TWM594994U - Hypergravity dust-removing, desulfurizing, and denitrifying apparatus - Google Patents

Hypergravity dust-removing, desulfurizing, and denitrifying apparatus Download PDF

Info

Publication number
TWM594994U
TWM594994U TW108217458U TW108217458U TWM594994U TW M594994 U TWM594994 U TW M594994U TW 108217458 U TW108217458 U TW 108217458U TW 108217458 U TW108217458 U TW 108217458U TW M594994 U TWM594994 U TW M594994U
Authority
TW
Taiwan
Prior art keywords
liquid
super
desulfurization
gravity
dust removal
Prior art date
Application number
TW108217458U
Other languages
Chinese (zh)
Inventor
彭兆盟
Original Assignee
智和股份有限公司
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 智和股份有限公司 filed Critical 智和股份有限公司
Priority to TW108217458U priority Critical patent/TWM594994U/en
Publication of TWM594994U publication Critical patent/TWM594994U/en

Links

Images

Landscapes

  • Treating Waste Gases (AREA)

Abstract

一種超重力除塵脫硫脫硝之裝置,係包含有:一煙道氣入口管得與臭氧充分混合,以使低價氮氧化成高價氮使其更好吸收,其後以風機經氣體入口送入多棒定子單旋轉超重力轉床;一儲液箱內部容置有稀釋液碱,其後以水泵經液體入口送入多棒定子單旋轉超重力轉床;三機一體的多棒定子單旋轉超重力轉床其多棒之定子為固定,而轉子得經由動力裝置帶動得以高速轉動,進而得以使氣、液充分混合切割成微米液滴,以使傳質效率大幅提升,再配合液碱吸收劑,得以達成除塵、脫硫、脫硝及排放氣體符合排放標準,有效保護環境安全及確保人體健康者。 An ultra-gravity dust removal, desulfurization and denitrification device includes: a flue gas inlet pipe must be fully mixed with ozone to oxidize low-priced nitrogen into high-priced nitrogen for better absorption, and then sent through a gas inlet with a fan Single-rotor super-gravity rotating bed with multi-rod stator; a liquid storage tank contains diluent alkali, and then fed into the multi-rod stator single-rotating super-gravity rotary bed with a water pump through the liquid inlet; The multi-rod stator of the rotating supergravity rotating bed is fixed, and the rotor must be driven by the power device to rotate at high speed, which can fully mix the gas and liquid and cut into micron droplets, so that the mass transfer efficiency is greatly improved, and then combined with liquid alkali Absorbent can achieve dust removal, desulfurization, denitration and exhaust gas compliance with emission standards, effectively protect environmental safety and ensure human health.

Description

超重力除塵脫硫脫硝之裝置 Super gravity dust removal, desulfurization and denitrification device

本創作提供一種除塵脫硫脫硝之技術領域,尤指其技術上提供一種超重力除塵脫硫脫硝之裝置,其得以加入高傳質、體積小、處理量大的多棒定子單旋轉超重力轉床配合臭氧與液碱,使淨化後氣體符合排放標準。 This creation provides a technical field of dedusting, desulfurization and denitrification, in particular, it technically provides a device for super-gravity desulfurization, desulfurization and denitration, which allows the addition of a multi-bar stator single-rotation super The gravity rotating bed cooperates with ozone and liquid alkali to make the purified gas comply with emission standards.

