurized gas has two functions. The first is to maintain the pressure of the upper closed space I ia in the pressurized tank 11, and the second is the suspended absorption liquid 5 containing the limestone that is in contact with the gas-liquid to absorb S 〇 2. Contact with the above oxygen-containing gas oxidizes S0 to produce calcium sulfate dihydrate (gypsum). The absorption liquid 5 stored in the pressure tank 11 is under the pressure of the closed space 1 1 a in the pressure tank 11 The absorption liquid supply nozzle 4 in the absorption tower 2 is circulated through a flow control valve 15 that controls the supply flow of the absorption liquid supply pipe 14 and the absorption liquid 5. * Next, the structure of the pressure tank 11 will be described below. At the top of the pressure tank 11 is a pressure control valve 16 that controls the atmospheric open pipe 17 and the pressure in the tank 11 or supplies raw materials such as neutralizers on the side wall of the tank --------- ^-( Please read the notes on the back first. . . (This page), ιτ line standard paper paper speed in the middle of the cocoon family standard rate (CNS > A4 specifications (210X297 mm) -29 · Central Sample Bureau of the Ministry of Economic Affairs, shellfish consumer cooperation Du printed 4386 1 9 a ? _B7__ V. Description of the invention) The pipes 1 and 8 are respectively installed by a drainage recovery pump 2 1 and a drainage recovery pipe 20 for recovering the absorption liquid 5 from the liquid storage part 5 6 provided at the bottom of the absorption tower 2. On the other hand, an extraction pipe 19 is installed at the bottom of the tank 11 so that gypsum and the like produced during the above-mentioned oxidation of S02 can be pulled out. The reason for constituting the pressure tank 11 is as follows. According to this embodiment, even if the absorption liquid 5 is sprayed upward in the absorption tower 2 and the absorption liquid 5 is recovered by the recoverer 9 provided on the upper part of the absorption tower 2, a part of the absorption liquid 5 will leak out simultaneously with the gas, and Part will fall towards the bottom of the absorption tower 2 | Therefore, the above-mentioned recovery device 9 'alone cannot recover 100% of the amount. Therefore, once the level of the liquid remaining in the bottom of the absorption tower 2 reaches a predetermined amount or more, it can be pumped 2 Pressing back to the pressure tank 1 1 1 "Also, while supplying the neutralizing agent from the raw material supply pipe 18 to the pressure tank 11 1 • Use the extraction pipe 19 to extract a part of it and return to Shiyin. Procedure> Therefore, in this embodiment, it is possible to balance the supply of the absorption liquid from the raw material supply pipe 18 and the amount of liquid removed from the gypsum recovery step (not shown) and the amount of liquid removed simultaneously with the gas. • The liquid in the pressure tank 11 is maintained. Level. The amount of air in the pressure tank I1 supplied from the air compressor 12 is injected into β corresponding to the amount of 302 in the exhaust gas 1. Therefore, the air pressure in the pressure tank 11 is controlled to a predetermined pressure so that the absorption liquid supply pipe 14 and The discharge amount of the absorption liquid of the extraction pipe 19; the discharge amount of the absorption liquid of the communication pipe 10, the raw material supply pipe 18, and the drainage recovery pipe 20; and the gas discharge amount of the air compressor 12 reached equilibrium. In addition, when the above-mentioned balance is broken and the pressure in the tank is higher than the predetermined pressure, the pressure control valve 16 can be automatically opened, and the pressure in the tank can be restored to the predetermined pressure, so that the pressure in the tank can be maintained at the predetermined pressure.圉 National Rubbing Standard (CNS > Α4 wash grid (2Ι0 × 297 mm) -30- 438619 Printed by the Shellfish Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs A7 B7_5. Description of the invention) Secondly, confirm the above embodiment with the following experiments Indicates the effect produced by the device. Fig. 2 is a graph showing an example of the relationship between the gas flow rate and the removal rate of SO2 in the gas treatment apparatus of the present invention, in which the absorption liquid is used as a suspension containing calcium carbonate and the circulation flow rate of the absorption liquid is constant. Through this experiment, it was learned that the performance of more than 90% obtained by the general sulfur dioxide removal rate can be obtained in a wide range. Therefore * when the load fluctuation of a gas generation source such as a boiler is reduced to reduce the flow rate, sulfur dioxide can be removed at an efficiency of more than 90%. In this experiment, the absorbent liquid can be recovered in its entirety by the recovery device 9 which is opened upward as shown in Fig. 1 and can be operated smoothly. In addition, even under the condition that the ventilation speed of the air flow is reduced, increasing the pressure in the pressure tank 11 can promote the absorption liquid 5 to reach the upper portion. At this time, the recovery liquid 9 can also be used to recover the absorption liquid 5 β in substantially the entire amount. In the embodiment, it is not necessary to use a jet pump, or even if the flow rate is decreased with the absorption liquid, the absorption liquid can be recovered smoothly. In particular, according to this embodiment, pressurized gas such as compressed air can be used to pressurize the pressure tank, so that the liquid level of the pressure tank does not need to be located at the upper part of the absorption liquid supply nozzle, except that the pressure tank can be lowered. And can be freely configured. In addition, as described above, the flow rate of the gas in the absorption tower 2 can be reduced by changing the load. Even if the absorption liquid is not followed, the pressure in the pressure tank can be increased to raise the absorption liquid to the vicinity of the mist eliminator, which can be recovered and absorbed. Liquid · Figure 3 is a line 槪 I ϋ II n I ^ n 11 n II n of the wet gas processing apparatus showing the gravity supply method of the absorption liquid without using an upward nozzle in the above embodiment according to the second embodiment of the present invention ( Please read the note f on the back side and write this page first) This paper size uses the Chinese National Standard (CNS) A4 size (210X297gt) -31-Central Office of the Ministry of Economic Affairs, Work and Consumption Cooperation, Du Printing 4 3 861 9 at ________B7_ V. Description of the invention b) Structure. As shown in the figure I, the exhaust gas introduction part 3 provided at the lower part of the absorption tower 2 is used to introduce the exhaust gas 1 from a combustion device such as a boiler, and the exhaust gas passage 2 A extending above the interior of the tower is conducted to form a rising exhaust gas flow and constitute a defog The chiller 6 discharges the smoke exhaust lead-out portion 8 at the top of the absorption tower. A liquid storage unit 56 is provided at the lower portion of the absorption tower 2 and can store the absorption liquid 5 such as a lime suspension from the upper and lower tribes of the tower 2 to be returned to the absorption liquid storage tank 27 by the recovery pump 21. On the other hand, in the inlet portion of the exhaust gas passage 2A directly above the smoke exhaust introduction portion 3, a plurality of substantially horizontal upper open water-conducting tubular absorption liquid pipes 31 are formed in a plurality of parallel sections and formed into a horizontal pipe row. The liquid level of the storage tank 2 7 which supplies the absorption liquid to the water-conducting tubular absorption liquid tube 31 is set to be slightly higher than the liquid level of the above-mentioned water-conducting tubular absorption liquid tube 31. The absorption liquid 5 can be used to make the absorption liquid 5 by its proper drop. After the liquid is introduced into the main manifold 190 (see FIG. 5) through the absorption liquid conduit 29 and the valve 60, the absorption liquid 5 introduced into the water-conducting tubular absorption liquid pipe 31 is configured more than the upper side of the water-conducting tubular absorption liquid pipe 31 through the main pipe 190. The film-like shape overflows toward the gap portions 30 between the adjacent water-conducting tubular absorption liquid pipes 31 (see FIGS. 4 and 5). Moreover, since the liquid level of the absorption liquid storage tank 27 is set to be slightly higher than the liquid level of the water-conducting tubular absorption liquid tube 31, the recovery pump 2 1 can be adjusted corresponding to the absorption liquid supplied by the absorption liquid supply valve 60. And the recovery amount of the recovery tube 2 4 a and the supply amount of the new absorbent liquid 5. Although Fig. 4 shows the arrangement form of the above-mentioned water-conducting tubular absorbent tube 31 1, Fig. 4 (A) shows the The inlet of the above exhaust gas channel 2A is along the binding line {please read the precautions on the back first, this page) This paper size applies to China's national standard (CNS > A4 specification (2 丨 0X297 mm) -32- 1 4386 19 A7 B7 V. Description of the invention) One parallel section is arranged in one section in a horizontal plane of one of the approximate cross sections, so that the gaps 30 between the adjacent tubes of the tube group 3 constitute a conductive exhaust gas flow 3 2 and at the same time, An absorbent liquid 5 such as a lime suspension suspended from the inner wall of the tower 2 is recovered. Therefore, 90 ° arc-shaped tubes 24 are provided on the inner walls of the left and right walls of the tower. According to the above configuration, the inlet portion of the exhaust gas passage 2A is provided with a plurality of water-conducting tubular absorption liquid pipes 3 1 arranged in a row through the predetermined gap portion 30. Therefore, the exhaust gas flow is reduced in the gap portion 30. The passage area of 3 2 can increase its speed to increase the speed. And the absorption liquid 30 overflows out of the exhaust gas flow 3 2 to form the high-speed air gap portion 30 to form a cross-shaped contact with the high-speed rising exhaust gas flow 3 2 Therefore, the absorption liquid 5 can be disrupted into micronized particles with the high-speed energy source caused by the exhaust gas flow 32. In addition, the absorption liquid 5 recovered by the 90 ° arc tube 24 will rise again due to the gas, so the power of the recovery pump 21 can be reduced. In the fourth (B), the above-mentioned water-conducting tubular absorption liquid pipe 31A that makes the inlet section of the above-mentioned exhaust gas channel 2A approximately horizontally arranged is arranged in the horizontal