CN109173688A - One kind is from stirring-type absorption tower - Google Patents
One kind is from stirring-type absorption tower Download PDFInfo
- Publication number
- CN109173688A CN109173688A CN201811306102.0A CN201811306102A CN109173688A CN 109173688 A CN109173688 A CN 109173688A CN 201811306102 A CN201811306102 A CN 201811306102A CN 109173688 A CN109173688 A CN 109173688A
- Authority
- CN
- China
- Prior art keywords
- absorption tower
- spoiler
- slurries
- stirring
- 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.)
- Pending
Links
- 238000010521 absorption reaction Methods 0.000 title claims abstract description 77
- 239000002002 slurry Substances 0.000 claims abstract description 101
- 238000011084 recovery Methods 0.000 claims abstract description 17
- 238000005266 casting Methods 0.000 claims description 13
- 239000007921 spray Substances 0.000 claims description 10
- 239000007788 liquid Substances 0.000 claims description 4
- 239000003517 fume Substances 0.000 abstract description 6
- 230000008021 deposition Effects 0.000 abstract description 5
- 238000000034 method Methods 0.000 abstract description 5
- 230000008569 process Effects 0.000 abstract description 3
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 17
- 239000003546 flue gas Substances 0.000 description 17
- 239000013049 sediment Substances 0.000 description 12
- 230000015572 biosynthetic process Effects 0.000 description 8
- 239000007789 gas Substances 0.000 description 6
- 238000006477 desulfuration reaction Methods 0.000 description 5
- 230000023556 desulfurization Effects 0.000 description 5
- 239000000779 smoke Substances 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical group [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- GBAOBIBJACZTNA-UHFFFAOYSA-L calcium sulfite Chemical compound [Ca+2].[O-]S([O-])=O GBAOBIBJACZTNA-UHFFFAOYSA-L 0.000 description 1
- 235000010261 calcium sulphite Nutrition 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/80—Semi-solid phase processes, i.e. by using slurries
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/48—Sulfur compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0283—Flue gases
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treating Waste Gases (AREA)
Abstract
The invention discloses one kind from stirring-type absorption tower, is related to fume environment protection Treatment process field.Including absorption tower, slurry circulating pump and smoke-intake pipe road are equipped with outside the absorption tower, slurries bleed pipe and slurries recovery tube are communicated on the slurry circulating pump, the slurries bleed pipe is located at absorption tower top, the slurries recovery tube is located at absorb the bottom of the tower, the absorption tower side wall is equipped with multiple first spoilers, first spoiler is distributed in a ring, the absorb the bottom of the tower is equipped with multiple second spoilers, second spoiler is distributed in a ring, second spoiler is vertical with absorb the bottom of the tower, the nozzle of the slurries recovery tube is consistent with the tangential direction of inner wall of tower is absorbed.The beneficial effects of the present invention are: slurries itself kinetic energy can be utilized, prevents absorb the bottom of the tower from forming deposition.
Description
Technical field
It is specifically a kind of from stirring-type absorption tower the present invention relates to fume environment protection Treatment process field.
Background technique
Environmental protection is closely bound up with people's lives, and requirement of the people to environmental protection is also higher and higher, and gas cleaning desulfurization is work
Factory's flue gas outlet has to implementation.
So fume desulfurating absorption tower, is a kind of most of purifying smoke equipment for having flue gas outlet factory.Currently,
During using absorption tower purifying smoke, since the slurries main component of purifying smoke is calcium hydroxide solution, absorb
After sulfurous gas in flue gas, it is easy to produce calcium sulfite, it is easy to be formed and be deposited in absorb the bottom of the tower.
Existing conventional absorption tower slurries deposition in absorption tower in order to prevent, generallys use blender or increases pulse suspension
For pump to solve the problems, such as this, which not only adds additional equipment purchase expenses, even more increase production energy consumption, are unfavorable for energy conservation
The implementation of emission reduction.
Summary of the invention
The purpose of the present invention is to provide one kind from stirring-type absorption tower, can utilize slurries itself kinetic energy, prevent from absorbing
Tower bottom forms deposition.
