TW546159B - The scrubber waste air treatment system and related method - Google Patents

The scrubber waste air treatment system and related method Download PDF

Info

Publication number
TW546159B
TW546159B TW91132134A TW91132134A TW546159B TW 546159 B TW546159 B TW 546159B TW 91132134 A TW91132134 A TW 91132134A TW 91132134 A TW91132134 A TW 91132134A TW 546159 B TW546159 B TW 546159B
Authority
TW
Taiwan
Prior art keywords
washing
tower
exhaust gas
scrubber
washing liquid
Prior art date
Application number
TW91132134A
Other languages
Chinese (zh)
Other versions
TW200406248A (en
Inventor
Chien-Hsing Tu
Yuan-Tsai Sung
Original Assignee
Powerchip Semiconductor Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Powerchip Semiconductor Corp filed Critical Powerchip Semiconductor Corp
Priority to TW91132134A priority Critical patent/TW546159B/en
Application granted granted Critical
Publication of TW546159B publication Critical patent/TW546159B/en
Publication of TW200406248A publication Critical patent/TW200406248A/en

Links

Landscapes

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

Abstract

A scrubber waste air treatment method is provided for treating the particles and acidic gas, which comprise to input the hardness softened scrubbing liquid to the scrubber; adjust the pH of scrubbing liquid over 10.5 by adding reagent; introduce the waste air into the scrubber; w a s h the waste air completely with the scrubbing liquid to remove the particles and acidic gas; exhaust the clean air to open air from the gas outlet of the scrubber. The method can enhance the remove efficiency of pollutant and save the waste air treatment cost by raising the pH of scrubbing liquid over 10.5 to increase the reaction for the weak acidic gas. It also employed the water softening apparatus to provide the hardness softened scrubbing liquid without calcium ion and magnesium ion, which can avoid forming the calcium hydroxide and magnesium hydroxide in the scrubber.

Description

546159 五、發明說明(1) 發明領、域 本發明是有關於一種廢氣處理系統,且特別是有關於 一種洗滌塔廢氣處理系統。 先前技術 一般工業製程所產生的製程廢氣通常包括有毒物質且 具有臭味,如果廢氣未經過妥善處理,就會造成空氣污 染。而且,若廢氣中之有毒物質濃度超過法規規定的限 值,就可能危害工廠員工及一般民眾的身體健康。為了控 制空氣污染物,必須利用空氣污染防制設備處理廢氣,以 使廢氣中之有毒物質濃度低於法規規定的限值,其中的一 種業界常用的空氣污染防治設備為洗滌塔廢氣處理系統。 一般的洗滌塔廢氣處理系統,係以液體洗滌的方法處 理廢氣。首先,將洗條液導入洗務塔中後,以洗;;條液循環 泵輸送至塔頂,並由塔頂進入洗滌塔中。接著,洗滌液經 喷灑裝置而均勻灑下並回到塔底,然後再由洗滌液循環泵 輸送至塔頂而成一循環。另一方面,廢氣則由塔底導入洗 滌塔中,然後向上流動並與洗滌液接觸,使廢氣中的污染 物(如微粒、酸氣等)溶入洗滌液,而經淨化的氣體則由塔 頂排出。因為,洗滌液與廢氣接觸後會帶有許多雜質,所 以需要補充乾淨的洗滌液至洗滌塔中,並排出不乾淨的洗 條液。對於洗縣:塔廢氣處理系統而言,由於洗;^條液與廢氣 接觸面積越大,洗條塔之廢氣洗滌效果會越好,因此洗條 塔通常需設計成具有大的液面面積和最低的氣體壓力損546159 V. Description of the invention (1) Field and domain of the invention The present invention relates to an exhaust gas treatment system, and more particularly to an exhaust gas treatment system for a scrubber tower. Prior technology The process exhaust gas produced by general industrial processes usually includes toxic substances and has an odor. If the exhaust gas is not properly treated, it will cause air pollution. In addition, if the concentration of toxic substances in the exhaust gas exceeds the limit set by regulations, it may endanger the health of factory employees and the general public. In order to control air pollutants, air pollution prevention equipment must be used to treat the exhaust gas so that the concentration of toxic substances in the exhaust gas is lower than the limit set by regulations. One of the commonly used air pollution prevention equipment in the industry is the scrubber exhaust gas treatment system. The general scrubber exhaust gas treatment system treats exhaust gas by liquid washing. First, the strip washing liquid is introduced into the washing tower and then washed; the strip liquid circulation pump is transported to the top of the tower and enters the washing tower from the top of the tower. Then, the washing liquid is uniformly sprayed through the spraying device and returned to the bottom of the tower, and then is sent to the top of the tower by the washing liquid circulation pump to form a cycle. On the other hand, the exhaust gas is introduced into the washing tower from the bottom of the tower, then flows upward and contacts the washing liquid, so that the pollutants (such as particles, acid gas, etc.) in the exhaust gas are dissolved in the washing liquid, and the purified gas is passed from the tower Top drain. Because the washing liquid comes with many impurities after coming into contact with the exhaust gas, it is necessary to replenish the clean washing liquid into the washing tower and discharge the dirty washing liquid. For Xiexian: tower exhaust gas treatment system, due to the washing; the larger the contact area between the stripe liquid and the exhaust gas, the better the exhaust gas washing effect of the stripping tower, so the stripping tower usually needs to be designed to have a large liquid surface area and Lowest gas pressure loss

