CN202410504U - Novel double-tower efficient desulfurizing and dedusting device - Google Patents
Novel double-tower efficient desulfurizing and dedusting device Download PDFInfo
- Publication number
- CN202410504U CN202410504U CN2012200269230U CN201220026923U CN202410504U CN 202410504 U CN202410504 U CN 202410504U CN 2012200269230 U CN2012200269230 U CN 2012200269230U CN 201220026923 U CN201220026923 U CN 201220026923U CN 202410504 U CN202410504 U CN 202410504U
- Authority
- CN
- China
- Prior art keywords
- tower
- dedusting
- desulfurization
- flue
- desulfurizing
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
- Y02A50/2351—Atmospheric particulate matter [PM], e.g. carbon smoke microparticles, smog, aerosol particles, dust
Landscapes
- Separating Particles In Gases By Inertia (AREA)
Abstract
Description
技术领域 technical field
本发明创造涉及一种脱硫除尘器,特别是一种新型的双塔式高效脱硫除尘器。 The invention relates to a desulfurization and dust collector, in particular to a novel double-tower high-efficiency desulfurization and dust collector.
背景技术 Background technique
现阶段烟气脱硫除尘器分为三类:湿法脱硫、半干法脱硫、干法脱硫技术。多为单极处理,除尘效率低,脱硫效率低,且不消烟。生产成本高、使用寿命短。 At present, flue gas desulfurization dust collectors are divided into three categories: wet desulfurization, semi-dry desulfurization, and dry desulfurization technologies. Most of them are single-pole treatment, with low dust removal efficiency, low desulfurization efficiency, and no smoke elimination. The production cost is high and the service life is short.
发明内容 Contents of the invention
为了解决上述存在的技术问题,本发明创造提供一种新型的双塔式高效脱硫除尘器,该除尘器集脱硫除尘为一体,消烟除尘效果好。 In order to solve the above-mentioned technical problems, the present invention provides a novel double-tower high-efficiency desulfurization and dust collector, which integrates desulfurization and dust removal, and has a good smoke and dust removal effect.
本发明创造的目的是这样实现的:一种新型的双塔式高效脱硫除尘器,其特征在于:S弯旋转式脱硫除尘塔与冲击湍流式脱硫除尘塔通过烟道连接,在烟道上安装风机; The purpose of the invention is achieved in this way: a new double-tower high-efficiency desulfurization and dust collector is characterized in that: the S-curved rotary desulfurization and dust removal tower is connected with the impact turbulent flow desulfurization and dust removal tower through a flue, and a fan is installed on the flue ;
所述的S弯旋转式脱硫除尘塔的塔身上设有进烟口,塔内进烟口的两侧分别设有S形漩涡通道,在塔身中上部设有折流板Ⅰ,在塔身底部设有灰斗Ⅰ; The tower body of the S-curved rotary desulfurization and dust removal tower is provided with a smoke inlet, S-shaped vortex passages are respectively arranged on both sides of the smoke inlet in the tower, and a baffle plate I is arranged at the middle and upper part of the tower body. There is an ash hopper I at the bottom;
所述的冲击湍流式脱硫除尘塔的塔身顶部设有出风口,在塔身底部设有灰斗Ⅱ;烟道末端位于冲击湍流式脱硫除尘塔的塔身内,在烟道出口处设有烟气冲击体,在塔身中上部设有折流板Ⅱ。 The top of the impact turbulent desulfurization and dust removal tower is provided with an air outlet, and an ash hopper II is arranged at the bottom of the tower; The gas impact body is equipped with a baffle plate II in the middle and upper part of the tower body.
所述的S弯旋转式脱硫除尘塔的塔身上设置若干个雾化喷嘴。 The tower body of the S-curved rotary desulfurization and dust removal tower is provided with several atomizing nozzles.
所述的烟道末端设有若干个雾化喷嘴。 The end of the flue is provided with several atomizing nozzles.
