TWM539982U - Exhaust gas treatment device for glass industry - Google Patents

Exhaust gas treatment device for glass industry Download PDF

Info

Publication number
TWM539982U
TWM539982U TW106200102U TW106200102U TWM539982U TW M539982 U TWM539982 U TW M539982U TW 106200102 U TW106200102 U TW 106200102U TW 106200102 U TW106200102 U TW 106200102U TW M539982 U TWM539982 U TW M539982U
Authority
TW
Taiwan
Prior art keywords
treatment device
gas treatment
fiber filter
exhaust gas
denitration
Prior art date
Application number
TW106200102U
Other languages
Chinese (zh)
Inventor
Fook-Yuan Jiang
Original Assignee
Clean Air Tech Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Clean Air Tech Ltd filed Critical Clean Air Tech Ltd
Priority to TW106200102U priority Critical patent/TWM539982U/en
Publication of TWM539982U publication Critical patent/TWM539982U/en

Links

Landscapes

  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Treating Waste Gases (AREA)

Description

玻璃業之廢氣處理裝置 Waste gas treatment device for glass industry

本創作係關於一種廢氣處理裝置,特別係關於一種玻璃業之廢氣處理裝置。 The present invention relates to an exhaust gas treatment device, and more particularly to an exhaust gas treatment device for the glass industry.

玻璃窯爐的生產過程中,需要消耗大量的能源,且燃料燃燒所產生的汙染物包含粉塵與酸性氣體(例如,NO、NO2、NO3及N2O等氮氧化物、SO2、SO3等硫氧化物),為使玻璃窯爐所排放之氣體可以符合環保標準,工廠均會設置有廢氣處理裝置。 In the production process of glass kiln, a large amount of energy is consumed, and the pollutants generated by fuel combustion contain dust and acid gases (for example, nitrogen oxides such as NO, NO 2 , NO 3 and N 2 O, SO 2 , SO) 3 sulfur oxides), in order to make the gas discharged from the glass furnace can meet environmental standards, the factory will be equipped with an exhaust gas treatment device.

請參照第1圖所示,一習知玻璃業之廢氣處理裝置9包含:一窯爐91、一電除塵器92、一脫硝件93、一脫硫件94、一集塵袋95及一煙囪96。該窯爐91具有一燃燒室911,玻璃原料可以於該燃燒室911熔融形成融漿,以進一步用以成形玻璃成品;該脫硝件93具有一脫硝空間931及一脫硝劑投入口932,該脫硝空間931內設置有呈蜂巢狀之脫硝觸媒,該脫硝劑投入口932連通該脫硝空間931,因而工者可以經由該脫硝劑投入口932投入一脫硝劑(例如,氨氣、液態氨、氨水或尿素),使該脫硝劑與該脫硝觸媒可以於該脫硝空間931共同進行脫硝反應,以去除該脫硝空間931中的廢氣的氮氧化物;該脫硫件94具有一脫硫空間941及一脫硫劑投入口942,該脫硫劑投入口942連通該脫硫空間941,因此工者可以經由該脫硫劑投入口942投入一脫硫劑(例如,消石灰、碳酸氫鈉或氫氧化鈉),而可以於該脫硫空間941進行脫硫反應,去除該脫硫空間941中的廢氣的 硫氧化物並產生石膏等顆粒物質。 Referring to FIG. 1 , a conventional glass exhaust gas treatment device 9 comprises: a kiln 91, an electric precipitator 92, a denitrification unit 93, a desulfurization unit 94, a dust bag 95 and a Chimney 96. The kiln 91 has a combustion chamber 911, and the glass material can be melted in the combustion chamber 911 to form a molten slurry for further forming a finished glass product. The denitration unit 93 has a denitration space 931 and a denitration agent inlet 932. The denitration space 931 is provided with a honeycomb-shaped denitration catalyst, and the denitration agent input port 932 is connected to the denitration space 931, so that the worker can input a denitration agent through the denitration agent input port 932 ( For example, ammonia gas, liquid ammonia, ammonia water or urea), the denitration agent and the denitration catalyst can be denitrified together in the denitration space 931 to remove nitrogen oxides of the exhaust gas in the denitration space 931. The desulfurization unit 94 has a desulfurization space 941 and a desulfurization agent inlet 942. The desulfurization agent inlet 942 communicates with the desulfurization space 941, so that the worker can put in the desulfurization agent inlet 942. a desulfurizing agent (for example, slaked lime, sodium hydrogencarbonate or sodium hydroxide), and the desulfurization reaction can be carried out in the desulfurization space 941 to remove the exhaust gas in the desulfurization space 941. Sulfur oxides and produce particulate matter such as gypsum.

