CN208287794U - A kind of wet-desulfurizing dust remover - Google Patents
A kind of wet-desulfurizing dust remover Download PDFInfo
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- CN208287794U CN208287794U CN201820549990.8U CN201820549990U CN208287794U CN 208287794 U CN208287794 U CN 208287794U CN 201820549990 U CN201820549990 U CN 201820549990U CN 208287794 U CN208287794 U CN 208287794U
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Abstract
The utility model discloses a kind of wet-desulfurizing dust remover, including desulfurization washing tower, is disposed with chill zone, uptake zone, filtering module dedusting area and mist eliminating zone in desulfurization washing tower from bottom to top；Chill zone is provided with air inlet, and a first spray head is equipped at air inlet；Uptake zone is vertically equidistantly arranged with multiple first spray heads, and the first spray head is pumped by first circulation and is connected to desulfurization washing tower bottom；Filtering module dedusting area includes the Venturi tube being vertically arranged, and second spray head is equipped with above Venturi tube, and second spray head is communicated with slurry pool by second circulation pump, and Venturi tube is arranged on slurry pool；Mist eliminating zone includes the chimney being connected to desulfurization washing tower top, and chimney bottom is equipped with droplet separator.Wet-desulfurizing dust remover provided by the utility model, solves that existing flue gas desulfurization technique long flow path, control is complicated, plant area is big, investment is high, generates secondary pollution, needs the problems such as drain processing unit of special configuration.
Description
Technical field
The utility model relates to exhuast gas desulfurization dedusting technology fields, more particularly to a kind of wet-desulfurizing dust remover.
Background technique
With country and local, domestic petroleum petrochemical industry row increasingly stringent for the pollutant emission norm controlling of industrial waste gas
The processing problem of the high-salt wastewater pollutant of industry, metal smelt industry etc. is more and more prominent, the production processes such as chemical plant, smeltery
It is middle to generate the high-temperature flue gas containing pollutants such as sulfur dioxide, nitrogen oxides, dust (PM10, PM2.5).Due to dry desulfurization
(such as recirculating fluidized bed, rotary spraying technique) there is treatment effeciencies it is low, energy consumption is high, medicament utilization rate is low the problems such as, and it is half-dried
Method (such as lime stone-gypsum method) there are slurrying it is complicated, treatment effeciency is low the problems such as.Chemical plant especially refinery is looked forward at home at present
70% is had more than in installed processing unit in the industry and uses wet treatment method, there are the wind of the escaping of ammonia for the ammonia process of desulfurization
Nearly, ammonium salts particle, these particulate matters such as the ammonium hydrogen sulfate for being difficult to trap easily are formed in flue gas simultaneously relatively to stick together, can be adhered to
The various pieces of device and pipeline, result in blockage；If with flue gas discharger, and will lead to serious secondary pollution.Cause
This need it is a kind of efficiently, take up little area, the desulfurization technology that process is short and process flow simplifies.
Utility model content
The purpose of the utility model is to provide a kind of wet-desulfurizing dust remover, to solve above-mentioned of the existing technology ask
Topic, solves that existing flue gas desulfurization technique long flow path, control is complicated, plant area is big, investment is high, generates secondary pollution, needs
The problems such as drain processing unit of special configuration.
To achieve the above object, the utility model provides following scheme:
The utility model provides a kind of wet-desulfurizing dust remover, optionally, including desulfurization washing tower, the desulfurization washing
Chill zone, uptake zone, filtering module dedusting area and mist eliminating zone are disposed in tower from bottom to top；The chill zone be provided with into
Port is equipped with a first spray head at the air inlet；The uptake zone is vertically equidistantly arranged with multiple first sprays
Head, the first spray head are pumped by first circulation and are connected to the desulfurization washing tower bottom；Filtering module dedusting area includes
The Venturi tube being vertically arranged, the Venturi tube top are equipped with second spray head, and the second spray head passes through second circulation and pumps
It is communicated with slurry pool, the Venturi tube is arranged on the slurry pool；The mist eliminating zone includes and the desulfurization washing tower top
The chimney of portion's connection, the chimney bottom are equipped with droplet separator.
Optionally, the first circulation pump is connected with liquid outlet and absorbent adding mouth.
Optionally, the slurry pool is pyramidal structure, is fixedly installed on inside the desulfurization washing tower.
