CN210138571U - Activated carbon flue gas purification system adsorbed layer exhanst gas outlet steel screen - Google Patents
Activated carbon flue gas purification system adsorbed layer exhanst gas outlet steel screen Download PDFInfo
- Publication number
- CN210138571U CN210138571U CN201920822325.6U CN201920822325U CN210138571U CN 210138571 U CN210138571 U CN 210138571U CN 201920822325 U CN201920822325 U CN 201920822325U CN 210138571 U CN210138571 U CN 210138571U
- Authority
- CN
- China
- Prior art keywords
- holes
- steel plate
- flue gas
- diamond
- activated carbon
- 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.)
- Active
Links
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 101
- 229910000831 Steel Inorganic materials 0.000 title claims abstract description 86
- 239000010959 steel Substances 0.000 title claims abstract description 86
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 46
- 239000003546 flue gas Substances 0.000 title claims abstract description 46
- 238000000746 purification Methods 0.000 title claims abstract description 25
- 239000007789 gas Substances 0.000 title claims description 9
- 229910003460 diamond Inorganic materials 0.000 claims abstract description 59
- 239000010432 diamond Substances 0.000 claims abstract description 59
- 239000000779 smoke Substances 0.000 claims abstract description 27
- 238000001179 sorption measurement Methods 0.000 claims abstract description 25
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 21
- 238000000034 method Methods 0.000 claims abstract description 18
- 230000000149 penetrating effect Effects 0.000 claims abstract description 16
- 230000008569 process Effects 0.000 claims abstract description 14
- QNRATNLHPGXHMA-XZHTYLCXSA-N (r)-(6-ethoxyquinolin-4-yl)-[(2s,4s,5r)-5-ethyl-1-azabicyclo[2.2.2]octan-2-yl]methanol;hydrochloride Chemical compound Cl.C([C@H]([C@H](C1)CC)C2)CN1[C@@H]2[C@H](O)C1=CC=NC2=CC=C(OCC)C=C21 QNRATNLHPGXHMA-XZHTYLCXSA-N 0.000 claims description 37
- 229910001220 stainless steel Inorganic materials 0.000 claims description 6
- 239000010935 stainless steel Substances 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 4
- 238000004140 cleaning Methods 0.000 claims 1
- 239000000428 dust Substances 0.000 abstract description 14
- 239000010419 fine particle Substances 0.000 abstract description 6
- 230000000694 effects Effects 0.000 description 9
- 239000003517 fume Substances 0.000 description 7
- 239000002245 particle Substances 0.000 description 6
- 239000008187 granular material Substances 0.000 description 5
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 4
- 239000003344 environmental pollutant Substances 0.000 description 4
- 231100000719 pollutant Toxicity 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 238000012216 screening Methods 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005536 corrosion prevention Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000011143 downstream manufacturing Methods 0.000 description 2
- 238000004080 punching Methods 0.000 description 2
- 235000009165 saligot Nutrition 0.000 description 2
- 239000007790 solid phase Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 235000003283 Pachira macrocarpa Nutrition 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 240000001085 Trapa natans Species 0.000 description 1
- 235000014364 Trapa natans Nutrition 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000004503 fine granule Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 244000017160 saligot Species 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Images
Landscapes
- Treating Waste Gases (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
The utility model provides an active carbon flue gas purification system adsorption layer flue gas outlet steel plate net, which is provided with a steel plate, wherein the steel plate is provided with a smoke vent, the shape of the smoke vent is a rhombus hole, the rhombus hole is a long rhombus hole, the rhombus hole consists of two corresponding straight edges and two groups of corresponding rhombus edges, and the connecting direction of two rhombus vertexes of the two groups of corresponding rhombus edges is vertical to the falling direction of active carbon; the diamond holes are through holes penetrating through the steel plate, and the penetrating direction of the diamond holes obliquely penetrates through the outer wall of the steel plate from the inner wall of the steel plate on one side contacting with the activated carbon to form penetrating through holes. The problem that the activated carbon does not fall outwards in the downward moving process in an independent space, smoke passes through the adsorption layer with small resistance, and fine particles and dust in the adsorption layer can be effectively controlled to be discharged along with the smoke is solved; the utility model discloses but wide application is in activated carbon flue gas clean system.