9954twf. pul 第6頁9954twf. Pul Page 6

I 546159 五,發明說明(2) 失。為、了達到上述之目的,通常在洗滌塔内會裝填一些填 充料(Packing),以增加液氣之交換面積,填充料具有許 多不同的形狀,而具有其獨特的表面積供設計者選擇使 用,常用的填充料如拉西環及貝爾鞍環。 一般而言,目前業界常採用之廢氣處理系統為將各個 設備端排放之廢氣分別依酸鹼特性各別集中後,直接以數 個洗滌塔廢氣處理系統進行處理。然而,隨著設備及產能 之擴充,設備端所產生的廢排氣亦大量增加,已超出原先 洗滌塔的處理設計量,隨之而來的結果是製程廢氣,未獲 妥善處理而逸散至空氣中。 習知的改善技術為在機台側安裝局部洗滌塔(1 oca 1 s c r u b b e r )以濕式洗滌或活性碳吸附之方法,降低製程廢 氣之含量,最後才排至濕式洗滌塔。但限於場地與成本, 並非每家工廠皆適用安裝局部洗滌塔,以提昇廢氣處理效 率。 另外習知的改善技術為增加循環水量,以降低循環水 内酸氣濃度,但會加重純水系統及廢水處理系統的負荷, 與造成全廠用水回收率驟降及全廠用水排放率驟升與用水 成本大增等問題。 發明概要 有鑑於此,本發明之一目的係提供一種洗滌塔廢氣處 理系統及方法,能夠有效的移除廢氣中的酸氣,而提高廢 氣洗條效果。I 546159 V. Description of Invention (2) In order to achieve the above-mentioned purpose, some packing materials are usually packed in the washing tower to increase the liquid-gas exchange area. The packing materials have many different shapes and have their unique surface area for designers to choose. Common fillers such as Raschig ring and Bell saddle ring. Generally speaking, the exhaust gas treatment system currently used in the industry is to concentrate the exhaust gas discharged from each equipment end according to the acid-base characteristics, and then directly treat it with several scrubber exhaust gas treatment systems. However, with the expansion of equipment and production capacity, the waste exhaust gas generated at the equipment end has also increased significantly, which has exceeded the original designed capacity of the washing tower. The consequent result is that the process exhaust gas is not properly treated and escapes to in the air. The conventional improvement technology is to install a local washing tower (1 oca 1 scr u b be r) on the machine side to reduce the content of process waste gas by wet washing or activated carbon adsorption, and finally discharge it to the wet washing tower. However, due to the limited space and cost, not every factory is suitable for installing a partial scrubber tower to improve the efficiency of exhaust gas treatment. In addition, the conventional improvement technology is to increase the amount of circulating water to reduce the concentration of acid gas in the circulating water, but it will increase the load on the pure water system and wastewater treatment system, and cause the plant water recovery rate to drop sharply and the plant water discharge rate to rise sharply. And the cost of water has increased dramatically. SUMMARY OF THE INVENTION In view of this, an object of the present invention is to provide an exhaust gas treatment system and method for a scrubbing tower, which can effectively remove the acid gas in the exhaust gas and improve the effect of the exhaust gas washing bar.

9954twf.ptd 第7頁 1 546159 Μ 五、發明說明(3) 本發明的目的係提供一種洗務塔廢氣處理系統及方 法,在不需安裝局部洗滌塔,且不增加洗滌塔的循環水量 情況下,可以提高廢氣洗滌效果,而能夠節省廢棄處理成 本0 本發明提供一種洗條塔廢氣處理系統,此系統是由洗 滌塔、洗滌液供給裝置、軟水裝置、洗滌液循環泵、加藥 裝置、廢氣注入管與廢氣排出管所構成。其中,洗滌液供 給裝置連接至洗滌塔,用以供給洗滌液至洗滌塔中;軟水 裝置設置於洗滌塔與洗滌液供給裝置之間,用以軟化洗滌 液供給裝置所供給之洗滌液,並送至洗滌塔中;洗滌液循 後泵連接洗滌塔之底部與頂部,使洗滌液可以在洗滌塔内 循環;加藥裝置連接洗滌塔,並控制洗滌塔内之洗滌液的 酸鹼值大於pH 1 0 . 5以上;廢氣注入管連結至洗滌塔,使廢 氣導入洗滌塔之中;廢氣排出管連結至洗滌塔上,使經洗 滌塔處理後之氣體排放至大氣中。 本發明係利用加藥裝置調整洗滌塔中之洗滌液的酸鹼 值為pH 1 0. 5以上,在反應時間内酸性氣體就能與強鹼充分 反應,如此可將氯化氫之去除率由82%〜95%提昇至100 % 、 氟化氫之去除率由39%〜91%提昇至9 9. 9 3%左右,完全解決 酸味的問題。然而,當洗務液之酸鹼值調升至1 0. 5以上 時,洗滌液含有之的鈣離子及鎂離子就會與氫氧根離子形 成氫氧化鈣及氫氧化鎂等結垢物而附著於洗滌塔内部造成 結垢,並導致洗滌塔内部堵死,造成内部壓差升高。因 此,本發明於洗滌液供給裝置與洗滌塔之間設置一座軟水9954twf.ptd Page 7 1 546159 Μ V. Description of the invention (3) The purpose of the present invention is to provide an exhaust gas treatment system and method for a washing tower, without installing a local washing tower and without increasing the circulating water volume of the washing tower It can improve the washing effect of exhaust gas and save the cost of waste treatment. The present invention provides an exhaust gas treatment system for a washing column. The system is composed of a washing tower, a washing liquid supply device, a soft water device, a washing liquid circulation pump, a dosing device, and exhaust gas. It is composed of an injection pipe and an exhaust pipe. The washing liquid supply device is connected to the washing tower to supply the washing liquid into the washing tower; the water softening device is provided between the washing tower and the washing liquid supply device to soften the washing liquid supplied by the washing liquid supply device and send it Into the washing tower; the washing liquid is pumped back and forth to connect the bottom and the top of the washing tower, so that the washing liquid can be circulated in the washing tower; the medicinal device is connected to the washing tower, and the pH value of the washing liquid in the washing tower is greater than pH 1 0.5 or more; the exhaust gas injection pipe is connected to the washing tower, so that the exhaust gas is introduced into the washing tower; the exhaust gas discharge pipe is connected to the washing tower, so that the gas treated by the washing tower is discharged to the atmosphere. The invention uses a dosing device to adjust the pH value of the washing liquid in the washing tower to be above pH 0.5, and the acidic gas can fully react with the strong alkali within the reaction time, so that the removal rate of hydrogen chloride can be reduced from 82% ~ 95% is increased to 100%, and the removal rate of hydrogen fluoride is increased from 39% to 91% to about 9 9. 9 3%, which completely solves the problem of sour taste. However, when the pH value of the washing solution is raised to more than 10.5, the calcium ions and magnesium ions contained in the washing solution will form scales such as calcium hydroxide and magnesium hydroxide with hydroxide ions. Attaching to the inside of the washing tower causes fouling, and causes the inside of the washing tower to be blocked, causing the internal pressure difference to rise. Therefore, the present invention sets a soft water between the washing liquid supply device and the washing tower.

