CN203564912U - De-dusting desulfurization chimney for liquid film - Google Patents

De-dusting desulfurization chimney for liquid film Download PDF

Info

Publication number
CN203564912U
CN203564912U CN201320751753.7U CN201320751753U CN203564912U CN 203564912 U CN203564912 U CN 203564912U CN 201320751753 U CN201320751753 U CN 201320751753U CN 203564912 U CN203564912 U CN 203564912U
Authority
CN
China
Prior art keywords
liquid film
liquid
cylindrical shell
stainless steel
chimney
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 - Fee Related
Application number
CN201320751753.7U
Other languages
Chinese (zh)
Inventor
王达胜
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN201320751753.7U priority Critical patent/CN203564912U/en
Application granted granted Critical
Publication of CN203564912U publication Critical patent/CN203564912U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Treating Waste Gases (AREA)

Abstract

The utility model relates to a de-dusting desulfurization chimney for a liquid film. The de-dusting desulfurization chimney for the liquid film comprises a barrel, and is characterized in that the barrel comprises an air inlet, an inner cavity, an air outlet, a flue gas automatic online monitor, a fan, a mist catching film, liquid film materials, stainless steel grid supports, liquid flow grooves, nozzles, a liquid pipe, a funnel and a liquid outlet. The inner cavity is provided with the fan, the mist catching film, the liquid film materials, the stainless steel grid supports, the liquid flow grooves and the nozzles in sequence from the air outlet to the air inlet; the stainless steel grid supports are obliquely arranged from top to bottom; one end of each nozzle passes through the barrel and is communicated with the inner cavity; the other end of each nozzle is located at the outer side of the barrel and connected with the liquid pipe. The de-dusting desulfurization chimney for the liquid film not only is capable of effectively treating hazardous substances emitted from flue gas but also is suitable for industrial large-scale emission and cyclic utilization. Industrial lands also can be reduced, transformation and building of new and old chimneys are convenient, and the flue gas emission quality is automatically monitored on line to achieve the goal of controlling atmospheric pollution.