Optionally, filtering module dedusting area spaced set has multiple Venturi tubes, in multiple Venturi tubes
A second spray head is correspondingly arranged at end opening respectively.
Optionally, the droplet separator includes that hollow rotation is in charge of, and the hollow rotation is in charge of top and is equipped with rotation fragment；Institute
Hollow rotation is stated to be in charge of lower part and be connected to the chimney bottom.
Optionally, water supplement port is offered on the desulfurization washing tower side wall.
Optionally, the sodium hydroxide solution that the absorbent is 30%.
Optionally, the first spray head is G400 spray head, and the second spray head is F130 spray head.
Wet-desulfurizing dust remover provided by the utility model achieves following technical effect compared with the existing technology:
Wet-desulfurizing dust remover treatment effeciency provided by the utility model is high, and absorbent, the oxidant spray of desulfurization are handed over
Fork carries out, and the space in device is preferably utilized, and greatly reduces and independently handles the process of pollutant, shortens work
Sequence simplifies device structure while also reducing the occupied area of processing unit, and pressure drop of the flue gas Jing Guo system is small, technology at
Ripe degree is high, takes up little area, and any post-processing problem is not present, and resistance drop of the flue gas Jing Guo this system is small, less scaling, easy cleaning,
Be not easy to block, Operation and Maintenance is simple, can long period continuous and steady operation, it can be achieved that modularized design.
Detailed description of the invention
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Needed in attached drawing be briefly described, it should be apparent that, the accompanying drawings in the following description is only the utility model
Some embodiments for those of ordinary skill in the art without any creative labor, can also basis
These attached drawings obtain other attached drawings.
Fig. 1 is the utility model wet-desulfurizing dust remover structural schematic diagram；
Wherein, 1 it is desulfurization washing tower, 2 be first circulation pump, 3 be second circulation pump, 4 be chill zone, 5 is uptake zone, 6
It is mist eliminating zone for filtering module dedusting area, 7,8 be G400 spray head, 9 be Venturi tube, 10 be F130 spray head, 11 is slurry pool, 12
It is chimney for droplet separator, 13,14 be liquid outlet, 15 be absorbent adding mouth, 16 be water supplement port, 17 is air inlet.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
Every other embodiment obtained, fall within the protection scope of the utility model.
The purpose of the utility model is to provide a kind of wet-desulfurizing dust remover, to solve above-mentioned of the existing technology ask
Topic, solves that existing flue gas desulfurization technique long flow path, control is complicated, plant area is big, investment is high, generates secondary pollution, needs
The problems such as drain processing unit of special configuration.
To keep the above objects, features, and advantages of the utility model more obvious and easy to understand, with reference to the accompanying drawing and have
Body embodiment is described in further detail the utility model.
Wet-desulfurizing dust remover provided by the utility model as shown in Figure 1, main equipment by desulfurization washing tower 1 and first
Circulating pump 2,3 composition of second circulation pump.Desulfurization washing tower 1 includes chill zone 4, uptake zone 5, filtering module dedusting area 6, mist eliminating zone
7 etc..
The middle lower end for the desulfurization washing tower 1 that chill zone 4 is horizontally mounted.Exhaust containing pollutant is in a horizontal manner from air inlet
Mouth 17 passes through chill zone 4.The G400 spray head 8 for being mounted on chill zone 4 sprays circulation fluid, forms highdensity curtain of liquid, cigarette
Air cooling reaches water saturation state.The direction and gas that liquid injection goes out flow to angled and extend to desulfurization washing tower
1 inner wall can rinse the inner wall of desulfurization washing tower 1 simultaneously.Spray liquid runs down into tower bottom along the inner wall of desulfurization washing tower 1, and desulfurization is washed
The tower bottom for washing tower 1 is provided with taper liquid storage tank, realizes circulated sprinkling by first circulation pump 2.It is some while cooling gas
Sulfur trioxide, sulfur dioxide and the biggish particle of partial size (being greater than 3 microns) are also removed.The pH-value of the loop slurry of spray is close
It is neutral.
Uptake zone 5 is located at 1 middle section of desulfurization washing tower, and vertical direction equidistantly installs a row G400 spray head 8.G400 spray head 8
The loop slurry of ejection is used for sulfur dioxide absorption.When water saturated wet flue gas flows up through uptake zone 5 in tower, remaining two
Sulfur oxide and biggish particulate matter are removed.Spray liquid runs down into the liquid storage tank of tower bottom along tower wall, is realized by first circulation pump 2
Circulated sprinkling.