9954twf.ptd 第8頁 546159 五、發明說明(4) 裝置,用於去除洗滌液中所含的鈣離子及鎂離子。使在洗 滌液酸鹼值控制調升至1 0. 5以上的狀況下,提高廢氣處理 效率,並使洗滌塔不會結垢而可順利操作。 而且,本發明不需要設置局部洗滌塔與增加用水量, 而只需要設置一套軟水裝置就可以提高廢氣處理效率,因 此可以節省成本。 本發明另外提出一種洗滌塔廢氣處理方法,此方法係 將經過軟化處理之洗滌液注入至洗滌塔中。然後加入藥劑 至洗游:塔内以調整洗條液的酸驗值大於ρ Η 1 0 . 5以上,並注 入廢氣至洗滌塔内。接著,使廢氣與洗滌液充分混和以移 除,廢氣中之微粒及酸氣後,排放經過洗滌液處理後之氣 體。 本發明係藉由提高洗務液的酸驗值至1 0. 5,以增加對 廢氣的酸鹼中和作用,而且利用軟水裝置以去除循環洗滌 液所含之鈣離子及鎂離子,可避免洗滌塔内部結垢而能夠 提高廢氣去除效率。由於本發明不需要設置局部洗滌塔與 增加用水量,而只需要設置一套軟水裝置就可以提高廢氣 處理效率,因此可以節省廢氣處理成本。 為讓本發明之上述目的、特徵、優點能更明顯易懂, 下文特舉一較佳實施例,並配合所附圖式,作詳細說明如 下: 圖式之標示說明: 1 0 0 :洗滌塔 1 0 2 :洗滌液供給裝置9954twf.ptd Page 8 546159 V. Description of the invention (4) Device for removing calcium and magnesium ions contained in the washing solution. Under the condition that the pH value of the washing liquid is adjusted to more than 10.5, the efficiency of the exhaust gas treatment is improved, and the washing tower can be smoothly operated without scaling. Moreover, the present invention does not need to install a local washing tower and increase the water consumption, but only needs to set a set of water softening device to improve the efficiency of exhaust gas treatment, thereby saving costs. The present invention also provides a method for treating exhaust gas from a washing tower. This method involves injecting a softened washing liquid into the washing tower. Then add medicament to the washing tour: adjust the acid value of the strip washing solution to be greater than ρ Η 10.5 or more in the tower, and inject the exhaust gas into the washing tower. Next, the exhaust gas and the washing liquid are thoroughly mixed to be removed. After the particulates and acid gas in the exhaust gas are discharged, the gas after the washing liquid treatment is discharged. In the present invention, the acid test value of the washing liquid is increased to 10.5 to increase the acid-base neutralization effect on the exhaust gas, and the soft water device is used to remove the calcium ions and magnesium ions contained in the circulating washing liquid, which can be avoided Fouling inside the washing tower can improve exhaust gas removal efficiency. Because the present invention does not need to install a local washing tower and increase the water consumption, only a set of water softening device can be used to improve the efficiency of exhaust gas treatment, so the cost of exhaust gas treatment can be saved. In order to make the above-mentioned objects, features, and advantages of the present invention more comprehensible, a preferred embodiment is given below in conjunction with the accompanying drawings to make a detailed description as follows: Symbols of the drawings: 100: washing tower 1 0 2: washing liquid supply device

