CN208553709U - Flue gas washing system - Google Patents
Flue gas washing system Download PDFInfo
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- CN208553709U CN208553709U CN201820761233.7U CN201820761233U CN208553709U CN 208553709 U CN208553709 U CN 208553709U CN 201820761233 U CN201820761233 U CN 201820761233U CN 208553709 U CN208553709 U CN 208553709U
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- clean water
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- 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
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- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
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Abstract
This disclosure relates to a kind of flue gas washing system, the system includes: scrubbing tower tower body (3), the chimney (5) being connected to the scrubbing tower tower body (3), the smoke inlet (2) for being set to scrubbing tower tower body (3) lower part and the exhanst gas outlet (6) being set at the top of the chimney (5), it is provided with absorbing liquid spray unit in the scrubbing tower tower body (3), is provided with clean water spray unit above the absorbing liquid spray unit；The clean water spray unit includes cleaning (operating) water nozzle (8), the clean water fluid reservoir (13) being located at below cleaning (operating) water nozzle (8) and multiple clean water fluid reservoir flues (19) axially through the clean water fluid reservoir (13).The system of the disclosure can effectively eliminate wet scrubbing tower flue gas trailing phenomenon, solve blue smoke and plume subsidence problems, and do not influence the operating flexibility of scrubbing tower and upstream device, while additionally aiding and slowing down equipment corrosion.
Description
Technical field
This disclosure relates to a kind of flue gas washing system.
Background technique
In industrial processes, especially in some production processes containing heat treatment step (dry, roasting, burning etc.)
In, the exhaust gas such as the tail gas containing pollutant or flue gas can be generated.For example, part during catalytic cracking (FCC), in raw material
Sulphur, nitrogen compound enter coke laydown on reclaimable catalyst in riser reaction process, and spent agent enters regenerator and burns
When regeneration, sulphur, nitrogen compound oxidation in these coke generate SOx、NOxEqual flue gas pollutants.For another example, the nothings such as catalyst production
In machine chemical process, whens heat resolves such as sulfate, nitrate, villaumite for containing in raw material, can be generated containing SOx、NOx、
Cl2, the pollutants and pernicious gas such as HCl tail gas.These flue gases and tail gas containing pollutant and pernicious gas need to be by purifications
It could qualified discharge after processing.
Power generation, petrochemical industry, inorganization is had been widely used for by the wet scrubbing technology of core equipment of wet scrubbing tower
The flue gas and tail gas clean-up of the industrial process such as work are handled.Although process flow and structure have certain difference, its basic principle is all
It is that the pollutant in gas phase is absorbed into liquid phase by gas-liquid contact, achievees the purpose that purifying smoke or tail gas.United States Patent (USP)
US20070189949A1 discloses a kind of wet scrubbing system for regeneration fume from catalytic cracking processing, by washing alkalinity
It washs liquid and flue gas and carries out spray and contact, efficient removal SO may be implemented2While trap dust effect.
But also gradually there are some problems for discovery wet scrubbing process in industry park plan, are also easy to produce flue gas hangover and blue
The problems such as plume sinks causes to seriously affect to plant area and periphery production and living environment.
Utility model content
Purpose of this disclosure is to provide a kind of flue gas washing systems, to solve the flue gas of existing and newly-built wet scrubbing system
Hangover and subsidence problems reduce the adverse effect to plant area and periphery production and living environment.
To achieve the goals above, the disclosure provides a kind of flue gas washing system, the system include: scrubbing tower tower body, with
The chimney of the scrubbing tower tower body connection is set to the smoke inlet of scrubbing tower tower body lower part and is set to the cigarette
Exhanst gas outlet at the top of chimney is provided with absorbing liquid spray unit in the scrubbing tower tower body, which is characterized in that the absorbing liquid spray
Clean water spray unit is provided with above leaching unit；
The clean water spray unit includes cleaning (operating) water nozzle, the clean water liquid storage below the cleaning (operating) water nozzle
Tank and multiple clean water fluid reservoir flues axially through the clean water fluid reservoir, the cleaning (operating) water nozzle with
Clean water fluid reservoir passes through pipeline respectively and is connected with clean water transfer pump.
Optionally, the clean water fluid reservoir has clean water fluid reservoir overflow port, which connects
It is connected to the clean water overflow line for extending to the absorbing liquid spray unit.
Optionally, the quantity of the clean water spray unit is one or more.
Optionally, the clean water spray unit is set in the chimney, the upper end tank mouth of the clean water fluid reservoir
It is tightly connected with the inner wall of the chimney；And/or
The clean water spray unit is set in the scrubbing tower tower body, the upper end tank mouth of the clean water fluid reservoir with
The inner wall of the scrubbing tower tower body is tightly connected.