The present invention to achieve the above object, is achieved through the following technical solutions:
One kind being communicated with slurry circulating pump and smoke-intake pipe from outside stirring-type absorption tower, including absorption tower, the absorption tower
Road, the slurry circulating pump are equipped with slurries bleed pipe and slurries recovery tube, and the slurries bleed pipe is located at absorption tower top, institute
It states slurries recovery tube and is located at absorb the bottom of the tower, the absorption tower side wall is equipped with multiple first spoilers, first spoiler
It being distributed in a ring, the absorb the bottom of the tower is equipped with multiple second spoilers, and second spoiler is distributed in a ring, and described second
Spoiler is vertical with absorb the bottom of the tower, and the nozzle of the slurries recovery tube is consistent with the tangential direction of inner wall of tower is absorbed.
First spoiler and absorption tower are side walls hinged, and first spoiler top is equipped with first rotating shaft, and described the
One shaft top, which is equipped with, swings disk, and the swing disk and first rotating shaft are hinged.
The cradle housing is equipped with arc-shaped rack, is equipped with motor outside the absorption tower, the output end of the motor is set
There is the second shaft, the end of second shaft is equipped with gear, and the gear is engaged with arc-shaped rack.
The cradle housing is equipped with square hole, and the rectangular hole width is consistent with first rotating shaft diameter, the square hole
Width be greater than first rotating shaft diameter.
First spoiler is located at minimum level top, and first spoiler lower part is equipped with pressure sensor, described
Receiver is equipped with outside absorption tower, the receiver is connect with pressure sensor.
First spoiler and the second flow-disturbing plate surface are equipped with casting lug thereon.
The casting lug thereon cross section is in arc-shaped.
The slurries spray one section that tube end is located in absorption tower and are equipped with multiple spray heads.
First spoiler and the second spoiler are in interleaved state up and down.
The prior art is compared, the beneficial effects of the present invention are:
1, when carrying out desulfurization to flue gas, flue gas enters in absorption tower from smoke-intake pipe road, and slurries are sprayed from slurries bleed pipe
Out, slurries are merged in absorption tower with flue gas, can absorb the sulfurous gas in flue gas, to realize the desulfurization to flue gas
Processing, then, slurries can accumulate in absorb the bottom of the tower, and slurries suction is entered to slurry circulating pump again by the slurries recovery tube,
Complete slurries recycling, when slurries absorb the bottom of the tower assemble after, due to slurries recovery tube absorb, rotate slurries, but
The kinetic energy that slurries positioned at absorption tower edge contain is smaller, can gradually deposit, first spoiler can to upper slurry into
Row is preliminary to be stirred, and second spoiler can be such that slurries are stirred again, so that the slurries at absorption tower edge is formed second level and is turned over
It is dynamic, enhance stirring for slurries, form turbulent flow, avoid the deposition of absorption tower edge slurries, in the feelings for not using external blender
Under condition, is realized and stirred using itself kinetic energy, reduce production cost.
2, first spoiler and absorption tower are side walls hinged, and first spoiler top is equipped with first rotating shaft, described
First rotating shaft top, which is equipped with, swings disk, and the swing disk and first rotating shaft are hinged, swings disk by rotation, makes first to disturb
The angle of flowing plate can be realized variation, and the angle of the first spoiler can be fixed according to the big minor adjustment of slurries kinetic energy, makes slurries
Maximum overturning amplitude can be obtained, simultaneously because between the first spoiler and absorption tower slurries sediment easy to form collection
Poly-, the angle for adjusting the first spoiler can be washed out sediment using slurries, ensure that the working efficiency of the first spoiler.
3, the cradle housing is equipped with arc-shaped rack, is equipped with motor, the output end of the motor outside the absorption tower
Equipped with the second shaft, the end of second shaft is equipped with gear, and the gear is engaged with arc-shaped rack, and the motor being capable of band
Dynamic second shaft rotation realizes so that the arc-shaped rack be driven to rotate and swings swinging back and forth for disk, to fast implement
The angular adjustment of first spoiler.
4, the cradle housing is equipped with square hole, and the rectangular hole width is consistent with first rotating shaft diameter, described rectangular
The width in hole is greater than the diameter of first rotating shaft, and the square hole can make the first spoiler can be realized quick swing, simultaneously also
The state of first spoiler can be fixed.
5, first spoiler is located at minimum level top, and first spoiler lower part is equipped with pressure sensor, institute
It states and is equipped with receiver outside absorption tower, the receiver is connect with pressure sensor, after slurries are located at minimum level or less, institute
Stating pressure sensor surface pressing is zero, can obtain the more of absorption tower inner pulp liquid measure by observing the received data of receiver
It is few, slurries are added in time convenient for staff.