按,鍋爐燃燒過程中產生的粉塵、SOx和NOx會對環境和人類造成嚴重的危害。隨著人們環保意識的加強,鍋爐煙道氣淨化要求日趨嚴苛。煤炭燃燒過程中,會產生大量的粉塵、SOx和NOx等污染物。SOx和NOx的排放不僅會引起酸雨酸霧,對人類及動植物都造成嚴重的危害,還會破壞臭氧層,引起全球變暖。粉塵中含有大量的重金屬與化學致癌物,會引起肺炎、肺癌及流感。工業鍋爐是除火電廠鍋爐以外的重要大氣污染物排放源。我國燃煤鍋爐量大面廣,這些鍋爐能源利用率低且污染嚴重,開發研究鍋爐的煙道氣淨化技術具有重要的環保意義。 According to the press, the dust, SOx and NOx generated in the boiler combustion process will cause serious harm to the environment and humans. With the strengthening of people's awareness of environmental protection, the requirements of boiler flue gas purification are becoming more and more stringent. During the combustion of coal, a lot of pollutants such as dust, SOx and NOx will be produced. SOx and NOx emissions will not only cause acid rain and acid mist, but also cause serious harm to humans, animals and plants, but also destroy the ozone layer and cause global warming. Dust contains large amounts of heavy metals and chemical carcinogens, which can cause pneumonia, lung cancer and flu. Industrial boilers are important sources of atmospheric pollutants except for thermal power plant boilers. The quantity of coal-fired boilers in my country is large and wide. These boilers have low energy efficiency and serious pollution. Therefore, the development and research of boiler flue gas purification technology has important environmental protection significance.

除塵、脫硫以及脫硝分段處理,將除塵裝置-噴淋除塵裝置或靜電除塵裝置、脫硫裝置-石灰石/石膏濕 法煙道氣脫硫(wet fluegas desulfurization,WFGD)和脫硝裝置一選擇性催化還原(selective catalytic reduction,SCR)串聯,達到除塵脫硫脫硝的目的。分步脫除技術污染物的脫除效率高,適用範圍廣,但存在占地面積大、運行成本高和操作條件要求苛刻等缺點。煙道氣同時除塵脫硫脫硝技術可分為濕法、半乾法和乾法3種類型。國內針對鍋爐的除塵脫硫脫硝一體化技術還無法做到經濟有效。有部分鍋爐使用濕法三機一體化技術進行除塵脫硫脫硝,該技術採用先氧化後吸收的方法,即採用強氧化劑如NaClO2、H2O2、KMnO4溶液和O3氣體等把低價態NOx氧化為高價態NOx,然後採用液鹼吸收,從而實現煙道氣的同時除塵脫硫脫硝。濕法一體化技術適用範圍寬、操作簡單、投資成本相對較低,特別適用於中小鍋爐煙道氣淨化。但是,由於該煙道氣淨化技術通常採用傳統洗滌塔設備,導致傳質效率低,污染物脫除率也相對較低。 Dust removal, desulfurization and denitrification staged treatment, the dust removal device-spray dust removal device or electrostatic dust removal device, desulfurization device-limestone/gypsum wet flue gas desulfurization (wet fluegas desulfurization, WFGD) and denitration device one Selective catalytic reduction (SCR) is connected in series to achieve the purpose of dust removal, desulfurization and denitrification. The step removal technology has high removal efficiency of pollutants and a wide range of application, but it has the disadvantages of large area, high operating cost and demanding operating conditions. Flue gas dedusting, desulfurization and denitrification technologies can be divided into three types: wet method, semi-dry method and dry method. Domestic integrated technology for boiler dust removal, desulfurization and denitration has not yet been economically effective. Some boilers use the wet three-machine integrated technology for dust removal, desulfurization and denitrification. This technology uses the method of oxidation before absorption, that is, using strong oxidants such as NaClO 2 , H 2 O 2 , KMnO 4 solution and O 3 gas. The low-valence NOx is oxidized to the high-valence NOx, and then absorbed by liquid alkali, so as to realize the dust removal, desulfurization and denitrification of flue gas at the same time. The wet process integration technology has a wide application range, simple operation, and relatively low investment cost, and is particularly suitable for the purification of small and medium boiler flue gas. However, because the flue gas purification technology usually uses traditional scrubber equipment, the mass transfer efficiency is low and the pollutant removal rate is relatively low.

是以,針對上述習知結構所存在之問題點,如何開發一種更具理想實用性之創新結構,實消費者所殷切企盼,亦係相關業者須努力研發突破之目標及方向。 Therefore, how to develop a more ideal and practical innovative structure in response to the problems of the above-mentioned conventional structure is what consumers are eagerly expecting, and it is also the goal and direction of the relevant industry to work hard to develop breakthroughs.