Optionally, the quantity of the cleaning (operating) water nozzle is 1~12；When the quantity more than one of the cleaning (operating) water nozzle,
The cleaning (operating) water nozzle is circumferentially and/or radial direction is equally spaced.
Optionally, the cleaning (operating) water nozzle is selected from least one of spiral nozzle, fan nozzle and nozzle ring.
Optionally, the salt content of clean water used in the clean water spray unit is not higher than and is collected by the exhanst gas outlet
Flue gas condensing water salt content.
Optionally, the clean water is selected from least one of fresh water, middle water and waste water Jing Guo desalting processing.
Through the above technical solutions, the disclosure in the case where not changing original main structure of wet scrubbing tower, increases
Clean water spray unit, the clean water for spraying out flue gas before tower out with cleaning (operating) water nozzle contact, can effectively eliminate wet process and wash
Tower flue gas trailing phenomenon is washed, solves blue smoke and plume subsidence problems, and do not influence the operating flexibility of scrubbing tower and upstream device, together
When additionally aid slow down equipment corrosion；It is recycled in addition, being collected by clean water fluid reservoir with the clean water after smoke contacts
It utilizes, the utilization rate of clean water can also be effectively improved, while improving the spray flow of clean water.The system structure that the disclosure provides
Simply, at low cost, it can be used for flue gas or vent gas treatment, including power generation, petrochemical industry, inorganic chemical industry of various industrial process etc..
Other feature and advantage of the disclosure will the following detailed description will be given in the detailed implementation section.
Detailed description of the invention
Attached drawing is and to constitute part of specification for providing further understanding of the disclosure, with following tool
Body embodiment is used to explain the disclosure together, but does not constitute the limitation to the disclosure.In the accompanying drawings:
Fig. 1 is a kind of structural schematic diagram of the specific embodiment for the flue gas washing system that the disclosure provides；
Fig. 2 is the schematic diagram that a kind of arrangement mode of (operating) water nozzle is cleaned in the flue gas washing system of disclosure offer；
Wherein, the arrow direction in figure refers to the direction of motion of fluid.
Description of symbols
1 replenisher entrance
2 smoke inlets
3 scrubbing tower tower bodies
4 replenisher entrances
5 chimneys
6 exhanst gas outlets
7 clean water transfer pumps
8 cleaning (operating) water nozzles
9 second absorbing liquid circulating pumps
10 second absorb nozzle for liquid
11 first absorbing liquid circulating pumps
12 efflux wastewater pipelines
13 clean water fluid reservoirs
15 first absorb nozzle for liquid
16 first absorbing liquid fluid reservoirs
17 second absorbing liquid fluid reservoirs
18 second fluid reservoir flues
19 clean water fluid reservoir flues
20 absorbing liquid overflow lines
21 clean water overflow lines
Specific embodiment
It is described in detail below in conjunction with specific embodiment of the attached drawing to the disclosure.It should be understood that this place is retouched
The specific embodiment stated is only used for describing and explaining the disclosure, is not limited to the disclosure.
In the disclosure, in the absence of explanation to the contrary, the noun of locality used such as " upper and lower " typically refers to system reality
Upper and lower when border works, " inside and outside " is for profile of structure itself.
The disclosure provides a kind of flue gas washing system, and with reference to Fig. 1, which includes: scrubbing tower tower body 3 and scrubbing tower tower
The chimney 5 of the connection of body 3 is set to the smoke inlet 2 of 3 lower part of scrubbing tower tower body and is set to 5 top of chimney
Exhanst gas outlet 6.Absorbing liquid spray unit (also referred to as absorbing liquid spray equipment), the suction are provided in the scrubbing tower tower body 3
It receives and is provided with clean water spray unit (also referred to as cleaning water spray system) above liquid spray unit.
The disclosure increases clean water spray unit, cigarette in the case where not changing original main structure of wet scrubbing tower
Spray of the gas before tower out Jing Guo clean water can effectively eliminate flue gas trailing phenomenon, solve blue smoke and plume subsidence problems, and
The operating flexibility of scrubbing tower and upstream device is not influenced, while being additionally aided and being slowed down equipment corrosion.