6, first spoiler and the second flow-disturbing plate surface are equipped with casting lug thereon, and the casting lug thereon can prevent sediment
Gather in the first spoiler and the formation of the second flow-disturbing plate surface, ensure that the first spoiler and the second spoiler can play always
So that slurries is formed the effect of turbulent flow, ensure that the operational efficiency of whole device.
7, the casting lug thereon cross section is in arc-shaped, and the casting lug thereon of the arc-shaped is capable of increasing the first spoiler and second
The roughness of flow-disturbing plate surface, is capable of increasing the overturning degree of slurries, to further reduce the formation of slurries sediment.
8, the slurries spray one section that tube end is located in absorption tower equipped with multiple spray heads, and multiple spray heads can increase
Big slurries mix with flue gas degree, can be improved the degree of absorption to the sulfurous gas in flue gas, improve fume treatment matter
Amount.
9, first spoiler and the second spoiler are in interleaved state up and down, can further increase the disorderly of slurries
Stream, is further reduced the formation of slurries sediment.
Detailed description of the invention:
Attached drawing 1 is main view schematic cross-sectional view of the invention.
Attached drawing 2 is the top view on absorption tower of the invention.
Attached drawing 3 is the enlarged diagram in attached drawing 1 at I.
Attached drawing 4 is the main view schematic cross-sectional view of embodiment 2.
The top view of 5 embodiment 2 of attached drawing.
Attached drawing 6 is the enlarged diagram in attached drawing 5 at II.
Attached drawing 7 is schematic diagram of the casting lug thereon on the first spoiler.
Attached drawing 8 is the front sectional view of embodiment 3.
Label shown in attached drawing:
11, absorption tower；12, slurry circulating pump；13, smoke-intake pipe road；14, slurries bleed pipe；15, slurries recovery tube；21,
One spoiler；22, the second spoiler；31, first rotating shaft；32, disk is swung；33, arc-shaped rack；34, motor；35, second turn
Axis；36, gear；4, square hole；51, pressure sensor；52, receiver；6, casting lug thereon；7, spray head.
Specific embodiment
As shown in Fig. 1 to Fig. 8 combined with specific embodiments below, illustrating the present invention.It should be understood that these embodiments are only used for
It is bright the present invention rather than limit the scope of the invention.In addition, it should also be understood that, after reading the content taught by the present invention, ability
Field technique personnel can make various changes or modifications the present invention, and such equivalent forms equally fall within model defined herein
It encloses.
Embodiment 1:
As shown in Figures 1 to 3, of the present invention is a kind of from stirring-type absorption tower, including absorption tower 11, the absorption tower 11
It is the main body for absorbing smoke reaction, is communicated with slurry circulating pump 12 and smoke-intake pipe road 13, the slurries outside the absorption tower 11
Circulating pump 12 is recycled for slurries, and the slurry circulating pump 12 is equipped with slurries bleed pipe 14 and slurries recovery tube 15,
The slurries bleed pipe 14 is located at 11 top of absorption tower, and the slurries recovery tube 15 is located at 11 bottom of absorption tower, the absorption tower
11 side walls are equipped with multiple first spoilers 21, and first spoiler 21 is distributed in a ring, and 11 bottom of absorption tower is equipped with
Multiple second spoilers 22, second spoiler 22 are distributed in a ring, and second spoiler 22 hangs down with 11 bottom of absorption tower
Directly, the nozzle of the slurries recovery tube 15 is consistent with the tangential direction of 11 inner wall of absorption tower, when carrying out desulfurization to flue gas, flue gas
Entered in absorption tower 11 from smoke-intake pipe road 13, slurries are sprayed from slurries bleed pipe 14, slurries and flue gas in absorption tower 11 into
Row fusion, can absorb the sulfurous gas in flue gas, to realize that then, slurries can accumulate in suction to the desulfurization process of flue gas
11 bottom of tower is received, slurries suction is entered to slurry circulating pump 12 again, completes the recycling of slurries by the slurries recovery tube 15,
When slurries are after 11 congregate of absorption tower, since slurries recovery tube 15 absorbs, rotate slurries, but be located at 11 edge of absorption tower
The kinetic energy that contains of slurries it is smaller, can gradually deposit, first spoiler 21 upper slurry can be carried out it is preliminary stir,
Second spoiler 22 can be such that slurries are stirred again, so that the slurries at 11 edge of absorption tower is formed second level and stir, enhancing slurry
Liquid stirs, and forms turbulent flow, avoids the deposition of 11 edge slurries of absorption tower, in the case where not using external blender, benefit
It is realized and is stirred with itself kinetic energy, reduce production cost.