Description

Liquid film dust-removal and desulfurizing chimney
Technical field
The utility model relates to a kind of device for dust-removal and desulfurizing, especially a kind of liquid film dust-removal and desulfurizing chimney.
Background technology
The harm that now atmosphere pollution causes the mankind and living environment thereof is huge with impact, has become common people's common recognition, and people can not have a meal for three days, but cannot three minutes no breathings, and the quality of air quality is directly connected to people's physical and mental health.CHINESE REGION large area produces serious " haze ", except the impact of weather sand and dust, pollution is mainly derived from all trades and professions in a large number to the harmful substance of having discharged in atmosphere, as: sulfur dioxide (SO2), carbon monoxide (CO), nitrogen oxide (NO), nitrogen dioxide (NO2), suspended particulate substance (floating dirt, depositing dust, flue dust, oil smoke etc.).Analyze after deliberation, except national resident's production, life soot emissions superposition, wherein the discharge capacity of chemical industry, thermal power plant, steel plant, automobile industry and building trade ranks prostatitis.When Yi Ge large chemical plant, thermal power plant, steel plant normally produce, in tail gas, major pollutants discharged discharge is: SO 2 ., nitre, NO x, flue dust, dust (pm2.5-pm10), NMCH, benzene,toluene,xylene, methyl alcohol, H 2 s, CO, NH 3 deng.Discharge amount of exhaust gas reaches 1000000m 3/ h left and right.If there is security incident, reality is also environmental protection accident, and gas, solid, liquid pollutant discharge amount will be more serious.Because China process of industrialization is accelerated, although small chemical factory, thermal power plant, steel plant's discharge capacity are little, discharge smoke pollution concentration is higher, and pollutant superposition is very fast, has caused quite serious atmosphere pollution.And discharge flue gas process is substantially effectively processed, and discharge capacity is also growing on and on, and makes air quality constantly decline.
Therefore, be badly in need of providing harmful substance in a kind of effectively smoke treatment discharge, and be suitable for the liquid film dust-removal and desulfurizing chimney that large-scale industrialization discharge cycle is utilized.
Summary of the invention
The purpose of this utility model is to provide harmful substance in a kind of effectively smoke treatment discharge, and is suitable for the liquid film dust-removal and desulfurizing chimney that large-scale industrialization discharge cycle is utilized.
Basic conception of the present utility model is: this product relates to chemical plant, thermal power plant, steel plant and fire coal, fuel oil big, medium-sized and small enterprises while normally producing, the processing of the flue gas pollutant discharging in chimney tail gas.According to smoke pollution properties, select different liquid fluxs, remove SO 2 ., nitre, NO x, flue dust, dust (pm2.5-pm10), NMCH, benzene,toluene,xylene, methyl alcohol, H 2 s, CO, NH 3 deng, to reach national atmospheric emission standard.Form a kind of allow product and chimney integrated; Liquid mist, liquid film are dedusting and desulphurization integrated; The acceleration of flue gas blower fan and flue gas are caught mist and are purified integrated; The chimney of fume emission and flue gas automatic on-line monitoring integration.Allow liquid mist, liquid film dust-removal and desulfurizing and pernicious gas, catch mist film and purify discharged gas fume, thereby reduce industrial land, be convenient to new, old chimney transformation and build, reach the object of control atmosphere pollution.The utility model is according to flue dust, dust in the flue gas of discharge, and toxic and harmful, easily by the characteristic of aqueous solvent adsorbing and removing.Take the mode that aqueous solvent regeneration cycle is used, thereby realize the decontamination process of flue gas pollutant.In the utility model solvent pump type selecting pressure, flow with Diameter of chimney, highly, nozzle diameter is relevant, how much relevant outside liquid pool is with circulating fluid volume.Exhanst gas outlet quality index adopts the liquid film number of plies to control, and increasing the liquid film number of plies is mainly to strengthen exchange area, with reference to exhanst gas outlet Quality Design.Solvent circulation processing pool size, designs according to solvent internal circulating load.After flue dust dehydration, can do the utilization of cement sanded brick, the utilization of solvent liquid regeneration cycle for the treatment of.Technical process of the present utility model is: 1, the purification process of flue gas: under blower fan draft effect, flue gas enters from chimney lower ports, by the vaporific solvent dust-removal and desulfurizing of two nozzle ejections, then the liquid film dust-removal and desulfurizing forming by ground floor and the vaporific dust-removal and desulfurizing of nozzle.Enter again the vaporific solvent dust-removal and desulfurizing of second layer liquid film and two nozzle ejections, then through the 3rd layer of liquid film and two vaporific solvent dust-removal and desulfurizings that nozzle sprays.Flue gas reaches emission abatement standard.By catching mist film, remove the free water solution in flue gas again, through blower fan, send into atmosphere, qualified discharge under the monitoring of flue gas automatic on-line.2, solvent circulation process: solvent is under the pressurized delivered of pump, deliver to each layer of nozzle and form spray film, on the 3rd layer of spray film is netted on 30 inclined-planes, degree left and right, form liquid film, flow to below half garden spout and enter the netted upper and thicker liquid film of same layer spray film formation in second layer inclined-plane.After liquid film and flue-gas dust-removing and desulfurization exchange, second layer solvent flows to below half garden spout and enters the netted upper and thicker liquid film of same layer spray film formation in ground floor inclined-plane, rich solution after liquid film and flue-gas dust-removing and desulfurization exchange enters the solution collecting funnel of bottom, from funnel, flow into the solvent cell of outside, through precipitation, regeneration, process and utilize by solvent pump pressurized circulation.Top flue gas is contacted by the outer row of outlet with the solvent after purification all the time, reach the clean-up effect of flue gas.It is little that the utility model takes up an area, reduced investment, and solvent, flue dust can recyclings, are convenient to implement, and operating cost is low.After domestic blowdown stack not up to standard transformation, can effectively solve the fog impact that atmosphere pollution and flue gas form.Be applicable to the transformation of old chimney, from entrance below in interior assembling.When also newly chimney is built, directly when building chimney, press design and assembly.