According to the disclosure, the clean water spray unit may include cleaning (operating) water nozzle 8, be located at the cleaning (operating) water nozzle 8
The clean water fluid reservoir 13 of lower section and multiple clean water fluid reservoir fume pipes axially through the clean water fluid reservoir 13
Road 19.The clean water fluid reservoir flue 19 for flue gas upwardly through clean water fluid reservoir 13, shape and size without
Especially limitation, can be Venturi tube, straight tube or other structures.Flue gas is risen by clean water fluid reservoir flue 19, is met clear
The clean water that clean (operating) water nozzle 8 sprays, to carry out the spray of clean water spray unit.The cleaning (operating) water nozzle 8 is stored up with clean water
Flow container 13 is connected by pipeline with clean water transfer pump 7 respectively, to collect the clean water of spray by clean water fluid reservoir 13
And be delivered to cleaning (operating) water nozzle 8 and recycled, the utilization rate of clean water is effectively improved, while improving the spray of clean water
Amount, the flue gas hangover for the scrubbing tower that effectively disappears and plume sinkage.It will be appreciated by persons skilled in the art that can be by clear
The intake pipeline of clean water transfer pump 7 conveys and/or supplements clean water to the cleaning (operating) water nozzle 8.
According to the disclosure, the clean water fluid reservoir 13 can have clean water fluid reservoir overflow port, the clean water liquid storage
Tank overflow port is connected with the clean water overflow line 21 for extending to the absorbing liquid spray unit.The effect of overflow port is this field
Known to technical staff, when the liquid level in clean water fluid reservoir 13 is excessively high and reaches the clean water fluid reservoir overflow port, cleaning
Water can be entered in underlying absorbent liquid spray unit by clean water overflow line 21, in this way, excessive clean water can be used as absorption
The replenisher of liquid spray unit, to reduce the absorbing liquid magnitude of recruitment of absorbing liquid spray unit.The clean water fluid reservoir overflows
The position that opens up of head piece can according to need and be designed, and preferably make the upper end opening of the clean water fluid reservoir flue 19
Higher than the clean water fluid reservoir overflow port, i.e. the exhanst gas outlet position of clean water fluid reservoir flue 19 is stored up higher than clean water
Liquid level in flow container 13, avoids that flue gas enters in clean water fluid reservoir 13 or clean water by 19 overflow of pipeline goes out fluid reservoir 13.
According to the disclosure, the quantity of the clean water spray unit can be one or more.In a kind of tool of the disclosure
In body embodiment, the clean water spray unit be can be set in the chimney 5.Further, the clean water liquid storage
The shape of tank 13 can be the tapered shaped can that diameter gradually decreasees from top to bottom, and the inner wall of upper end tank mouth and the chimney 5 seals
Connection, in this way it can be ensured that it is real in turn to fall into clean water fluid reservoir 13 after clean water and smoke contacts that cleaning (operating) water nozzle 8 sprays
Now recycle.In another specific embodiment of the disclosure, the clean water spray unit can be set to be washed in described
It washs in tower tower body 3, at this moment, the tapered shaped can that the clean water fluid reservoir 13 or diameter gradually decrease from top to bottom, and on
The inner wall of tank mouth and the scrubbing tower tower body 3 is held to be tightly connected.Both the above embodiment can be individually present, can also be mutual
In conjunction with.Generally, the structure in chimney 5 is more simple compared in scrubbing tower tower body 3, therefore, engineered easy to implement in order to make,
It is preferred that clean water spray unit is arranged in the chimney 5, as shown in Figure 1；In addition, the clean water spray unit is set to
In the chimney 5, flue gas cleaned water spray before it will go out tower can be made, remove smoke trailing phenomenon to the greatest extent, solves
Blue smoke and plume subsidence problems, and the operating flexibility of scrubbing tower and upstream device is not influenced, while being additionally aided and being slowed down equipment corruption
Erosion.
According to the disclosure, the quantity of the cleaning (operating) water nozzle 8 of each clean water spray unit can be 1~12
It is a, preferably 4~8.When it is described cleaning (operating) water nozzle 8 quantity more than one when, the cleaning (operating) water nozzle 8 can circumferentially with/
Or radial direction is equally spaced, to improve spraying effect, wherein the circumferential direction and radial direction here and below is with scrubbing tower
And/or defined on the basis of the periphery of chimney.For example, it is 4 and circumferentially arranged one kind that Fig. 2, which is clean water nozzle quantity,
The schematic diagram of embodiment.When the quantity of the clean water spray unit is the clear of more than one and each clean water spray unit
When the quantity more than one of clean (operating) water nozzle, the cleaning (operating) water nozzle of two neighboring clean water spray unit can be circumferential and/or radial
Upper position is arranged across, to further increase spraying effect, for example, multiple cleaning (operating) water nozzles of each cleaning water unit can be with
It is arranged radially evenly, that is, is formed as a row, two rows of cleaning (operating) water nozzles of two neighboring clean water spray unit can be in 90 °
Or other angles be arranged.The shape of the cleaning (operating) water nozzle 8 can include but is not limited to common spiral spray without particular/special requirement
Mouth, fan nozzle, nozzle ring and various hole shapes the pressure atomized fog jet that shower water atomization may be implemented.It is described clear
The material of clean (operating) water nozzle can include but is not limited to that polytetrafluoro, stainless steel etc. are various to commonly use corrosion-resistant material also without particular/special requirement.