9954twf.ptd 第9頁 i 546159 五、發明說明(5) 104 軟 水 裝 置 106 洗 滌 液 循 環 泵 108 加 藥 裝 置 110 廢 氣 注 入 管 112 廢 氣 排 出 管 114 廢 氣 116 洗 滌 液 118 洗 條 液 喷 灑 裝置 120 填 充 料 122 酸 驗 偵 測 器 124 藥 劑 實施 例 第1圖所繪示為本發明較佳實施例之一種洗滌塔廢氣 處理系統。請參照第1圖,本發明之洗滌塔廢氣處理系統 至少是由洗滌塔1 0 0、洗滌液供給裝置1 0 2、軟水裝置 1 0 4、洗滌液循環泵1 0 6、加藥裝置1 0 8、廢氣注入管1 1 0與 廢氣排出管1 1 2等裝置所構成。 洗滌塔1 0 0包括一槽體,其提供空間使廢氣11 4與洗滌 液1 1 6發生接觸與作用。常用的洗滌塔1 0 0種類例如填充 塔、泡罩塔、喷霧塔與文式塔。 洗滌液供給裝置1 0 2例如是連接至洗滌塔1 0 0,用以供 給洗滌液1 1 6至洗滌塔1 0 0中。其中,洗滌液1 1 6包括清 水、自來水及冷凝水。 軟水裝置1 0 4設置於洗滌塔1 0 0與洗滌液供給裝置1 0 29954twf.ptd Page 9 i 546159 V. Description of the invention (5) 104 Soft water device 106 Washing liquid circulation pump 108 Dosing device 110 Exhaust gas injection pipe 112 Exhaust gas discharge pipe 114 Exhaust gas 116 Washing liquid 118 Washing liquid spraying device 120 Filling material 122 Acid Test Detector 124 Medicine Example Figure 1 shows a scrubber exhaust gas treatment system according to a preferred embodiment of the present invention. Please refer to FIG. 1. The exhaust gas treatment system of the washing tower of the present invention is at least a washing tower 100, a washing liquid supply device 10, a soft water device 10, a washing liquid circulation pump 10, and a dosing device 10. 8. The exhaust gas injection pipe 1 10 and the exhaust gas discharge pipe 1 12 are configured. The washing tower 100 includes a tank which provides space for the exhaust gas 11 4 to come into contact with the washing liquid 1 16. Common types of washing towers 100 are, for example, packed towers, blister towers, spray towers and venturi towers. The washing liquid supply device 10 2 is, for example, connected to the washing tower 100 to supply the washing liquid 1 16 to the washing tower 100. The washing liquid 1 1 6 includes clean water, tap water, and condensed water. The water softener 1 0 4 is installed in the washing tower 1 0 0 and the washing liquid supply device 1 0 2

9954twf.ptd 第10頁 546159 五、發明說明(6) 之間’用以軟化洗滌液供給裝置丨〇 2所供給之洗滌液丨丨6, 並送至洗滌塔1 〇 〇中。軟水裝置丨〇 4例如是用於去除洗滌液 1 2 〇中的鈣離子及鎂離子,其中去除鈣離子及鎂離子的方 法包括化學沉降法或離子交換法。 洗條液循環泵1 〇 6之入水端及出水端分別連接洗滌塔 1 〇 〇之底部與頂部使洗滌液丨丨6在洗滌塔1 〇 〇内循環。亦 即。此洗滌液循環泵1 〇 6從洗滌塔1 〇 〇底部抽取洗滌液 1 1 6 ’並將洗滌液1 1 6送至洗滌塔1 〇 〇頂部後,經由洗滌液 臭’麗k置1 1 8喷入塔中後,散成液滴狀而流回到洗蘇塔1 〇 〇 底部’再從洗滌塔1 〇 〇底部抽取洗滌液送至洗滌塔丨〇 〇頂 可,而使洗滌液1 1 6在洗滌塔1 0 0内循環。其中,洗滌液喷 灑裝置1 1 8可將洗滌液1 1 6均勻分配向下喷灑,充分與廢氣 接觸。 加藥裝置1 0 8例如是連接至洗滌塔1 0 0,用以控制洗滌 土合内之循環洗;;條液的酸驗值例如是大於ρ Η1 〇. 5以上。加藥 裳置1 0 8加入之藥劑可使洗滌液與廢氣發生酸鹼中和反 應’而有效的移除廢氣中之酸性物質。 廢氣注入管11 0連結至洗滌塔1 0 0,使一廢氣導入洗滌 塔1 0 0之中。其中所欲處理廢氣11 4如氟化氫、氯化氫、硝 酸氣體的混和酸氣或至少包括其中之一的氣體。 廢氣排出管11 2連結至洗滌塔上,使經洗滌塔1 〇 〇處理 後之氣體排放至大氣中。 而且,為了增加液氣交換面積,通常在洗滌塔1 〇 0内 會裝填一些填充料(Packing) 120,填充料具有許多不同的 lllgllii nil9954twf.ptd Page 10 546159 V. Description of the invention (6) Between '6' to soften the washing liquid supplied by the washing liquid supply device 丨 〇 2 and send it to the washing tower 100. The water softening device 04 is, for example, a method for removing calcium ions and magnesium ions in the washing solution 120, and the method for removing calcium ions and magnesium ions includes a chemical precipitation method or an ion exchange method. The inlet end and outlet end of the washing liquid circulation pump 106 are respectively connected to the bottom and the top of the washing tower 1000 to circulate the washing liquid 丨 6 in the washing tower 100. That is. This washing liquid circulation pump 1 06 draws the washing liquid 1 16 'from the bottom of the washing tower 100, and sends the washing liquid 1 16 to the top of the washing tower 100, and then sets the washing liquid through the washing liquid 1 1 8 After spraying into the tower, it will drop into a droplet shape and flow back to the bottom of the washing tower 1000. Then, the washing liquid will be drawn from the bottom of the washing tower 100 and sent to the top of the washing tower. 6 circulates in the washing tower 100. Among them, the washing liquid spraying device 1 1 8 can evenly distribute the washing liquid 1 1 6 and spray downwards, and fully contact the exhaust gas. The dosing device 108 is, for example, connected to the washing tower 100 to control the cycle washing in the washing soil; the acid test value of the strip liquid is, for example, greater than ρ Η 1 0.5. Dosing The medicine added by Changzhi 108 can make acid and alkali neutralization reaction between the washing liquid and the exhaust gas, and effectively remove the acidic substances in the exhaust gas. The exhaust gas injection pipe 110 is connected to the washing tower 100, and an exhaust gas is introduced into the washing tower 100. The exhaust gas 114 to be treated therein is a mixed acid gas such as hydrogen fluoride, hydrogen chloride, nitric acid gas or a gas including at least one of them. The exhaust gas exhaust pipe 112 is connected to the washing tower, so that the gas treated by the washing tower 1000 is discharged into the atmosphere. In addition, in order to increase the liquid-gas exchange area, some packing materials (Packing) 120 are usually filled in the washing column 1000. The packing materials have many different lllgllii nil