Description
Technical Field
The utility model relates to a exhanst gas outlet steel sheet net especially relates to an active carbon flue gas purification system adsorbed layer exhanst gas outlet steel sheet net, belongs to the environmental engineering field.
Background
The active carbon flue gas purification technology has the advantages of good resource utilization and water saving performance, no water consumption in the operation process, no waste water and waste residue, short process flow, small occupied area, no dilute acid generation in the purification process, no corrosion prevention of equipment, dust removal function, no need of configuring a special dust remover, and capability of removing SO difficult to remove by a wet method3The chimney has the advantages of no need of corrosion prevention, no need of temperature rise of purified flue gas, transparent chimney outlet, no smoke plume phenomenon and the like.
The active carbon flue gas purification technology has the following principle that2O and O2The SO in the flue gas is removed by physical and chemical adsorption under the condition of2The NOx in the smoke reacts with ammonia gas to generate N under the catalytic action of the activated carbon2HCl, HF, dioxin and heavy metals are removed by physical adsorption of a microporous structure rich in activated carbon, and purification of various pollutants is realized in one set of device. The activated carbon adsorbing SO2 is recycled after regeneration, and meanwhile, the released sulfur dioxide-enriched gas can be processed into various sulfide chemical products, SO that the resource utilization of pollutants is realized.
In the activated carbon flue gas purification device, the fresh activated carbon which is filled or supplemented for the first time falls, is abraded and is sheared by rotating equipment in the transfer process in a circulating transportation system, and then the breakage is generated. The material system is provided with a screening device for screening out fine particles and powder so as to keep the air permeability and the adsorption efficiency of the adsorption tower. In the existing cross-flow moving bed adsorption device, flue gas enters an adsorption layer from a middle air inlet chamber and is discharged from air outlet chambers at two sides after purification. Activated carbon gets into the adsorbed layer from the top, adsorb saturated activated carbon and discharge from the lower part, pollutant among the adsorbed layer flue gas accomplishes the conversion between the gas-solid phase, the adsorbed layer activated carbon outwards falls easily among the downstream process, activated carbon piles up and can produce great resistance at the steel sheet mesh when the flue gas is outwards discharged from the steel mesh simultaneously, most passes through the screening plant along with the tiny granule of activated carbon and sieves except, nevertheless the tiny granule of the activated carbon and dust of surplus of sieving, some can be along with the fume emission after the purification, can influence the dust emission effect.
Therefore, the utility model provides an adsorbed layer exhanst gas outlet expanded metal net, activated carbon get into the adsorbed layer from the top, and the activated carbon that adsorbs saturation is discharged from the lower part, and the pollutant in the adsorbed layer flue gas accomplishes the conversion between the gas-solid phase, can realize that activated carbon is independent space and outwards falls at the downstream in-process, and the flue gas passes through the adsorbed layer with less resistance, also can the fine granule and the dust of effective control in the adsorbed layer along with the fume emission simultaneously.
SUMMERY OF THE UTILITY MODEL
The utility model discloses in the flue gas purification device to current active carbon, the adsorbed layer active carbon outwards falls from the steel sheet net easily in the downstream process, the active carbon is piled up and can produce great resistance at the steel sheet mesh when the flue gas is outwards discharged from the steel mesh, the tiny granule of the active carbon and dust of surplus of sieve, partly can accompany the fume emission after the purification, influence technical problem such as dust emission effect, an active carbon flue gas purification system adsorbed layer exhanst gas outlet steel sheet net is provided, can realize that the active carbon is independent space and outwards fall at the downstream in-process, the flue gas passes through the adsorbed layer with less resistance, tiny granule and dust in the effective control adsorbed layer simultaneously are along with fume emission.
Therefore, the flue gas outlet steel plate mesh of the adsorption layer of the activated carbon flue gas purification system is provided with a steel plate, the steel plate is provided with a smoke exhaust hole, the smoke exhaust hole is shaped like a rhombus hole, the rhombus hole is a long rhombus hole, the rhombus hole consists of two corresponding straight edges and two groups of corresponding rhombus edges, and the connecting line direction of two rhombus vertexes of the two groups of corresponding rhombus edges is vertical to the falling direction of activated carbon; the diamond holes are through holes penetrating through the steel plate, and the penetrating direction of the diamond holes obliquely penetrates through the outer wall of the steel plate from the inner wall of the steel plate on one side contacting with the activated carbon to form penetrating through holes.