According to the disclosure, the clean water is the liquid without detergent, and further, the salt content of the clean water is not
Higher than the salt content for the flue gas condensing water collected by the exhanst gas outlet 6.Specifically, the clean water can be for selected from fresh
At least one of water, middle water and waste water Jing Guo desalting processing.In addition, according to actual needs, the clean water can also contain
There is additive, as long as the salt content increase of absorbing liquid used in absorbing liquid spray unit will not be made by meeting the additive,
The type of the additive does not have special limitation, such as can include but is not limited to defoaming agent etc..
The flue gas washing system of the disclosure can also include quenching unit, for carrying out fast cooling to flue gas, along flue gas
Flow direction is set to before absorbing liquid spray unit, such as can be set in scrubbing tower or outside scrubbing tower, and structure can be with
To be common in existing wet flue gas washing system, the disclosure does not have special limitation and repeats no more.
According to the disclosure, the absorbing liquid spray unit can be structure common in existing wet flue gas washing system,
The disclosure does not have special limitation to it.Only the specific embodiment of absorbing liquid spray unit property for example is retouched below
State, those skilled in the art it should be understood that how the specific structure of absorbing liquid spray unit has no effect on the disclosure
It realizes.
For example, the absorbing liquid spray unit can be multiple.The absorbing liquid spray unit may include the first absorption
Liquid spray unit and the second absorbing liquid spray unit, the first absorbing liquid spray unit and the second absorbing liquid spray unit are along cigarette
The setting of flow of air direction interval, i.e., flue gas first passes through the first absorbing liquid spray unit and sprays using second absorbing liquid
Unit.The first absorbing liquid spray unit may include the first absorption nozzle for liquid 15 and be located under the first absorption nozzle for liquid
First absorbing liquid fluid reservoir 16 of side, described first absorb nozzle for liquid 15 and the first absorbing liquid fluid reservoir 16 respectively by pipeline with
First absorbing liquid circulating pump 11 is connected, and absorbing liquid used in the first absorbing liquid spray unit can be in the work of the first absorbing liquid circulating pump
With lower recycling.At this moment, the smoke inlet 2 can be provided with the first absorption nozzle for liquid 15 and the first absorbing liquid liquid storage
On 3 side wall of scrubbing tower tower body between tank 16, in this way, flue gas encounters upwards after entering scrubbing tower tower body 3 by the smoke inlet 2
First absorbs the absorbing liquid that nozzle for liquid 15 sprays, and starts the spray washing for carrying out the first absorbing liquid spray unit.Described first inhales
The efflux wastewater pipeline 12 for efflux wastewater can also be connected with by receiving liquid circulating pump 11.
Further, the first absorbing liquid fluid reservoir 16 can be the tapered shaped can that diameter gradually decreasees from top to bottom, and
The inner wall of upper end tank mouth and the scrubbing tower tower body 3 is tightly connected, so that it is guaranteed that first absorbs the absorbing liquid that nozzle for liquid 15 sprays
It is recycled with falling into the first absorbing liquid fluid reservoir 16 after smoke contacts and then realizing.Optional, the first absorbing liquid liquid storage
Waste liquid discharge pipe can be arranged in bottom in tank 16, for excluding absorbing liquid therein, to adjust the liquid level and absorption of absorbing liquid
The concentration of liquid.
Further, the described first quantity for absorbing nozzle for liquid 15 can be one or more.When first absorbing liquid
When the quantity of nozzle 15 is multiple, the first absorption nozzle for liquid 15 can circumferentially and/or be evenly radially arranged, to improve
Spraying effect.Described first absorbs the shape of nozzle for liquid 15 without particular/special requirement, can include but is not limited to common spiral nozzle,
The pressure atomized fog jet that shower water atomization may be implemented of fan nozzle, nozzle ring and various hole shapes.The cleaning
The material of (operating) water nozzle can include but is not limited to that polytetrafluoro, stainless steel etc. are various to commonly use corrosion-resistant material also without particular/special requirement.