IPIP

II 995 仏Vi.ptd 第11頁 546159 五、發明說明(7) 形狀,其具有其獨特的表面積可供設計者選擇使用,^ 的填充料如拉西環及貝爾鞍環。 系用 此外’在洗滌塔内設有一酸鹼偵測器丨22,此酸於 測器1 22連接加藥裝置,用以監測洗滌液丨丨6的酸驗""值'價、, 控制加樂裝置1 〇 8加入洗滌塔1 〇 〇中之加藥量。舉例來〜並 當酸驗偵測器所偵測的酸鹼值低於設定值時,傳送—及 至加藥裝置,而使加藥裝置丨〇 8開啟而加入藥劑至 Λ唬 中。 /疋4塔 本發明係利用加藥裝置1 08調整洗滌塔丨00中之洗條夜 11 6的酸鹼值為pH1 〇 · 5以上,使酸性氣體能夠與強鹼在*反之 馬時間内充分反應,如此提升廢氣中酸性氣體之去除率, 完全解決酸味的問題。然而,當洗滌液丨丨6之酸鹼值調升 至1^以上時,洗滌液11 6含有之的鈣離子及鎂離子就會 與氫^根離子形成氫氧化鈣及氫氧化鎂等結垢物而附著曰於 冼森L 〇 ,内邛造成結垢,而導致洗滌塔1 0 0内部堵死並造 成内4 I差升问。因此,本發明於洗滌液供給裝置1 〇 2與 洗滌塔1 0 0之間設置—庙紗士奸W 1 ^人 1 压孝人水裝置1 04,用於去除洗滌液 1 1 6中所含的|弓離子及锃M^ , t L , n c 及鎮離子。使在洗滌液1 1 6酸鹼值控制 調升至1 0 · 5以上的妝汉T ^ ^ ^ ,^ , π Λ 尺 下,如问廢氧1 1 4處理效率,並使 洗條塔1 0 0不會結垢而可順利操作。 、上σ兒月本叙明之洗滌塔廢氣處理系統,接著說明本 實施例所揭露之洗條塔廢氣處理方法。首先,提供洗務液 塔100使用/洗務液116由塔頂流入經喷灑裝置 :二/鹿下’與廢氣接觸後的洗祿液i i 6流至塔底,再由II 995 仏 Vi.ptd Page 11 546159 V. Description of the invention (7) The shape has its unique surface area for the designer to choose to use, such as Raschig ring and Bell saddle ring. In addition, there is an acid-base detector 22 in the washing tower. This acid is connected to the dosing device at the detector 1 22 to monitor the acid test of the washing solution. The amount of drug added to the washing tower 100 was controlled by the galler device 108. For example, ~ and when the acid-base value detected by the acid detection detector is lower than the set value, send-and to the dosing device, so that the dosing device is turned on and the medicine is added to Λ. / 疋 4 Tower The present invention uses a dosing device 108 to adjust the pH value of the washing strip 11 in the washing tower 11 00 to pH 1 0.5 or more, so that the acid gas can be fully reacted with the strong alkali within the maximum time. Reaction, so that the removal rate of acid gas in the exhaust gas is improved, and the problem of sour taste is completely solved. However, when the pH value of the washing solution 6 is increased to more than 1 ^, the calcium ions and magnesium ions contained in the washing solution 116 will form scales such as calcium hydroxide and magnesium hydroxide with hydrogen ions. Attachment to the object is caused by 冼 森 L 〇, internal contamination caused scaling, which caused the internal clogging of the washing tower 100 and caused the internal 4 I difference. Therefore, the present invention is provided between the washing liquid supply device 10 and the washing tower 100. The temple yarn clerk W 1 ^ person 1 is a filial piety water device 1 04 for removing the liquid contained in the washing liquid 1 1 6 | Bow ions and 锃 M ^, t L, nc and town ions. Make the pH value of the washing solution 1 1 6 to be adjusted to more than 10.5 · T ^ ^ ^, ^, π Λ feet, such as the waste oxygen 1 1 4 treatment efficiency, and make the strip washing tower 1 0 0 No fouling and smooth operation. The exhaust gas treatment system of the washing tower described in the previous article will be described next, and the exhaust gas treatment method of the strip washing tower disclosed in this embodiment will be described next. First, a washing liquid is provided. The use of the washing liquid 100 / washing liquid 116 flows from the top of the tower and passes through the spraying device: 二 / 鹿 下 ’The washing liquid i i 6 after coming into contact with the exhaust gas flows to the bottom of the tower, and then