direction. Please read the notes on the back before reading this page) 3 1 B, so that the gaps 30A and 30B between the pipes 3 1A and 3 1 B adjacent to the pipe group can pass through the exhaust gas flow 32, so At this time, a section of the water-conducting tubular absorption liquid pipes 3 1 A on one side reduces the passage area of the exhaust gas flow 3 2 and increases the speed to form a high-speed person. In addition, the exhaust gas flow 32 forms the high-speed exhaust space 30A, and the absorption liquid 5 flows out. The high-speed rising exhaust gas flow 3 2 is the same as that in FIG. 4 (A), but the water is conducted on the side of the above section. The open position between the tubular absorbent pipe 3 1 A and the water-conducting tubular absorbent pipe 3 1 B on the second stage side. • The use of the above-mentioned high-speed exhaust gas flow 3 2 to reduce and expand the high-speed fluid of the exhaust gas 1 creates a negative pressure, and This paper size is applicable to China Solid State Standards (CNS) A4 (210X297 mm) -33- Consumption Cooperation with Employees of the Central Sample Rate Bureau of the Ministry of Economic Affairs Du Yin 4386 19 A7 _B7_ V. Description of the Invention h) The open surface of the water-conducting tubular absorption liquid pipe 31A causes the fine particles of the absorption liquid 5 to be atomized, and the second-side side of the water-conducting tubular absorption liquid pipes 3 1 B is used to pass the exhaust gas flow 3 2 through again. Increasing the area and increasing its speed to form a high speed has the same effect as above, which can further improve the efficiency of gas-liquid contact. Of course, the number of segments can be three or more. Fig. 5 shows the flow state of the absorption liquid 5 in the water-conducting tubular absorption liquid tube 31 of Fig. 4 (A). In the same figure, the main pipe 1 9 0 connected to the absorption liquid pipe 29 is arranged along the inner wall of the tower, for example, and the side opening 19 1 a of the main pipe 1 0 0 is connected with the along and the One end of the water-conducting tubular absorbent pipe 3 1 parallel and parallel to the pipe axis. The water-conducting tubular absorbent pipe 3 1 is structured as shown in Fig. 5 (A). The entire length of the upper surface of the side wall of the tubular absorption liquid pipe 31 allows the absorption liquid 5 to overflow out of the gap portion 30 side. It is difficult to set the upper surface of the side wall of the water-conducting tubular absorbent tube 31 horizontally. As shown in FIG. 5 (B), plural upper sides of the left and right side walls of the water-conducting tubular absorbent tube 31 are axially provided with a plurality of predetermined intervals. Each of the notches 3 1 a can form an overflow 3 9 intermittently on the side of the void portion 30 through the notches 3 1 a, and constitute a cross-contact with the high-speed exhaust flow 32. According to the above-mentioned embodiment, the exhaust gas 1 introduced into the absorption tower 2 with respect to the lateral film-like overflow is passed through a plurality of gaps 30 between a plurality of water-conducting tubular absorption liquid pipes 31 to form a high-speed updraft (The tower speed of the exhaust gas is about 10m / s). After the cross-contact with the absorption liquid 5 as mentioned above, the absorption liquid 5 that cross-contacts through the contact is to make the micro-IIH ^ li HI line {谙 先The note on the back of this page is really on this page.) This paper size is applicable to China Standards for Fixing Standards (CNS) A4 (210X25 »7mm). • 34- Printed by Beige Consumer Cooperative, Central Prototype Bureau, Ministry of Economic Affairs 43 86 1 9 a? _B7_ V. Description of the invention) The small liquid droplets are dispersed and dispersed in the upper part of the water-conducting tubular absorption liquid pipe 31 to form a turbulent flow. In the expanding updraft, at the same time, the absorption liquid 5 on the water guiding tube is atomized 'from the open surface of the water guiding tubular absorption liquid pipe 31 at the same time under negative pressure, dispersed and mixed to effectively form gas-liquid dispersed gas after gas-liquid contact. The above gas-liquid dispersion gas system forms a gas-liquid contact zone space 2A on the upper side and reaches the mist eliminator 6 above the absorption tower. However, the objective component in the exhaust gas during this time is to absorb the absorption liquid 5 from the exhaust gas 1. In addition, the combination of the target component in the gas and the absorbent liquid 5 is in the embodiment that the target component that is soluble in the absorbent liquid 5 is sulfur dioxide (S02), and the absorbent liquid 5 uses a suspension containing limestone that forms an absorbent. liquid. On the other hand, the exhaust gas 1 passing through the air region 2 A of the gas-liquid contact zone can be recovered by the mist eliminator 6 and the absorbent liquid 5 that is subsequently dispersed, and then returned to the absorbent liquid storage tank 27 through the recovery pipe 2 4 a. The recovered absorption liquid 5 is returned to the absorption liquid storage tank 27 through a recovery tube 2 4 b using a half-cut arc-shaped tube 24 for recovery provided on the inner wall of the tower. The target component in the absorption tower 2 is absorbed by the absorption liquid, and the accompanying absorption liquid is separated by the mist eliminator 6, and finally the exhaust gas 1 forming the purified gas is sent to the atmosphere or the downstream downstream (not shown) through the smoke exhaust outlet 8 machine. Fig. 6 shows another embodiment which is different from the water-conducting tubular absorbent tube of the above embodiment. The upper closed tubular member constitutes the absorbent tube 31 at the same time as the absorbent tube 31 described above. A slit-like opening or a plurality of small hole rows are provided along the pipe axis direction on the surrounding surface of the gap portion 30 where the exhaust fluid 32 is vented. At this time, as shown in the figure, in order to suppress the resistance of the fluid, the cross section of the lower side of the absorption liquid pipe 31 is preferably formed into a curved shape (for example, circular, streamlined ---------- installed ----- --Order ^ ------ line (please read the precautions on the back to get this page) This paper size is in accordance with Chinese standard (CNS > June 4th (210X297) > -35- Economy Printed by Shellfish Consumer Cooperative of Central Ministry of Standards and Technology of the PRC 438619 at _. _B7 V. Description of the invention), spinning drops, etc.) or wedges or triangles, for example, Figure 6 (A) shows the bottom of the absorption liquid tube 31 is a semi-circular tubular member with a circular cross-section closed by a flat cover 31d 3 1 c The upper surface is formed by intermittently passing a plurality of small holes 3 6 along the axis direction on the opposite side of the gap portion 30 on the side walls of both sides so that the gap is opened 3 7 (see Figures 6 (D) and (E)). . In the embodiment shown in FIG. 6 (B), a plurality of small holes 3 are intermittently inserted along the axial direction on the left and right generatrixes of the horizontal section including the axial center using a hollow circular tubular member 34 in cross section. 6 so that the slit opening 3 7 (see Figure 6 (D), (E)). In addition, the embodiment shown in FIG. 6 (C) uses a hollow elliptical tubular member 34 in cross section, and a plurality of small holes 3 are intermittently formed along the axial direction on the left and right generatrixes of the horizontal section including the axis. 6 so that the slit opening 3 7 (see Figures 6 (D) and (E)). In addition, the small holes 36, or the slit openings 37, are not necessarily provided on the horizontal cross-sectional left and right generatrixes that include the axis center | may be provided above or below them. Therefore, according to the embodiment of the present invention, it is different from the conventional upward nozzle. The above-mentioned absorption liquid 5 only needs to form a substantially horizontal overflow or outflow toward the side of the gap portion between the adjacent tubes. Therefore, it is possible to reduce the equipment cost and obtain the effect of reducing energy. In this embodiment, it is preferable that the absorption liquid supply source configured by the absorption liquid supply source using gravity is used to supply the absorption liquid to the absorption liquid tube. However, the present invention may also adopt a configuration using an absorption liquid supply pump. , Can also reduce the cost of equipment. .  In the embodiment, a predetermined empty binding line is used at the inlet of the above-mentioned exhaust gas channel 2 A (please read the precautions on the back to write this page) This paper size is applicable to the Chinese standard (cns > A4 specification ( uoxw mm). 36- 438619 A7 B7 V. Description of the invention) The central government ’s bureau of the Ministry of Economic Affairs ’s work co-operative consumer cooperative prints the gap section 30. It is equipped with a plurality of absorbing liquid pipes arranged in series. As a result, the above-mentioned gap section can simultaneously carry out exhaust gas flow 3 2 The effective gas-liquid contact with the absorption liquid 5 and the supply of the absorption liquid can be performed more effectively in a short period of time compared with the gas-liquid contact completed from the beginning of the ditch flow accompanying the liquid column type liquid column at the top. The large-scale gas-liquid contact makes it possible to efficiently absorb / remove the target components in the exhaust gas, and at the same time, to make the absorption liquid 5 finer and disperse in a shorter time, thereby reducing the equipment cost. Fig. 7 is a circuit diagram showing a wet gas processing apparatus according to a third embodiment of the present invention. In Fig. 7, exhaust gas 1 from a combustion device such as a boiler is introduced into a smoke exhaust introduction portion 3 provided at a lower portion of the absorption tower 2. The introduced waste gas 1 is in contact with the absorption liquid 5 supplied by the absorption liquid supply nozzle groups 4A to 4 C provided in the lower part of the absorption tower 2, and the target component in the waste gas 1 can be moved from the gas 1 to the absorption liquid 5 · This At this time, the combination of the target component in the exhaust gas 1 and the absorption liquid 5 in this embodiment. The target component soluble in the absorption liquid 5 is sulfur dioxide (S02). The absorption liquid 5 is a suspension using limestone containing an absorbent. . A liquid storage unit 56 is formed in the lower part of the absorption tower 2 to store the absorption liquid 5 such as a lime suspension, and passes through the recovery pump 21, the regeneration buffer tank 