玻璃原料於該燃燒室911燃燒所形成之廢氣進入該電除塵器92,以藉由該電除塵器92內部的負高壓電場來去除廢氣中的粉塵,經去除粉塵的廢氣續進入該脫硝件93之脫硝空間931,並受到該脫硝劑與該脫硝觸媒的共同作用而去除廢氣中的氮氧化物,續進入該脫硫件94之脫硫空間941而去除其中的硫氧化物,接著以該集塵袋95過濾石膏等顆粒物質後,合乎空氣排放標準之淨氣即可以經由該煙囪96排放至大氣中。 The exhaust gas formed by burning the glass raw material in the combustion chamber 911 enters the electrostatic precipitator 92 to remove dust in the exhaust gas by a negative high-voltage electric field inside the electrostatic precipitator 92, and the dust-removed exhaust gas continues to enter the denitration component. The denitration space 931 of 93 is subjected to the action of the denitration agent and the denitration catalyst to remove nitrogen oxides in the exhaust gas, and continues to enter the desulfurization space 941 of the desulfurization unit 94 to remove sulfur oxides therein. Then, after the particulate matter such as gypsum is filtered by the dust collecting bag 95, the clean air which meets the air discharge standard can be discharged to the atmosphere via the chimney 96.

然而,該習知玻璃業之廢氣處理裝置9雖可以藉由該電除塵器92去除廢氣中的粉塵,惟該電除塵器92的效果仍顯不佳,且長時間使用下,堆積在電極板上的粉塵更會影響其除塵效果;再者,該習知玻璃業之廢氣處理裝置9更需要額外設置該脫硝件93及該脫硫件94,結構略顯複雜而增加該習知玻璃業之廢氣處理裝置9的設置成本。有鑑於此,確實有必要提供一種玻璃業之廢氣處理裝置,以改善上述的問題。 However, the exhaust gas treatment device 9 of the conventional glass industry can remove the dust in the exhaust gas by the electrostatic precipitator 92, but the effect of the electrostatic precipitator 92 is still not good, and it is deposited on the electrode plate under long-term use. The dust on the dust will affect the dust removal effect. Moreover, the exhaust gas treatment device 9 of the conventional glass industry needs to additionally provide the denitration member 93 and the desulfurization member 94, and the structure is slightly complicated to increase the conventional glass industry. The installation cost of the exhaust gas treatment device 9. In view of this, it is indeed necessary to provide an exhaust gas treatment device for the glass industry to improve the above problems.

為解決上述問題,本創作提供一種玻璃業之廢氣處理裝置,可以有效去除廢氣中的汙染物(例如,粉塵與氮氧化物、硫氧化物等酸性氣體)者。 In order to solve the above problems, the present invention provides an exhaust gas treatment device for the glass industry, which can effectively remove pollutants in the exhaust gas (for example, acid gases such as dust, nitrogen oxides and sulfur oxides).

本創作另提供一種玻璃業之廢氣處理裝置,具有較簡化之構件,因而可以降低其設置成本者。 The present invention further provides an exhaust gas treatment device for the glass industry, which has a simplified component and thus can reduce the installation cost.