Filtering module dedusting area 6 is mounted on the top of uptake zone 5.By one group of Venturi tube, 9, one groups of F130 spray heads 10 and one
The slurry pool 11 of a taper forms.When flue gas passes through the Venturi tube 9 of filtering module dedusting area 6, flue gas first accelerates (compression) simultaneously
After deceleration, 1~3 μm of dust particles and more tiny dust particles are contacted with the water in spray liquid, particle surface forms one layer
Thin moisture film, entire partial size increase, it is easier to which the cascade sprayed by top F130 spray head 10 captures, and realizes flue gas ash removal, captures
In the slurry pool 11 for falling on taper to the liquid of dust particles, circulated sprinkling is realized by second circulation pump 3.
The top of F130 spray head 10 is equipped with droplet separator 12, is in charge of by one group of hollow rotation and is formed, what each rotation was in charge of
Static rotation fragment of the middle and upper part installation with angle.Flue gas is in charge of centre after desulfurization, dedusting, along desulfurization washing tower 1 and rotation
Part, which is up to rotation, to be in charge of behind top 180 ° of directions of adjustment and is in charge of downlink from rotation, and flue gas passes through the work of centrifugal force through overwinding fragment
With drop rotates and flows to tube wall.Collected water ceaselessly rinses the inner wall that rotation is in charge of, and flows in the weir of bottom end, then flows into
Second circulation pumps 3 circulated sprinklings.
Chimney 13 is installed on 12 top of droplet separator of desulfurization washing tower 1, chimney 13 is arranged in the top of desulfurization washing tower 1
Portion acts on to guide and being discharged in atmosphere by flue gas.13 the top of chimney, gas keep low velocity in chimney 13, therefore,
The water of condensation can flow back into tower without being brought in atmosphere.Before flue gas is discharged by the chimney 13 of desulfurization washing tower 1, cigarette
Gas reinforces the collection of condensed water by a set of 13 tornadotron of chimney, reduces the white cigarette of 13 periphery of chimney of desulfurization washing tower 1
A possibility that plumage.
The utility model supplements water by water supplement port, realizes water balance by liquid outlet drain.High-temperature flue gas is made in spray
Reaching water saturation state with the cooling of lower Quench, a part of liquid gasification is into flue gas, as purified flue gas is discharged into atmosphere, one
Partial moisture loss；Loop slurry is added sodium hydroxide solution and is neutralized due to absorbing sulfur dioxide, forms sulfurous acid
Sodium and sodium sulphate, salt content are constantly accumulated, and are needed to be discharged a part of loop slurry and are filled into fresh water, and salinity balance is maintained,
Otherwise the excessively high precipitation of salinity causes pipeline and equipment scaling, blocking.
When the utility model wet-desulfurizing dust remover works, flue gas enters the chill zone 4 of desulfurization washing tower 1, hot fume
It being come into full contact in the circulation fluid containing lye that chill zone 4 and G400 spray head 8 sprays, flue-gas temperature is down to saturation temperature, this
The large-sized catalyst granules of process and a part of SO2Be absorbed, saturated flue gas after chill zone 4 on be advanced into SO2Absorption
Area 5, this region arrange G400 spray head 8, and the circulation fluid that saturated flue gas is sprayed with spray head comes into full contact with, most SO2It is inhaling
It receives area 5 to remove, saturated flue gas enters the removing of filtering module dedusting area 6 fine particle, the flue gas of saturation state after leaving uptake zone 5
Through herein filtering module effect first accelerate afterwards slow down, hypersaturated state is reached by adiabatic expansion, the water in flue gas is wrapped in
On fine particle, the size of fine particle be increased dramatically, and the water sprayed by F130 spray head 10 captures, and be flushed to the leakage of filtering module
In bucket.To guarantee that flue gas is free of drop into signs of human habitation chimney 13, into being provided with droplet separator 12 before chimney 13 for further
By the water droplet removing in flue gas, saturated flue gas enters droplet separator 12, flue gas flow deflector in droplet separator 12 from above
Under the action of change direction, the drop in flue gas is got rid of to wall under the action of the centrifugal force, is separated with gas.After separating drop
Clean flue gas passes through the chimney 13 on top, is provided with chimney droplet separator at chimney 13 and further removes the drop in flue gas.