22, the nozzle pump 23, and the flow control switch valve 43A. ˜43C, and communicates with the liquid storage portion 56 and the introduction pipes 49 of the nozzles 4A to 4C. In addition, the nozzle group is an upward nozzle group 4A to 4C, and the absorption liquid 5 is sprayed upward from the upward nozzle group 4A to 4C, so that the exhaust gas 1 introduced by the smoke exhaust introduction section 3 follows the nozzle group. The absorption liquid 5 ejected from 4A to 4C can be brought into contact with the gas through the absorption liquid 5a. Please read Item 4 on the back first, write this page. The paper is a Chinese standard for quick-use Chinese standard (CNS) A4 specification (2 丨 0X297 mm) _ _ A7 43 86 1 9 __B7_ 5. Description of the invention & 5 A mist eliminator 6 ′ is arranged on the upper part of the absorption tower 2 near the apex of the nozzle, and the mist eliminator 6 is used to remove and recover the absorption liquid 5 generated with the gas 1. The target component is removed from the absorption liquid 5 in the absorption tower 2, and the purified gas 7 that removes the absorption liquid 5 with the mist eliminator 6 is finally sent to the atmosphere through the smoke exhausting section 8 or necessary (not shown) Backflow machine. On the other hand, a recovery device 9 with an upper opening is arranged around the side wall of the absorption tower 2 below the mist eliminator 6. The absorption liquid 5 captured by the mist eliminator 6 is recovered by the recovery device 9 and passed through the buffer tank. 22 etc. are recycled for their needs. Therefore, the height of the absorption liquid 5 sprayed from the upward nozzle groups 4A to 4C is pushed up by the flow rate of the exhaust gas 1, and the flow rate of the exhaust gas 1 rising above the position of the recoverer 9 can be set, but a gas generation source such as a boiler Generally, load fluctuations occur, so when the gas flow rate is reduced, the absorption liquid 5 can be generated as the gas flow rate is reduced as described above. Therefore, in the present embodiment, the upward nozzles 4A to 4C are configured by three groups of left, center, and right in the figure. On-off valves 4 3A to 4 are provided in each of the absorption liquid conduits 49 of the respective nozzle groups 4A to 4C. 3 C, the ejection / stop of the absorption liquid 5 can be performed in independent nozzle groups 4A to 4C, respectively. In addition, although the nozzle groups 4A to 4C form only one nozzle in the figure, actually, a plurality of nozzles are arranged in a row in the front-rear direction. Further, the above-mentioned left nozzle group 4A and the center nozzle group 4B, and the center nozzle group 4B and the right nozzle group 4C are provided with vertical dividing plates 4 0 A, 4 〇 ». The upper ends of the dividing plates 4 0A and 4 〇 B are extended to the vicinity of the installation position of the mist eliminator 6 higher than the recoverer 9 described above, but the lower ends of the plates --------- ^ ------ , π. ------ 0 (Please read the notes on the back first. This paper) This paper is printed by the Consumer Cooperative of the Central Procurement Bureau of the Ministry of Economic Affairs. The paper size is applicable to the Chinese National Standard (CMS) A4 specification (210 × 297 mm) -38- Printed by the Central Procurement Bureau of the Ministry of Economic Affairs and Consumer Cooperative. 4386 19_B7_ V. Description of the invention ^).  The height position is different from this. One of the division plates 40 A is suspended to the liquid level of the liquid storage portion 5 6 A of the absorption liquid 5 to its position. The other splitting plate 4 〇 B is a liquid level level that sags to a level higher than the liquid level of B above A. On the above splitting plates 4 0A and 4 〇 B, three divided gas flow areas 41A, 41B, and 41C are formed. . According to the above-mentioned Embodiment 1, the liquid level of the absorption liquid 5 in the liquid storage portion 56 is raised by the pump drive control. Before the liquid level is raised to the liquid level of A, The lower end of a dividing plate 4 0A is submerged into the absorption liquid 5, thereby closing the gas introduction opening of the gas flow area 4 1 A on the left side. As a result, the flow area of the exhaust gas 1 introduced by the smoke exhaust introduction portion 3 forms only the center 4 1 B and 4 1 C on the right. In this state, the on-off valve 43A of the left nozzle group 4A is closed, so that the area of the gas flow can be formed to be only two-thirds of the central and right exhaust gas flow areas 41B and 41A. As a result, even when the introduction flow rate of the exhaust gas 1 is reduced by 2/3, a constant gas flow rate can be maintained. Therefore, the absorption liquid 5 can maintain the ejection height of the absorption liquid 5 of the nozzle groups 4 B and 4 C with the gas flow rate. Gas-liquid contact between the absorption liquid 5 and the air flow 32 can be performed smoothly. In addition, the above-mentioned liquid level is raised to the liquid level of B, so that the lower end of any of the two split plates 40A and 40B can also be submerged into the absorption liquid 5, thereby closing the left and central gas flow areas 4 1 A, 4 1 B gas introduction openings | As a result, the drainage area of the exhaust gas 1 introduced by the smoke exhaust introduction portion 3 can be only 4 1 C on the right side. In this state, the opening and closing valves 4 3A and 4 3 B of the left and central nozzle groups 4A and 4 B are closed, thereby allowing the air flow passage area to form only one third of the area of the gas flow area 4 1 C. As a result, the introduction flow of exhaust gas 1 can be reduced (please read the precautions on the back first: ^ this page). Binding-The size of the paper is applicable to China National Standard (CNS) Α4 (210 × 297 mm) -39- 438619 Economy The Ministry of Standards and Standards Bureau prints A7, B7, and F5. Description of the invention) to maintain a certain gas flow rate. Therefore, according to this embodiment, when the gas flow rate in the absorption tower 2 is reduced, and the flow rate flowing through the exhaust gas passage is reduced in proportion to this, 1 the plurality of gas flow regions 4 1 A ~ 4 0 A, which are separated by the partition plate, are closed. For one side of 4 1 C • Corresponding to the decrease of the above flow rate, the flow rate can be controlled to form a certain area of gas passage. Fig. 8 is a modification of the embodiment shown in Fig. 7. The lower ends of the partition plates 40A and 40B are configured as "J" -shaped curved portions 4 5 which can be directed toward the smoke exhaust introduction portion 3 which is introduced into the absorption tower 2. . According to the above-mentioned embodiment, the exhaust gas 1 introduced from the smoke exhaust introduction part 3 into the absorption tower 2 in a downwardly inclined direction is rectified in the jet flow direction of the nozzle group 4A to 4C along the above-mentioned "j-shaped curved part 4 5". Guided vertically upwards. As a result, the above-mentioned split plates 40A and 40B also have the function of an exhaust rectification plate, which can make gas-liquid contact more smoothly. Fig. 9 shows another embodiment of the present invention. The above-mentioned upward nozzle group 4A, 4B is composed of two groups on the left and right in the figure, and the on-off valves 43A and 43B are provided on the introduction pipes 49 of the nozzle groups 4A and 4B. The absorption liquid 5 can be sprayed / stopped on the independent nozzle groups 4A * 4B. Between the left nozzle group 4A and the right nozzle group 4 B, a dividing plate 4 0A extending in the vertical direction is provided vertically. The dividing plate 4 0A is provided with the fulcrum 4 8 at the installation position of the nozzle groups 4A and 4 B. Further down | and install the rotating plate 4 6 which is centered on the fulcrum 4 8 toward the smoke exhaust introduction portion 3. According to the above-mentioned embodiment, make the above-mentioned rotation plate 46 toward the smoke exhaust introduction portion 3 (please first (Read the note on the back of the page.) China National Standards (CNS > Α4 specifications (2 丨 0X297 mm) -40 · Printed by the Consumer Cooperatives of the Central Standardization Bureau of the Ministry of Economic Affairs 11 4386 1 9 A7 A7 _B7 V. Description of the invention ί8) Turn to the side and keep it to the slightest Down position below the level, which opens the right simultaneously. Gases in the gas flow areas 4 1 A and 4 1 B on either side of the left side are opened to form normal gas-liquid contact. Next, by rotating the above-mentioned rotating plate 46 from the smoke exhaust introduction portion 3 side toward the liquid storage portion vertically downward, the lower end of the rotating plate 4 6 can be submerged into the absorption liquid 5. This can close the gas flow area 4 1 on the left side. As a result, only the right side 4 1 B is formed in the exhaust gas flow area introduced by the smoke exhaust introduction part 3. Further, in this state, the on-off valve 43A of the left nozzle group 4A is closed, whereby the area through which the gas flows is only half of the area on the right. Fig. 10 is another modification of Fig. 7. The difference from the modification of Fig. 9 is that the above-mentioned dividing plate 4 OA is located below the installation position of the nozzle groups 4 A and 4 B, and can be vertically lifted freely. Lifting board 4 7. According to the above-mentioned embodiment, the above-mentioned lifting plate 47 is raised above the liquid storage portion 56, and the gas introduction openings of the gas flow areas 4 1 A and 4 1 B on the left and right sides can be opened at the same time. Gas-liquid contact person. Next, the above-mentioned lifting plate 47 is lowered and moved vertically downward. The lower end of the lifting plate 47 is immersed in the absorption liquid 5, thereby closing the gas introduction opening of the gas flow area 4 1 A on the left side. The exhaust gas channel introduced by 3 forms only 4 1 B on the right side. In addition, in this state, the on-off valve 4 3A of the left nozzle group 4A is closed, so that the gas flow passage area is only 1/2 of the area on the right side. The split plate 4 0 A may also be formed to be perpendicular to the exhaust gas flow direction. Move horizontally. Fig. 11 is another modified example of the movable partition plate 40A. The partition plate 40A is configured to be substantially orthogonal to the flow direction of the exhaust gas, and the suction 1 · II nn I ^ 1 ^ 1—n «I n (Please read the precautions on the back first. . Λ This page) This paper is based on the Chinese National Standards (CNS M Choi I (210 × 297 mm) -41-Shellfish Consumer Cooperation of the Central Sample Rate Bureau of the Ministry of Economic Affairs Du printed 438619 A7 _. _B7 V. Description of the invention fo) The left wall surface of the