本創作的一種玻璃業之廢氣處理裝置,係包含:一窯爐,內部具有一燃燒室;一陶纖過濾器,以一第一排氣管連通該窯爐之燃燒室,該陶纖過濾器包含至少一陶纖濾管,該至少一陶纖濾管由數個陶瓷纖維及數個脫硝觸媒顆粒所共同形成,該數個脫硝觸媒顆粒附著於該數個陶瓷纖維的表面,該第一排氣管具有一脫硝劑投入口及一脫硫劑投入口;及一煙囪,以一第二排氣管連通該陶纖過濾器;如此,本創作之玻璃業之廢氣處 理裝置可以藉由附著於該數個陶瓷纖維的表面之數個脫硝觸媒顆粒,不僅可以有效去除廢氣中的粉塵與酸性氣體等污染物,更可以免除複雜的脫硫件與脫硝件的設置,而降低該玻璃業之廢氣處理裝置的設置成本,為本創作之功效。 The invention relates to a glass industry exhaust gas treatment device, comprising: a kiln having a combustion chamber therein; a ceramic fiber filter connected to the combustion chamber of the kiln by a first exhaust pipe, the ceramic fiber filter The method comprises at least one ceramic fiber filter tube, wherein the at least one ceramic fiber filter tube is formed by a plurality of ceramic fibers and a plurality of denitration catalyst particles, and the plurality of denitration catalyst particles are attached to the surface of the plurality of ceramic fibers. The first exhaust pipe has a denitration agent input port and a desulfurization agent input port; and a chimney is connected to the ceramic fiber filter by a second exhaust pipe; thus, the waste gas of the glass industry of the present invention The device can not only effectively remove dust and acid gas and other pollutants in the exhaust gas by means of several denitration catalyst particles attached to the surface of the plurality of ceramic fibers, but also eliminate complicated desulfurization parts and denitration parts. The setting, while reducing the installation cost of the exhaust gas treatment device of the glass industry, is the effect of the creation.

本創作的一種玻璃業之廢氣處理裝置中,該玻璃業之廢氣處理裝置包含一第一熱交換器及一第二熱交換器,該第一熱交換器設於該第一排氣管,該第二熱交換器設於該第二排氣管,如此可以回收該高溫廢氣與高溫淨氣中的熱氣,達到能源回收再利用之功效。 In an exhaust gas treatment device of the glass industry, the waste gas treatment device of the glass industry comprises a first heat exchanger and a second heat exchanger, and the first heat exchanger is disposed on the first exhaust pipe, The second heat exchanger is disposed in the second exhaust pipe, so that the hot gas in the high-temperature exhaust gas and the high-temperature clean air can be recovered, thereby achieving the effect of energy recovery and reuse.

本創作的一種玻璃業之廢氣處理裝置中,該脫硫劑投入口位於該脫硝劑投入口及該陶纖過濾器之間,或者該脫硝劑投入口位於該脫硫劑投入口及該陶纖過濾器之間,如此工者可以依據需求選擇該脫硝投入口及該脫硫投入口的設置位置,使本創作之玻璃業之廢氣處理裝置具有較佳的設置變化可能性。 In the glass gas exhaust gas treatment device of the present invention, the desulfurizing agent input port is located between the denitration agent input port and the ceramic fiber filter, or the denitration agent input port is located at the desulfurizing agent input port and the Between the ceramic fiber filters, the worker can select the denitration input port and the setting position of the desulfurization input port according to the requirements, so that the waste gas treatment device of the glass industry of the present invention has a better possibility of setting changes.

〔本創作〕 [this creation]

1‧‧‧窯爐 1‧‧‧Kilns

11‧‧‧燃燒室 11‧‧‧ combustion chamber

2‧‧‧陶纖過濾器 2‧‧‧Ceramic fiber filter

21‧‧‧陶纖濾管 21‧‧‧Ceramic fiber filter tube

211‧‧‧陶瓷纖維 211‧‧‧Ceramic fiber

212‧‧‧脫硝觸媒顆粒 212‧‧‧Denitration catalyst particles

3‧‧‧煙囪 3‧‧‧ chimney

H1‧‧‧第一熱交換器 H1‧‧‧ first heat exchanger

H2‧‧‧第二熱交換器 H2‧‧‧ second heat exchanger

W1‧‧‧第一排氣管 W1‧‧‧first exhaust pipe

W2‧‧‧第二排氣管 W2‧‧‧Second exhaust pipe

O1‧‧‧脫硝劑投入口 O1‧‧‧Denitration agent input

O2‧‧‧脫硫劑投入口 O2‧‧‧desulfurizer input

〔習知〕 [study]