9954twf.ptd9954twf.ptd

II 第12頁 546159 五、發明說明(8) 洗務液循環泵1 〇6輸送至塔頂循環使用,使用前對洗滌液 11 6進行液體中金屬離子如鈣離子及鎂離子的軟化步驟, 然後再加入藥劑1 2 4例如是液驗,調整洗滌液的酸鹼值大 於1 0 · 5以上;接著由塔底導入欲處理的廢氣丨丨4如氟化 氫、氣化氫、硝酸氣體混合的酸氣或至少包括其中之一的 氣體至洗;;條塔1 〇 〇内,向上流動與洗務液接觸,廢氣1 1 4中 的污染物溶入洗滌液1 1 6,經過洗滌液1 1 6淨化的氣體由塔 頂排出。 本發明係將洗務液1 1 6之酸驗值控制調升至1 〇. 5以 上 ®文性氣體就能與強驗在反應時間内充分反應,如此可 碍氣化氫之去除率由82%〜95%提昇至100% 、氟化氫之去除 率由39%〜91%提昇至99· 93%左右,完全解決酸味的問題。 但疋將洗條液之酸驗值調升至1 〇 · 5以上時,洗務塔内部就 會開始結垢’造成内部壓差升高以致内部堵死。其原因為 供應的洗條液11 6本身就含濃度極高的詞離子及鎮離子, 當酸驗值在9 · 0以下時,會形成硫酸詞及硫酸錤懸浮固 體,並不會造成結垢,但當酸鹼值大於丨〇 · 5時,洗條液 116中的鈣離子及鎂離子就會與氫氧根離子形成氫氧化約 及氫氧化鎂等結垢物。 為了解決在洗滌液酸鹼值大於ρΗΐ〇· 5環境下,洗條炫 1 0 0内部結垢問題,係於洗滌液供給裝置丨〇 2,提供洗條夜 1 16至洗滌塔100之前,加設一座軟水裝置1〇4,用於去除 洗滌液1 1 6中所含的鈣離子及鎂離子。使在洗滌液丨丨6酸鹼 值控制調升至1 0· 5以上的狀況下,提高廢氣處理效率,】II Page 12 546159 V. Description of the invention (8) The washing liquid circulation pump 1 06 is transported to the top of the tower for recycling. Before use, the washing liquid 11 6 is subjected to a softening step of metal ions such as calcium ions and magnesium ions in the liquid, and then Adding agent 1 2 4 is liquid test, for example, adjusting the pH value of the washing liquid to be greater than 10 · 5; and then introducing the waste gas to be treated from the bottom of the tower 丨 4 such as hydrogen fluoride, hydrogen gas, and nitric acid mixed acid gas Or at least one of the gases is included in the scrubbing; in the column 1000, upward flow comes into contact with the washing liquid, and the pollutants in the exhaust gas 1 1 4 are dissolved in the washing liquid 1 1 6 and purified by the washing liquid 1 1 6 The gas is discharged from the top of the tower. The present invention adjusts the acid test value of the washing liquid 1 16 to more than 10.5. The cultural gas can fully react with the strong test within the reaction time, so that the removal rate of hydrogen gas can be prevented from 82. % ~ 95% is increased to 100%, and the removal rate of hydrogen fluoride is increased from 39% to 91% to about 99.93%, which completely solves the problem of sour taste. However, when the acid test value of the strip washing liquid is raised to more than 10 · 5, the inside of the washing tower will begin to fouling ', causing the internal pressure difference to rise and the internal blockage. The reason for this is that the supplied strip washing liquid 11 6 itself contains extremely high concentrations of word ions and ballast ions. When the acid test value is below 9 · 0, sulfate words and suspended solids of rubidium sulfate will be formed, which will not cause scaling. However, when the acid-base value is greater than 0.5, the calcium ions and magnesium ions in the washing liquid 116 will form hydroxide scales and hydroxide scales with hydroxide ions. In order to solve the problem of scaling inside the washing bar under the environment where the pH value of the washing liquid is greater than ρΗΐ0.5, it is tied to the washing liquid supply device 丨 〇2 to provide washing bar night 1 16 to the washing tower 100, add A water softening device 104 is set up to remove calcium ions and magnesium ions contained in the washing liquid 116. In order to improve the efficiency of waste gas treatment under the condition that the pH value of the washing solution 丨 6 is adjusted to more than 10.5,

9954twf .ptcl 546159 五、發明說明(9) 使洗滌塔1 0 0不會結垢而可順利操作。 本發明係藉由提高洗滌液的酸鹼值至1 0. 5,以增加對 廢氣的酸鹼中和作用,而且利用軟水裝置以去除循環洗滌 液所含之鈣離子及鎂離子,可避免洗滌塔内部結垢而能夠 提高廢氣去除效率。由於本發明不需要設置局部洗滌塔與 增加用水量,而只需要設置一套軟水裝置就可以提高廢氣 處理效率,因此可以節省廢氣處理成本。 雖然本發明已以一較佳實施例揭露如上,然其並非用 以限定本發明,任何熟習此技藝者,在不脫離本發明之精 神和範圍内,當可作些許之更動與潤飾,因此本發明之保 言|範圍當視後附之申請專利範圍所界定者為準。9954twf.ptcl 546159 V. Description of the invention (9) The washing tower 100 can be prevented from scaling and can be operated smoothly. The present invention increases the acid-base neutralization of exhaust gas by increasing the pH value of the washing liquid to 10.5, and uses a soft water device to remove the calcium ions and magnesium ions contained in the circulating washing liquid, which can avoid washing. Fouling inside the tower can improve exhaust gas removal efficiency. Because the present invention does not need to install a local washing tower and increase the water consumption, only a set of water softening device can be used to improve the efficiency of exhaust gas treatment, so the cost of exhaust gas treatment can be saved. Although the present invention has been disclosed as above with a preferred embodiment, it is not intended to limit the present invention. Any person skilled in the art can make some modifications and retouching without departing from the spirit and scope of the present invention. The guarantee of the invention | The scope shall be determined by the scope of the attached patent application.