receiving tower 2 is moved to the central position, and the movement toward the central position can be divided vertically between the left nozzle group 4 A and the right nozzle group 4 B, and extends in a vertical direction. Board 40A. The lower end of the dividing plate 40A is submerged in the absorption liquid 5 of the liquid storage portion 56. As a result, only the right exhaust gas flow area 4 1 B of the above-mentioned partition plate 40A opens the gas introduction opening. The right exhaust gas flow area 4 1 B is formed by moving the partition plate 40A from the left wall surface of the absorption tower 2 to the center position, and the exhaust gas 1 can be formed. A narrow cross-sectional area of the channel of the right gas channel 4 B introduced. According to the above-mentioned embodiment, as the flow rate of the exhaust gas is reduced, the partition plate 40A is moved to the center side *, and the cross-sectional area of the channels of the narrow gas flow areas 41A and 4B can be formed freely. Therefore, according to the above-mentioned embodiment, the gas flow in the absorption tower is reduced due to load fluctuations of combustion devices such as boilers. Even when the flow path in the exhaust gas passage is reduced in proportion to this, the gas passage area of the gas inflow zone can be controlled. By making the gas flow constant, the absorption liquid discharge height of a certain nozzle group can be maintained substantially. As a result, not only can the gas-liquid contact between the absorption liquid and the air flow be smoothly performed, but also the absorption liquid can be smoothly recovered in the upper part of the absorption tower. According to this embodiment > it is possible to save unnecessary driving power of the pump and the like, and to prevent unwanted circulation of the absorption liquid. Furthermore, the gas passing area can be controlled to make the gas flow rate constant by controlling one of the plurality of gas basins spaced by the partition plate or narrowing the gas passage area, in response to the decrease in the flow rate. In addition, ^, and through the adjustment of the liquid level of the absorption liquid or selective division (please read the precautions on the back of the bird first page) This paper applies the Chinese standard (CNS) standard (210X297 mm) ) -42- 4 3 8 6 19 A7 B7 Printed by the Central Bureau of Fengfeng Bureau of the Ministry of Economic Affairs, Shellfish Consumer Cooperative, Co., Ltd. 11 V. Description of the buckle) The lower end of the board is lowered and submerged in the absorption liquid. The channel of the gas flow area can be simply selected. In addition, according to this embodiment, it is possible to easily perform flow control or switch control of gas inflow in a gas flow area by swing steering at the lower end side of the partition plate. In addition, according to the device of Fig. 8, the above-mentioned dividing plate also has the function of an exhaust gas rectifying plate, which can more conveniently form gas-liquid contact. "According to the devices of Figs. 9 to 11, it can respond to the fluctuation of the exhaust gas flow rate. By moving the dividing plate, the cross-sectional area of the channel in the gas flow area can be freely adjusted. Fig. 12 is a diagram showing a schematic configuration of a wet-type exhaust gas treatment apparatus according to a fourth embodiment of the present invention, and a description of overlapping portions of the apparatus configuration described in the above embodiment is omitted. As shown in No. 12 (2), an existing maintenance blower tank 60 and a blower tank pump 60a are provided in the lower part of the liquid storage part 56 of the absorption tank at the lower part of the absorption tower 2. In addition, an electromagnetic switch valve 6 7 is provided in the passage 6 8 from the liquid storage section 56 to the blowing tank 60, so that the control circuit 6 6 can detect an exhaust gas flow velocity detection sensor 6 5 provided in the smoke exhaust introduction section 3. Exhaust gas flow rate (tower speed), when the absorption tower 2 is rising and falling, the electromagnetic switch valve 6 7 can be opened to make the flow rate of the exhaust gas 1 reach the loading flow rate. • The liquid storage part 5 6 · * blow tank 6 0 —blow tank pump 6 0 a -Pressure tank 1 1Circumference return flow path for return > In addition, the upper space of the storage liquid surface of the pressure tank 11 provided outside the absorption tower 2 passes through the pressure compressor 1 7 a and the pressure regulator 1 6 The pressure can be controlled at any pressure by the control circuit 6 9. The control circuit 69 detects the pressure on the inlet side of the absorption liquid supply pipe 14 through the pressure sensor 62, and provides a certain absorption liquid supply pressure to the nozzle 4 ^! ^ LnllJ nn ^ (Please read the back Note $ item / i. . (Write this page) This paper is in accordance with the China National Standard (CNS) A4 specification (2 丨 0X297g t > · 43 · 438619 A7 B7 Printed by the Central Bureau of Standards, Ministry of Economic Affairs, Shellfish Consumer Cooperative, Fifth, Invention Description h) Direction, the pressure regulator 16 is used to control the pressure of the pressure tank 1 1 the space above the liquid level 1 1 a. Therefore, even if the storage level of the liquid tank 1 1 fluctuates | The device 16 controls the pressure 1 acting on the space above the liquid surface, thereby irrespective of the liquid surface of the tank 11 up and down. A certain absorption liquid 5 can be supplied. In addition, the recovery tube 61 of the absorption liquid 5 separated by the mist eliminator 6 provided on the upper part of the absorption tower 2 has a structure inserted under the liquid surface of the pressure tank 11. Result > A pressure-carrying tank 11 1—absorbing liquid supply pipe 1 4—nozzle 4—exhaust gas 1 and other gas-liquid contact, and a current carrying step for absorbing the target component—the mist eliminator 6 is separated and returned to the recovery pipe—pressurizing The circulation system of tank 11 (hereinafter referred to as the main circulation system). 0 In the above embodiment, when the exhaust gas flow rate is 8m / S or more, the jet 5a of the absorption liquid 5 ejected from the nozzle 4 is lifted to exhaust gas 1 Up to the atomizer 6, the absorption liquid 5 can be circulated by the above-mentioned main circulation system, that is, the pressure tank 1 1 is used to control the pressure of the space 1 1 a above the liquid surface of the pressure tank 11 to obtain the pressure tank 1 1 The pressure 5 of the absorption liquid 5 sprayed by the nozzle 4 through the absorption liquid supply pipe 14 through the nozzle 4 is controlled to form a predetermined velocity of the spray flow, and is brought into contact with the rising gas-liquid of the exhaust gas rising to the absorption tower 2. The process absorbs the target components of the exhaust gas 1 and reaches the mist eliminator 6. The absorption liquid that has reached the carrier current is separated by the mist eliminator 6 and returned to the pressure tank 11 through the recovery pipe. Second, when the absorption tower 2 rises or is closed, the exhaust gas flow rate becomes below the above loading speed as shown in FIG. 13. Therefore ----- V ------ ^-(Please read the note on the back first to write this page) Alignment The paper size is applicable to the Chinese standard (CNS) A4 specifications (210X297 mm). 44 · 438619 A7 B7 V. Description of the invention &) (Please read the “Notes on the back side / 丨 pain on this page”) Jet 5a and the exhaust liquid 5 that failed to rise to the upper part of the absorption tower by the exhaust gas 1 Almost the entire amount is dropped to the lower liquid storage portion 5 6 (indicated by the symbol 5 b). -The control circuit 6 6 detects the exhaust gas flow velocity of the exhaust gas flow velocity detection sensor 6 5 provided in parallel with the smoke exhaust introduction part 3 and opens the electromagnetic opening and closing valve 6 7 until the exhaust gas flow rate reaches the above-mentioned loading flow rate * via liquid storage Section 5 6 —blow tank 6 0 —blow tank pump 6 0 a —a circuitous return channel of the pressure tank 11 to return the absorption liquid 5 stored in the liquid storage section 56 to the tank 11. That is, the absorption liquid 5 b dropped to the liquid storage part 56 is introduced into the blower tank 60 provided in the lower part, and the liquid storage part 56 can be accommodated in the blower tank 60 without special increase in the size of the liquid storage part 56. The liquid 5 can be returned to the successive pressure tank 11 by the tank blowing pump 60a. In addition, even when the storage liquid level of the tank 11 is fluctuated by the above-mentioned circuit, the control circuit 6 9 can use the pressure sensor 6 2 to detect the pressure on the inlet side of the absorption liquid supply pipe 1 4 and use the pressure regulator 1 6 The control causes the absorption and supply pressure of the nozzle 4 to form a certain direction, so that a certain amount of the absorption liquid 5 can be supplied regardless of the liquid level of the tank 11. Printed by the Consumers' Cooperative of the Central Government Bureau of the Ministry of Economic Affairs. Therefore, in this embodiment, the upper space of the liquid surface of the pressure tank 11 can be pressurized to a predetermined pressure by using the compressor 17 a. Therefore, it is not necessary to set the spray absorption from the nozzle 4. Liquid 5 circulation pump. However, the front end of the recovery pipe 61 is inserted into the pressure tank 11 to prevent leakage of air. Therefore, according to this embodiment, even when the exhaust gas speed decreases due to the load fluctuation on the burner side, it can be passed through. The liquid storage tank at the bottom of the absorption tower and the second liquid storage tank use the absorption liquid return channel connected to the pressure tank, the most -45- This paper size applies to China National Standard (CNS) A4 (210X297 mm) Central of the Ministry of Economy Printed by the Bureau of Standardization and Consumer Engineering Cooperative 438619 A7 B7 V. Invention description Magic) Fortunately, the effective use of the maintenance circulation system can make the absorption liquid continuously circulate, and the maintenance circulation system can use the existing blow trough and blow trough pump | For the related equipment, it is not necessary to increase the size or increase the driving force, and it can bear the low cost and low equipment cost. In addition, according to this embodiment, the control of the jet pressure of the absorption liquid can be obtained by the pressure of the pressure tank. The pressure is controlled arbitrarily, so not only does the pump need not be pressurized, but a certain amount of absorption liquid can be supplied regardless of the liquid surface of the pressure tank. In addition, when the absorption tower 2 rises or is closed, as shown in FIG. 13, the exhaust gas flow rate will be less than the above-mentioned load speed, so the jet 5 a of the absorption liquid 5 ejected from the nozzle 4 is not lifted by the exhaust gas 1 to the upper part of the absorption tower. Almost the entire amount of the discharged absorption liquid 5 drops to the lower liquid storage portion 56 (indicated by symbol 5b). In order to solve the above-mentioned shortcomings, when the absorption tower is raised and closed, the exhaust gas from a burner or a boiler is not allowed to pass through the absorption tower. The flow velocity forms the exhaust gas bypass system existing when the absorption liquid is raised above the reference level above the loading flow velocity. In addition, as shown in FIG. 17, the above-mentioned exhaust gas bypass system connects the exhaust gas source such as a boiler or a burner with a large amount of exhaust gas such as a chimney to the main channel 74, and the exhaust gas of the boiler or the like is separated by 1 liter. A booster fan 7 1 capable of increasing speed and the above-mentioned wet absorption tower 2 are provided, and a bypass passage connecting the inlet side of the booster fan 7 1 and the exit side of the absorption tower 2 is provided, and a bypass plate 7 3 is connected to the chimney. 