Further, the second absorbing liquid spray unit may include the second absorption nozzle for liquid 10, be located at described second
Absorb the second absorbing liquid fluid reservoir 17 of 10 lower section of nozzle for liquid and axially through the more of the second absorbing liquid fluid reservoir 17
A second fluid reservoir flue 18.The second fluid reservoir flue 18 is for accommodating flue gas upwardly through the second absorbing liquid
Fluid reservoir 17, shape and size are not particularly limited, and can be Venturi tube similar with structure of column scrubber or other structures.Cigarette
Gas meets the absorbing liquid of the second absorption nozzle for liquid 10 ejection upwards, to carry out the spray washing of the second absorbing liquid spray unit.It is described
Second absorption nozzle for liquid 10 and the second absorbing liquid fluid reservoir 17 are connected by pipeline with the second absorbing liquid circulating pump 9 respectively, and second
Absorbing liquid used in absorbing liquid spray unit can be recycled under the action of the second absorbing liquid circulating pump.
Further, the quantity of the second absorbing liquid spray unit can be one or more.Second absorbing liquid
Fluid reservoir 17 can have the second fluid reservoir overflow port, and the second fluid reservoir overflow port, which is connected with, extends to the adjacent storage in lower section
Absorbing liquid overflow line 20 in flow container.When the quantity of the second absorbing liquid spray unit is one, the second absorbing liquid fluid reservoir
17 the second fluid reservoir overflow port is connected with the absorbing liquid overflow line 20 for extending to the first absorbing liquid fluid reservoir 16；When the second suction
When the quantity of receipts liquid spray unit is multiple, the second fluid reservoir overflow port connection for the second absorbing liquid fluid reservoir 17 being located above
There are the absorbing liquid overflow line 20 for extending to the second adjacent absorbing liquid fluid reservoir 17 of lower section, the second absorbing liquid liquid storage of bottom
Second fluid reservoir overflow port of tank 17 is connected with the absorbing liquid overflow line 20 for extending to the first absorbing liquid fluid reservoir 16；And
At this moment, clean water overflow line 21 can be extended to the second absorbing liquid fluid reservoir 17 of the top by clean water fluid reservoir overflow port
In；In this way, absorbing liquid can lead to when the liquid level in the second absorbing liquid fluid reservoir 17 is excessively high and reaches the second fluid reservoir overflow port
It crosses absorbing liquid overflow line 20 to enter in the fluid reservoir of lower section, recycles the absorbing liquid in whole system rationally.Described
The position that opens up of two fluid reservoir overflow ports can according to need and be designed, but need to make the second fluid reservoir flue 18
Upper end opening is higher than the second fluid reservoir overflow port, i.e. exhanst gas outlet position is higher than the liquid in the second absorbing liquid fluid reservoir 17
Position avoids flue gas from entering in the second absorbing liquid fluid reservoir 17.
Further, the second absorbing liquid fluid reservoir 17 can be the tapered shaped can that diameter gradually decreasees from top to bottom, and
The inner wall of upper end tank mouth and the scrubbing tower tower body 3 is tightly connected, in this way it can be ensured that second absorbs the suction that nozzle for liquid 10 sprays
The second absorbing liquid fluid reservoir 17 is fallen into after receiving liquid and smoke contacts and then realization recycles.
Further, the quantity of the second absorption nozzle for liquid 10 of each second absorbing liquid spray unit can be
It is multiple, and circumferentially and/or be evenly radially arranged, to improve spraying effect.Further, the second fluid reservoir fume pipe
It is consistent that the quantity in road 18 can absorb the quantity of nozzle for liquid 10 with described second, and is located at second absorbing liquid correspondingly
The lower section of nozzle 10 is absorbed in this way, the flue gas overflowed by the second fluid reservoir flue 18 can directly be encountered by top second
The absorbing liquid that nozzle for liquid 10 sprays most optimally realizes the washing absorption effect of absorbing liquid.Described second absorbs nozzle for liquid 10
Shape can include but is not limited to common spiral nozzle, fan nozzle, nozzle ring and various aperture shapes without particular/special requirement
The pressure atomized fog jet that shower water atomization may be implemented of shape.The material of the cleaning (operating) water nozzle can wrap also without particular/special requirement
Include but be not limited to that polytetrafluoro, stainless steel etc. are various commonly uses corrosion-resistant material.
According to the disclosure, absorbing liquid used in the absorbing liquid spray unit can be common in wet flue gas washing system
, the disclosure does not have special limitation.For example, absorbing liquid used in the absorbing liquid spray unit can be for selected from sodium hydroxide
At least one of solution, potassium hydroxide solution, sodium carbonate liquor and sodium bicarbonate solution.