Preferably, the diamond holes on the steel plate are arranged from top to bottom, and each row of diamond holes and an adjacent row of diamond holes are distributed in a staggered manner.
Preferably, the penetrating angle of the diamond holes which penetrate from the inner wall of the steel plate contacting with the activated carbon to the outer wall of the steel plate in an inclined and upward manner is 50-60 degrees.
Preferably, the opening of the diamond-shaped hole has the size that the distance between the connecting lines of two diamond vertexes of two corresponding diamond sides is 1.3 mm-1.5 mm, and the width between two corresponding straight sides of the diamond-shaped hole is 0.8mm-1 mm.
Preferably, the rhombic holes are three-dimensional rhombic holes, the row spacing of the three-dimensional rhombic holes is 10mm-11mm, and the line spacing is 4mm-5 mm.
Preferably, the rhombic holes are arranged in staggered rows, and the right side rhombus vertex of one row of rhombic holes in two adjacent rows of rhombic holes and the left side rhombus vertex of the other row of rhombic holes are arranged in the vertical direction.
Preferably, the rhombic holes are arranged in a staggered manner, and the rhombus vertexes of the rhombic holes in one of two adjacent rows of rhombic holes penetrate through a connecting line of the rhombus vertexes of the two connected rhombic holes and are positioned in the middle of the two connected rhombic holes.
Preferably, the steel plate net is made of stainless steel materials, and the thickness of the steel plate net is 0.7mm-1.0 mm.
Preferably, the diamond-shaped holes are stretching holes made by a stretching process.
The beneficial effects of the utility model are that, because the shape of the exhaust port on the steel sheet net is diamond-shaped hole, the percent opening of steel sheet net is greater than 25% for the pressure drop of discharging fume is less than 200Pa, is favorable to better discharging fume, and the pressure drop of steel sheet net self is less than 200Pa, and the flue gas passes through steel sheet net resistance and just very little, does not increase flue gas system's booster fan power almost, and energy-conserving effect is very obvious.
And the selection of the opening size of the three-dimensional diamond holes of the steel plate net is matched with the particle size of the smallest particles in the active carbon particle fraction, so that the active carbon is controlled in the adsorption layer and does not fall outwards, and the emission of fine particles and dust along with flue gas from the smoke exhaust holes of the steel plate net can be effectively controlled.
Meanwhile, the diamond holes are stretching holes manufactured by a stretching process, the diamond holes of the stretching process are similar to the shape of a shutter, and compared with a punching plane steel plate net, the steel plate net manufactured by the process has the same opening size, and the steel plate net with shutter type three-dimensional diamond holes can further effectively control the active carbon to be controlled in the adsorption layer without falling outwards, further effectively control the emission of fine particles and dust along with smoke from the open holes of the steel plate net, and has good emission effect.
The utility model discloses S31603 stainless steel is selected to the material of steel sheet net, and corrosion resistance is better, and the diamond hole forms tensile turn-ups for the tensile hole of tensile technology preparation, and intensity is better.
Drawings
Fig. 1 is a schematic view of a conventional steel plate net;
FIG. 2 is a schematic view of the installation of a steel plate net at the flue gas outlet of the adsorption layer of the flue gas purification system using activated carbon of the embodiment of the present invention;
FIG. 3 is a schematic diagram of a moving unit of an adsorption layer according to an embodiment of the present invention;
FIG. 4 is a schematic cross-sectional view of a diamond-shaped hole of a steel plate mesh according to an embodiment of the present invention;
FIG. 5 is a schematic diagram of a diamond hole plan arrangement;
FIG. 6 is a schematic view of a further diamond-shaped hole plan arrangement;
FIG. 7 is a schematic illustration of diamond shaped holes.
The symbols in the drawings illustrate that:
1. steel plate nets; 101. a steel plate; 102. a smoke vent; 103. straight sides; 104. a water chestnut edge; 105 water caltrop vertexes; 2. an air intake chamber; 3. an air outlet chamber; 4. activated carbon.