9954twf.ptd 第14頁 i546159 圖式簡單說明 第1、圖所繪示為洗滌塔廢氣處理系統的基本構造。9954twf.ptd Page 14 i546159 Brief description of the drawings Figure 1 and Figure 1 show the basic structure of the scrubber exhaust gas treatment system.

9954twf.ptd 第15頁9954twf.ptd Page 15

Claims (1)

546159 六、申請專利範圍 1. 一種洗滌塔廢氣處理系統,該系統至少包括: 一洗滌塔; 一洗滌液供給裝置,該洗滌液供給裝置連接至該洗滌 塔,用以供給一洗條液至該洗條塔中; 一軟水裝置,該軟水裝置設置於該洗滌塔與該洗滌液 供給裝置之間,用以軟化該洗滌液供給裝置所供給之該洗 滌液,並送至該洗滌塔中; 一洗務液循環泵,該洗務液循環泵連接該洗條塔之底 部與頂部,使該洗滌液可以在該洗滌塔内循環; 一加藥裝置,該加藥裝置連接該洗滌塔,並控制該洗 释塔内之該洗條液的酸驗值大於ρ Η 1 0. 5以上; 一廢氣注入管,該廢氣注入管連結至該洗滌塔,使一 廢氣導入該洗丨條塔之中,以及 一廢氣排出管,該廢氣排出管連結至該洗滌塔上,使 經該洗滌塔處理後之氣體排放至大氣中。 2. 如申請專利範圍第1項所述之洗滌塔廢氣處理系 統,其中更包括一酸鹼偵測器,該酸鹼偵測器設置於該洗 條塔中用以監測該洗務液之酸驗值。 3. 如申請專利範圍第1項所述之洗滌塔廢氣處理系 統,其中更包括一洗滌液喷灑裝置,該洗滌液喷灑裝置設 置於該洗滌塔頂部用以喷灑該洗滌液。 4. 如申請專利範圍第1項所述之洗滌塔廢氣處理系 統,其中該廢氣至少包括氟化氫氣體、氣化氫氣體、硝酸 氣體之其中之一。546159 6. Application patent scope 1. A scrubber exhaust gas treatment system, the system includes at least: a scrubber tower; a scrubber liquid supply device, the scrubber liquid supply device is connected to the scrubber tower, and is used to supply a scrubber liquid to the In the washing column; a water softening device, which is disposed between the washing tower and the washing liquid supply device, to soften the washing liquid supplied by the washing liquid supply device and send the washing liquid to the washing tower; A washing liquid circulation pump, the washing liquid circulation pump connects the bottom and the top of the washing tower, so that the washing liquid can be circulated in the washing tower; a medicine adding device, the medicine adding device is connected to the washing tower and controls The acid check value of the strip washing solution in the elution tower is greater than ρ Η 1 0.5 or more; an exhaust gas injection pipe connected to the washing tower, so that an exhaust gas is introduced into the washing tower, And an exhaust gas exhaust pipe, which is connected to the washing tower to discharge the gas processed by the washing tower to the atmosphere. 2. The scrubbing tower exhaust gas treatment system as described in item 1 of the scope of patent application, which further includes an acid-base detector, which is arranged in the strip washing tower to monitor the acid of the washing solution Verification value. 3. The scrubber exhaust gas treatment system according to item 1 of the scope of the patent application, further comprising a scrubbing liquid spraying device, the scrubbing liquid spraying device is disposed on the top of the scrubbing tower to spray the scrubbing liquid. 4. The scrubber exhaust gas treatment system according to item 1 of the scope of the patent application, wherein the exhaust gas includes at least one of hydrogen fluoride gas, hydrogen gas gas, and nitric acid gas. 9954twf.ptd 第16頁 546159 六、申請專利範圍 5 ·如申請專利範圍第1項所述之洗滌塔廢氣處理系 統,其中該加藥裝置加入該洗滌塔中之藥劑包括氫氧化 鈉。 6. 如申請專利範圍第1項所述之洗條塔廢氣處理系 統,其中該洗滌塔包括填充塔、泡罩塔、喷霧塔與文式塔 之其中之一。 7. 如申請專利範圍第1項所述之洗滌塔廢氣處理系 統,其中該洗滌塔内填充有拉西環。 8. 如申請專利範圍第1項所述之洗滌塔廢氣處理系 統,其中該洗滌液包括清水。 、9.如申請專利範圍第1項所述之洗滌塔廢氣處理系 統,其中該洗務液包括自來水。 1 0.如申請專利範圍第1項所述之洗滌塔廢氣處理系 統,其中該洗條液包括冷凝水。 1 1. 一種洗滌塔廢氣處理方法,該方法至少包括下列 步驟: 提供一洗滌液,並對該洗滌液進行一軟化步驟; 注入經軟化之該洗條液至一洗務塔中; 加入一藥劑至該洗〉條塔内以調整該洗)條液的酸驗值大 於pHl 0. 5以上; 注入一廢氣至該洗滌塔内; 混合該廢氣與該洗滌液;以及 排放經過該洗滌液處理後之氣體。 1 2.如申請專利範圍第1 1項所述之洗滌塔廢氣處理方9954twf.ptd Page 16 546159 6. Scope of Patent Application 5 · The scrubber exhaust gas treatment system described in item 1 of the scope of patent application, wherein the medicament added to the scrubber by the dosing device includes sodium hydroxide. 6. The scrubbing tower exhaust gas treatment system according to item 1 of the scope of the patent application, wherein the scrubbing tower includes one of a packed tower, a blister tower, a spray tower and a vent tower. 7. The scrubber exhaust gas treatment system according to item 1 of the scope of the patent application, wherein the scrubber is filled with a Raschig ring. 8. The scrubber exhaust gas treatment system according to item 1 of the scope of the patent application, wherein the washing liquid includes clean water. 9. The scrubber exhaust gas treatment system as described in item 1 of the scope of patent application, wherein the washing liquid includes tap water. 10. The exhaust gas treatment system for a scrubbing tower as described in item 1 of the scope of the patent application, wherein the strip washing liquid includes condensed water. 1 1. A method for treating exhaust gas from a washing tower, the method comprising at least the following steps: providing a washing liquid and subjecting the washing liquid to a softening step; injecting the softened washing liquid into a washing tower; adding a medicament To the washing> strip column to adjust the washing) the acid value of the strip solution is greater than pHl 0.5; inject an exhaust gas into the washing tower; mix the exhaust gas with the washing liquid; and discharge after the washing liquid treatment Of gas. 1 2. The scrubber exhaust gas treatment party as described in item 11 of the scope of patent application 9954twf.ptd 第17頁 546159 %9954twf.ptd Page 17 546159% 9954twf.ptd 第18頁9954twf.ptd Page 18
TW91132134A 2002-10-30 2002-10-30 The scrubber waste air treatment system and related method TW546159B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
TW91132134A TW546159B (en) 2002-10-30 2002-10-30 The scrubber waste air treatment system and related method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
TW91132134A TW546159B (en) 2002-10-30 2002-10-30 The scrubber waste air treatment system and related method