9‧‧‧習知玻璃業之廢氣處理裝置 9‧‧‧The exhaust gas treatment device of the glass industry

91‧‧‧窯爐 91‧‧‧Kilns

911‧‧‧燃燒室 911‧‧‧ combustion chamber

92‧‧‧電除塵器 92‧‧‧Electric precipitator

93‧‧‧脫硝件 93‧‧‧Denitration parts

931‧‧‧脫硝空間 931‧‧‧Denitration space

932‧‧‧脫硝劑投入口 932‧‧‧Denitration input

94‧‧‧脫硫件 94‧‧‧Desulfurization parts

941‧‧‧脫硫空間 941‧‧‧desulfurization space

942‧‧‧脫硫劑投入口 942‧‧‧Desulfurizer input

95‧‧‧集塵袋 95‧‧‧ dust bag

96‧‧‧煙囪 96‧‧‧ chimney

第1圖:係習知玻璃業之廢氣處理裝置的示意圖。 Fig. 1 is a schematic view of an exhaust gas treatment device of the conventional glass industry.

第2圖:係本創作一實施例玻璃業之廢氣處理裝置的示意圖。 Fig. 2 is a schematic view showing an exhaust gas treating apparatus of a glass industry according to an embodiment of the present invention.

第3圖:係第2圖之玻璃業之廢氣處理裝置的陶纖濾管之側視剖面圖。 Fig. 3 is a side cross-sectional view showing the ceramic fiber filter of the exhaust gas treatment device of the glass industry of Fig. 2.

為讓本創作之上述及其他目的、特徵及優點能更明顯易懂,下文特舉本創作之較佳實施例,並配合所附圖式,作詳細說明如下:請參照第2圖所示,本創作一實施例的玻璃業之廢氣處理裝置係可以包含:一窯爐1、一陶纖過濾器2及一煙囪3,該窯爐1以一第一排氣管W1連通該陶纖過濾器2,該陶纖過濾器2以一第二排氣管W2連通該煙囪3。 In order to make the above and other objects, features and advantages of the present invention more comprehensible, the preferred embodiments of the present invention will be described in detail below with reference to the accompanying drawings. The exhaust gas treatment device of the glass industry according to an embodiment of the present invention may include: a kiln 1, a ceramic fiber filter 2, and a chimney 3, the kiln 1 is connected to the ceramic fiber filter by a first exhaust pipe W1. 2. The ceramic fiber filter 2 is connected to the chimney 3 by a second exhaust pipe W2.

詳而言之,該窯爐1具有一燃燒室11,工者係可以將玻璃原料(例如,矽砂、碳酸鈣、碳酸鈉等)置於該燃燒室11中,並使該玻璃原料於約為800℃之高溫下熔融形成融漿,以進一步用以成形玻璃成品。 In detail, the kiln 1 has a combustion chamber 11, and a worker can place a glass raw material (for example, cerium, calcium carbonate, sodium carbonate, etc.) in the combustion chamber 11, and make the glass raw material The molten slurry is melted at a high temperature of 800 ° C to further form a finished glass product.

該玻璃原料高溫熔融所產生的廢氣可以經由該第一排氣管W1流向該陶纖過濾器2。於本實施例中,該玻璃業之廢氣處理裝置較佳可以包含一第一熱交換器H1,該第一熱交換器H1設於該第一排氣管W1,以將該廢氣的溫度降低至約為380℃,使該廢氣可以於適當之溫度下進入該陶纖過濾器2,不僅可以維持該陶纖過濾器2的良好過濾效果,並能夠避免過高的溫度(例如,380℃以上的溫度)對該陶纖過濾器2之脫硝觸媒顆粒212造成效能的減低或失效(詳如下述)。 The exhaust gas generated by the high-temperature melting of the glass raw material can flow to the ceramic fiber filter 2 via the first exhaust pipe W1. In this embodiment, the exhaust gas treatment device of the glass industry preferably includes a first heat exchanger H1 disposed on the first exhaust pipe W1 to reduce the temperature of the exhaust gas to At about 380 ° C, the exhaust gas can enter the ceramic fiber filter 2 at a suitable temperature, not only can maintain the good filtration effect of the ceramic fiber filter 2, but also can avoid excessive temperature (for example, above 380 ° C) The temperature) causes a decrease in the effectiveness or failure of the denitration catalyst particles 212 of the ceramic fiber filter 2 (described in detail below).