In order to improve fume treatment quality, 14 end of slurries bleed pipe be located in absorption tower 11 one section is equipped with multiple
Spray head 7, multiple spray heads 7 are capable of increasing slurries and mix with flue gas degree, can be improved to the sulfurous gas in flue gas
Degree of absorption improves fume treatment quality.
In order to be further reduced the formation of slurries sediment, first spoiler 21 is in the second about 22 spoiler
Interleaved state can further increase the turbulent flow of slurries, be further reduced the formation of slurries sediment.
Embodiment 2:
As shown in Figs. 4-6, of the present invention is a kind of from stirring-type absorption tower, first spoiler 21 and absorption tower
11 is side walls hinged, and 21 top of the first spoiler is equipped with first rotating shaft 31, and 31 top of first rotating shaft, which is equipped with, swings disk
32, the swing disk 32 and first rotating shaft 31 are hinged, swing disk 32 by rotation, enable the angle of the first spoiler 21
It realizes variation, the angle of the first spoiler 21 can be fixed according to the big minor adjustment of slurries kinetic energy, slurries is enable to obtain maximum
Overturning amplitude adjusted simultaneously because slurries sediment easy to form gathers between the first spoiler 21 and the absorption tower 11
The angle of first spoiler 21 can be washed out sediment using slurries, ensure that the working efficiency of the first spoiler 21.
In order to fast implement the angular adjustment of the first spoiler 21, the cradle housing is equipped with arc-shaped rack 33, described
Motor 34 is equipped with outside absorption tower 11, the output end of the motor 34 is equipped with the second shaft 35, the end of second shaft 35
Equipped with gear 36, the gear 36 is engaged with arc-shaped rack 33, and the motor 34 is able to drive the rotation of the second shaft 35, thus band
It moves the arc-shaped rack 33 to rotate, realizes and swing swinging back and forth for disk 32, to fast implement the first spoiler 21
Angular adjustment.
It quickly swings and the state of the first spoiler 21 is fixed, the cradle housing in order to realize
It is equipped with square hole 4,4 width of square hole is consistent with 31 diameter of first rotating shaft, and the width of the square hole 4 is big
In the diameter of first rotating shaft 31, the square hole 4 can make the first spoiler 21 can be realized quick swing, while can also incite somebody to action
The state of first spoiler 21 is fixed.
Embodiment 3:
As shown in Fig. 7 to 8, of the present invention is a kind of from stirring-type absorption tower, and first spoiler 21 is located at minimum
Ullage, 21 lower part of the first spoiler are equipped with pressure sensor 51, are equipped with receiver 52, institute outside the absorption tower 11
Receiver 52 is stated to connect with pressure sensor 51, after slurries are located at minimum level or less, 51 surface of the pressure sensor pressure
Power is zero, by observe the received data of receiver 52 can obtain 11 inner pulp liquid measure of absorption tower number, be convenient for work people
Member adds slurries in time.
In order to guarantee the operational efficiency of whole device, first spoiler 21 and 22 surface of the second spoiler are equipped with convex
Block 6 out, the casting lug thereon 6 can prevent sediment from gathering in the first spoiler 21 and the formation of 22 surface of the second spoiler, guarantee
First spoiler 21 and the second spoiler 22 can play the effect for making slurries form turbulent flow always, ensure that whole device
Operational efficiency.
In order to be further reduced the formation of slurries sediment, 6 cross section of casting lug thereon is in arc-shaped, the arc-shaped
Casting lug thereon 6 is capable of increasing the roughness on 22 surface of the first spoiler 21 and the second spoiler, is capable of increasing the overturning degree of slurries, from
And further reduce the formation of slurries sediment.
Claims (9)
1. one kind is communicated with slurry circulating pump and smoke-intake pipe road from outside stirring-type absorption tower, including absorption tower, the absorption tower,
The slurry circulating pump is equipped with slurries bleed pipe and slurries recovery tube, and the slurries bleed pipe is located at absorption tower top, described
Slurries recovery tube is located at absorb the bottom of the tower, it is characterised in that: and the absorption tower side wall is equipped with multiple first spoilers, and described the
One spoiler is distributed in a ring, and the absorb the bottom of the tower is equipped with multiple second spoilers, and second spoiler is distributed in a ring,
Second spoiler is vertical with absorb the bottom of the tower, the nozzle of the slurries recovery tube and the tangential direction one for absorbing inner wall of tower
It causes.
