CN107789923A - High humidity condensation flue gas microparticle remover and removal methods - Google Patents
High humidity condensation flue gas microparticle remover and removal methods Download PDFInfo
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- CN107789923A CN107789923A CN201711033990.9A CN201711033990A CN107789923A CN 107789923 A CN107789923 A CN 107789923A CN 201711033990 A CN201711033990 A CN 201711033990A CN 107789923 A CN107789923 A CN 107789923A
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- air
- filter cylinder
- flue
- aerosol
- gas
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/24—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
- B01D46/2403—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies characterised by the physical shape or structure of the filtering element
- B01D46/2411—Filter cartridges
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/66—Regeneration of the filtering material or filter elements inside the filter
- B01D46/70—Regeneration of the filtering material or filter elements inside the filter by acting counter-currently on the filtering surface, e.g. by flushing on the non-cake side of the filter
- B01D46/71—Regeneration of the filtering material or filter elements inside the filter by acting counter-currently on the filtering surface, e.g. by flushing on the non-cake side of the filter with pressurised gas, e.g. pulsed air
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/66—Regeneration of the filtering material or filter elements inside the filter
- B01D46/70—Regeneration of the filtering material or filter elements inside the filter by acting counter-currently on the filtering surface, e.g. by flushing on the non-cake side of the filter
- B01D46/72—Regeneration of the filtering material or filter elements inside the filter by acting counter-currently on the filtering surface, e.g. by flushing on the non-cake side of the filter with backwash arms, shoes or nozzles
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- Geometry (AREA)
- Treating Waste Gases (AREA)
Abstract
The present invention relates to a kind of high humidity condensation flue gas microparticle remover and removal methods.The technical scheme of use is：Air-purifying chamber and lower chamber are respectively equipped with housing from top to bottom, lower chamber sets air inlet, air-purifying chamber sets out gas port, dividing plate is provided between lower chamber and air-purifying chamber, dividing plate is provided with several air flue seats connection air-purifying chamber and lower chamber, air flue seat divide into filter cylinder and skeleton, dividing plate is provided with cloth tank, air-purifying chamber side wall is provided with water inlet and liquid level sensor, and housing is externally provided with high pressure gas holder, and high pressure gas holder is connected through magnetic valve, high-pressure air pipe, high pressure gas branch pipe, aerosol generator with aerosol uniform device.The particulates such as the flue dust gypsum droplet that the present invention is adhered in filter cylinder air inlet face using high-pressure aerial fog to accumulation are thoroughly washed away flushing, the technical scheme can completely ensure the normal filtering function of filter cylinder, and condensation flue gas or the problems such as treatment effeciency is low can not be handled by solving traditional deduster.
Description
Technical field
The present invention relates to a kind of high humidity condensation flue gas microparticle remover and removal methods, belong to field of environment protection equipment.
Background technology
At present, environmental problem caused by industrial production is outstanding day by day, and haze weather happens occasionally, and has had a strong impact on people's
Quality of life and health.When haze is mainly industrial smoke discharge, the suspension such as contained fine particle in flue gas
Removing does not cause thoroughly, how can be to prevent to the progress of the suspensions such as various flue gas fine particles and real effective and thorough removing
The Main Means that haze weather occurs, and environmental technology field urgent problem to be solved.
Following technical scheme is mainly taken in terms of dust pollution is prevented at present；
1. sack cleaner is easily processed to the flue gas that do not condense, but the processing of the inadaptable flue gas that condensed to high humidity.Flue gas wet method takes off
After sulphur, humidity of flue gas is big, temperature is low and carries the suspension such as gypsum droplet and fine particle, and also other high humidity low temperature are containing thin
The flue gas of microparticle suspension, condensation is formed when passing through filter bag into deduster under low-temperature condition.The generation of dew condensation phenomenon,
The aggregation of grain thing causes pocket to block, and dust layer pulp, filtrate can not be removed by sticky, and resistance of the filter bag sharply increases, until
Stomata, which blocks, makes deduster not run.
2. although wet dust removal technology can condense to high humidity to a certain extent, flue gas is effectively treated, technique
Equipment is huge, and equipment investment amount is big, maintenance cost is high.Wet cottrell efficiency in the running of reality only has
70% or so, want to reach current its smoke inlet dust concentration of minimum discharge 5mg/m3 standards no more than 18mg/m3,
Want to reach " near-zero release " difficulty larger.