有鑑於此,創作人本於多年從事相關產品之製造開發與設計經驗,針對上述之目標,詳加設計與審慎評估後,終得一確具實用性之本創作。 In view of this, the creator has many years of experience in the manufacturing development and design of related products. In view of the above goals, after detailed design and careful evaluation, he finally has a practical original creation.

本創作之主要目的在於提供一種超重力除塵脫硫脫硝之裝置,其得以加入臭氧使低價氮氧化成高價氮,再利用高傳質、體積小、處理量大的多棒定子單旋轉超重力轉床配合液碱吸收劑,使淨化後氣體符合排放標準者。 The main purpose of this creation is to provide a device for supergravity dust removal, desulfurization and denitrification, which can add ozone to oxidize low-valent nitrogen to high-valent nitrogen, and then use the multi-rod stator single-rotation ultra-high mass transfer, small volume and large processing capacity. Gravity rotating bed combined with liquid alkali absorbent to make the purified gas meet the emission standards.

為達上述目的,本創作提供一種超重力除塵脫硫脫硝之裝置,係包含有:一煙道氣入口管得與臭氧充分混合,以使低價氮氧化成高價氮,其後以風機經氣體入口送入多棒定子單旋轉超重力轉床;一儲液箱內部容置有稀釋液碱,其後以水泵經液體入口送入多棒定子單旋轉超重力轉床,三機一體的多棒定子單旋轉超重力轉床多棒之定子為固定,而轉子得經由動力裝置帶動得以高速轉動,進而得以氣、液充分混合切割成微米液滴,以使傳質效率大幅提升,配合稀釋液碱吸收劑微米液滴高傳質的吸收效果,來達成除塵、脫硫及脫硝(脫氮,因氮與水產生硝)效果,讓排放的氣體符合排放標準,對污染物的處理效果更好、臭氧利用率更高,且設備體積小、成本較洗滌塔低、處理量大等特點,有效保護環境安全及確保人體健康者。 In order to achieve the above purpose, this creation provides a device for degraving, desulfurization and denitrification by super-gravity, which includes: a flue gas inlet pipe must be fully mixed with ozone to oxidize low-priced nitrogen into high-priced nitrogen, and then a fan The gas inlet is fed into the multi-rod stator single-rotation super-gravity rotating bed; a liquid storage tank contains the diluent alkali, and then it is sent to the multi-rod stator single-rotation super-gravity rotating bed through the liquid inlet through a liquid pump. The stator of the single-rotor super-gravity rotary bed with multiple rods is fixed, and the rotor must be driven by the power device to rotate at high speed, so that the gas and liquid can be fully mixed and cut into micron droplets, so that the mass transfer efficiency is greatly improved. The high mass transfer absorption effect of the alkali absorbent micron droplets achieves the effects of dust removal, desulfurization and denitrification (denitrification, which produces nitrate due to nitrogen and water), so that the discharged gas meets the emission standards, and the treatment effect of pollutants is more Good, higher ozone utilization rate, small size of equipment, lower cost than washing tower, large processing capacity, etc., effectively protect environmental safety and ensure human health.

有關本創作所採用之技術、手段及其功效,茲舉一較佳實施例並配合圖式詳細說明於後,相信本創作上述之目的、構造及特徵,當可由之得一深入而具體的瞭解。 Regarding the techniques, methods and functions used in this creation, I will give a preferred embodiment and detailed descriptions in conjunction with the drawings. I believe that the above-mentioned purposes, structures and features of this creation can be obtained from an in-depth and specific understanding .