Detailed Description
The present invention will be further described with reference to the following examples.
Fig. 1 is a schematic view of a conventional steel plate mesh, and it can be seen that smoke discharge holes 102 on the steel plate mesh 1 are straight holes, activated carbon 4 is easily leaked from the straight holes, and the activated carbon 4 also easily blocks the straight holes, which causes difficulty in smoke discharge.
Fig. 2-7 are drawings of the embodiment of the present invention, and it can be seen that the present invention discloses an activated carbon flue gas purification system adsorption layer flue gas outlet steel plate net 1, which is provided with a steel plate 101, the steel plate 101 is provided with a smoke vent 102, the smoke vent 102 is shaped as a diamond 102, the diamond 102 is a long diamond, the diamond 102 is composed of two corresponding straight edges 103 and two groups of corresponding diamond edges 104, the connection direction of two diamond vertexes 105 of the two groups of corresponding diamond edges 104 is perpendicular to the falling direction of activated carbon; the rhombic holes are through holes penetrating through the steel plate 101, the penetrating direction of the rhombic holes 102 obliquely penetrates through the outer wall of the steel plate 101 from the inner wall of the steel plate 101, which is in contact with one side of the activated carbon, to form the penetrating through holes, the row spacing of the three-dimensional rhombic holes 102 is 10-11 mm, and the row spacing is 4-5 mm. As the smoke exhaust holes 102 in the steel plate net 1 are rhombic holes 102, and the aperture ratio of the steel plate net 1 is larger than 25%, the pressure drop of the exhausted smoke is smaller than 200Pa, better smoke exhaust is facilitated, the pressure drop of the steel plate net 1 is smaller than 200Pa, the resistance of the smoke passing through the steel plate net 1 is small, the power of a booster fan of a smoke system is hardly increased, and the energy-saving effect is very obvious.
The diamond holes 102 on the steel plate 101 are arranged from top to bottom, each row of diamond holes 102 and the adjacent row of diamond holes 102 are distributed in a staggered mode, the penetrating angle of the diamond holes penetrating from the inner wall of the steel plate 101, which is in contact with one side of the activated carbon, to the outer wall of the steel plate 101 in the upward inclined mode is 50-60 degrees, the activated carbon 4 can not leak as much as possible due to the arrangement of the angle in the direction, and the smooth discharge of the smoke discharge holes 102 is guaranteed.
The opening size of the diamond holes 102 is that the distance between the connecting lines of two diamond vertexes 104 of two groups of corresponding diamond edges 104 is 1.3 mm-1.5 mm, the width between two corresponding straight edges 103 of the diamond holes 102 is 0.8mm-1mm, generally 0.9mm, because the selection of the opening size of the three-dimensional diamond holes 102 of the steel screen 1 is matched with the particle size of the smallest particles in the active carbon particle fraction, generally the distance between the connecting lines of two diamond vertexes 104 of two groups of corresponding diamond edges 104 is 1.4mm, the effect is very good, the active carbon is controlled in the adsorption layer without falling outwards, and the emission of fine particles and dust from the smoke exhaust holes 102 of the steel screen 1 along with smoke can be effectively controlled.
As can be seen in fig. 5, the rhombic holes 102 are arranged in staggered rows, and the right rhombic vertex 104 of one row of rhombic holes 102 in two adjacent rows of rhombic holes 102 is vertically arranged with the left rhombic vertex 104 of the other row of rhombic holes 102, so that the aperture ratio can be increased, and the smoke dispersing effect can be improved; the diamond holes 102 can also be arranged in staggered rows according to the arrangement mode in fig. 6, the diamond vertexes of the diamond holes 102 in one of two adjacent rows of the diamond holes 102 pass through the connection line of the diamond vertexes 105 of the two connected upper and lower diamond holes 102 and are positioned in the middle of the two connected upper and lower diamond holes 102, and the opening ratio is further increased.
The arrangement pitch of the rhombic holes 102 arranged in parallel is 4mm-6mm, generally 5mm, the error can be controlled between 0.1mm-0.2mm, and the strength and the smoke scattering effect can be ensured.