According to the disclosure, can be offered on the side wall of the scrubbing tower tower body 3 for supplementing cleaning into the system
The replenisher entrance Isosorbide-5-Nitrae of water and/or absorbing liquid.The replenisher entrance Isosorbide-5-Nitrae opens up position on the side wall of scrubbing tower tower body 3
It can be designed according to the structure of absorbing liquid spray unit, for example, in embodiment listed above, the replenisher entrance
Open up position of the Isosorbide-5-Nitrae on the side wall of scrubbing tower tower body 3 can be for close to the first absorbing liquid fluid reservoir 16 and/or the second suction
Receive the upper end tank mouth of liquid fluid reservoir 17.When the upper end of the first absorbing liquid fluid reservoir 16 and/or the second absorbing liquid fluid reservoir 17
When the inner wall of tank mouth and the scrubbing tower tower body 3 is tightly connected, the replenisher entrance 17 can be provided with the junction.
According to the disclosure, the structure of the chimney 5 can be the common structure in existing wet flue gas washing system, this public affairs
Open not special limitation.For example, the chimney 5 can be the tubular that upper and lower ends are open respectively, at this moment, flue gas can be direct
Chimney 5 is entered by scrubbing tower tower body 3.In addition, the tubular of the chimney 5 or upper end opening, lower end closed, and close
The periphery at cylinder bottom has flue gas to collect bent passage, and flue gas can first rise to the passway, and then downlink enters back into chimney 5, with reality
The separation of existing flue gas and drop.In such cases, the clean water overflow line 21 can be with the bottom end of chimney 5 described in hermetically passing
And it extends in underlying absorbent liquid fluid reservoir.
The flue gas washing system of the disclosure can be used for various industrial process, including power generation, petrochemical industry, inorganic chemical industry
Deng the pollutant in handled flue gas can include but is not limited to SOx、NOx、NH3、CO、CO2、Cl2, HCl etc..Particularly, originally
Disclosed system is particularly suitable for the wet scrubbing processing of catalytic cracking unit regenerated flue gas, the technique of the catalytic cracking unit
Without specifically limited, regenerative operation mode can be regeneration or incomplete regen-eration completely for type, process scale, catalyst etc..
The washing side in specific embodiment using the system of the disclosure to flue gas is simply introduced below in conjunction with attached drawing 1-2
Method with the system for further illustrating the disclosure, but does not constitute the limitation to the disclosure.
By taking flue gas washing system as shown in Figure 1 is for the wet scrubbing processing of catalytic cracking unit regenerated flue gas as an example.
With SO2It counts, SO in heat boiler outlet flue gasxContent can be in 50-10000mg/m3, preferably in 100-5000mg/m3；Solid
Particle content can be in 10-1000mg/m3, preferably in 30-500mg/m3.Temperature into the regenerated flue gas of system can be
50-500 DEG C, preferably at 100-300 DEG C.The salt content for the efflux wastewater collected by efflux wastewater pipeline 12 is in 0.1-10 weight
% is measured, preferably in 2-8 weight %.The salt content for the flue gas condensing water collected by exhanst gas outlet 6 can be 0.01-0.5 weight %.
Flue gas enters system by smoke inlet 2, successively sprays upwards through the first absorbing liquid spray unit and the second absorbing liquid
The pH of absorbing liquid used in the spray washing of unit, the first absorbing liquid spray unit and the second absorbing liquid spray unit can be in 5-
10, preferably in 6.5-9.The quantity of second absorbing liquid spray unit is 1.First absorbing liquid fluid reservoir 16 and the storage of the second absorbing liquid
Flow container 17 is respectively the tapered shaped can that diameter gradually decreasees from top to bottom, and the inner wall of upper end tank mouth and scrubbing tower tower body 3 seals and connects
It connects.Second fluid reservoir overflow port of the second absorbing liquid fluid reservoir 17 is connected with the absorption extended in the first absorbing liquid fluid reservoir 16
Liquid overflow line 20.The upper end opening of second fluid reservoir flue 18 is higher than the second fluid reservoir overflow port.