10‧‧‧煙道氣入口管 10‧‧‧ flue gas inlet pipe

11‧‧‧臭氧入口管 11‧‧‧Ozone inlet pipe

111‧‧‧第一流量計 111‧‧‧ First flow meter

112‧‧‧第一閥門 112‧‧‧ First valve

12‧‧‧風機 12‧‧‧Fan

13‧‧‧第一管路 13‧‧‧ First pipeline

14‧‧‧第二流量計 14‧‧‧Second flow meter

15‧‧‧第二管路 15‧‧‧Second pipeline

16‧‧‧進口取樣裝置 16‧‧‧Imported sampling device

20‧‧‧多棒定子單旋轉超重力轉床 20‧‧‧Multi-bar stator single-rotation supergravity rotary bed

21‧‧‧氣體入口 21‧‧‧Gas inlet

22‧‧‧氣體出口 22‧‧‧ gas outlet

221‧‧‧氣體出口管 221‧‧‧Gas outlet pipe

222‧‧‧出口取樣裝置 222‧‧‧Export sampling device

23‧‧‧液體入口 23‧‧‧ liquid inlet

24‧‧‧液體出口 24‧‧‧Liquid outlet

25‧‧‧動力裝置 25‧‧‧Power plant

26‧‧‧轉子 26‧‧‧Rotor

30‧‧‧儲液箱 30‧‧‧Reservoir

31‧‧‧水泵 31‧‧‧Water pump

32‧‧‧第三管路 32‧‧‧Third pipeline

33‧‧‧第二閥門 33‧‧‧Second valve

34‧‧‧第三流量計 34‧‧‧The third flowmeter

第一圖係本創作其一實施例之流程圖。 The first figure is a flow chart of one embodiment of the author.

第二圖係本創作其一實施例之多棒定子單旋轉超重力轉床平面剖示圖。 The second figure is a plan cross-sectional view of a multi-rod stator single-rotation supergravity rotary bed of an embodiment of the present invention.

本創作係提供一種超重力除塵脫硫脫硝之裝置之設計者。 This creation provides the designer of a device for super gravity dust removal, desulfurization and denitrification.

為使貴審查委員對本創作之目的、特徵及功效能夠有更進一步之瞭解與認識,茲配合實施方式及圖式詳述如後: In order to enable your reviewing committee to have a better understanding and understanding of the purpose, features and functions of this creation, we hereby cooperate with the implementation mode and the detailed drawings as follows:

參閱第一至第二圖所示,本創作提供一種超重力除塵脫硫脫硝之裝置,係包含有: Referring to the first to second figures, this creation provides a device for super-gravity dust removal, desulfurization and denitration, which includes:

一煙道氣入口管10; One flue gas inlet pipe 10;

一臭氧入口管11,前述臭氧入口管11連接一第一流量計111,再連接一第一閥門112,其後與前述煙道氣入口管10導通連接,前述煙道氣入口管10再接至一風機12,其後前述風機12以一第一管路13串接一第二流量計14; An ozone inlet pipe 11, the ozone inlet pipe 11 is connected to a first flow meter 111, and then connected to a first valve 112, and then connected to the flue gas inlet pipe 10, the flue gas inlet pipe 10 is then connected to A fan 12, and then the fan 12 is connected in series with a second flowmeter 14 through a first pipeline 13;

一多棒定子單旋轉超重力轉床20,設有氣體入口21、氣體出口22、液體入口23及液體出口24,前述多棒定子單旋轉超重力轉床20得由一動力裝置25帶動轉子26進行高速旋轉;一第二管路15連接前述第二流量計14 與前述氣體入口21;以及 A multi-rod stator single-rotation super-gravity rotary bed 20 is provided with a gas inlet 21, a gas outlet 22, a liquid inlet 23 and a liquid outlet 24. The aforementioned multi-rod stator single-rotation super-gravity rotary bed 20 is driven by a power device 25 to drive the rotor 26 Perform high-speed rotation; a second pipeline 15 is connected to the aforementioned second flowmeter 14 With the aforementioned gas inlet 21; and

一儲液箱30,用以儲存25~34%濃度的液碱(NaOH),一水泵31以負壓抽取前述儲液箱30內的液碱(NaOH),一第三管路32連接前述水泵31與一第二閥門33及一第三流量計34,其後前述第三管路32連接至前述液體入口23。 A liquid storage tank 30 for storing liquid alkali (NaOH) with a concentration of 25 to 34%, a water pump 31 to extract the liquid alkali (NaOH) in the liquid storage tank 30 with a negative pressure, and a third pipeline 32 connected to the water pump 31 and a second valve 33 and a third flow meter 34, and then the third pipe 32 is connected to the liquid inlet 23.