Publications (2)

Publication Number Publication Date
TW546159B true TW546159B (en) 2003-08-11
TW200406248A TW200406248A (en) 2004-05-01

Family

ID=29730084

Family Applications (1)

Application Number Title Priority Date Filing Date
TW91132134A TW546159B (en) 2002-10-30 2002-10-30 The scrubber waste air treatment system and related method

Country Status (1)

Country Link
TW (1) TW546159B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006024073A1 (en) * 2004-08-31 2006-03-09 Kostech Limited Filtration and purification systems
CN112387036A (en) * 2020-11-04 2021-02-23 惠州市晟利科技有限公司 Efficient spraying waste gas treatment method and device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006024073A1 (en) * 2004-08-31 2006-03-09 Kostech Limited Filtration and purification systems
CN112387036A (en) * 2020-11-04 2021-02-23 惠州市晟利科技有限公司 Efficient spraying waste gas treatment method and device

Also Published As

Publication number Publication date
TW200406248A (en) 2004-05-01

Similar Documents

Publication Publication Date Title
KR100986245B1 (en) Apparatus and method of high efficiency chemical cleaning-type deodorization using non-motorized mixing feeder
US20180311606A1 (en) Complex malodor removing equipment
US20090250396A1 (en) Drainage water-treating method and drainage water-treating apparatus
KR101918005B1 (en) Hybrid two step cleaning apparatus using multistage deodorising filter
CN106731522A (en) A kind of air purification method and purifier
KR102202651B1 (en) Deodorizing system using medicine fluid and single tower for acidic and alkaline gas
US20090152193A1 (en) Drainage water-treating method and drainage water-treating apparatus
KR102024871B1 (en) Device for removing residual ozone gas
JP2007209922A (en) Exhaust gas treatment method and apparatus
CN107434294A (en) Waste liquid treatment device and use this waste liquid treatment device's dirty treatment facility of sky
TW546159B (en) The scrubber waste air treatment system and related method
JPWO2007023749A1 (en) Deodorizing device and deodorizing method
CN209662969U (en) Full-automatic exhaust treatment system
CN101157487A (en) Method for aerating separating and purifying weak acidic harmful gas dissolved in waste water
JP2005013789A (en) Air cleaner
KR20070121497A (en) Gas purifier with deodoriger and mixing system
TW200808431A (en) Fume exhaust treatment device
KR200425412Y1 (en) Gas Purifier With Deodoriger and Mixing System
JP4254943B2 (en) Wastewater treatment system
JP5183538B2 (en) Surplus sludge reduction device
JP2010069423A (en) Deodorization system, deodorization apparatus, and deodorization method
JP2007144340A (en) Method and apparatus for decomposing diluted organic substance in waste water
TWI598147B (en) Exhaust purifier
JP2005254136A (en) Device for treating organic material-containing water by ozone
CN218089196U (en) Integrated machine for adding chemicals, blowing off and repairing underground water

Legal Events

Date Code Title Description
GD4A Issue of patent certificate for granted invention patent
MM4A Annulment or lapse of patent due to non-payment of fees