又,該第一排氣管W1可以具有一脫硝劑投入口O1及一脫硫劑投入口O2,該脫硝劑投入口O1及該脫硫劑投入口O2均位於該窯爐1及該陶纖過濾器2之間,且分別用以供工者將一脫硝劑(例如,氨氣、液態氨、氨水或尿素等氨基還原劑)及一脫硫劑(例如,消石灰、碳酸氫鈉及氫氧化鈉等鹼劑)投入該第一排氣管W1中,且被投入該第一排氣管W1中的脫硝劑及脫硫劑則可以受到該廢氣的帶動,沿該第一排氣管W1流向該陶纖過濾器2。於本實施例中,該脫硫劑投入口O2位於該脫硝劑投入口O1及該陶纖過濾器2之間,惟本創作具有通常知識者亦可以視需求將該脫硝劑投入口O1設置於該脫硫劑投入口O2及該陶纖過濾器2之間,於此不加以限制。 Moreover, the first exhaust pipe W1 may have a denitration agent inlet O1 and a desulfurizer inlet O2, and the denitration agent inlet O1 and the desulfurizer inlet O2 are located in the furnace 1 and the Between the ceramic fiber filters 2, and respectively for the workers to use a denitrification agent (for example, ammonia, liquid ammonia, ammonia or urea and other amino reducing agents) and a desulfurizing agent (for example, slaked lime, sodium bicarbonate And an alkali agent such as sodium hydroxide) is introduced into the first exhaust pipe W1, and the denitration agent and the desulfurizing agent charged into the first exhaust pipe W1 can be driven by the exhaust gas along the first row The gas pipe W1 flows to the ceramic fiber filter 2. In the present embodiment, the desulfurizer input port O2 is located between the denitration agent input port O1 and the ceramic fiber filter 2, but the person having the usual knowledge can also put the denitration agent into the mouth O1 as needed. It is provided between the desulfurizer input port O2 and the ceramic fiber filter 2, and is not limited thereto.

請參照第2、3圖所示,該陶纖過濾器2可以包含至少一陶纖濾管21,該陶纖濾管21係由數個陶瓷纖維211及數個脫硝觸媒顆粒212所共同形成,該數個脫硝觸媒顆粒212附著於該數個陶瓷纖維211的表面,使該數個脫硝觸媒顆粒212可以均勻分布於該陶纖濾管21,提升該數個脫硝觸媒顆粒212與該廢氣的接觸面積。 Referring to FIGS. 2 and 3, the ceramic fiber filter 2 may include at least one ceramic fiber filter tube 21, which is composed of a plurality of ceramic fibers 211 and a plurality of denitration catalyst particles 212. Forming, the plurality of denitration catalyst particles 212 are attached to the surface of the plurality of ceramic fibers 211, so that the plurality of denitration catalyst particles 212 can be evenly distributed on the ceramic fiber filter tube 21 to enhance the plurality of denitration touches. The contact area of the media particles 212 with the exhaust gas.

如此,該陶纖濾管21除了可以過濾去除該廢氣中的粉塵之外,該廢氣中的氮氧化物可以在該脫硝劑及該脫硝觸媒顆粒212的作用下,以選擇性催化還原法(SCR)轉化為無毒且可以直接排放至大氣中的氮氣,而該廢氣中的硫氧化物則可以在該脫硫劑的作用下轉化為固態的硫酸鈣或石膏(二水合硫酸鈣),並被該陶纖濾管21所過濾去除,因而在該陶纖過濾器2、經該脫硝劑投入口O1投入之脫硝劑與經該脫硫劑投入口O2投入之脫硫劑的共同作用之下,該廢氣中的汙染物(例如,粉塵、氮氧化物及硫氧化物)即可以被有效率地去除,並能夠形成一淨氣並經由該第二排氣管W2流向該煙囪3。 In this way, in addition to filtering and removing dust in the exhaust gas, the nitrogen oxides in the exhaust gas can be selectively catalytically reduced by the denitration agent and the denitration catalyst particles 212. The method (SCR) is converted into nitrogen which is non-toxic and can be directly discharged into the atmosphere, and the sulfur oxides in the exhaust gas can be converted into solid calcium sulfate or gypsum (calcium sulfate dihydrate) under the action of the desulfurizing agent. And the ceramic fiber filter 21 is filtered and removed, and the denitration agent which is supplied through the denitration agent inlet O1 and the desulfurizing agent which is supplied through the desulfurization agent inlet O2 are collectively used in the ceramic fiber filter 2. Under the action, the pollutants in the exhaust gas (for example, dust, nitrogen oxides and sulfur oxides) can be efficiently removed, and can form a clean gas and flow to the chimney via the second exhaust pipe W2. .

