CN107569962A - A kind of biomass directly-heated type fume high-temperature purifier - Google Patents
A kind of biomass directly-heated type fume high-temperature purifier Download PDFInfo
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- CN107569962A CN107569962A CN201711034546.9A CN201711034546A CN107569962A CN 107569962 A CN107569962 A CN 107569962A CN 201711034546 A CN201711034546 A CN 201711034546A CN 107569962 A CN107569962 A CN 107569962A
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Abstract
The invention discloses a kind of biomass directly-heated type fume high-temperature purifier, including shell, the top installation crown cap of the shell, and at the top opening of spiral demisting layer installation inside the housing, the inner middle layer of the shell is provided with active carbon layer, and the both sides up and down of active carbon layer are provided with shower, lead to stainless steel pipes between the water inlet and drainage pump delivery port of the shower to be tightly connected, the bottom of the shell is provided with cooling water tank, and the outlet side for the stainless steel pipes installed at the gas outlet of dedusting box is placed in cooling water tank, the inside and bottom of the dedusting box are respectively arranged with basket strainer and dust collection box, the cooling water tank and static put are tightly connected by stainless steel pipes between sedimentation basin, air dividing plate is installed at the gas outlet of the cooling water tank, and air dividing plate is arranged on the lower surface of lime white liquid layer.The present invention uses multilayer purification device, can effectively remove the pernicious gas after biomass combustion.
Description
Technical field
The present invention relates to flue gas purifying equipment technical field, specially a kind of biomass directly-heated type fume high-temperature purification dress
Put.
Background technology
At present, the mixture of gas and flue dust during flue gas, it is the main reason for polluting the atmosphere, in industrial production or to burn
During fired biomass stalk, flue gas is that purifying step is all had to pass through before discharging or reclaiming, and is calmed the anger in processing high temperature
When, especially boiler smoke when, the temperature of flue gas reaches Baidu's even more high sometimes, may result in cleaning device and is damaged,
So as to cause maintenance of equipment cost input larger, deficiency in economic performance is set.
The content of the invention
It is an object of the invention to provide a kind of biomass directly-heated type fume high-temperature purifier, to solve above-mentioned background skill
The problem of being proposed in art, possessed beneficial effect are；The present apparatus uses multilayer purification device, first by smog water process, drop
The temperature of low pressure gas, effectively purifier can be protected, so as to the service life of extension fixture, reduce user's
Economic input.
To achieve the above object, the present invention provides following technical scheme：A kind of biomass directly-heated type fume high-temperature purification dress
Put, including shell, the top installation crown cap of the shell, and at the top opening of spiral demisting layer installation inside the housing, it is described
The inner middle layer of shell is provided with active carbon layer, and the both sides up and down of active carbon layer are provided with shower, the shower
Lead to stainless steel pipes between water inlet and drainage pump delivery port to be tightly connected, and drainage pump is arranged on the bottom plate of shell, it is described
The bottom of shell is provided with cooling water tank, and the outlet side for the stainless steel pipes installed at the gas outlet of dedusting box is placed on cooling
In tank, the inside and bottom of the dedusting box are respectively arranged with basket strainer and dust collection box, the cooling water tank with it is static put it is heavy
Shallow lake is tightly connected between pond by stainless steel pipes, and is staticly settled pond and be divided into two Room of left and right, the drainage pump by filter
The water inlet of the pipeline of water inlet installation is placed on right ventricle, air dividing plate is provided with the gas outlet of the cooling water tank, and divide gas
Plate is arranged on the lower surface of lime white liquid layer.
Preferably, described staticly settle is provided with choke valve on the pipeline connected between pond and cooling water tank.
Preferably, stainless steel pipes are led between the delivery port of the drainage pump and the water inlet of cooling water tank to be tightly connected.
Preferably, the one side of the dedusting box is provided with flue dust import.
Preferably, the lime white liquid layer is arranged on the downside of shower.
Compared with prior art, the beneficial effects of the invention are as follows：The equipment is provided with reflux line below cooling water tank,
Water after use can be reused, solve the consumption of water resource, and in water circulation, can be again to temperature lowering water
Cold water supplement is carried out in groove, has reached the purpose of temperature with high efficiency, lime white liquid layer, Neng Gouyou is installed above cooling water tank
The organism-absorbing matter of effect reduces the discharge capacity of carbon dioxide and sulfur dioxide, to the greatest extent in sulfide caused by burning and carbide
The possible pollution for reducing biomass in burning to air, sets crown cap on the top of device, can effectively prevent down
Phenomena such as gas discharge speed slows down during the rainy day.