本发明创造采用双塔式结构,在前端设置一级S弯旋转式脱硫除尘塔,后端设置一级冲击湍流式脱硫除尘塔通过烟道连接风机。烟气被风机从S弯旋转式脱硫除尘塔的进烟口吸入,由于S弯旋转式脱硫除尘塔内设置多组雾化喷嘴,雾化喷嘴喷出无死角全区域碱水水雾对烟气进行初步净化,然后烟气通过S形漩涡通道进行特殊水旋流,利用烟气自身的动能产生气动旋流,气液两相充分接触,进行传质反应,清除大部分S02、S03、CO及灰尘,再通过S弯旋转式脱硫除尘塔上部设置的折流板Ⅰ进行脱水,烟气出S弯旋转式脱硫除尘塔后通过风机被高速吹入冲击湍流式脱硫除尘塔,由于烟道末端设置在塔内,并在烟道末端设置雾化喷嘴,通过雾化喷嘴净化后,进入烟气冲击体,利用高强度水压使通过烟气冲击体的烟气完全净化,最后烟气变为纯净的带水气体通过折流板Ⅱ过滤水分,最终烟气从出风口排出除尘器,其中折流板根据重力、惯性力、离心力等气水分离原理设计,脱水效率高(出口液态水份浓度<100mg/Nm3),确保风机正常运行。 The invention adopts a double-tower structure, with a first-stage S-curved rotary desulfurization and dust removal tower at the front end, and a first-stage impact turbulent flow desulfurization and dust removal tower at the rear end, which is connected to the fan through the flue. The flue gas is inhaled by the fan from the smoke inlet of the S-curved rotary desulfurization and dust removal tower. Since the S-curved rotary desulfurization and dust removal tower is equipped with multiple groups of atomizing nozzles, the atomizing nozzles spray alkali water and water mist in the whole area without dead ends to affect the flue gas. After preliminary purification, the flue gas passes through the S-shaped vortex channel for special water swirl flow, using the kinetic energy of the flue gas itself to generate aerodynamic swirl flow, the gas-liquid two-phase is fully contacted, and the mass transfer reaction is carried out to remove most of the S0 2 , S0 3 , CO and dust are dehydrated through the baffle plate I set on the upper part of the S-curved rotary desulfurization and dust removal tower. The end is set in the tower, and an atomizing nozzle is installed at the end of the flue. After being purified by the atomizing nozzle, it enters the flue gas impact body, and the flue gas passing through the flue gas impact body is completely purified by high-intensity water pressure. The pure water-laden gas passes through the baffle plate II to filter the water, and finally the flue gas is discharged from the dust collector from the air outlet. The baffle plate is designed according to the principle of gas-water separation such as gravity, inertial force, and centrifugal force, and the dehydration efficiency is high (the liquid moisture at the outlet Concentration <100mg/Nm 3 ), to ensure the normal operation of the fan.
本发明创造集脱硫除尘为一体,通过两级脱硫除尘塔,达到了高效脱硫无烟无尘的目的。该装置不排废水,无二次污染,工艺简单,易操作维护,脱硫率在99%左右,除尘率在99%左右,脱硫除尘效果好。 The invention integrates desulfurization and dust removal, and achieves the purpose of efficient desulfurization without smoke and dust through two-stage desulfurization and dust removal towers. The device does not discharge waste water, has no secondary pollution, is simple in process, easy to operate and maintain, has a desulfurization rate of about 99%, a dust removal rate of about 99%, and a good desulfurization and dust removal effect. the
附图说明 Description of drawings
图1是本发明创造的结构示意图。 Fig. 1 is a structural schematic diagram of the invention.
具体实施方式 Detailed ways
一种新型的双塔式高效脱硫除尘器,如图1所示,该装置包括S弯旋转式脱硫除尘塔1、冲击湍流式脱硫除尘塔2、烟道9、风机10,其中S弯旋转式脱硫除尘塔1与冲击湍流式脱硫除尘塔2通过烟道9连接,在烟道9上安装风机10。
A new double-tower high-efficiency desulfurization and dust collector, as shown in Figure 1, the device includes S-curved rotary desulfurization and
S弯旋转式脱硫除尘塔1的塔身上设有进烟口3及若干个雾化喷嘴13,塔内进烟口3的两侧分别设有S形漩涡通道4,在塔身中上部设有折流板Ⅰ5,在塔身底部设有灰斗Ⅰ11。
The tower body of the S-curved rotary desulfurization and
在冲击湍流式脱硫除尘塔2的塔身顶部设有出风口8,在塔身底部设有灰斗Ⅱ12;在烟道9末端位于冲击湍流式脱硫除尘塔2的塔身内,在烟道9末端设有若干个雾化喷嘴14,在烟道9出口处设有烟气冲击体6,在塔身中上部设有折流板Ⅱ7。
An
Claims (3)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2012200269230U CN202410504U (en) | 2012-01-20 | 2012-01-20 | Novel double-tower efficient desulfurizing and dedusting device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2012200269230U CN202410504U (en) | 2012-01-20 | 2012-01-20 | Novel double-tower efficient desulfurizing and dedusting device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN202410504U true CN202410504U (en) | 2012-09-05 |
Family
ID=46735303