再請參照第2圖所示,該淨氣可以直接經由一第二排氣管W2流向該煙囪3,而排放至大氣中;惟由於經由該陶纖過濾器2過濾的空氣的溫度約為330℃,因而於本實施例中,該玻璃業之廢氣處理裝包含一第二熱交換器H2,該第二熱交換器H2設於該第二排氣管W2,以進一步降低該淨氣的溫度,如此可以進一步對該淨氣所攜帶之熱能進行回收,而可以提升熱能的回收效率。 Referring again to FIG. 2, the clean gas can be directly discharged to the atmosphere through a second exhaust pipe W2, and discharged to the atmosphere; however, since the temperature of the air filtered through the ceramic fiber filter 2 is about 330. °C, in this embodiment, the exhaust gas treatment package of the glass industry comprises a second heat exchanger H2, and the second heat exchanger H2 is disposed in the second exhaust pipe W2 to further reduce the temperature of the clean gas. Therefore, the heat energy carried by the clean gas can be further recovered, and the recovery efficiency of the heat energy can be improved.

綜合上述,本創作之玻璃業之廢氣處理裝置中,藉由該陶纖過濾器的設置,可以有效過濾清除玻璃原料高溫熔融所產生的廢氣中的粉塵,並藉由該脫硝劑投入口與附著於該數個陶瓷纖維的表面之數個脫硝觸媒顆粒的設置,可以有效將該廢氣中的氮氧化物轉化為無毒且可以直接排放至大氣中的氮氣,同時藉由該脫硫劑投入口與該陶纖過濾器的設置,可以有效將該廢氣中的硫氧化物轉化固態且可以輕易被過濾去除的硫酸鈣或石膏,如此即可以有效率地去除該廢氣中的粉塵與酸性氣體等污染物,為本創作之功效。 In summary, in the waste gas treatment device of the glass industry of the present invention, the setting of the ceramic fiber filter can effectively filter and remove the dust in the exhaust gas generated by the high-temperature melting of the glass raw material, and the denitration agent is put into the mouth. The plurality of denitration catalyst particles attached to the surface of the plurality of ceramic fibers can effectively convert the nitrogen oxides in the exhaust gas into nitrogen gas which is non-toxic and can be directly discharged to the atmosphere, and the desulfurizing agent is simultaneously The inlet and the ceramic fiber filter can effectively convert the sulfur oxides in the exhaust gas into solid calcium sulfate or gypsum which can be easily removed by filtration, so that the dust and acid gas in the exhaust gas can be efficiently removed. Contaminants are the efficacy of this creation.

再者,本創作之玻璃業之廢氣處理裝置中,僅需要於該第一排氣管設有該脫硝劑投入口及該脫硫劑投入口,及於該數個陶瓷纖維的表 面附著有該數個脫硝觸媒顆粒,即可以有效率地去除該廢氣中的酸性氣體,可以免除習知玻璃業之廢氣處理裝置中複雜的脫硫件與脫硝件的設置,如此可以達成簡化裝置及降低裝置設置成本等功效。 Furthermore, in the exhaust gas treatment device of the glass industry of the present invention, it is only necessary to provide the denitration agent input port and the desulfurization agent input port in the first exhaust pipe, and the table of the plurality of ceramic fibers. The plurality of denitration catalyst particles are attached to the surface, so that the acid gas in the exhaust gas can be efficiently removed, and the complicated desulfurization and denitration components in the exhaust gas treatment device of the conventional glass industry can be eliminated. Achieve simplification of the device and reduce the cost of device setup.