2. a kind of from stirring-type absorption tower according to claim 1, it is characterised in that: first spoiler and absorption tower side
Wall is hinged, and first spoiler top is equipped with first rotating shaft, and the first rotating shaft top, which is equipped with, swings disk, the swing circle
Disk is hinged with first rotating shaft.
3. a kind of from stirring-type absorption tower according to claim 2, it is characterised in that: the cradle housing is equipped with arc-shaped gear
Item, the absorption tower outside are equipped with motor, and the output end of the motor is equipped with the second shaft, and the end of second shaft is equipped with
Gear, the gear are engaged with arc-shaped rack.
4. a kind of from stirring-type absorption tower according to claim 2, it is characterised in that: the cradle housing is equipped with rectangular
Hole, the rectangular hole width is consistent with first rotating shaft diameter, and the width of the square hole is greater than the diameter of first rotating shaft.
5. a kind of from stirring-type absorption tower according to claim 1, it is characterised in that: first spoiler is located at minimum liquid
Face top, first spoiler lower part are equipped with pressure sensor, are equipped with receiver outside the absorption tower, the receiver with
Pressure sensor connection.
6. a kind of from stirring-type absorption tower according to claim 1, it is characterised in that: first spoiler and the second flow-disturbing
Plate surface is equipped with casting lug thereon.
7. a kind of from stirring-type absorption tower according to claim 6, it is characterised in that: the casting lug thereon cross section is in circular arc
Shape.
8. a kind of from stirring-type absorption tower according to claim 1, it is characterised in that: the slurries spray tube end and are located at suction
One section received in tower is equipped with multiple spray heads.
9. a kind of from stirring-type absorption tower according to claim 1, it is characterised in that: first spoiler and the second flow-disturbing
Plate is in interleaved state up and down.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811306102.0A CN109173688A (en) | 2018-11-05 | 2018-11-05 | One kind is from stirring-type absorption tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811306102.0A CN109173688A (en) | 2018-11-05 | 2018-11-05 | One kind is from stirring-type absorption tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109173688A true CN109173688A (en) | 2019-01-11 |
Family
ID=64941630
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811306102.0A Pending CN109173688A (en) | 2018-11-05 | 2018-11-05 | One kind is from stirring-type absorption tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109173688A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111097280A (en) * | 2019-12-23 | 2020-05-05 | 四川天壹环保科技有限公司 | Anti-sedimentation arrangement process for slurry of internal circulation desulfurization tower |
| CN112058072A (en) * | 2020-08-12 | 2020-12-11 | 北新建材(陕西)有限公司 | Desulfurizing device |
| CN116850763A (en) * | 2023-08-30 | 2023-10-10 | 济宁市嘉祥生态环境监控中心 | High-efficient thermal power flue gas desulfurization purification treatment device |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202942805U (en) * | 2012-12-10 | 2013-05-22 | 任传法 | Desulfurization tower bottom jet mixing system |
| US20130195728A1 (en) * | 2010-05-14 | 2013-08-01 | Houjie Sun | Wet flue gas desulfurization absorption tower for for power plant |
| CN209060885U (en) * | 2018-11-05 | 2019-07-05 | 山东国舜建设集团有限公司 | One kind is from stirring-type absorption tower |
-
2018
- 2018-11-05 CN CN201811306102.0A patent/CN109173688A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20130195728A1 (en) * | 2010-05-14 | 2013-08-01 | Houjie Sun | Wet flue gas desulfurization absorption tower for for power plant |
| CN202942805U (en) * | 2012-12-10 | 2013-05-22 | 任传法 | Desulfurization tower bottom jet mixing system |
| CN209060885U (en) * | 2018-11-05 | 2019-07-05 | 山东国舜建设集团有限公司 | One kind is from stirring-type absorption tower |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111097280A (en) * | 2019-12-23 | 2020-05-05 | 四川天壹环保科技有限公司 | Anti-sedimentation arrangement process for slurry of internal circulation desulfurization tower |
| CN112058072A (en) * | 2020-08-12 | 2020-12-11 | 北新建材(陕西)有限公司 | Desulfurizing device |
| CN116850763A (en) * | 2023-08-30 | 2023-10-10 | 济宁市嘉祥生态环境监控中心 | High-efficient thermal power flue gas desulfurization purification treatment device |
| CN116850763B (en) * | 2023-08-30 | 2024-02-23 | 济宁市嘉祥生态环境监控中心 | High-efficient thermal power flue gas desulfurization purification treatment device |
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