In summary, how to design it is a kind of it is simple efficiently, can be to various containing fine particle suspension high humidity condensation
Flue gas is thoroughly handled, and can realize that the equipment of " near-zero release " is art personnel's urgent problem to be solved.
The content of the invention
Can be to various high humidity knots the present invention relates to a kind of high humidity condensation flue gas microparticle remover and removal methods, the remover
Reveal the fine particle suspension that flue gas carries to implement thoroughly to remove, the flue gas fine particle suspension content after removing can be realized
" near-zero release ", present apparatus small volume, treating capacity are big, removal efficiency is high, small investment, energy consumption are low.
To achieve the above object, the technical solution adopted by the present invention is：
High humidity condensation flue gas microparticle remover, including housing, enclosure interior are provided with superposed air-purifying chamber and air-purifying chamber
The lower chamber in portion, lower chamber are provided with air inlet, and air-purifying chamber sets out gas port, are provided with dividing plate between lower chamber and air-purifying chamber, on dividing plate
Provided with some through holes, through hole arranged anyhow on dividing plate it is evenly distributed, each through hole set respectively cylindrical shape air flue seat pass through through hole
And UNICOM's air-purifying chamber and lower chamber on dividing plate are fixed on, air flue seat forms in the upper part of dividing plate with air-purifying chamber inwall and dividing plate
Cloth tank, air flue seat edge suitable for reading are additionally provided with water inlet and liquid level sensor higher than upper water level, air-purifying chamber side wall in cloth tank；
Air flue seat middle upper portion sets jet branch pipe, and jet branch pipe divides into aerosol generator, and jet branch pipe is passed through controllable on top
High pressure gas, aerosol generator bottom set aerosol uniform device, and aerosol generator is passed through under the water surface in cloth tank provided with suction hose,
Filter cylinder is set below air flue seat, the skeleton of support filter cylinder is provided with filter cylinder, lower chamber bottom is provided with Sewage outlet.
Preferably, the jet branch pipe connects high-pressure air pipe on top, high-pressure air pipe is set through air-purifying chamber access is outside
Some high pressure gas holders, being passed through for solenoid valve control high pressure gas is set on high-pressure air pipe.
Preferably, the cloth tank is provided with liquid level sensor, liquid level sensor highly controls according to water distribution trough inner water position
The water inlet of water inlet.
As preferred：The air flue seat upper inner diameter is more than bottom, and the filter cylinder is fixed on air flue seat bottom one week, aerosol
Uniform device is suitable for reading to be connected with spout under aerosol generator, and aerosol uniform device caliber suitable for reading is more than the aerosol generator jet pipe
Footpath, high-pressure air pipe caliber are more than the jet branch diameter, and aerosol uniform device is located in filter cylinder.
The procedure of removing, appropriate water is passed through in cloth tank to desired liquid level, is passed through in high pressure gas holder
High pressure gas；
Pending high humidity condensation flue gas is passed through lower chamber from air inlet and enters cartridge interior after filter cylinder filters, is passed through in filter cylinder
Flue gas after filter cylinder purification is discharged from air flue seat into air-purifying chamber through gas outlet；
Condensation flue gas containing the particulate matter such as fine soot and gypsum droplet causes filter cylinder surface sweating, flue dust when passing through filter cylinder
It is adhered to Deng fine particulates in filter cylinder air inlet face, the particulate buildup such as flue dust for the adhesion that condensed in filter cylinder air inlet face is to a certain amount of
When filter cylinder air-hole blockage cross gas and be obstructed, high-pressure air pipe solenoid is opened, and high pressure gas is through jet branch pipe, aerosol generator and aerosol
Uniform device sprays, and by forming negative pressuren zone in aerosol generator during aerosol generator, the water in cloth tank passes through high pressure gas
Suction hose is inhaled into aerosol generator, and water impacts to form aerosol in aerosol generator by high pressure gas, and aerosol is uniform through aerosol
Device backwashes to the dispersed injection of filter cylinder inner surface, the outside swash of wave of aerosol to filter cylinder, the microparticle such as flue dust, gypsum droplet
Thing flows to lower chamber bottom after being washed down, discharged through Sewage outlet.
