CN210786672U - Slurry plant odor washing tower - Google Patents
Slurry plant odor washing tower Download PDFInfo
- Publication number
- CN210786672U CN210786672U CN201921120600.6U CN201921120600U CN210786672U CN 210786672 U CN210786672 U CN 210786672U CN 201921120600 U CN201921120600 U CN 201921120600U CN 210786672 U CN210786672 U CN 210786672U
- Authority
- CN
- China
- Prior art keywords
- tower body
- spraying device
- tower
- trays
- washing tower
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000005406 washing Methods 0.000 title claims abstract description 31
- 239000002002 slurry Substances 0.000 title description 3
- 238000005507 spraying Methods 0.000 claims abstract description 48
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 27
- 238000010521 absorption reaction Methods 0.000 claims abstract description 13
- 238000012856 packing Methods 0.000 claims abstract description 12
- 238000005201 scrubbing Methods 0.000 claims abstract description 5
- 239000007921 spray Substances 0.000 abstract description 17
- 239000000428 dust Substances 0.000 abstract description 12
- 238000001816 cooling Methods 0.000 abstract description 8
- 239000007788 liquid Substances 0.000 abstract description 8
- 230000000694 effects Effects 0.000 abstract description 5
- 230000000149 penetrating effect Effects 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- QMMFVYPAHWMCMS-UHFFFAOYSA-N Dimethyl sulfide Chemical compound CSC QMMFVYPAHWMCMS-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000004537 pulping Methods 0.000 description 1
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- Separation Of Particles Using Liquids (AREA)
Abstract
The utility model discloses a thick liquid factory foul gas washing tower, including the tower body, have the gas outlet that is close to the air inlet on the lateral wall of tower body bottom and is located the tower body top on the tower body, in the tower body between air inlet and gas outlet, from bottom to top has set gradually first spray set, water spray tray, pall ring packing layer, second floor spray set, third spray set and defroster. The water spraying disc comprises a plurality of trays arranged on the upper portion of the water spraying disc, wherein the tray openings of the trays face upwards, and an absorption cover arranged on the lower portion of the water spraying disc, the trays are arranged in a vertically staggered mode, and an absorption cavity longitudinally penetrating through the tower body is formed in the absorption cover. The utility model discloses thick liquid factory foul smell scrubbing tower has increased the design of trickle dish except adopting multistage spray set, and the staggered arrangement about a plurality of tray of trickle dish, the trickle flows from upper tray both sides top-down, forms the water film, and the foul smell passes the water film from bottom to top, has increased foul smell and washing liquid area of contact and contact time, and it is more abundant to wash, can effectively guarantee to remove dust and cooling effect.
Description
Technical Field
The utility model belongs to the technical field of the foul smell of pulp mill is handled, concretely relates to pulp mill foul smell scrubbing tower.
Background
The process is characterized in that each workshop of a pulp mill evaporation, pulping, causticization and alkali furnace can generate odor in the operation process, the odor mainly comprises hydrogen sulfide, methyl mercaptan, methyl sulfide, water vapor and trace salt, although the concentration is extremely low, the direct discharge can still influence the surrounding environment, and the current treatment mode is dust removal, washing and cooling and then putting into a hearth (or an incinerator) for combustion.
The odor washing tower plays a very important role in the whole odor treatment process, and has the main functions of washing and cooling the odor and simultaneously having a partial dust removal function. The odor of the traditional odor washing tower enters the washing tower from the bottom, passes through the pall ring packing layer and the spraying device and then is discharged out of the washing tower. The washing tower has simple structure and convenient manufacture, but has poor dust removal effect, and the packing layer and the equipment at the rear section of the system are easy to block, so that the temperature of the odor out of the washing tower can not meet the requirement.
In view of the above, it is an urgent technical problem in the art to provide a new pulp mill ozone washing tower to overcome the above drawbacks in the prior art.
Disclosure of Invention
An object of the utility model is to overcome the aforesaid not enough, provide a washing more abundant, be difficult for blockking up rear end equipment, can effectively guarantee the thick liquid factory odor washing tower of dust removal and cooling effect.