72, when the absorption tower 2 rises and closes * the booster fan 7 1 can be stopped, and the baffle plate 73 can be opened and the baffle plates 77 and 78 can be closed. * The paper size of the burner or boiler is in accordance with the Chinese national standard ( CNS) A4 size (210X297mm) _ aq _ n Binding line {Please read the notes on the back ^ This page) Central Samples Bureau of the Ministry of Economic Affairs, Shellfish Consumer Cooperative, India, Pei 4386 1 9 at B7 V. Invention Description W) After the discharged exhaust gas 1 is discharged to the chimney side through the bypass channel 71 bypassing the absorption tower 2 instead of passing through the absorption tower 2, when the exhaust gas flow rate is formed to increase the absorption liquid 5 above the reference flow rate • While driving the boost fan 71, The baffle 73 is closed, the baffles 77, 7 8 are opened, and the bypass passage 7 2 is closed, so that the exhaust gas 1 passes from the boiler side through the main passage 7 4 indicated by the arrow * via the booster fan 7 1 and passes through the desorption used by the absorption tower 2 Sulfur treatment is discharged from the chimney side. However, in the above-mentioned conventional technology, when the absorption tower is raised and closed, the exhaust gas does not pass through the absorption tower, and therefore there is a problem that the sulfur dioxide gas or dust contained in the exhaust gas cannot be removed without performing exhaust gas treatment. Also, when the light oil with low emissions such as S02 and coal dust is burned without avoiding the above problems, problems such as high fuel costs may occur. Fig. 14 shows a fifth embodiment in which the conventional bypass passage 72 is effectively used, and the same effect as in the fourth embodiment can be improved. An exhaust source such as a boiler or a burner and an exhaust gas such as a chimney are connected. The main channel 7 4 of the atmospheric emission part utilizes the flow velocity of the exhaust gas to make contact with the gas-liquid contact with both of the absorption liquid 5 by using a gas-liquid separation system. Treatment system (A) shows the closed state of each baffle before the rise of the absorption tower and the flow of the exhaust gas, and (B) shows the baffle when the flow velocity of the exhaust gas introduced from the pan into the absorption tower is above the loading flow rate Switch status and flow diagram of exhaust gas. As shown in Figure 14 | In the main channel 7 4 connecting the exhaust gas exhaust source such as a boiler or a burner to the exhaust part of the atmosphere such as a chimney, the exhaust gas i can be boosted by the boiler to increase the interval. The booster fan 71 and the above-mentioned wet absorption tower 2 are connected to the booster fan 7 1 at the entrance side and the exit side 1 of the absorption tower 2 at the same time. (Please read the precautions on the back first to write this page) This paper is applicable to China Standard (CNS) A4 specification (210X297 mm) -47- Duan Yin, Offset and Consumer Cooperation of Central Bureau of Standards, Ministry of Economic Affairs «.  4386 19 A7 A / _B7_ V. Description of the invention (15) Bypass channel 7 3 of the baffle plate 7 3 connected to the chimney »In the above embodiment, when raising the exhaust gas before the absorption tower 2 is introduced, such as The baffle 73 is opened as shown in FIG. 14 (A), and a bypass passage 72 and a main passage 74 are formed to form an ascending house circulation passage * so that the exhaust gas 1 of the boiler is not discharged to the discharge passage 76, but the gas flow velocity in the circulation passage The pressure increase by the booster pump 7 1 is continued until the internal flow velocity of the absorption tower 2 becomes equal to or higher than the loading flow velocity. When the flow velocity in the tower is maintained to be equal to or higher than the loaded flow velocity, the baffle plate 7 3 of the bypass passage 72 is closed as shown in No. 14 (B), and the absorption process of the exhaust gas 1 is performed. The change in the amount of exhaust gas discharged with respect to the operation time of the boiler as shown in Fig. 13 illustrates the use of the above-mentioned booster circulation path as follows. That is, as shown in FIG. 13, the rise time after the start of the operation and the decrease before the completion of the operation T2 will reduce the amount of exhaust gas. In order to make the liquid velocity of the tower ’s flow velocity in the absorption tower 2 that processes the exhaust gas 1 (loading) Speed) V, below, as shown in Figure 14 (A), switch the baffle plate 73 to control the flow rate in the tower to reach the loading flow rate or higher. • When the flow rate in the tower reaches the loading flow rate, see Figure 14 (B). It is shown that a person who performs the opening and closing control of the baffle 7 3 to make the operation of the absorption tower 2 fully function. Fig. 15 is a second embodiment in which a partition plate for limiting the width of the exhaust gas passage is provided in the absorption tower 2. A partition plate 40 extending in the vertical direction is provided on the air-liquid contact area space 41 to constitute the partition plate 4 0 The variable gas-liquid contact zone airspace 4 moving in the horizontal direction 4 1 The exhaust gas passing area * FIG. 16 is a third embodiment of the first figure corresponding to the partition plate provided in the absorption tower 2 to limit the width of the exhaust gas passage. The air-liquid contact area airspace 41 is stepped --------- ^ ------ tr. ------- ^ {Please read the note on the back page first) This paper size uses the Chinese Standard for Household Standards (CMS) Α4 (210X297 mm) -48- Shellfish Consumption of the Central Bureau of the Ministry of Economic Affairs Cooperative printed 4386 1 9 at __B7_ V. Description of the invention & 6) A plurality of partition plates 40 with different height positions at the lower end in the vertical direction are arranged, and a variable exhaust gas passage area is formed by controlling the lower liquid level . In addition, when the internal flow velocity of the exhaust gas 1 introduced into the absorption tower 2 is below the loading flow velocity, the exhaust gas passage area in the absorption tower 2 is reduced by using the partition plate 40, and the bypass channel 7 2 is opened by the baffle plate 7 3 to allow the treatment. The exhaust gas is returned to the inlet side of the absorption tower 2 via the booster pump 7 1, thereby rapidly increasing the flow velocity in the tower of the exhaust gas 1 introduced into the absorption tower 2. Therefore, according to this embodiment, the flow velocity in the tower can be constantly maintained above the loading flow rate, so the performance of the absorption tower can be completely maintained when the equipment is raised and lowered. At the same time, it is not necessary to increase the liquid storage part and the recovery pump in the lower part of the absorption tower. capacity. 18 and 19 are views showing a front view and a side view of a wet-type exhaust gas treatment apparatus according to a sixth embodiment of the present invention, and descriptions of the same configuration as the above embodiment are omitted in the same figure. The middle portion in the height direction of the absorption tower 2 is provided with an arbitrary number of header pipes 1 90 provided with upward nozzles 4. Between the main pipe 190 and the above-mentioned liquid storage section 56, an absorption liquid supply pipe 14 having a circulation recovery pump 21 interposed therebetween is connected in communication, so that the absorption liquid 5 is dispersed in the absorption tower 2, The purpose component for absorbing and removing sulfur dioxide gas, dust, etc. is the same as that described above. A mist eliminator 6 is provided at a position below the smoke exhaust outlet 8 in the upper part of the absorption tower 2. The best example of the mist eliminator 6 installed here is, for example, those shown in FIG. 20. The defogger 6 is formed by a plurality of plates 6 a having a mountain-shaped (flat V-shaped) cross section at intervals, and the plates 6 are superimposed and fixed by a fixing rod 9 2, and the whole is a row of plates Column 6a with its lower position facing right and left I — I m I n I ^ (Read the notes on the back of the poem first and hold the page down) This paper size applies to the Chinese Standard for Households (CNS) A4 ( 210X297 mm) • 49 · A7 B7 438619 V. Description of the invention ο) [---. — ： --- ^ — (Please read the notes on the back first, then. vr page) Cross each other and be installed on the absorption tower 2 β by converging with other plate rows 6 b. However, the shape and arrangement type of the mist eliminator 6 is not limited to the example of No. 20 囵, but to reduce it as described later. Undertake the mist eliminator. The number of receiving containers 8 0A of the absorption liquid 5 flowing down from 6 can also make adjacent pairs of plate rows 6 a and 6 b alternately tilt and condense at the lower end side positions, and can also cross the plate rows 6 a The receiving container 80A is arranged in the direction of 6b, but in order for the spray of the absorption liquid 5 of the carrier gas 1 to be effectively captured by the mist eliminator 6, it must be able to conduct the gap of the carrier current. Next, the configuration of essential parts according to the present invention will be described below. The lower part of the above-mentioned mist eliminator 6 is provided with any number of receiving containers 80A which can receive the water collecting pipe (see FIG. 20) such as the absorption liquid 5 flowing down by the mist eliminator 6. In this embodiment, the number of three receiving containers 80A is set. However, the arrangement state of the mist eliminators 6 and the number of the evacuators 6 may be set as appropriate. In addition, each receiving container 80A is connected to the upper end of the return liquid pipe 8A, and the return liquid pipe 8A has a vertical pipe line extending a predetermined length downward.  