High humidity condensation flue gas microparticle remover of the present invention, using pressure-air and aquatic products anger mist, aerosol leads to
Cross aerosol uniform distribution device and wash away and rinse accumulation and be adhered to the particulates such as flue dust gypsum droplet in filter cylinder air inlet face.The high humidity knot
The condensation bur for revealing flue gas microparticle remover for filter cylinder surface is removed thoroughly, can completely ensure the normal mistake of filter cylinder
Function is filtered, condensation flue gas or the problems such as treatment effeciency is low can not be handled by solving traditional deduster.
Brief description of the drawings
Accompanying drawing is used for providing a further understanding of the present invention, is used to explain the present invention together with the embodiment of the present invention, and
Do not form limitation of the invention.
Fig. 1 is the structural representation one of high humidity of the present invention condensation flue gas microparticle remover；
Fig. 2 is the structural representation two of high humidity of the present invention condensation flue gas microparticle remover；
Reference：1st, housing；2nd, air inlet；3rd, water inlet；4th, high-pressure air pipe；5th, magnetic valve；6th, high pressure gas import；
7th, high pressure gas holder；8th, gas outlet；9th, Sewage outlet；10th, jet branch pipe；11st, aerosol generator；12nd, air flue seat；
13rd, dividing plate；14th, cloth tank；15th, air-purifying chamber；16th, filter cylinder；17th, skeleton；18th, lower chamber；19th, liquid level sensor； 20、
Aerosol uniform device.
Embodiment
The preferred embodiments of the present invention are illustrated below in conjunction with the accompanying drawings, it should be understood that described herein to be preferable to carry out
Example is merely to illustrate and explain the present invention, and is not intended to limit the present invention.
Fig. 1 and Fig. 2 is the internal structure view of the different directions of present patent application, as depicted in figs. 1 and 2, including housing
1, the inside of housing 1 is provided with superposed air-purifying chamber 15 and the lower chamber 18 of the bottom of air-purifying chamber 15, and lower chamber 18 is provided with air inlet
Mouth 2, air-purifying chamber 15 sets out gas port 8, and dividing plate 13 is provided between lower chamber 18 and air-purifying chamber 15.
Dividing plate 13 is provided with some through holes, and through hole is arranged evenly distributed anyhow on dividing plate 13, and each through hole sets cylinder respectively
The air flue seat 12 of shape is through through hole and is fixed on UNICOM's air-purifying chamber 15 and lower chamber 18 on dividing plate 13, and air flue seat 12 is in dividing plate 13
Upper part and the inwall of air-purifying chamber 15 and dividing plate 13 form cloth tank 14,12 edge suitable for reading of air flue seat is higher than upper water in cloth tank 14
Position, the side wall of air-purifying chamber 15 are additionally provided with water inlet 2 and liquid level sensor 19.
The middle upper portion of air flue seat 12 sets jet branch pipe 10, and jet branch pipe 10 divides into aerosol generator 11, and jet branch pipe 10 exists
Top is passed through controllable high pressure gas, and the bottom of aerosol generator 11 sets aerosol uniform device 20, and aerosol generator 11 leads to provided with suction hose
Entering under the water surface in cloth tank 14, the lower section of air flue seat 12 sets filter cylinder 16, and filter cylinder 16 is provided with the skeleton 17 of support filter cylinder 16, under
The bottom of air chamber 18 is provided with Sewage outlet 9.
The top connection high-pressure air pipe 4 of jet branch pipe 10, high-pressure air pipe 4 access the outside high pressure being provided with through air-purifying chamber 15
Gas tank 7, magnetic valve 5 is set on high-pressure air pipe 4 and controls being passed through for high pressure gas.
Cloth tank 14 is provided with liquid level sensor 19, and liquid level sensor 19 gives outside automatic water-supply according to water level in cloth tank 14
System provides waterlevel data, and controls inflow, cloth tank 14 is obtained appropriate moisturizing, water level is remained at setting
In the range of.
The upper inner diameter of air flue seat 12 is more than bottom, and the upper inner diameter increase of air flue seat 12 can be solved because of aerosol generator 11
Insertion causes net airflow to go out to be obstructed, reduce resistance to outflow.
Filter cylinder 16 is fixed on 12 bottom of air flue seat one week, and aerosol uniform device 20 is suitable for reading to be connected with 11 times spouts of aerosol generator
Connect, 20 caliber suitable for reading of aerosol uniform device is more than described 11 times spout calibers of aerosol generator, and the caliber of high-pressure air pipe 4 is more than the spray
The caliber of gas branch pipe 10, aerosol uniform device 20 are located in filter cylinder 16.