Specifically, liquid film dust-removal and desulfurizing chimney described in the utility model comprises cylindrical shell, it is characterized in that described cylindrical shell comprises air inlet, inner chamber, gas outlet, flue gas automatic on-line monitoring instrument, blower fan, catch mist film, liquid film material, Stainless steel mesh supports, spout, nozzle, liquor pipe, funnel and liquid outlet, intracavity inter-connection is passed through in described air inlet and gas outlet, described liquid outlet is by funnel and intracavity inter-connection, described flue gas automatic on-line monitoring instrument be arranged on cylindrical shell gas outlet place outer wall and with the intracavity inter-connection of cylindrical shell, described inner chamber is disposed with blower fan by gas outlet to air inlet, catch mist film, liquid film material, Stainless steel mesh supports, spout and nozzle, described Stainless steel mesh supports and is from top to bottom obliquely installed, described Stainless steel mesh support level gradient is 30 degree left and right, described nozzle one end communicates with inner chamber through cylindrical shell, the described nozzle other end is positioned at cylindrical shell outside and is connected with liquor pipe.
Cylindrical shell described in the utility model can be stainless steel cylinder, fiber reinforced plastic barrel or plastic cylinder.When cylindrical shell is selected stainless steel, fiberglass or plastic cylinder plate, can acid-resistance medium gas, liquor corrosion.
Described in the utility model, catch mist film and catch mist film for being less than 400 order plastics fine-meshed screens.
Liquid film described in the utility model is for being less than 200 order plastics fine-meshed screen liquid film materials.Described liquid film material is arranged on Stainless steel mesh and supports above, forms one deck and filters.Certainly, for better filtration, in the utility model, multiple filtration can be set, namely can allow the Stainless steel mesh that is provided with liquid film material be supported on cylinder lumen is respectively arranges which floor more, strengthen filter effect.
Spout described in the utility model is greater than 180 degree along cylindrical shell and is less than 360 degree layouts.Can allow formation liquid film, flowing to below half garden spout, to enter lower one deck inclined-plane netted upper and form a thicker liquid film with layer spray film.
Nozzle described in the utility model is at least two stainless steel nozzles.That is to say, every layer of below of described nozzle can be 2 to 4; Specifically also need to determine with reference to Diameter of chimney, ejection distance should be more than or equal to Diameter of chimney.The pipe of liquor described in the utility model can be from the external top that extends to of cylindrical shell, as long as described liquor pipe is communicated with nozzle.
Cylindrical shell described in the utility model is outer can also be provided with support.Described support can be four; Select I-steel or channel-section steel, while being convenient to transform old chimney, allow chimney wall be connected with cylindrical shell.
Compared with the aforementioned existing similar products, liquid film dust-removal and desulfurizing chimney of the present utility model is harmful substance in smoke treatment discharge effectively, and is suitable for the utilization of large-scale industrialization discharge cycle.Can also reduce industrial land, reduce chimney height, reduce construction investment.Be convenient to new, old chimney transformation and build, automatic on-line is monitored fume emission quality, reaches the object of control atmosphere pollution.
Content of the present utility model is further described with the following Examples, but content of the present utility model is not limited only to content related in embodiment.
Accompanying drawing explanation
Fig. 1 is the structural representation of liquid film dust-removal and desulfurizing chimney in embodiment.
The specific embodiment
As shown in Figure 1, the dust-removal and desulfurizing of liquid film described in the present embodiment chimney comprises cylindrical shell 1, it is characterized in that described cylindrical shell 1 comprises air inlet 2, inner chamber 3, gas outlet 4, flue gas automatic on-line monitoring instrument 5, blower fan 6, catch mist film 7, liquid film material 8, Stainless steel mesh supports 9, spout 10, nozzle 11, liquor pipe 12, funnel 13 and liquid outlet 14, described air inlet 2 is connected by inner chamber 3 with gas outlet 4, described liquid outlet 14 is connected with inner chamber 3 by funnel 13, described flue gas automatic on-line monitoring instrument 5 is arranged on gas outlet 4 place's outer walls of cylindrical shell 1 and is connected with the inner chamber 3 of cylindrical shell 1, and described inner chamber 3 is disposed with blower fan 6 by gas outlet 4 to air inlet 2, catch mist film 7, liquid film material 8, Stainless steel mesh supports 9, spout 10 and nozzle 11, described Stainless steel mesh supports and is from top to bottom obliquely installed, it is 30 degree that described Stainless steel mesh supports 9 horizontal gradients, and described nozzle 11 one end communicate with inner chamber 3 through cylindrical shell 1, and described nozzle 11 other ends are positioned at cylindrical shell 1 outside and are connected with liquor pipe 12.
Cylindrical shell described in the present embodiment 1 is stainless steel cylinder.
Described in the present embodiment, catch mist film 7 and catch mist film for being less than 400 order plastics fine-meshed screens.
The material of liquid film described in the present embodiment 8 is for being less than 200 order plastics fine-meshed screen liquid film materials.
Spout described in the present embodiment 10 is arranged along cylindrical shell 190 degree.
Nozzle described in the present embodiment 11 is every layer of two stainless steel nozzle.
The outer channel-section steel support 15 that is also provided with of cylindrical shell described in the present embodiment 1.