此外,本創作之玻璃業之廢氣處理裝置,更可以藉由該第一熱交換器及該第二熱交換器的設置,回收該廢氣與該淨氣中的熱能,降低熱能逸散造成的能源浪費,進一步可以達到能源回收再利用之功效。 In addition, the waste gas treatment device of the glass industry of the present invention can further recover the heat energy of the exhaust gas and the clean gas by the arrangement of the first heat exchanger and the second heat exchanger, thereby reducing energy generated by heat dissipation. Waste can further achieve the effect of energy recycling.

雖然本創作已利用上述較佳實施例揭示,然其並非用以限定本創作,任何熟習此技藝者在不脫離本創作之精神和範圍之內,相對上述實施例進行各種更動與修改仍屬本創作所保護之技術範疇,因此本創作之保護範圍當視後附之申請專利範圍所界定者為準。 Although the present invention has been disclosed by the above-described preferred embodiments, it is not intended to limit the present invention, and it is still within the spirit and scope of the present invention to make various changes and modifications to the above embodiments. The technical scope of the protection is created, so the scope of protection of this creation is subject to the definition of the patent application scope attached.

1‧‧‧窯爐 1‧‧‧Kilns

11‧‧‧燃燒室 11‧‧‧ combustion chamber

2‧‧‧陶纖過濾器 2‧‧‧Ceramic fiber filter

21‧‧‧陶纖濾管 21‧‧‧Ceramic fiber filter tube

3‧‧‧煙囪 3‧‧‧ chimney

H1‧‧‧第一熱交換器 H1‧‧‧ first heat exchanger

H2‧‧‧第二熱交換器 H2‧‧‧ second heat exchanger

W1‧‧‧第一排氣管 W1‧‧‧first exhaust pipe

W2‧‧‧第二排氣管 W2‧‧‧Second exhaust pipe

O1‧‧‧脫硝劑投入口 O1‧‧‧Denitration agent input

O2‧‧‧脫硫劑投入口 O2‧‧‧desulfurizer input

Claims (5)

一種玻璃業之廢氣處理裝置,包含:一窯爐,內部具有一燃燒室;一陶纖過濾器,以一第一排氣管連通該窯爐之燃燒室,該陶纖過濾器包含至少一陶纖濾管,該至少一陶纖濾管由數個陶瓷纖維及數個脫硝觸媒顆粒所共同形成,該數個脫硝觸媒顆粒附著於該數個陶瓷纖維的表面,該第一排氣管具有一脫硝劑投入口及一脫硫劑投入口,該脫硝劑投入口及該脫硫劑投入口均位於該窯爐及該陶纖過濾器之間;及一煙囪,以一第二排氣管連通該陶纖過濾器。 An exhaust gas treatment device for a glass industry, comprising: a kiln having a combustion chamber therein; a ceramic fiber filter connected to the combustion chamber of the kiln by a first exhaust pipe, the ceramic fiber filter comprising at least one ceramic a fiber filter tube, the at least one ceramic fiber filter tube is formed by a plurality of ceramic fibers and a plurality of denitration catalyst particles, and the plurality of denitration catalyst particles are attached to the surface of the plurality of ceramic fibers, the first row The gas pipe has a denitration agent input port and a desulfurization agent input port, the denitration agent input port and the desulfurizer input port are located between the furnace and the ceramic fiber filter; and a chimney, A second exhaust pipe communicates with the ceramic fiber filter. 如申請專利範圍第1項所述之玻璃業之廢氣處理裝置,其中,該玻璃業之廢氣處理裝置包含一第一熱交換器,該第一熱交換器設於該第一排氣管。 The waste gas treatment device of the glass industry according to claim 1, wherein the waste gas treatment device of the glass industry comprises a first heat exchanger, and the first heat exchanger is disposed in the first exhaust pipe. 如申請專利範圍第1項所述之玻璃業之廢氣處理裝置,其中,該玻璃業之廢氣處理裝置包含一第二熱交換器,該第二熱交換器設於該第二排氣管。 The waste gas treatment device of the glass industry according to claim 1, wherein the waste gas treatment device of the glass industry comprises a second heat exchanger, and the second heat exchanger is disposed in the second exhaust pipe. 如申請專利範圍第1項所述之玻璃業之廢氣處理裝置,其中,該脫硫劑投入口位於該脫硝劑投入口及該陶纖過濾器之間。 The waste gas treatment device of the glass industry according to claim 1, wherein the desulfurization agent inlet is located between the denitration agent inlet and the ceramic fiber filter. 如申請專利範圍第1項所述之玻璃業之廢氣處理裝置,其中,該脫硝劑投入口位於該脫硫劑投入口及該陶纖過濾器之間。 The waste gas treatment device of the glass industry according to the first aspect of the invention, wherein the denitration agent inlet is located between the desulfurizer input port and the ceramic fiber filter.
TW106200102U 2017-01-04 2017-01-04 Exhaust gas treatment device for glass industry TWM539982U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
TW106200102U TWM539982U (en) 2017-01-04 2017-01-04 Exhaust gas treatment device for glass industry