Printed by the Central Sample Rate Bureau Shellfish Consumer Cooperative of the Ministry of Economic Affairs 9 0 | The vertical pipe section 90 can be used to make the return absorption liquid 5 c have potential energy (gravitational energy), and extend to the scattered absorption liquid storage area in Figure 5 Lower position | A nozzle-shaped opening 8 2A is provided at the lower end. Furthermore, the length of the vertical pipe 90 of the return liquid pipe 8 1 A may vary depending on the height of the liquid ejected from the upward nozzle 4, but it may be set to a height equal to or more than the mist eliminator 6, for example. The specific structure of the above-mentioned container 80 and the return liquid pipe 81A will be described in detail with reference to FIG. 19 as follows. The closing container 80A, which is located at the lower end of the pair of plate rows 6a and 6b, crosses the closing position of the lower end of most of the mist eliminators, and this paper scale is used by Chinese impoverished households (CNS) A4 this grid ( (210X297 mm) • 50 cracks printed by the Shell Specimen Consumer Cooperative of the Central Procurement Bureau of the Ministry of Economic Affairs 4 3 8 6 19 A7 _B7_ V. Description of the invention).  The horizontal extension is arranged in the tower 2 and at the same time, the bottom surface of the receiving container 8 O A is only slightly inclined downwards. The return liquid 5 c can be set to flow in one direction. In addition, the upper end of the return liquid pipe 8 1 A is connected to the side wall of the absorption tower 2 at the inclined downstream end position of the receiving container 8 0 A, and can communicate with the inclined downstream end of the receiving container 80 A. In addition, the return liquid pipe 8 1A is formed into a "3" shape, and the vertical pipe portion 90 is drooped along the outer side wall of the tower toward the same height as the mist eliminator 6, and then penetrates the tower horizontally again | and horizontally A plurality of nozzle-shaped openings 8 2A are provided on the lower side of the horizontal pipe section 91 that penetrates into the tower at a predetermined axial distance. More specifically, it is located above the nozzle 4 and approximately vertically above the liquid column. Nozzle-shaped openings 8 2A are respectively provided at the positions below the openings of the scattered absorption liquid storage area directly below the mist eliminator 6. The nozzle-shaped openings 8 2A eject the return liquid 5 c by using the (gravity) vertical pipeline portion 9 A level of zero flow can make it continue to spray and collide with the ejected liquid column to form droplets, which can more effectively form gas-liquid contact. In this embodiment, the direction of the piping 8 1 A is set directly under the mist eliminator 6 (inlet portion) of the absorbing liquid storage area that avoids the position above the top of the liquid column of the absorbing liquid 5 sprayed from the upward nozzle 4 and easily scatters the absorbing liquid storage area. The lower length is located below it. Also, as shown in FIG. 19, the return liquid piping 8 1A may pass a part of it through the outside of the absorption tower 2 or it may be provided to allow all of the vertical pipe portion 90 to pass through the absorption. Inside tower 2. Next, another embodiment of the present invention shown in 21st (1) will be described. In this example, only the structure different from the embodiment shown in Figure 19 above (please read the note on the back, first page ¾) This paper size applies to Chinese national standards (CNS > A4 specifications ( 21〇χπ7mm) -51-Printed by Shellfish Consumer Cooperative of Central Bureau of Standards of the Ministry of Economic Affairs 438619 A7 _____B7__ 5. Description of the invention. In Fig. 21, the components or positions indicated by the same symbols as those in Figs. 18 to 20 are equivalent components or positions. Therefore, the description is omitted to avoid repetition. The second embodiment is the same as that in FIG. 18, and the receiving containers 8 OB are set at the lower end of the pair of mist eliminators 6, respectively. However, the respective receiving containers 8 0 B are assembled with each other. After the tube 80 is assembled into one, the collection tube 80 is connected to the upper end of the drooping return liquid pipe 8 1 B. In addition, the return liquid pipe 8 1 B hangs the inside of the tower 2 downward, and sets the lower end opening 8 2 B in the liquid storage portion 5 6. The opening 8 2 B is different from the above embodiment and does not have a nozzle. It just forms an opening. Therefore, this embodiment is different from the related devices of the embodiments in FIG. 18 and FIG. 19, and instead of spraying the return liquid concentrated in the container 80B toward the upper position of the liquid columnar jet, it takes The structure of the return to the liquid storage section 56 is as follows. The operation of the embodiment in which the above-mentioned FIG. 18 to FIG. 21 are combined is described below. In the apparatus of each embodiment, the flow rate of the exhaust gas 1 passing upward through the absorption tower 2 is set to 5. At a height of 5 m / s or higher, as the droplets of the exhaust gas 1 adhere to the mist eliminator 6, a large amount of the absorption liquid 5 flows out from the lower portion. The absorption liquid 5 does not fall directly into the tower from the mist eliminator 6 | Instead, it is directly captured by the collection containers 80A, 80B | The return liquid 5c captured by the collection containers 80A, 80B flows to the return by gravity In the liquid pipes 81A and 81B, in the embodiment shown in Figs. 18 and 19, the nozzle liquid is used instead of directly below the demister 6 but at a position below the vertical amount of the return liquid pipe 81A. Opening -----. ----- ^ ------ 1T ------ ^ (Please read the note on the back " " this page first) This paper size is applicable to China National Standard (CNS) A4 specification (210X297 (Mm) -52- Cooperated with Bei Gongxiao, Central Bureau of Standards, Ministry of Economic Affairs, Du printed 43 86 1 9 A7 A7 _B7____ V. Description of the invention fco) 8 2 A gravity energy is ejected to the upward nozzle in the absorption tower 2 4 on the ejection liquid column (absorption liquid) 1 and the return liquid 5 c ejected from the nozzle-shaped opening 8 2A and the ejection liquid column conflict to form a droplet ,. Gas-liquid contact can be constituted more effectively. On the other hand, in Fig. 21, the return liquid 5 c collected in the receiving container 8 OB is returned to the liquid storage portion 5 6. It is again ejected upward through the main pipe 190 and the ejection nozzle 4. Therefore, in any of the above In the implementation form. It will not increase the amount of liquid droplets near the defogger 6 which is easy to form a scattered liquid storage area, and can prevent the re-scattering of the absorption liquid 5 caused by the exhaust gas 1 of the part. The second circle is expressed as The logarithmic circular table of the relationship between the gas flow rate in the tower and the spray concentration at the outlet of the mist eliminator is compared with those for excluding the absorption liquid (the device of the present invention) and those who do not exclude the absorption liquid (the conventional device). For example, the liquid column height is 1. In the 7m conventional device 0, the gas velocity in the tower exceeds 5. At 5m, the spray outlet concentration rises sharply, but the liquid column height is 1. 8m invention device ♦, even if it exceeds 5. 8m does not increase the spray outlet concentration. Also, for example, the height of the liquid column is 3. The conventional device of 4m △ and the height of the liquid column are 3. 3m 的 发明 装置 ▲, the device side of the present invention is 5. Compared with the conventional device, the spray outlet concentration at 8m was found to be greatly reduced to less than 1/5. Therefore, according to this figure, it can be known that the device of the present invention has a gas flow rate of about 5. In the area of 5m / s or more, it has excellent spray discharge resistance against the outside of the tower. The device of the invention of this test uses the embodiment of FIG. 21. Other conditions are as follows: (and the height of the liquid column in the figure is a columnar spray that forms an absorption liquid. {Please read the precautions on the back before starting (Write this page) This paper size is applicable to China National Standard (CNS) A4 (210X297 mm) -53- Printed by the Central Industry Standards Bureau, Ministry of Economic Affairs, 5 Industrial Consumer Cooperative, 1 43 86 19 A7 _. _B7 V. Description of the invention h) Jet height. ) The mist eliminator used: the curved plate type uses a 45-degree tilt distance between the mist eliminator and the upward nozzle :. 8m Fig. 23 is a graph showing the relationship between the gas flow rate in the tower and the spray scattering rate at the inlet of the mist eliminator. The spray scattering rate at the inlet of the mist eliminator of the device of the present invention X 1 0 0) its liquid column height is 2. The conventional device of 4 m and the height of the liquid column are 1. In the 9 m invented device, no major changes were seen, they all showed a low rate, but the liquid column height was 2. The conventional device of 8m △ and the height of the liquid column are 3. In the 3m invention device ▲, it is known that the conventional device will increase significantly compared to the low rate of the spray scattering rate of the invention. As a result, the height of the liquid column was increased to 3. About 3m, the gas velocity is 5. In the high-speed area of about 5 m / s, it can be known that the spray scattering rate still shows a sufficiently low rate. The test using device is the same as the embodiment in FIG. 21. The other conditions are as follows. (Also, the height of the liquid column in the figure is the quotient of the columnar jet flow forming the absorption liquid.) The used mist eliminator: The curved plate type uses a 45-degree inclined mist eliminator and the distance between the upward nozzle: 8m. Therefore, according to In this embodiment, even if the flow velocity of the exhaust gas in the absorption tower is increased at a high speed, a very small amount of the absorption liquid spray discharged from the absorption tower with the exhaust gas after the scrubbing treatment remains, so as the exhaust gas passing through the tower is accelerated, It can improve the operation efficiency of the exhaust gas treatment, which is extremely beneficial. According to the embodiment shown in Figs. 18 and 19, the absorption liquid system and the upward nozzle sprayed from the return liquid pipe back to the absorption part near the upper side of the jet stream are sprayed ( (Please read the notes on the back first to write this page) < CNS > A4 size (210X297 mm) -54-4386 19 a7 B7 5. The jet stream of the absorption liquid of the invention also reabsorbs the exhaust gas at the same time, so in addition to the above effects, it can maintain High level of exhaust gas treatment performance. According to the embodiment shown in FIG. 21, even if the amount of the absorbing liquid reaching the mist eliminator is greatly increased, it can be smoothly returned to the liquid storage section and can be reused. "Ind order * IH line (Please read the precautions on the back and this page first. ¾ This page) The printed paper size of the Central Consumers ’Cooperative of the Ministry of Economic Affairs of the People ’s Republic of China is applicable to China National Standard (CNS) A4 (210X297) -55-