Claims (7)

1. a liquid film dust-removal and desulfurizing chimney, comprise cylindrical shell, it is characterized in that described cylindrical shell comprises air inlet, inner chamber, gas outlet, flue gas automatic on-line monitoring instrument, blower fan, catch mist film, liquid film material, Stainless steel mesh supports, spout, nozzle, liquor pipe, funnel and liquid outlet, intracavity inter-connection is passed through in described air inlet and gas outlet, described liquid outlet is by funnel and intracavity inter-connection, described flue gas automatic on-line monitoring instrument be arranged on cylindrical shell gas outlet place outer wall and with the intracavity inter-connection of cylindrical shell, described inner chamber is disposed with blower fan by gas outlet to air inlet, catch mist film, liquid film material, Stainless steel mesh supports, spout and nozzle, described Stainless steel mesh supports and is from top to bottom obliquely installed, described nozzle one end communicates with inner chamber through cylindrical shell, the described nozzle other end is positioned at cylindrical shell outside and is connected with liquor pipe.
2. liquid film dust-removal and desulfurizing chimney as claimed in claim 1, is characterized in that described cylindrical shell is stainless steel cylinder, fiber reinforced plastic barrel or plastic cylinder.
3. liquid film dust-removal and desulfurizing chimney as claimed in claim 2, catches mist film and catches mist film for being less than 400 order plastics fine-meshed screens described in it is characterized in that.
4. liquid film dust-removal and desulfurizing chimney as claimed in claim 3, is characterized in that described liquid film material is for being less than 200 order plastics fine-meshed screen liquid film materials.
5. liquid film dust-removal and desulfurizing chimney as claimed in claim 4, is characterized in that described spout is greater than 180 degree along cylindrical shell and is less than 360 degree layouts.
6. liquid film dust-removal and desulfurizing chimney as claimed in claim 5, is characterized in that described nozzle is at least two stainless steel nozzles.
7. the liquid film dust-removal and desulfurizing chimney as described in claim 1 or 2 or 3 or 4 or 5 or 6, is characterized in that described cylindrical shell is also provided with support outward.
CN201320751753.7U 2013-11-26 2013-11-26 De-dusting desulfurization chimney for liquid film Expired - Fee Related CN203564912U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201320751753.7U CN203564912U (en) 2013-11-26 2013-11-26 De-dusting desulfurization chimney for liquid film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201320751753.7U CN203564912U (en) 2013-11-26 2013-11-26 De-dusting desulfurization chimney for liquid film

Publications (1)

Publication Number Publication Date
CN203564912U true CN203564912U (en) 2014-04-30

Family

ID=50532676

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201320751753.7U Expired - Fee Related CN203564912U (en) 2013-11-26 2013-11-26 De-dusting desulfurization chimney for liquid film

Country Status (1)

Country Link
CN (1) CN203564912U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106390644A (en) * 2016-11-03 2017-02-15 关云彪 Guaranteeing apparatus for realizing ultralow discharge after standard reaching of fire coal flue gas

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106390644A (en) * 2016-11-03 2017-02-15 关云彪 Guaranteeing apparatus for realizing ultralow discharge after standard reaching of fire coal flue gas

Similar Documents

Publication Publication Date Title
CN102172468B (en) Three-pass dedusting devulcanizer
CN104150552B (en) The heat-engine plant desulfurized waste water evaporate to dryness tower of a kind of process
CN208727090U (en) A kind of fuel oil heating desulphurization denitration dust-extraction unit
CN208449022U (en) Precision desulfurizing filter
CN206823398U (en) Off-gas cleaning equipment
CN206372683U (en) A kind of sewage plant waste gas collection device
CN102397733A (en) Whirlwind dedusting and desulphuration device
CN204933167U (en) A kind of self-loopa desulfurization case
CN204841408U (en) Flue gas desulfurization system
CN203564912U (en) De-dusting desulfurization chimney for liquid film
CN203916431U (en) A kind of gaseous oxidation is in conjunction with the flue gas combined desulfurization and denitration device of wet absorption
CN203564949U (en) Flue gas cleaning system for biomass boiler
CN102380304A (en) Desulfuration and dust removal device of industrial coal furnace
CN202460452U (en) Wet type cyclone desulfuring and dust-removing device
CN201030287Y (en) Cyclone boiler flue gas desulfurization dust cleaning apparatus
CN212651619U (en) Industrial flue gas dust removal desulfurization clarification plant
CN204039090U (en) Process heat-engine plant desulfurized waste water evaporate to dryness tower
CN210251744U (en) A processing apparatus for boiler smoke abatement
CN201799192U (en) Cyclone dust-removal desulphurization device
CN208340380U (en) Boiler desulphurization denitration dedusting minimum discharge system
CN205796935U (en) High-efficiency cyclone dust remover
CN203750366U (en) Wet-method dust-removal absorption tower
CN205815451U (en) A kind of boiler desulfurization device
CN205760590U (en) A kind of desulfation dust-extraction device
CN205042356U (en) Wet or dry of organic flue gas mixes gas sprinkler

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20140430

Termination date: 20171126