所述之超重力除塵脫硫脫硝之裝置,其中前述第二管路15上得設有一進口取樣裝置16。 In the super-gravity dust removal, desulfurization and denitrification device, an inlet sampling device 16 may be provided on the second pipeline 15.

所述之超重力除塵脫硫脫硝之裝置,其中前述氣體出口22得連接一氣體出口管221,前述氣體出口管221上得設有一出口取樣裝置222。 In the device for super-gravity dust removal, desulfurization and denitrification, the gas outlet 22 may be connected to a gas outlet pipe 221, and the gas outlet pipe 221 may be provided with an outlet sampling device 222.

參閱第一至第二圖所示,本創作提供一種超重力除塵脫硫脫硝之裝置,係包含有: Referring to the first to second figures, this creation provides a device for super-gravity dust removal, desulfurization and denitration, which includes:

以風機12形成負壓吸入煙道氣及臭氧,臭氧係經由一第一流量計111控制流量及第一閥門112控制啟閉的進入與煙道氣充分混合,並將低價態氮(NOx)氧化成為高價態氮(NOx),其後經由一第二流量計14控制流量的送入至多棒定子單旋轉超重力轉床20內; The fan 12 forms negative pressure to inhale the flue gas and ozone. The ozone is controlled by a first flow meter 111 to control the flow rate and the first valve 112 to control the opening and closing of the inlet and fully mixed with the flue gas, and the low price nitrogen (NOx) It is oxidized into high valence nitrogen (NOx), which is then fed into a multi-rod stator single-rotation supergravity rotating bed 20 through a second flow meter 14 to control the flow rate;

液碱(NaOH)以25~34%濃度送入至一儲液箱30,一水泵31形成負壓吸入液碱(NaOH)經一第二閥門33控制啟閉及一第三流量計34控制流量的送入至多棒定子單旋轉超重力轉床20內; Liquid alkali (NaOH) is sent to a storage tank 30 at a concentration of 25 to 34%, a water pump 31 forms a negative pressure suction liquid alkali (NaOH), which is controlled by a second valve 33 to open and close and a third flow meter 34 to control the flow Is fed into a single-rotor super-gravity rotary bed 20 with a multi-rod stator;

啟動多棒定子單旋轉超重力轉床20,將氣液充分混合切割成微米液滴,以使傳質效率大幅提升,並使氧化的氣體內塵、硫化物(SOx)、氮化物(NOx)得為液碱(NaOH)吸收,其後氣液分流,使其合於標準的氣體由氣體出口22送出,而其混合的液體則由液體出口24送出。 Start multi-rod stator single-rotation super-gravity rotary bed 20, fully mix and cut gas and liquid into micron droplets, so as to greatly improve the mass transfer efficiency, and make the oxidized gas dust, sulfide (SOx), nitride (NOx) It is absorbed by liquid alkali (NaOH), and then the gas-liquid shunt, so that the standard gas is sent from the gas outlet 22, and the mixed liquid is sent from the liquid outlet 24.

所述之超重力除塵脫硫脫硝之裝置,其中前述氣體出口22得接至一低溫電漿裝置,以其低溫電漿再降低氮化物的含量。 In the device for super-gravity dust removal, desulfurization and denitrification, the aforementioned gas outlet 22 may be connected to a low-temperature plasma device to reduce the content of nitride with its low-temperature plasma.

所述之超重力除塵脫硫脫硝之裝置,其中前述氣體出口22得接至一觸媒裝置,以其觸媒再降低氮化物的含量。 In the device for super-gravity dust removal, desulfurization and denitrification, the gas outlet 22 has to be connected to a catalyst device to reduce the content of nitride with its catalyst.