Condense the method that flue gas microparticle removes, and comprises the following steps,
Appropriate water is passed through in cloth tank 14 to desired liquid level, high pressure gas is passed through in high pressure gas holder 7；It will wait to locate
The condensation flue gas of reason from air inlet 2 be passed through lower chamber 18 through filter cylinder 16 filtering after enter filter cylinder 16 inside, containing flue dust and gypsum mist
The flue gas of the fine particulates such as drop causes the air inlet face of filter cylinder 16 to condense when by filter cylinder 16, flue dust and gypsum droplet etc. in flue gas
Fine particulates intercept absorption by filter cylinder 16, and the interior flue gas after the purification of filter cylinder 16 of filter cylinder 16 enters air-purifying chamber 15 from air flue seat 12
Discharged by gas outlet 8；
The accumulation of the microparticle such as the appearance of dew condensation phenomenon and flue dust makes the surface of filter cylinder 16 gradually form adhesion layer, remover work
Cause the stomata of filter cylinder 16 to cross gas after a period of time to be obstructed, resistance gradually increases, and when resistance reaches the limit value of setting, automatically controls
System opens the solenoid 5 of high-pressure air pipe 4, and high pressure gas sprays through jet branch pipe 10, aerosol generator 11 and aerosol uniform device 20,
High pressure gas forms negative pressuren zone when by aerosol generator 11 in aerosol generator 11, and the water in cloth tank 14 sucks through suction hose
In aerosol generator 11, water forms aerosol after being impacted by high pressure gas in the aerosol generator 11, aerosol through aerosol uniform device 20 to
The dispersed injection of the inner surface of filter cylinder 16, the outside swash of wave of aerosol backwash to filter cylinder 16, are adhered in the air inlet face of filter cylinder 16
Flue dust, the microparticle thing such as gypsum droplet flow to the bottom of lower chamber 18 after being washed down, discharged through Sewage outlet 9.
The present apparatus high humidity can be condensed the microparticle such as the droplet of gypsum containing flue dust flue gas obtained by special filter cylinder it is thorough
The particulate matter such as the removing at bottom, the fine soot and gypsum droplet that are adhered to after flue gas removing on filter cylinder is removed by high pressure air fog flushing
Thoroughly, the technical scheme can completely ensure the normal filtering function of filter cylinder, and solving traditional high-efficiency dust remover can not be handled
Condense the problem of flue gas and wet electrical dust precipitator volume are big, investment is high, treatment effeciency is low.
The present invention is widely used, and the processing of the various condensation flue gases of adaptation, discharges the preceding flue gas that condenses after especially adapting to desulfurization
Precision processing.The concentration of emission of the microparticle pollutants such as flue dust, gypsum droplet after processing disclosure satisfy that the " requirement of nearly zero " discharge.
The remover can realize that Automated condtrol, small volume, treatment quantity are big, removal efficiency is high, floor space is few, structure letter
Single, low cost, operation maintenance is conveniently.
Finally it should be noted that：The preferred embodiment of the present invention is these are only, is not intended to limit the present invention, all essences in the present invention
God and any modification within principle, made, equal replacement, improvement etc., should be included within the scope of the present invention.
Claims (6)
- The flue gas microparticle remover 1. a kind of high humidity condenses, including housing（1）, housing（1）It is interior to be provided with superposed air-purifying chamber （15）With the lower chamber of air-purifying chamber bottom（18）, lower chamber（18）Provided with air inlet（2）, air-purifying chamber（15）Provided with gas outlet（8）, Lower chamber（18）And air-purifying chamber（15）Between be provided with dividing plate（13）,It is characterized in that：Dividing plate（13）Some through holes are provided with, through hole arranges evenly distributed, each through hole difference anyhow on dividing plate Air flue seat (12) provided with cylindrical shape, air flue seat (12) are fixed on dividing plate (13) through through hole and connect air-purifying chamber（15）With under Air chamber（18）, upper part and air-purifying chamber of the air flue seat (12) in dividing plate（15）Inwall and dividing plate composition cloth tank（14）, air flue seat (12) edge suitable for reading is higher than cloth tank（14）Interior upper water level, air-purifying chamber（15）Side wall is additionally provided with water inlet（3）And liquid level sensor （19）；Air flue seat (12) endoporus center sets aerosol generator（11）, aerosol generator（11）Top is provided with jet branch pipe（10）, spray Gas branch pipe（10）Top is provided with high-pressure air pipe（4）, aerosol generator（11）Bottom is provided with aerosol uniform device（20）, aerosol generator （11）Cloth tank is passed through provided with suction hose（14）Under the interior water surface,Filter cylinder is set below air flue seat (12)（16）, filter cylinder（16）The interior skeleton for being provided with support filter cylinder（17）, lower chamber (18) bottom Provided with Sewage outlet (9).