Brief description of the drawings
Fig. 1 is the structural representation of the present invention；
Fig. 2 is the internal structure schematic diagram of the present invention.
In figure：1- dedusting boxes；2- basket strainers；3- top caps；4- shells；5- dust collection box；6- stainless steel pipes；7- activated carbons
Layer；8- showers；9- lime white liquid layers；10- air dividing plates；11- cooling water tanks；12- spiral demisting layers；13- drainage pumps；14- is saved
Flow valve；15- staticly settles pond；16- filters.
Embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Site preparation describes, it is clear that described embodiment is only part of the embodiment of the present invention, rather than whole embodiments.It is based on
Embodiment in the present invention, those of ordinary skill in the art are obtained every other under the premise of creative work is not made
Embodiment, belong to the scope of protection of the invention.
Refer to Fig. 1 and Fig. 2, a kind of embodiment provided by the invention：A kind of biomass directly-heated type fume high-temperature purification dress
Put, including shell 4, the top installation crown cap 3 of shell 4, and spiral demisting layer 12 is arranged at the top opening inside shell 4, outside
The inner middle layer of shell 4 is provided with active carbon layer 7, and the both sides up and down of active carbon layer 7 are provided with shower 8, and shower 8 enters
Lead to stainless steel pipes 6 between the mouth of a river and the delivery port of drainage pump 13 to be tightly connected, and drainage pump 13 is arranged on the bottom plate of shell 4,
The bottom of shell 4 is provided with cooling water tank 11, and the outlet side for the stainless steel pipes 6 installed at the gas outlet of dedusting box 1 is placed
In cooling water tank 11, the inside and bottom of dedusting box 1 are respectively arranged with basket strainer 2 and dust collection box 5, cooling water tank 11 with it is static
Put and be tightly connected by stainless steel pipes 6 between sedimentation basin 15, and staticly settle pond 15 and two Room of left and right are divided into by filter 16,
The water inlet of the pipeline of the water inlet of drainage pump 13 installation is placed on right ventricle, and air dividing plate is provided with the gas outlet of cooling water tank 11
10, and air dividing plate 10 is arranged on the lower surface of lime white liquid layer 9, staticly settles the pipeline connected between pond 15 and cooling water tank 11
On be provided with choke valve 14, between the delivery port of drainage pump 13 and the water inlet of cooling water tank 11 lead to stainless steel pipes 6 sealing connect
Connect, the one side of dedusting box 1 is provided with flue dust import, and lime white liquid layer 9 is arranged on the downside of shower 8.
Operation principle：Device is arranged at the outlet flue of biomass combustion furnace during use, and dedusting box 1 is entered into flue gas
Mouth is connected with the smoke gas port of combustion furnace, and biomass enters inside dedusting box 1 in smog caused by burning along pipeline, and
The dust in smog in do not burn sufficient stalk and smog is stopped in dedusting box 1 by dedusting plate 2, is dropped and is being gathered dust
In box 5, then entered with the smog of high heat in cooling water tank 1, heat is only absorbed by the water, smog after rise to air dividing plate
10 enter lime white liquid layer 9 therewith, and lime white liquid layer 9 absorbs the sulfide in smog, and in sulfide and lime slurry
In substance reaction when, produce heat and cause vapor and a small amount of unreacted sulfide to continue to rise, active carbon layer 7 will be right
Sulfide in vapor is absorbed, and is flowed at top opening of the final innocuous gas through device extraneous.
It is obvious to a person skilled in the art that the invention is not restricted to the details of above-mentioned one exemplary embodiment, Er Qie
In the case of without departing substantially from spirit or essential attributes of the invention, the present invention can be realized in other specific forms.Therefore, no matter
From the point of view of which point, embodiment all should be regarded as exemplary, and be nonrestrictive, the scope of the present invention is by appended power
Profit requires rather than described above limits, it is intended that all in the implication and scope of the equivalency of claim by falling
Change is included in the present invention.Any reference in claim should not be considered as to the involved claim of limitation.