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2012200269230U Expired - Lifetime CN202410504U (en) | 2012-01-20 | 2012-01-20 | Novel double-tower efficient desulfurizing and dedusting device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN202410504U (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102553415A (en) * | 2012-01-20 | 2012-07-11 | 尤凯军 | Novel double-tower type efficient desulfuration dust collector |
CN104740966A (en) * | 2015-03-17 | 2015-07-01 | 王金志 | Omni-directional efficient impact dust collector |
CN106422728A (en) * | 2016-11-28 | 2017-02-22 | 无锡市莱达热工工程有限公司 | Desulfurization dust remover |
CN114345062A (en) * | 2021-12-31 | 2022-04-15 | 万华化学集团股份有限公司 | Scrubber and extruder volatile waste gas treatment method |
-
2012
- 2012-01-20 CN CN2012200269230U patent/CN202410504U/en not_active Expired - Lifetime
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102553415A (en) * | 2012-01-20 | 2012-07-11 | 尤凯军 | Novel double-tower type efficient desulfuration dust collector |
CN104740966A (en) * | 2015-03-17 | 2015-07-01 | 王金志 | Omni-directional efficient impact dust collector |
CN104740966B (en) * | 2015-03-17 | 2017-03-01 | 广州高唐科技发展有限公司 | A kind of full angle high-efficiency impulse dust removal machine |
CN106422728A (en) * | 2016-11-28 | 2017-02-22 | 无锡市莱达热工工程有限公司 | Desulfurization dust remover |
CN114345062A (en) * | 2021-12-31 | 2022-04-15 | 万华化学集团股份有限公司 | Scrubber and extruder volatile waste gas treatment method |
CN114345062B (en) * | 2021-12-31 | 2023-05-26 | 万华化学集团股份有限公司 | Scrubber and volatile waste gas treatment method of extruder |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103203147B (en) | Spraying water storage impact type internal circulating dust remover and dust removal method | |
CN203315937U (en) | Cyclone venturi spray desulfurization dust collector | |
CN201823405U (en) | Cyclone demister exhausting gas down | |
CN105107356B (en) | A kind of sulfurous gas desulfurization cyclone reaction isolation integral system and technique | |
CN202410504U (en) | Novel double-tower efficient desulfurizing and dedusting device | |
CN201101941Y (en) | Desulfurization and dust removal integrated device of fiberglass of industry coal-fired boiler | |
CN101322908A (en) | Wet-type high-efficient desulfation dust-extraction device and method | |
CN102600994B (en) | Electric spraying cyclone dust collector and application thereof | |
CN202620955U (en) | Cyclone desulphurization deduster with water-film baffles | |
CN102553415B (en) | Novel double-tower type efficient desulfuration dust collector | |
CN201912859U (en) | Spiral guide plate type desulfurization equipment | |
CN102886189A (en) | Spiral venturi scrubber and wet-method desulphurization and denitration dust-collecting system | |
CN2330401Y (en) | Wet cyclone integrated separator | |
CN106237724B (en) | A kind of sound wave coupled rotational flow-racemization high-effective dust-removing demister | |
CN203208891U (en) | Turn-round type flue gas dedusting and desulfurizing device | |
CN204768247U (en) | Defogging wet -type desulfurizing tower system | |
CN201108800Y (en) | Girdle type dust removal desulfurization unit | |
CN202909586U (en) | Spiral venturi washer and wet-method desulfuration and denitration dust removal system | |
CN203208886U (en) | Volute-type flue-gas dedusting and desulfurizing device | |
CN212999014U (en) | Matte granulation steam collection device | |
CN203208888U (en) | Suspension-spraying striking-down-type dedusting and desulfurizing device | |
CN210613300U (en) | Flue gas dust removal and desulfurization device | |
CN200987951Y (en) | Turbulent flow dust removing and desulfurizing tower | |
CN201342317Y (en) | A dust removal desulphurization purifier | |
CN209865748U (en) | High-efficient desulfurization cyclone plate tower that removes dust |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
AV01 | Patent right actively abandoned |
Granted publication date: 20120905 Effective date of abandoning: 20140115 |
|
AV01 | Patent right actively abandoned |
Granted publication date: 20120905 Effective date of abandoning: 20140115 |
|
RGAV | Abandon patent right to avoid regrant |