多棒定子單旋轉超重力轉床是新一代化工過程強化技術,可以極大的強化傳質和混合的效果。在超重力環境下,其傳質速率要比傳統的塔器高1至3個數量級。同時,多棒定子單旋轉超重力轉床具有體積小,傳質效率高、易於操作、設備投資小、物料的停留時間短,單台設備處理氣量最大可達3萬CMH,處理量大等優點,在納米材料、化工、環保和能源等領域都有十分廣闊的應用前景。多棒定子單旋轉超重力轉床的除塵脫硫脫硝效果,與傳統技術煙道氣處理的效果相差甚大。超重力除塵脫硫脫硝三機一體技術對污染物的處理效果更好,臭氧利用率更高,說明超重力技術在鍋爐煙道氣淨化方面有很好效果。本創 作的多棒定子單旋轉超重力轉床,對於粉塵脫除率可達90%以上,SOx脫除率為90%以上,NOx脫除率為接近70%,處理後煙道氣能達標排放。超重力除塵脫硫脫硝三機一體技術具有成本低、效率高、設備小和投資少等優點,在鍋爐煙道氣淨化效果極佳。 Multi-rod stator single-rotation supergravity rotary bed is a new generation of chemical process strengthening technology, which can greatly enhance the effect of mass transfer and mixing. In a hypergravity environment, the mass transfer rate is 1 to 3 orders of magnitude higher than traditional towers. At the same time, the multi-rod stator single-rotation super-gravity rotary bed has the advantages of small volume, high mass transfer efficiency, easy operation, small equipment investment, short residence time of materials, maximum gas processing capacity of a single device of up to 30,000 CMH, and large processing capacity. It has a very broad application prospect in the fields of nanomaterials, chemical industry, environmental protection and energy. The dust removal, desulfurization and denitrification effect of the multi-rod stator single-rotation super-gravity rotary bed is very different from the effect of traditional technology flue gas treatment. The three-in-one technology of supergravity dust removal, desulfurization and denitrification has better treatment effect on pollutants and higher ozone utilization rate, indicating that the supergravity technology has a good effect on the purification of boiler flue gas. Original The multi-rod stator single-rotation super-gravity rotating bed can achieve a dust removal rate of more than 90%, a SOx removal rate of more than 90%, and a NOx removal rate of nearly 70%. After treatment, the flue gas can reach the standard emission. The three-in-one technology of super-gravity dust removal, desulfurization and denitration has the advantages of low cost, high efficiency, small equipment and low investment, and has excellent purification effect in boiler flue gas.

由其上述可知,本創作之超重力除塵脫硫脫硝之裝置,確為業界首見而符合新型專利之新穎性要件者,而其全面性之創新設計,符合新型專利之進步性要件,而其得以加入臭氧使低價態氮氧化成為高價態氮,再利用高傳質、體積小、處理量大的多棒定子單旋轉超重力轉床配合液碱,使淨化後氣體符合排放標準,符合較佳之產業利用性者。 From the above, it can be seen that the super-gravity dust removal, desulfurization and denitrification device created in this book is indeed the first in the industry to meet the novelty requirements of new patents, and its comprehensive and innovative design meets the progressive requirements of new patents. It can add ozone to oxidize low-valence nitrogen into high-valence nitrogen, and then use multi-rod stator single-rotation super-gravity rotary bed with high mass transfer, small volume and large processing capacity combined with liquid alkali to make the purified gas comply with emission standards and meet Better industry utilization.

前文係針對本創作之較佳實施例為本創作之技術特徵進行具體之說明;惟,熟悉此項技術之人士當可在不脫離本創作之精神與原則下對本創作進行變更與修改,而該等變更與修改,皆應涵蓋於如下申請專利範圍所界定之範疇中。 The foregoing is a detailed description of the technical characteristics of this creation for the preferred embodiment of this creation; however, persons familiar with this technology may make changes and modifications to this creation without departing from the spirit and principles of this creation. Such changes and modifications should be covered in the scope defined by the scope of the patent application as follows.

綜上所述,本創作係提供一種超重力除塵脫硫脫硝之裝置,其確已達到本創作之所有目的,另其組合結構之空間型態未見於同類產品,亦未曾公開於申請前,已符合專利法之規定,爰依法提出申請。 In summary, this creation provides a device for super-gravity dust removal, desulfurization and denitrification, which has indeed achieved all the purposes of this creation. In addition, the spatial structure of its combined structure has not been seen in similar products, nor has it been disclosed before the application. Having complied with the provisions of the Patent Law, the application was submitted in accordance with the law.