Claims (1)

438619 A8 B8 D8 經濟部中央揉率局βς工消費合作社印製 六、申請專利範圍 1 .一種濕式氣體處理裝置，係將儲存在吸收液儲存部的吸 收液從吸收塔內的噴嘴等吸收液流出部朝著預定方向噴流，使 該噴流與通氣於上述吸收塔內的廢氣氣液接觸，而吸收/除去 廢氣中的目的成份，其特徵爲： 藉產生加壓氣體之加壓槽將上述吸收液儲存部形成在儲存 液面上方空間，利用該加壓氣體的壓力，構成可從吸收塔內的 噴嘴部噴出儲存在上述加壓槽內的吸收液。 2. 如申請專利範圍第I項之濕式氣體處理裝置•其中當吸 收/除去的上述吸收液中之一目的成份爲二氧化硫（S 〇2)時 •上述加壓氣體爲含氧氣體|將此含氧氣體噴入加壓槽內底部 之儲存液。 3. —種濕式氣體處理裝置，係將上述儲存於吸收液儲存部 之吸收液從吸收塔內的噴嘴部朝上方噴流，使該噴流與通氣於 上述吸收塔內的廢氣氣液接觸而吸收/除去廢氣中的目的成分 中·*其特徵爲： 以產生加壓空氣之加壓槽將上述吸收液儲存部形成於儲存 液面上方空間，另一方面將可回收吸收上述目的成份之吸收液 的回收部配置在高於上述加壓槽內儲存液面高之吸收塔內的預 定位置，或使上述回收部吸收液回流至加壓側之連通管的出口 端開口而定位在上述加壓槽內的儲存液內者。 4. 一種濕式氣體處理裝置，係將儲存於吸收液儲存槽之吸 收液導入吸收塔內，使該吸收液隨著沿上述吸收塔內的廢氣通 道而通氣之廢氣流速與該廢氣流氣液接觸，吸收/除去上述排 氣中的目的成份中，其特徵爲： ---------裝-- (請先閲讀背面之注意事項！4 ;耗本頁) 訂- 線 本紙張尺度逋用中Β两家橾率（CNS ) Α4规格{ 210Χ297公釐） -56- ^38619 經濟部中央揉车局βί工消費合作社印製 A8 B8 C8 D8六、申請專利範圍 . 於大致橫斷上述排氣通路內的方向並設之複數吸收液管上 ’使該吸收液與上述排氣通氣方向交叉的方向，更具體而言朝 著大致橫向方向形成呈溢流或噴出流之吸收液流出部.使該流 出部流出之吸收液與上述排氣流的交叉接觸而加以微粒化進行 氣液接觸。 5. 如申請專利範圍第4項之濕式氣體處理裝置，其中沿著 大致橫斷上述排氣通路內之一或複數面內列設一段或複數段（ 包含上下鋸齒狀配置）上述吸收液管群，構成可於該列設之管 群的鄰接管互相間之空隙部導通上述廢氣流者。 6. 如申請專利範圍第.4項或第5項之濕式氣體處理裝置-其中以上部開放式導水管狀構件構成上述吸收液管的同時，也 可以在該導水管狀構件上設置朝著與通氣方向交叉之大致水平 方向的溢流形成手段。 7. 如申請專利範圍第4項之濕式氣體處理裝置，其中以上 部封閉式管狀構件構成上述吸收液管的同時，也可以在與導通 該吸收液管之上述廢氣流的空隙部相對之周圍面上，沿著管軸 線方向設置縫隙狀開口或多數小孔列之構成。 8. 如申請專利範圍第4項之濕式氣體處理裝置，其中對上 述吸收液管之吸收液供應也可以構成利用重力之上述吸收液供 應源，具體而言以稍具高低差將吸收液供應源配置在吸收液管 上方者。 9. 一種濕式氣體處理方法，係將使儲存在吸收液儲存部的 吸收液從吸收塔內的噴嘴部朝著預定方向噴流，使該噴流與上 述吸收塔內通氣之排氣氣液接觸1而吸收/除去排氣中的目的 (請先《讀背面之注意事項五>%本頁) -裝- 訂 本紙張尺度埴用中國國家揉车（CNS ) A4洗格（210X297公釐） -57- 經濟部中央橾隼局貝工消費合作社印製 4386 19 if C8 _ DS六、申請專利範圍 成份中，其特徵爲： 使上述吸收塔內通氣之廢氣通路對應上述排出量進行寬度 領域控制•可進行上述廢氣通路之氣體通路領域的調節》 1 0 .如申請專利範圍第9項之濕式氣體處理方法|其中 係停止來自上述氣體流入所阻止區域的噴嘴部之吸收液的噴流 0 1 1 . 一種濕式氣體處理裝置，係將上述吸收塔內通氣之 廢氣通路，以沿著廢氣流動方向延伸設置至噴嘴噴流領域之分 割板分割成複數個氣體流域，設置可對應上述廢氣量進行上述 所分割之氣體流域的氣體流入之流量控制或開關控制的通路控 制手段。 1 2 . —種濕式氣'體處理裝置•係於吸收塔下部配置吸收 液儲存部|將噴嘴部定位於其上方吸收塔內，顯示在該噴嘴部 上方特定噴流吸收液所成，其特徵爲：使沿著排氣流動方向延 伸垂直設置至噴嘴噴流頜域爲止之至少一分割板的下端延伸設 置於吸收液儲存部爲止，藉該儲存部內吸收液之液位位準的調 節，可選擇性地使分割板下端沒入吸收液內，而構成可選擇性 地開關該分割板所分割之氣體通路。 1 3 . —種濕式氣體處理裝置，係於吸收塔下部設置吸收 液儲存部，將噴嘴部定位在其上方吸收塔內而從該噴嘴部朝上 方噴射吸收液所成的裝置中•其特徵爲： 在吸收液儲存部側構成可自由升降之沿著廢氣流動方向垂 直延伸設置至噴嘴噴流頜域的至少一分割板下端側，選擇性地 使該分割板下端下降而沒入吸收液內，構成可選擇性地開關該 ---------^------ ------.^ (請先«讀背面之注意事項具._.私本頁) 本紙浪尺度逍用中國國家揉準（CNS ) Α4规格（210X297公釐） • 58- 4386 1 9 A8 經濟部中央標隼局負工消費合作社印*. ___ D8六、申請專利範圍 分割板所分割之氣體流域的通道者》 1 4 .如申請專利範圍第1 1項之濕式氣體處理裝置，其 中係沿著廢氣流動方向構成可自由擺動地延伸設置至噴嘴流域 爲止之至少1分割板的下端側，藉著該下端部的擺動轉向，構 成可進行以分割板分割之氣體流域的的氣體流入流量控制或開 關控制。 15.如申請專利範圍第11項之濕式氣體處理裝置•其 中係構成使上述分割板下端可朝著導入吸收塔內之廢氣導入部 側轉向者，從上述導入部導入吸收塔內的廢氣是沿著上述轉向 部整流並引導至噴嘴噴流方向。 1 6 .如申請專利範圍第1 1項之濕式氣體處理裝置，其 中係構成可相對於廢氣流動方向大致朝著垂直方向移動之上述 分割板•藉著該分割板的移動構成可調節分割氣體流域之通道 剖面積者。 1 7 . —種濕式氣體處理方法I係利用從吸收塔下部朝頂 部通氣的廢氣而隨著吸收液的氣液接觸·使上述廢氣中的目的 成份吸收於吸收液所成之方法中，其特徵爲： 上述廢氣的流速在預定流速以下時，使落下至設於上述吸 收塔底部之吸收塔底部液體儲存槽的吸收液經由第2液體儲存 槽，回流於供應吸收液至吸收塔內的吸收液儲存槽內。 1 8 . —種濕式氣體處理裝匱1係藉由吸收塔下部朝著頂 部通氣的廢氣而隨吸收液予以氣液接觸，藉此構成可將上述廢 氣中之目的成份吸收於吸收液內之裝置中，其特徵爲： 具備吸收塔底部液體儲存槽；接受來自該吸收塔底部液體 本紙張尺度遄用中困國家揉準（CNS ) A4規格（210X297公釐） -59- 438619 經濟部央揉车局月工消费合作社印*. 六、申請專利範圍 儲存槽的第2液體儲存槽；供應吸收液於吸收塔內之吸收液儲 存槽：經由上述吸收塔底部液體儲存槽及第2液體儲存槽而與 吸收液儲存槽連結之吸收液回流通道；及，上述廢氣的流速在 預定速度以下時，使上述吸收塔底部液體儲存槽的吸收液經由 上述第2液體儲存槽而回流至吸收液儲存槽之控制手段。 1 9 .如申請專利範圍第1 8項之濕式氣體處理裝置，其 中具備使吸收液儲存槽內部加壓之加壓手段，及控制使上述加 壓手段朝著對吸收塔之吸收液供應壓力形成一定方向的控制手 段。 2 0 . —種濕式氣體處理方法，係於連接鍋爐或燃燒機等 燃燒廢氣排出源與煙囪等之該廢氣大氣放出部的主通道上，利 用廢氣的流速而在廢氣中隨著吸收液之兩者的氣液接觸，藉吸 收廢氣中目的成份之吸收液的濕式吸收塔所成的廢氣處理方法 中，其特徵爲： 上述廢氣之吸收塔內的流速在預定速度以下時|從上述吸 收塔所排出之處理後的廢氣是利用旁通通道而回流至吸收塔入 口側· 2 1 . —種濕式氣體處理裝置，係於連接鍋爐等燃燒廢氣 排出源與煙囪等該廢氣之大氣放出部的主通道上，利用廢氣的 流速而在廢氣中隨著吸收液之兩者的氣液接觸|藉吸收廢氣中 目的成份之吸收液的濕式吸收塔所成的廢氣處理裝置中，其特 徵爲： 具備使上述吸收塔所排出之處理後的廢氣回流至吸收塔入 口側之#通通道： ---------^-- (诛先Η讀背面之注意事項声舄本頁) 訂 線 本纸張尺度適用中國a家揉準（CNS > A4規格（2丨0X297公釐） 經濟部中央標窣局貝工消费合作社印製 4:8619 b! C8 _____ D8六、申請專利範圍 上述廢氣的吸收塔內流速在預定速度以下時，開放上述旁 通通道控制使處理後廢氣回流至吸收塔入口側之控制手段。 22·如申請專利範圍第2 1項之濕式氣體處理裝置，其中係設 置於上述吸收塔內，當上述廢氣的流速在預定速度以下時，使 上述吸收塔內的廢氣形成可變之通過面積可變手段；及•使處 理後的廢氣回流至吸收塔入口側之旁通通道。 2 3 .—種濕式氣體處理裝置，係於吸收塔內使儲存在吸 收塔之儲存槽的吸收液從噴射噴嘴噴出*同時使其噴射流與廢 氣於吸收塔內自下方朝著上方運轉流動而氣液接觸*吸收除去 廢氣中的目的成分，同時以設於吸收塔上部之消霧器捕捉隨廢 氣而產生霧狀吸收液之濕式廢氣處理裝置中，其特徵爲： •在上述消霧器下部設置接受從該消霧器流下之吸收液的收 容器，其收容器上連通朝下方延伸設置預定長度之回流液配管 的上端部*同時在該配管下端部設置可以吸收塔內的預定位置 放出上述回流液之開口。 2 4 .如申請專利範圍第2 3項之濕式氣體處理裝置 > 其 中上述噴射噴嘴係以向上者，在較此向上噴嘴所噴射之液柱髙 度的上方位置上，使上述回流液配管之下端開口定位者· 2 5 .如申請專利範圍第2 4項之濕式氣體處理裝置，其 中係將上述回流液配管的下端開口形成噴嘴狀》 2 6 .如申請專利範圍第2 3項之濕式氣體處理裝置*其 中係構成可將上述回流液配管的下端開口定位在液體儲存部內 者。 I I I I — II 訂 I I 線 (請先閱讀背面之注意事項尹‘寫各頁) 本紙張尺度適用中《困家梯準（CNS ) A4規格（210X297公釐） -61 -438619 A8 B8 D8 Printed by the Central Kneading Bureau of the Ministry of Economic Affairs, βς Industrial Cooperative Cooperative 6. Application for Patent Scope 1. A wet gas processing device, which absorbs liquid stored in the absorption liquid storage section from nozzles in the absorption tower, etc. The outflow part sprays a stream in a predetermined direction, and makes the jet contact the exhaust gas gas-liquid ventilated in the absorption tower to absorb / remove the target component in the exhaust gas, which is characterized in that the absorption is performed by a pressurized tank that generates pressurized gas. The liquid storage portion is formed in a space above the liquid storage surface, and the pressure of the pressurized gas is used to form an absorption liquid stored in the pressure tank from a nozzle portion in the absorption tower. 2. For example, a wet gas treatment device in the scope of application for a patent I. Where one of the above-mentioned absorption liquids to be absorbed / removed is sulfur dioxide (SO 2) • The above-mentioned pressurized gas is an oxygen-containing gas | The oxygen-containing gas is sprayed into the storage liquid at the bottom of the pressure tank. 3. A kind of wet gas treatment device, which sprays the absorption liquid stored in the absorption liquid storage part upward from the nozzle part in the absorption tower, and makes the spray flow contact with the exhaust gas gas-liquid ventilated in the absorption tower to absorb it. / Remove the target components in the exhaust gas. * It is characterized by: forming the above-mentioned absorption liquid storage section in a space above the storage liquid surface in a pressurized tank that generates pressurized air, and on the other hand, the absorption liquid that can absorb the above-mentioned target components is recovered. The recovery part is disposed in a predetermined position in the absorption tower higher than the storage liquid level in the pressure tank, or the return end absorption liquid is returned to the outlet end of the communication pipe on the pressure side to be positioned in the pressure tank. Inside the storage solution. 4. A wet-type gas treatment device, which introduces the absorption liquid stored in the absorption liquid storage tank into the absorption tower, and makes the absorption liquid flow with the exhaust gas flowing along the exhaust gas passage in the absorption tower to contact the exhaust gas and liquid To absorb / remove the target components in the above exhaust gas, its characteristics are: --------- install-(please read the precautions on the back first! 4; consume this page) order-thread paper size The use of two Chinese B rate (CNS) A4 specifications {210 × 297 mm) -56- ^ 38619 Printed by the central government bureau of the Ministry of Economic Affairs β 工 consumer cooperatives A8 B8 C8 D8 6. The scope of patent application. A plurality of absorption liquid pipes arranged in parallel in the direction of the exhaust passage 'a direction in which the absorption liquid intersects the above-mentioned exhaust ventilation direction, and more specifically, an absorption liquid outflow portion that overflows or spouts is formed in a substantially lateral direction. The absorption liquid flowing out of the outflow portion is brought into contact with the above-mentioned exhaust gas flow to make it micronized for gas-liquid contact. 5. If the wet gas treatment device of item 4 of the scope of patent application, one or more sections (including the upper and lower zigzag arrangement) of the above-mentioned absorption liquid pipe are arranged along one or more planes which substantially cross the above-mentioned exhaust passage. The group constitutes a person capable of conducting the above-mentioned exhaust gas flow in a gap portion between adjacent tubes constituting the tube group arranged in the row. 6. If the wet gas treatment device in the scope of patent application Nos. 4 or 5-in which the upper open water-conducting tubular member constitutes the above-mentioned absorption liquid pipe, the water-conducting tubular member may also be provided with a vent and aeration. Means for forming an overflow in a substantially horizontal direction where the directions intersect. 7. For a wet gas processing device according to item 4 of the patent application, in which the upper closed tubular member constitutes the above-mentioned absorption liquid pipe, it may also be located around the space opposite to the gap portion of the above-mentioned exhaust gas flow that conducts the absorption liquid pipe. On the surface, a slit-like opening or a plurality of small hole rows are provided along the tube axis direction. 