- The flue gas microparticle remover 2. high humidity according to claim 1 condenses, it is characterised in that housing（1）Outside is provided with High pressure gas holder（7）And magnetic valve（5）, the jet branch pipe（10）In top connection high-pressure air pipe (4), high-pressure air pipe（4）Caliber More than the jet branch pipe（10）Caliber, high-pressure air pipe（14）Through air-purifying chamber（15）High pressure gas holder (7 outside access）, it is high Magnetic valve is set on air pipe（5）Control high pressure gas is passed through.
- The flue gas microparticle remover 3. high humidity according to claim 1 condenses, it is characterised in that the aerosol uniform device （20）Suitable for reading and aerosol generator（11）Lower spout is docked and connected, aerosol uniform device（20）Caliber suitable for reading occurs more than the aerosol Device（11）Lower spout caliber.
- The flue gas microparticle remover 4. high humidity according to claim 1 condenses, it is characterised in that the air-purifying chamber（15）Side Wall is provided with liquid level sensor（19）, liquid level sensor（19）The water inlet of water inlet is highly controlled according to water distribution trough inner water position.
- A kind of 5. high humidity condensation flue gas microparticle remover according to claim 1, it is characterised in that：The air flue seat （12）Upper inner diameter is more than bottom, the filter cylinder（16）And skeleton（17）It is docked and connected with air flue seat (12) bottom.
- 6. a kind of high humidity using described in claim 1 condenses, flue gas microparticle remover progress high humidity condensation flue gas microparticle takes off The method removed, it is characterised in that comprise the following steps,In cloth tank（14）Appropriate water is inside passed through to desired liquid level, high pressure gas holder（7）Inside it is passed through high pressure gas；Pending high humidity is condensed into flue gas from air inlet（2）Into lower chamber（18）, lower chamber（18）Interior flue gas is through filter cylinder （16）After purification, filter cylinder（16）Interior neat stress enters air-purifying chamber through air flue seat (12)（15）Through gas outlet（8）Discharge；High-humidity gas fume containing the particulate matter such as fine soot and gypsum droplet is passing through filter cylinder（16）When, cause filter cylinder（16）Air inlet face The fine particulates such as condensation, flue dust are adhered to filter cylinder（16）In air inlet face, filter cylinder（16）Condense flue dust of adhesion etc. in air inlet face Particulate buildup to it is a certain amount of when filter cylinder（16）Air-hole blockage is crossed gas and is obstructed, high-pressure air pipe（4）Solenoid（5）Open, high pressure gas Through jet branch pipe（10）, aerosol generator（11）With aerosol uniform device（20）Spray, high pressure gas is by aerosol generator（11） When in aerosol generator（11）Interior formation negative pressuren zone, cloth tank（14）Interior water is inhaled into aerosol generator by suction hose（11） Interior, water is in aerosol generator（11）Interior to be impacted to form aerosol by high pressure gas, aerosol is through aerosol uniform device（20）To filter cylinder（16）It is interior The dispersed injection in surface, the outside swash of wave of aerosol is to filter cylinder（16）Backwashed, the microparticle thing such as flue dust, gypsum droplet is rushed Lower chamber is flowed to after brushing down（18）Bottom, through Sewage outlet（9）Discharge.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711033990.9A CN107789923A (en) | 2017-10-30 | 2017-10-30 | High humidity condensation flue gas microparticle remover and removal methods |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711033990.9A CN107789923A (en) | 2017-10-30 | 2017-10-30 | High humidity condensation flue gas microparticle remover and removal methods |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107789923A true CN107789923A (en) | 2018-03-13 |
Family
ID=61547831
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711033990.9A Withdrawn CN107789923A (en) | 2017-10-30 | 2017-10-30 | High humidity condensation flue gas microparticle remover and removal methods |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107789923A (en) |
-
2017
- 2017-10-30 CN CN201711033990.9A patent/CN107789923A/en not_active Withdrawn
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| PB01 | Publication | ||
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Application publication date: 20180313 |