10‧‧‧煙道氣入口管 10‧‧‧ flue gas inlet pipe

11‧‧‧臭氧入口管 11‧‧‧Ozone inlet pipe

111‧‧‧第一流量計 111‧‧‧ First flow meter

112‧‧‧第一閥門 112‧‧‧ First valve

12‧‧‧風機 12‧‧‧Fan

13‧‧‧第一管路 13‧‧‧ First pipeline

14‧‧‧第二流量計 14‧‧‧Second flow meter

15‧‧‧第二管路 15‧‧‧Second pipeline

16‧‧‧進口取樣裝置 16‧‧‧Imported sampling device

20‧‧‧多棒定子單旋轉超重力轉床 20‧‧‧Multi-bar stator single-rotation supergravity rotary bed

21‧‧‧氣體入口 21‧‧‧Gas inlet

22‧‧‧氣體出口 22‧‧‧ gas outlet

221‧‧‧氣體出口管 221‧‧‧Gas outlet pipe

222‧‧‧出口取樣裝置 222‧‧‧Export sampling device

23‧‧‧液體入口 23‧‧‧ liquid inlet

24‧‧‧液體出口 24‧‧‧Liquid outlet

25‧‧‧動力裝置 25‧‧‧Power plant

26‧‧‧轉子 26‧‧‧Rotor

30‧‧‧儲液箱 30‧‧‧Reservoir

31‧‧‧水泵 31‧‧‧Water pump

32‧‧‧第三管路 32‧‧‧Third pipeline

33‧‧‧第二閥門 33‧‧‧Second valve

34‧‧‧第三流量計 34‧‧‧The third flowmeter

Claims (3)

一種超重力除塵脫硫脫硝之裝置,包括: A device for super-gravity dust removal, desulfurization and denitrification, including: 一煙道氣入口管; A flue gas inlet pipe; 一臭氧入口管,前述臭氧入口管連接一第一流量計,再連接一第一閥門,其後與前述煙道氣入口管導通連接,前述煙道氣入口管再接至一風機,其後前述風機以一第一管路串接一第二流量計; An ozone inlet pipe, the ozone inlet pipe is connected to a first flow meter, and then connected to a first valve, and then connected to the flue gas inlet pipe, and the flue gas inlet pipe is connected to a fan, after which The fan is connected in series with a second flowmeter through a first pipeline; 一多棒定子單旋轉超重力轉床,設有氣體入口、氣體出口、液體入口及液體出口,前述多棒定子單旋轉超重力轉床得由一動力裝置帶動轉子進行高速旋轉;一第二管路連接前述第二流量計與前述氣體入口;以及 A multi-rod stator single-rotation super-gravity rotating bed is provided with a gas inlet, a gas outlet, a liquid inlet and a liquid outlet. The foregoing multi-rod stator single-rotation super-gravity rotating bed must be driven by a power device to rotate the rotor at high speed; a second tube Connect the aforementioned second flow meter to the aforementioned gas inlet; and 一儲液箱,用以儲存稀釋的液碱(NaOH),一水泵以負壓抽取前述儲液箱內的液碱(NaOH),一第三管路連接前述水泵與一第二閥門及一第三流量計,其後前述第三管路連接至前述液體入口。 A liquid storage tank is used to store the diluted liquid alkali (NaOH), a water pump extracts the liquid alkali (NaOH) in the liquid storage tank with a negative pressure, a third pipeline connects the water pump with a second valve and a first Three flow meters, after which the aforementioned third pipeline is connected to the aforementioned liquid inlet. 如申請專利範圍第1項所述之超重力除塵脫硫脫硝之裝置,其中前述第二管路上得設有一進口取樣裝置。 As described in the first paragraph of the scope of the patent application, the device for super-gravity dust removal, desulfurization and denitration, wherein the second pipeline may be provided with an inlet sampling device. 如申請專利範圍第1項所述之超重力除塵脫硫脫硝之裝置,其中前述氣體出口得連接一氣體出口管,前述氣體出口管上得設有一出口取樣裝置。 As described in item 1 of the patent application scope, the device for super-gravity dust removal, desulfurization and denitrification, wherein the gas outlet must be connected to a gas outlet pipe, and an outlet sampling device must be provided on the gas outlet pipe.
TW108217458U 2019-12-31 2019-12-31 Hypergravity dust-removing, desulfurizing, and denitrifying apparatus TWM594994U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
TW108217458U TWM594994U (en) 2019-12-31 2019-12-31 Hypergravity dust-removing, desulfurizing, and denitrifying apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
TW108217458U TWM594994U (en) 2019-12-31 2019-12-31 Hypergravity dust-removing, desulfurizing, and denitrifying apparatus