In order to solve the technical problem, the utility model adopts the following technical scheme:
a slurry plant odor washing tower is characterized by comprising
The tower body, the said tower body is close to the sidewall of the bottom to have air inlets, the top of the said tower body has air outlets;
the first spraying device is arranged in the tower body and close to the upper part of the air inlet, and a plurality of nozzles are arranged on the first spraying device;
the water spraying disc is arranged above the first spraying device and comprises a plurality of trays with upward disc openings and an absorption cover, the trays are arranged on the upper portion of the water spraying disc, the absorption cover is arranged on the lower portion of the water spraying disc, the trays are arranged in a vertically staggered mode, and an absorption cavity which is longitudinally communicated with the tower body is formed in the absorption cover;
the pall ring packing layer is arranged above the water spraying disc;
and the second spraying device is arranged above the pall ring packing layer and is provided with a plurality of nozzles.
In the above technical solution, the spraying device further comprises a demister, and the demister is arranged above the second spraying device.
In the technical scheme, a third spraying device is arranged below the demister, and a plurality of nozzles are arranged on the third spraying device.
In the above technical solution, the third spraying device is set to be intermittently opened.
In the above technical scheme, the air inlet is an air inlet pipe arranged in a downward inclination manner.
In the above technical scheme, the nozzle is a spiral nozzle.
Compared with the prior art, the beneficial effects of the utility model reside in that: the utility model discloses thick liquid factory foul smell scrubbing tower has increased the design of trickle dish except adopting multistage spray set, and the staggered arrangement about a plurality of tray of trickle dish, the trickle flows from upper tray both sides top-down, forms the water film, and the foul smell passes the water film from bottom to top, has increased foul smell and washing liquid area of contact and contact time, and it is more abundant to wash, can effectively guarantee to remove dust and cooling effect.
Drawings
Fig. 1 is a schematic structural diagram of the odor washing tower of the pulp mill.
Wherein: 1-tower body (101-air inlet, 102-air outlet), 2-first spray device, 3-water spray tray (301-tray, 302-absorption hood), 4-pall ring packing layer, 5-second spray device, 6-demister, 7-third spray device, a-nozzle.
Detailed Description
The present invention will be described in further detail with reference to the accompanying drawings and specific embodiments.
As shown in figure 1, the odor washing tower of the pulp mill mainly has the functions of washing, cooling and dedusting the odor of the pulp mill, and comprises a tower body 1, a first spraying device 2, a water spraying disc 3, a pall ring packing layer 4 and a second spraying device 5.
The side wall of the tower body 1 close to the bottom is provided with an air inlet 101, and the top of the tower body is provided with an air outlet 102. Preferably, the intake port 101 is an intake pipe disposed to be inclined downward. The odor of the pulp mill enters the washing tower from the air inlet 101 at the bottom of the washing tower, the air inlet 101 is an air inlet pipe which is arranged in a downward inclination mode, the odor enters the tower body 1 and slightly inclines downward, and the gas can be ensured to flow upwards more uniformly.
The first spraying device 2 is arranged in the tower body 1 and close to the upper portion of the air inlet 101, and a plurality of nozzles a are arranged on the first spraying device 2. Preferably, the nozzle a is a spiral nozzle which can prevent the nozzle from being scaled and blocking the spray head. Preferably, the nozzles a of the first spray device 2 are opened downward so that the spray space of the nozzles can fully cover the entire odor inlet plane when the first spray device 2 is used. The first layer of spraying device 2 mainly has the function of removing dust and particles carried in odor.
The shower tray 3 sets up 2 tops of first spray set, the shower tray 3 is including locating a plurality of tray 301 of its upper portion's dish mouth up and locating the cage 302 of its lower part, staggered arrangement about a plurality of tray 301, the last edge of having seted up of cage 302 the absorption chamber that vertically link up of tower body 1. The shower water flows out from the top to the bottom from two sides of the shower tray 3 to form a water film, the odor passes through the water film from bottom to top, and dust and salt in the odor can be well captured, so that the purpose of dust removal is achieved. Preferably, the number of the water spraying discs 3 is determined by calculation.
The pall ring packing layer 4 is arranged above the water spraying disc 3. The second spraying device 5 is arranged above the pall ring packing layer 4. The pall ring packing layer and the second spraying device 5 mainly have the functions of cooling odor and removing dust. Preferably, a plurality of nozzles a are arranged on the second spraying device 5. Preferably, the nozzles a on the second spraying device 5 open downwards.