8. For the wet gas processing device in the scope of patent application No. 4, wherein the supply of the absorption liquid to the absorption liquid pipe can also constitute the above-mentioned absorption liquid supply source using gravity, specifically, the absorption liquid is supplied with a slight height difference. The source is arranged above the absorption tube. 9. A wet-type gas treatment method, in which an absorption liquid stored in an absorption liquid storage portion is sprayed in a predetermined direction from a nozzle portion in an absorption tower, and the jet is brought into contact with exhaust gas and liquid vented in the absorption tower 1 The purpose of absorbing / removing the exhaust gas (please read "Notes on the back side five>% of this page first)-binding-book size, using China National Kneading Car (CNS) A4 wash grid (210X297 mm)- 57- Printed by the Central Government Bureau of the Ministry of Economic Affairs, Shellfish Consumer Cooperative, 4386 19 if C8 _ DS 6. In the scope of the patent application, it is characterized by: the exhaust gas passage in the absorption tower is controlled in a wide area corresponding to the above-mentioned discharge amount. The above-mentioned exhaust gas passage can be adjusted in the gas passage field "1 0. The wet gas treatment method such as the scope of the patent application No. 9 | wherein the jet of the absorption liquid from the nozzle portion of the above-mentioned gas flowing into the blocked area is stopped 0 1 1 A wet-type gas treatment device, which divides the exhaust gas passage vented in the absorption tower into a plurality of gas streams by a dividing plate extending along the flow direction of the exhaust gas to the nozzle jet field Provided corresponding to the exhaust gas amount control means for passage of gas flowing into the divided flow of the gas control or basin off control. 1 2. — A kind of wet gas body treatment device • The absorption liquid storage unit is arranged at the lower part of the absorption tower. The nozzle unit is positioned in the absorption tower above it, and it displays the formation of a specific jet of absorption liquid above the nozzle unit. In order to make the lower end of at least one of the dividing plates extending vertically along the flow direction of the exhaust gas to the nozzle jet jaw area extended to the absorption liquid storage section, the liquid level of the absorption liquid in the storage section can be selected by adjusting The lower end of the dividing plate is immersed into the absorption liquid, and the gas path divided by the dividing plate is selectively opened and closed. 1 3. — A wet gas treatment device is a device formed by absorbing a liquid storage part under the absorption tower, positioning the nozzle part in the absorption tower above it, and spraying the absorption liquid upward from the nozzle part • Characteristics It is: at the side of the absorbing liquid storage part, a freely lifting and lowering side of at least one partition plate which is vertically extended along the flow direction of the exhaust gas to the nozzle jet jaw area is selectively formed, and the lower end of the partition plate is selectively lowered to be submerged into the absorbing liquid, The composition can be switched on and off selectively --------- ^ ------ ------. ^ (Please «read the precautions on the back ._. Private page] Standards are used in China National Standard (CNS) A4 (210X297 mm) • 58- 4386 1 9 A8 Printed by the Consumers ’Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs *. ___ D8 VI. Gas divided by the patent application division board Channelists in the watershed "1. For example, the wet gas treatment device of item 11 in the scope of patent application, wherein the lower end side of at least one dividing plate that is freely swingable and extends to the nozzle watershed is formed along the flow direction of the exhaust gas, By swinging the lower end portion, The gas inflow control or switch control of the gas flow area divided by the partition plate is performed. 15. If the wet gas treatment device according to item 11 of the scope of the patent application, which is constituted so that the lower end of the partition plate can be turned toward the side of the exhaust gas introduction part introduced into the absorption tower, the exhaust gas introduced into the absorption tower from the introduction part is It is rectified and guided to the nozzle flow direction along the said turning part. 16. The wet gas processing device according to item 11 of the scope of patent application, wherein the above-mentioned dividing plate is configured to be able to move substantially vertically with respect to the flow direction of the exhaust gas. The division of the gas can be adjusted by the movement of the dividing plate. The cross-sectional area of the watershed. 1 7. A wet gas treatment method I is a method in which the exhaust gas vented from the lower part of the absorption tower to the top is contacted with the gas-liquid of the absorption liquid. The target component in the above-mentioned exhaust gas is absorbed in the absorption liquid. It is characterized in that: when the flow rate of the exhaust gas is below a predetermined flow rate, the absorption liquid dropped to the liquid storage tank at the bottom of the absorption tower provided at the bottom of the absorption tower passes through the second liquid storage tank to flow back to the absorption that supplies the absorption liquid into the absorption tower Fluid storage tank. 1-8. A kind of wet gas treatment equipment 1 is to make gas-liquid contact with the absorption liquid through the exhaust gas vented from the lower part of the absorption tower toward the top, thereby constituting the purpose components in the exhaust gas that can be absorbed in the absorption liquid. The device is characterized by: equipped with a liquid storage tank at the bottom of the absorption tower; accepting liquid from the bottom of the absorption tower at the paper size standard (CNS) A4 (210X297 mm) -59- 438619 Central Ministry of Economic Affairs Printed by the Bureau of the Moon Industry Consumer Cooperative Co., Ltd. VI. The second liquid storage tank of the patent application storage tank; the absorption liquid storage tank that supplies the absorption liquid in the absorption tower: via the liquid storage tank at the bottom of the absorption tower and the second liquid storage tank An absorption liquid return channel connected to the absorption liquid storage tank; and when the flow rate of the exhaust gas is below a predetermined speed, the absorption liquid in the liquid storage tank at the bottom of the absorption tower is returned to the absorption liquid storage tank through the second liquid storage tank Means of control. 19. The wet gas processing device according to item 18 of the scope of patent application, which includes a pressurizing means for pressurizing the inside of the absorption liquid storage tank, and controls the pressure of the pressure means to supply the pressure to the absorption liquid of the absorption tower. Form a certain direction of control. 2 0. — A wet gas treatment method, which is connected to the main channel of the exhaust gas emission part of the exhaust gas such as a boiler or a burner, and a chimney, and uses the flow velocity of the exhaust gas to follow the absorption liquid in the exhaust gas. In the gas-liquid contact between the two, an exhaust gas treatment method by a wet absorption tower that absorbs an absorption liquid of a target component in the exhaust gas is characterized in that when the flow velocity in the exhaust gas absorption tower is below a predetermined speed | The treated exhaust gas discharged from the tower is returned to the inlet side of the absorption tower using a bypass channel. 2 1. A wet gas treatment device connected to the exhaust gas emission source such as a boiler and a chimney The main channel of the exhaust gas uses the flow velocity of the exhaust gas to contact the gas-liquid with the absorption liquid in the exhaust gas. The characteristics of the exhaust gas treatment device formed by the wet absorption tower that absorbs the absorption liquid of the target component in the exhaust gas are characterized by ： The # channel for returning the treated exhaust gas discharged from the absorption tower to the inlet side of the absorption tower: --------- ^-(诛 Read the notes on the back first 舄 this page) Order This paper size is applicable to China's standard (CNS > A4 size (2 丨 0X297mm) Printed by the Central Standards Bureau of the Ministry of Economic Affairs, Shellfish Consumer Cooperative, 4: 8619 b! C8 _____ D8 When the flow velocity in the absorption tower is below the predetermined speed, the above-mentioned bypass channel is opened to control the control means for returning the treated exhaust gas to the inlet side of the absorption tower. 22. · For example, the wet gas treatment device in the scope of the patent application No. 21, where It is installed in the absorption tower, and when the flow velocity of the exhaust gas is below a predetermined speed, the exhaust gas in the absorption tower can be formed with variable passage area variable means; and the treated exhaust gas can be returned to the side of the inlet of the absorption tower. 2 3 .—A kind of wet gas processing device, which is attached to the absorption tower to make the absorption liquid stored in the storage tank of the absorption tower spray out from the injection nozzle * while making its jet stream and exhaust gas in the absorption tower from below to face The upper part flows and the gas-liquid comes into contact * Absorbs and removes the target components in the exhaust gas. At the same time, the mist exhauster provided on the upper part of the absorption tower is used to capture the wet exhaust gas that generates mist-like absorption liquid with the exhaust gas. The device is characterized by: • A receiving container for receiving the absorbing liquid flowing down from the defogger is provided on the lower part of the defogger, and the upper end of the receiving container which communicates with a predetermined length of return liquid pipe extending downward is connected to The lower end of the pipe is provided with an opening that can absorb the above-mentioned reflux liquid at a predetermined position in the absorption tower. 2 4. The wet gas processing device according to item 23 of the patent application > At the upper position of the liquid column sprayed by the upward nozzle, the lower end of the above-mentioned return liquid pipe is positioned to open. 2 5. For example, the wet gas processing device of item 24 of the patent application scope, wherein the above-mentioned return liquid pipe The lower end opening is formed into a nozzle shape "2 6. For example, the wet-type gas treatment device according to item 23 of the patent application * is configured to position the lower end opening of the return liquid pipe in the liquid storage section. I I I I — II order I I line (please read the note on the back first Yin ‘write each page) This paper is applicable to“ Standard for Home Stairs (CNS) A4 (210X297 mm) -61-
TW87118702A 1997-11-11 1998-11-10 Wet gas processing method and the apparatus using the same TW438619B (en)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
JP32520297 1997-11-11
JP23206198 1998-08-18
JP23206298 1998-08-18
JP23206098 1998-08-18
JP26433298 1998-09-18

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TW438619B true TW438619B (en) 2001-06-07

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TW87118702A TW438619B (en) 1997-11-11 1998-11-10 Wet gas processing method and the apparatus using the same

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TW (1) TW438619B (en)

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