Flue gas by continuing to rise after the spray washing of the first absorbing liquid spray unit and the second absorbing liquid spray unit, into
Enter chimney 5.The quantity of clean water spray unit is 1.It cleans (operating) water nozzle 8 and uses polytetrafluoro material spiral nozzle, quantity 4
Branch is circumferentially 90 ° of arrangements by angle, as shown in Figure 2.Clean water fluid reservoir 13 is the taper that diameter gradually decreasees from top to bottom
Tank, and the inner wall of upper end tank mouth and chimney 5 is tightly connected.The clean water collected in clean water fluid reservoir 13 can be stored up by clean water
Flow container overflow port enters in the second absorbing liquid fluid reservoir 17.The upper end opening of clean water fluid reservoir flue 19 is higher than clean water
Fluid reservoir overflow port.Clean water used is fresh process water, and salt content is not higher than 0.01 weight %.
The pump discharge pressure for cleaning (operating) water nozzle 8 can be 0.1-10MPa, preferably 0.1-1.0MPa.It is supplied in clean water
In the case that 7 conveying clean water circulation of pump is for spraying, the spray flow of clean water can be much higher than the magnitude of recruitment of clean water, practical to spray
Leaching amount depends on the efficiency of clean water transfer pump 7 and cleans the quantity and bore size of (operating) water nozzle 8.Clean water magnitude of recruitment, which is included in, is
In moisturizing total amount of uniting, and convert according to evaporation capacity and outer displacement rate of water make-up (the moisturizing total amount of system of other replenisher entrances
Equal to the sum of evaporation capacity and efflux wastewater amount).In the limiting case, system water supplement can be entered by cleaning (operating) water nozzle 8, total
Water consumption is not significantly increased, or even flue gas hangover and subsidence problems are solved in the case where decreasing.For example, fresh clean water
The ratio of magnitude of recruitment and flue gas is typically not greater than 0.15kg/Nm3, preferably 0.001-0.05kg/Nm3.With the cleaning after smoke contacts
Water recycles after can collecting, and to reuse and increase spray flow, the ratio of the spray flow of clean water and flue gas can be with are as follows:
0.001-0.5kg water/Nm3Flue gas, preferably 0.01-0.2kg water/Nm3Flue gas, wherein Nm3Refer to the gas volume under the status of criterion.
Finally, the flue gas after washing, by 6 discharge system of exhanst gas outlet, observation has no that flue gas hangover, blue smoke and plume sink
Phenomena such as.
The preferred embodiment of the disclosure is described in detail in conjunction with attached drawing above, still, the disclosure is not limited to above-mentioned reality
The detail in mode is applied, in the range of the technology design of the disclosure, a variety of letters can be carried out to the technical solution of the disclosure
Monotropic type, these simple variants belong to the protection scope of the disclosure.
It is further to note that specific technical features described in the above specific embodiments, in not lance
In the case where shield, can be combined in any appropriate way, in order to avoid unnecessary repetition, the disclosure to it is various can
No further explanation will be given for the combination of energy.
In addition, any combination can also be carried out between a variety of different embodiments of the disclosure, as long as it is without prejudice to originally
Disclosed thought equally should be considered as disclosure disclosure of that.
Claims (8)
1. a kind of flue gas washing system, which includes: scrubbing tower tower body (3), the chimney that is connected to the scrubbing tower tower body (3)
(5), the flue gas for being set to the smoke inlet (2) of scrubbing tower tower body (3) lower part and being set at the top of the chimney (5)
It exports (6), is provided with absorbing liquid spray unit in the scrubbing tower tower body (3), which is characterized in that the absorbing liquid spray unit
Top be provided with clean water spray unit；
The clean water spray unit includes cleaning (operating) water nozzle (8), is located at the clean water liquid storage cleaned below (operating) water nozzle (8)
Tank (13) and multiple clean water fluid reservoir flues (19) axially through the clean water fluid reservoir (13) are described
Cleaning (operating) water nozzle (8) is connected by pipeline with clean water transfer pump (7) respectively with clean water fluid reservoir (13).
2. system according to claim 1, which is characterized in that the clean water fluid reservoir (13) has clean water fluid reservoir
Overflow port, the clean water fluid reservoir overflow port are connected with the clean water overflow line for extending to the absorbing liquid spray unit
(21)。
3. system according to claim 1, which is characterized in that the quantity of the clean water spray unit is one or more
It is a.
4. system according to claim 3, which is characterized in that the clean water spray unit is set to the chimney (5)
Interior, the upper end tank mouth of the clean water fluid reservoir (13) and the inner wall of the chimney (5) are tightly connected；And/or
The clean water spray unit is set in the scrubbing tower tower body (3), the upper end tank of the clean water fluid reservoir (13)
Mouth and the inner wall of the scrubbing tower tower body (3) are tightly connected.