The circulation fluid PH in first circulation pump and second circulation pump in the utility model is controlled in 6.8-7 to SO2It inhales
Fruit of producing effects is best, carries out supplement lye adjustment PH, therefore the utility model first circulation pump 2 is connected with liquid outlet 14 and inhales
Agent adding mouth 15 is received, offers water supplement port 16 on 1 side wall of desulfurization washing tower.
Specific case is applied in the utility model to be expounded the principles of the present invention and embodiment, it is above
The explanation of embodiment is merely used to help understand the method and its core concept of the utility model；Meanwhile for the one of this field
As technical staff, based on the idea of the present invention, there will be changes in the specific implementation manner and application range.To sum up
Described, the content of the present specification should not be construed as a limitation of the present invention.
Claims (8)
1. a kind of wet-desulfurizing dust remover, it is characterised in that: including desulfurization washing tower, in the desulfurization washing tower from bottom to top
It is disposed with chill zone, uptake zone, filtering module dedusting area and mist eliminating zone；The chill zone is provided with air inlet, it is described into
One first spray head is installed at port；The uptake zone is vertically equidistantly arranged with multiple first spray heads, and described first
Spray head is pumped by first circulation and is connected to the desulfurization washing tower bottom；Filtering module dedusting area includes the text being vertically arranged
Venturi, the Venturi tube top are equipped with second spray head, and the second spray head is communicated with slurry pool by second circulation pump,
The Venturi tube is arranged on the slurry pool；The mist eliminating zone includes the chimney being connected to at the top of the desulfurization washing tower,
The chimney bottom is equipped with droplet separator.
2. wet-desulfurizing dust remover according to claim 1, it is characterised in that: the first circulation pump is connected with out liquid
Mouth and absorbent adding mouth.
3. wet-desulfurizing dust remover according to claim 2, it is characterised in that: the slurry pool is pyramidal structure, Gu
Surely it is set to inside the desulfurization washing tower.
4. wet-desulfurizing dust remover according to claim 3, it is characterised in that: filtering module dedusting area is equidistant
Multiple Venturi tubes are provided with, are correspondingly arranged on a second spray head respectively at multiple Venturi tube upper end openings.
5. wet-desulfurizing dust remover according to claim 4, it is characterised in that: the droplet separator includes hollow rotation
It is in charge of, the hollow rotation is in charge of top and is equipped with rotation fragment；The hollow rotation is in charge of lower part and is connected to the chimney bottom.
6. wet-desulfurizing dust remover according to claim 5, it is characterised in that: opened up on the desulfurization washing tower side wall
There is water supplement port.
7. wet-desulfurizing dust remover according to claim 6, it is characterised in that: the hydroxide that the absorbent is 30%
Sodium solution.
8. wet-desulfurizing dust remover according to claim 7, it is characterised in that: the first spray head is G400 spray head,
The second spray head is F130 spray head.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820549990.8U CN208287794U (en) | 2018-04-18 | 2018-04-18 | A kind of wet-desulfurizing dust remover |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820549990.8U CN208287794U (en) | 2018-04-18 | 2018-04-18 | A kind of wet-desulfurizing dust remover |
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| Publication Number | Publication Date |
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| CN208287794U true CN208287794U (en) | 2018-12-28 |
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ID=64725313
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| CN201820549990.8U Active CN208287794U (en) | 2018-04-18 | 2018-04-18 | A kind of wet-desulfurizing dust remover |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110219637A (en) * | 2019-06-18 | 2019-09-10 | 兰冰芯 | A kind of gs-oil separator interface instrument high-efficiency rinsing deslagging one cone |
| CN111203081A (en) * | 2019-10-18 | 2020-05-29 | 云南中陇生态环境工程有限公司 | Flue gas ultra-low emission comprehensive treatment device |
| CN112275114A (en) * | 2020-09-09 | 2021-01-29 | 程学芳 | Two-stage wet desulphurization tower |
-
2018
- 2018-04-18 CN CN201820549990.8U patent/CN208287794U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110219637A (en) * | 2019-06-18 | 2019-09-10 | 兰冰芯 | A kind of gs-oil separator interface instrument high-efficiency rinsing deslagging one cone |
| CN111203081A (en) * | 2019-10-18 | 2020-05-29 | 云南中陇生态环境工程有限公司 | Flue gas ultra-low emission comprehensive treatment device |
| CN112275114A (en) * | 2020-09-09 | 2021-01-29 | 程学芳 | Two-stage wet desulphurization tower |
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