Publications (1)

Publication Number Publication Date
TWM594994U true TWM594994U (en) 2020-05-11

Family

ID=71896611

Family Applications (1)

Application Number Title Priority Date Filing Date
TW108217458U TWM594994U (en) 2019-12-31 2019-12-31 Hypergravity dust-removing, desulfurizing, and denitrifying apparatus

Country Status (1)

Country Link
TW (1) TWM594994U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114105400A (en) * 2021-07-15 2022-03-01 北京科技大学 Integrated device for separating black water from treatment source
CN114196446A (en) * 2021-11-04 2022-03-18 宁波章甫能源科技有限公司 Method and device for hydrolyzing organic sulfur in coal gas and performing wet desulphurization

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114105400A (en) * 2021-07-15 2022-03-01 北京科技大学 Integrated device for separating black water from treatment source
CN114196446A (en) * 2021-11-04 2022-03-18 宁波章甫能源科技有限公司 Method and device for hydrolyzing organic sulfur in coal gas and performing wet desulphurization

Similar Documents

Publication Publication Date Title
CN103055675B (en) Industrial smoke comprehensive treatment system and method based on advanced oxidation
CN105032142B (en) Gas-like phase pre-oxidation combines the flue gas integration removing system and method absorbing
CN102343212A (en) Denitration process combining co-oxidation of ozone and hydrogen peroxide with wet absorption
CN110354677B (en) Sintering and pelletizing machine head smoke emission purifying system
CN103170228B (en) A kind of denitrating flue gas mixed solution and application process thereof
TWM594994U (en) Hypergravity dust-removing, desulfurizing, and denitrifying apparatus
CN206253000U (en) A kind of CFB absorption towers integration desulfurization denitration smoke processing system
CN105536467A (en) Flue gas purification device and method combining photo-catalytic oxidization and double cyclic absorption
CN103611400B (en) A kind of vertical pneumatic revolution self-excitation waste gas purification apparatus
CN205760536U (en) A kind of device of oxidizing process gas cleaning desulfurization denitration demercuration
CN203315987U (en) Environment-friendly equipment for desulfurization and denitrification through utilizing ultraviolet rays
CN104338425A (en) Technological method for wet-process flue gas denitration
CN105536466A (en) Device and method for removing various pollutants in flue gas through photoassisted catalytic oxidization
CN206897142U (en) A kind of integrative coordinated removing sulfur trioxide device suitable for sulphur coal
TW202126374A (en) Device and process for super gravity dust removal, desulfurization, and denitrification capable of making discharge gas complied with emission standards, so as to effectively protect environmental safety and ensure human health
CN210495923U (en) Flue gas emission purification system
CN205386400U (en) Joint schizolysis of ozone oxidation arouses flue gas desulfurization denitration integrated device
CN204093282U (en) A kind for the treatment of apparatus utilizing ozonization to remove nitrogen oxide
CN205570079U (en) SOx/NOx control demercuration removes ultralow discharge system of micronic dust integration
CN205361018U (en) Light helps device of many pollutants in catalytic oxidation desorption flue gas
CN203281189U (en) Adsorption-type desulfurization and denitrification bag-type dust collector
CN212215107U (en) Normal-temperature hypergravity desulfurization and denitrification device
CN205412654U (en) Sintering machine flue gas ammonia process H2O2 oxidation denitrification facility
CN212188549U (en) Hypergravity dust removal SOx/NOx control's device
TWM626251U (en) Steam jetting device for fully mixing ozone and waste gas in flue