5. system according to claim 1, which is characterized in that the quantity of cleaning (operating) water nozzle (8) is 1~12；When
When the quantity more than one of cleaning (operating) water nozzle (8), the cleaning (operating) water nozzle (8) is circumferentially and/or radial direction is equally spaced set
It sets.
6. system according to claim 1, which is characterized in that the cleaning (operating) water nozzle (8) is selected from spiral nozzle, sector
At least one of nozzle and nozzle ring.
7. system according to claim 1, which is characterized in that the salt of clean water used in the clean water spray unit contains
Salt content of the amount not higher than the flue gas condensing water collected by the exhanst gas outlet (6).
8. system according to claim 7, which is characterized in that the clean water is selected from fresh water, middle water and by de-
At least one of waste water of salt treatment.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2017110816255 | 2017-11-07 | ||
| CN201711081625 | 2017-11-07 |
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| Publication Number | Publication Date |
|---|---|
| CN208553709U true CN208553709U (en) | 2019-03-01 |
Family
ID=65482020
Family Applications (5)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820761233.7U Active CN208553709U (en) | 2017-11-07 | 2018-05-21 | Flue gas washing system |
| CN202311735143.2A Pending CN118320548A (en) | 2017-11-07 | 2018-05-21 | Flue gas scrubbing process and catalytic cracking process |
| CN201820761234.1U Active CN208626955U (en) | 2017-11-07 | 2018-05-21 | Flue gas washing system |
| CN201810491397.7A Pending CN109745803A (en) | 2017-11-07 | 2018-05-21 | Method for washing flue gas and catalyst cracking method |
| CN201820761232.2U Active CN208865401U (en) | 2017-11-07 | 2018-05-21 | Flue gas washing system |
Family Applications After (4)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202311735143.2A Pending CN118320548A (en) | 2017-11-07 | 2018-05-21 | Flue gas scrubbing process and catalytic cracking process |
| CN201820761234.1U Active CN208626955U (en) | 2017-11-07 | 2018-05-21 | Flue gas washing system |
| CN201810491397.7A Pending CN109745803A (en) | 2017-11-07 | 2018-05-21 | Method for washing flue gas and catalyst cracking method |
| CN201820761232.2U Active CN208865401U (en) | 2017-11-07 | 2018-05-21 | Flue gas washing system |
Country Status (1)
| Country | Link |
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| CN (5) | CN208553709U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114288826A (en) * | 2021-12-30 | 2022-04-08 | 苏州赢众环保有限公司 | Height difference overflow water supplementing method for multistage waste gas spray tower |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5296973A (en) * | 1976-02-12 | 1977-08-15 | Babcock Hitachi Kk | Mist removing apparatus |
| JPH0722675B2 (en) * | 1986-03-26 | 1995-03-15 | バブコツク日立株式会社 | Wet flue gas desulfurization equipment |
| CN201871320U (en) * | 2010-11-12 | 2011-06-22 | 中国石油化工股份有限公司 | Catalytic cracking regeneration flue gas desulfurization dedusting device |
| CN103059923B (en) * | 2011-10-18 | 2015-09-23 | 中国石油化工股份有限公司 | A kind of Light hydrocarbon oil catalytic conversion method with heat exchange |
| CN104258668B (en) * | 2014-10-13 | 2016-04-06 | 北京国电龙源环保工程有限公司 | A kind of washing degree of depth dust arrester |
| CN104874255A (en) * | 2015-06-08 | 2015-09-02 | 北京香源溪环保科技有限公司 | Demisting system with dedusting, demisting and water recovery functions |
-
2018
- 2018-05-21 CN CN201820761233.7U patent/CN208553709U/en active Active
- 2018-05-21 CN CN202311735143.2A patent/CN118320548A/en active Pending
- 2018-05-21 CN CN201820761234.1U patent/CN208626955U/en active Active
- 2018-05-21 CN CN201810491397.7A patent/CN109745803A/en active Pending
- 2018-05-21 CN CN201820761232.2U patent/CN208865401U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114288826A (en) * | 2021-12-30 | 2022-04-08 | 苏州赢众环保有限公司 | Height difference overflow water supplementing method for multistage waste gas spray tower |
| CN114288826B (en) * | 2021-12-30 | 2024-03-19 | 苏州赢众环保有限公司 | Height difference overflow water supplementing method of multi-stage waste gas spray tower |
Also Published As
| Publication number | Publication date |
|---|---|
| CN109745803A (en) | 2019-05-14 |
| CN208626955U (en) | 2019-03-22 |
| CN118320548A (en) | 2024-07-12 |
| CN208865401U (en) | 2019-05-17 |
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