In order to reduce the water content of the odor at the outlet of the gas outlet 102 of the washing tower, the washing tower of the utility model is further provided with a demister 6, wherein the demister 6 is arranged above the second spraying device 5. Preferably, the demister 6 is a corrugated plate demister, the removal rate of the corrugated plate demister to liquid drops with the particle size of more than or equal to 20 microns is up to more than 90%, and the load of a post-stage treatment system can be reduced after moisture is removed.
And a third spraying device 7 is arranged below the demister 6, and a plurality of nozzles a are arranged on the third spraying device 7. To avoid clogging of the corrugated plate mist eliminator, it is preferable that the nozzles a on the third spray device 7 open upward. Preferably, the third spraying device 7 is set to be intermittently opened according to the blockage condition of the demister, and when the demister 6 is blocked, the third spraying device 7 is opened; when the demister 6 is not clogged, the third spraying device 7 is closed.
The utility model discloses a pulp mill foul gas scrubbing tower, except adopting multistage spray set, increased the design of trickle dish, the staggered arrangement about a plurality of tray of trickle dish, the trickle flows from upper tray both sides top-down, forms the water film, and the foul smell passes the water film from bottom to top, has increased foul smell and washing liquid area of contact and contact time, and it is more abundant to wash, can effectively guarantee to remove dust and cooling effect. The odor treated by the washing tower reduces the dust content, the rear-section equipment is not easy to block, and the combustion condition in the furnace can be met after the temperature is reduced and the moisture is removed.
Finally, it should be noted that the above embodiments are only used for illustrating the present invention and do not limit the protection scope of the present invention. In addition, after reading the technical content of the present invention, a person skilled in the art can make various changes, modifications or variations to the present invention, and all the equivalents thereof also belong to the protection scope defined by the claims of the present application.
Claims (6)
1. The utility model provides a pulp mill foul gas scrubbing tower which characterized in that: comprises that
The tower body, the said tower body is close to the sidewall of the bottom to have air inlets, the top of the said tower body has air outlets;
the first spraying device is arranged in the tower body and close to the upper part of the air inlet, and a plurality of nozzles are arranged on the first spraying device;
the water spraying disc is arranged above the first spraying device and comprises a plurality of trays with upward disc openings and an absorption cover, the trays are arranged on the upper portion of the water spraying disc, the absorption cover is arranged on the lower portion of the water spraying disc, the trays are arranged in a vertically staggered mode, and an absorption cavity which is longitudinally communicated with the tower body is formed in the absorption cover;
the pall ring packing layer is arranged above the water spraying disc;
and the second spraying device is arranged above the pall ring packing layer and is provided with a plurality of nozzles.
2. The pulp mill odor washing tower of claim 1, characterized in that: the spraying device further comprises a demister, and the demister is arranged above the second spraying device.
3. The pulp mill odor washing tower of claim 2, characterized in that: and a third spraying device is arranged below the demister, and a plurality of nozzles are arranged on the third spraying device.
4. The pulp mill odor washing tower of claim 3, characterized in that: the third spraying device is set to be opened intermittently.
5. The pulp mill odor washing tower of claim 1, characterized in that: the air inlet is an air inlet pipe which is arranged in a downward inclined mode.
6. The pulp mill odor washing tower of claim 1, characterized in that: the nozzle is a spiral nozzle.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201921120600.6U CN210786672U (en) | 2019-07-17 | 2019-07-17 | Slurry plant odor washing tower |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201921120600.6U CN210786672U (en) | 2019-07-17 | 2019-07-17 | Slurry plant odor washing tower |
Publications (1)
Publication Number | Publication Date |
---|---|
CN210786672U true CN210786672U (en) | 2020-06-19 |
Family
ID=71233790
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201921120600.6U Expired - Fee Related CN210786672U (en) | 2019-07-17 | 2019-07-17 | Slurry plant odor washing tower |
Country Status (1)
Country | Link |
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CN (1) | CN210786672U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114890383A (en) * | 2022-04-29 | 2022-08-12 | 浙江本源醇氢科技有限公司 | Skid-mounted methanol hydrogen production and filling integrated device |
-
2019
- 2019-07-17 CN CN201921120600.6U patent/CN210786672U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114890383A (en) * | 2022-04-29 | 2022-08-12 | 浙江本源醇氢科技有限公司 | Skid-mounted methanol hydrogen production and filling integrated device |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20200619 |