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
TW106200102U TWM539982U (en) 2017-01-04 2017-01-04 Exhaust gas treatment device for glass industry

Publications (1)

Publication Number Publication Date
TWM539982U true TWM539982U (en) 2017-04-21

Family

ID=59254496

Family Applications (1)

Application Number Title Priority Date Filing Date
TW106200102U TWM539982U (en) 2017-01-04 2017-01-04 Exhaust gas treatment device for glass industry

Country Status (1)

Country Link
TW (1) TWM539982U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111623360A (en) * 2020-05-28 2020-09-04 瑞必科净化设备(上海)有限公司 Biogas factory tail gas treatment system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111623360A (en) * 2020-05-28 2020-09-04 瑞必科净化设备(上海)有限公司 Biogas factory tail gas treatment system

Similar Documents

Publication Publication Date Title
RU2484883C2 (en) Flue gas cleaner
CN102921297A (en) SCR denitrification device for dedusting smoke of cement kiln at high temperature
KR101841019B1 (en) A flue gas treatment system for simultaneous treatment of fine dust and harmful gas generated from incineration power plant
CN110252051B (en) Method for dedusting, desulfurizing and denitrating boiler flue gas and removing dioxin
CN105705218A (en) Method for cleaning bypass gases of the cement or mineral industry, and system of the cement or mineral industry
JP2014171986A (en) Method for recovering mercury in exhaust gas
KR100965912B1 (en) Method for operating purification system of an incinerator exhaust gas
CN107469595A (en) A kind of dust removal integrated device and method of waste gas of industrial kiln and furnace desulphurization denitration
JP2013173106A (en) Method and device for recovering mercury in exhaust gas
CN205412681U (en) Tail gas desulfurization , denitration, dust removal integration treatment device
KR100711940B1 (en) Wet scrubbing unit for a exhausted gas purifying device
CN106123613A (en) A kind of glass furnace cigarette advanced purification process
CN110864561A (en) Tail gas purification process method and device for titanium dioxide calcining kiln adopting sulfuric acid method
CN110484283A (en) A kind of coking residual heat integrative recovery process and system
CN113842761A (en) Garbage tail gas treatment system and method
CN110437849A (en) Dry coke quenching and coke oven flue gas combined purifying technique and system
TWM539982U (en) Exhaust gas treatment device for glass industry
CN105233604A (en) Purification device for conducting flue gas desulfurization and dedusting on brick and tile kiln
CN210278800U (en) Low-temperature catalyst denitration dust removal equipment with pottery fine filter tube
CN115945061A (en) Integration denitration desulfurization dust pelletizing system
CN217431221U (en) Water dust removal device for active lime digestion
CN211177990U (en) Kiln tail gas cleanup unit is calcined to sulfuric acid process titanium dioxide
CN211120700U (en) Useless regeneration utilization processing system of aluminium oxide class industry solid useless danger
CN212523640U (en) Metal sludge sintering flue gas treatment system
CN211585689U (en) Industrial kiln furnace gas purification system