Claims (5)
1. a kind of biomass directly-heated type fume high-temperature purifier, including shell (4), it is characterised in that：The top of the shell (4)
End installation crown cap (3), and spiral demisting layer (12) is arranged at the internal top opening of shell (4), in the inside of the shell (4)
Layer is provided with active carbon layer (7), and the both sides up and down of active carbon layer (7) are provided with shower (8), the shower (8)
Lead to stainless steel pipes (6) between water inlet and drainage pump (13) delivery port to be tightly connected, and drainage pump (13) is arranged on shell (4)
Bottom plate on, the bottom of the shell (4) is provided with cooling water tank (11), and is installed at the gas outlet of dedusting box (1) stainless
The outlet side of steel conduit (6) is placed in cooling water tank (11), and the inside and bottom of the dedusting box (1) are respectively arranged with dedusting
Net (2) and dust collection box (5), the cooling water tank (11) and static put are sealed by stainless steel pipes (6) between sedimentation basin (15)
Connection, and staticly settle pond (15) and two Room of left and right, the pipe of drainage pump (13) the water inlet installation are divided into by filter (16)
The water inlet in road is placed on right ventricle, and air dividing plate (10), and air dividing plate (10) are provided with the gas outlet of the cooling water tank (11)
It is arranged on the lower surface of lime white liquid layer (9).
A kind of 2. biomass directly-heated type fume high-temperature purifier according to claim 1, it is characterised in that：The standing
Choke valve (14) is provided with the pipeline being connected between sedimentation basin (15) and cooling water tank (11).
A kind of 3. biomass directly-heated type fume high-temperature purifier according to claim 1, it is characterised in that：The drainage
Lead to stainless steel pipes (6) between the delivery port of pump (13) and the water inlet of cooling water tank (11) to be tightly connected.
A kind of 4. biomass directly-heated type fume high-temperature purifier according to claim 1, it is characterised in that：The dedusting
The one side of box (1) is provided with flue dust import.
A kind of 5. biomass directly-heated type fume high-temperature purifier according to claim 1, it is characterised in that：The lime
Slurry layer (9) is arranged on the downside of shower (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711034546.9A CN107569962A (en) | 2017-10-28 | 2017-10-28 | A kind of biomass directly-heated type fume high-temperature purifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711034546.9A CN107569962A (en) | 2017-10-28 | 2017-10-28 | A kind of biomass directly-heated type fume high-temperature purifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107569962A true CN107569962A (en) | 2018-01-12 |
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ID=61040994
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711034546.9A Pending CN107569962A (en) | 2017-10-28 | 2017-10-28 | A kind of biomass directly-heated type fume high-temperature purifier |
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| CN (1) | CN107569962A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114590607A (en) * | 2022-03-09 | 2022-06-07 | 上海电气集团股份有限公司 | Slag discharging system for high-temperature ash and use method thereof |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103638763A (en) * | 2013-11-28 | 2014-03-19 | 昆山亿诚化工容器有限公司 | Waste gas purification tower |
| CN104474870A (en) * | 2014-12-08 | 2015-04-01 | 冯学岭 | Novel desulfurization dust remover |
| CN104815505A (en) * | 2015-04-24 | 2015-08-05 | 东至绿洲环保化工有限公司 | Cyclic waste gas recovery purification device |
| CN106823764A (en) * | 2017-04-06 | 2017-06-13 | 齐东 | Devulcanizer, desulfurizing tower and desulphurization system |
| CN206295798U (en) * | 2016-12-07 | 2017-07-04 | 武汉中电楚能环保工程有限公司 | A kind of wet desulphurization device with float valve sieve aperture combined tray |
-
2017
- 2017-10-28 CN CN201711034546.9A patent/CN107569962A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103638763A (en) * | 2013-11-28 | 2014-03-19 | 昆山亿诚化工容器有限公司 | Waste gas purification tower |
| CN104474870A (en) * | 2014-12-08 | 2015-04-01 | 冯学岭 | Novel desulfurization dust remover |
| CN104815505A (en) * | 2015-04-24 | 2015-08-05 | 东至绿洲环保化工有限公司 | Cyclic waste gas recovery purification device |
| CN206295798U (en) * | 2016-12-07 | 2017-07-04 | 武汉中电楚能环保工程有限公司 | A kind of wet desulphurization device with float valve sieve aperture combined tray |
| CN106823764A (en) * | 2017-04-06 | 2017-06-13 | 齐东 | Devulcanizer, desulfurizing tower and desulphurization system |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114590607A (en) * | 2022-03-09 | 2022-06-07 | 上海电气集团股份有限公司 | Slag discharging system for high-temperature ash and use method thereof |
| CN114590607B (en) * | 2022-03-09 | 2024-03-19 | 上海电气集团股份有限公司 | Slag discharging system for high-temperature ash and using method thereof |
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Application publication date: 20180112 |
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| RJ01 | Rejection of invention patent application after publication |