In the embodiment, the steel plate net 1 is made of stainless steel, the thickness of the steel plate net 1 is 0.7mm-1.0mm, the diamond holes 102 are stretching holes manufactured by a stretching process, the diamond holes 102 are stretching holes manufactured by the stretching process, the shape of the diamond holes 102 of the stretching process is similar to that of a shutter, compared with a punching plane steel plate net, the steel plate net 1 manufactured by the process has the same opening size, the steel plate net 1 with the shutter type three-dimensional diamond holes 102 can further effectively control the active carbon 4 to be controlled in the adsorption layer without falling outwards, fine particles and dust are further effectively controlled to be discharged from the open holes of the steel plate net along with smoke, and the discharge effect is good.
The steel plate net 1 of the embodiment is made of S31603 stainless steel, so that the corrosion resistance is better, the diamond holes 102 are stretching holes manufactured by a stretching process, a stretching flanging is formed, the strength is better, the thickness of the stainless steel plate can be reduced, and the cost is reduced.
This embodiment has realized that active carbon 4 is independent space and outwards falls at the downward removal in-process, and the adsorbed layer is passed through with less resistance to the flue gas, and tiny granule and dust in the effective control adsorbed layer simultaneously also can be along with fume emission.
However, the above description is only an embodiment of the present invention, and the scope of the present invention should not be limited thereto, so that the replacement of the equivalent components or the equivalent changes and modifications made according to the protection scope of the present invention should be covered by the claims of the present invention.
Claims (9)
1. The utility model provides an active carbon gas cleaning system adsorbed layer exhanst gas outlet steel sheet net, is equipped with the steel sheet, be equipped with the exhaust hole on the steel sheet, characterized by: the smoke exhaust hole is in the shape of a rhombus hole, the rhombus hole is a long rhombus hole, the rhombus hole consists of two corresponding straight sides and two groups of corresponding rhombus sides, and the connecting direction of two rhombus vertexes of the two groups of corresponding rhombus sides is vertical to the falling direction of the active carbon; the diamond-shaped holes are through holes penetrating through the steel plate, and the penetrating direction of the diamond-shaped holes obliquely penetrates through the outer wall of the steel plate from the inner wall of the steel plate on one side contacting with the activated carbon to form penetrating through holes.
2. The activated carbon flue gas purification system adsorption layer flue gas outlet steel plate mesh of claim 1, which is characterized in that: the diamond holes on the steel plate are arranged from top to bottom, and each row of diamond holes and an adjacent row of diamond holes are distributed in a staggered mode.
3. The activated carbon flue gas purification system adsorption layer flue gas outlet steel plate mesh of claim 1, which is characterized in that: the penetrating angle of the diamond holes which obliquely penetrate from the inner wall of the steel plate on the side contacting with the active carbon to the outer wall of the steel plate is 50-60 degrees.
4. The activated carbon flue gas purification system adsorption layer flue gas outlet steel plate mesh of claim 1, which is characterized in that: the opening size of the rhombic hole is that the distance between the connecting lines of two rhombic vertexes of two corresponding rhombic sides of two groups of rhombic holes is 1.3-1.5 mm, and the width between two corresponding straight sides of the rhombic hole is 0.8-1 mm.
5. The activated carbon flue gas purification system adsorption layer flue gas outlet steel plate mesh of claim 1, which is characterized in that: the diamond holes are three-dimensional diamond holes, the row spacing of the three-dimensional diamond holes is 10mm-11mm, and the line spacing is 4mm-5 mm.
6. The activated carbon flue gas purification system adsorption layer flue gas outlet steel plate mesh of claim 1, which is characterized in that: the rhombic holes are arranged in staggered rows, and the right side diamond corner vertex of one row of rhombic holes in two adjacent rows of rhombic holes and the left side diamond corner vertex of the other row of rhombic holes are arranged in the vertical direction.
7. The activated carbon flue gas purification system adsorption layer flue gas outlet steel plate mesh of claim 1, which is characterized in that: the rhombic holes are arranged in a staggered manner, and the diamond vertex of one of the rhombic holes in two adjacent rows of the rhombic holes passes through a connecting line of the diamond vertexes of two connected upper and lower rhombic holes and is positioned in the middle of the two connected upper and lower rhombic holes.
8. The activated carbon flue gas purification system adsorption layer flue gas outlet expanded steel of any one of claims 1 to 7, wherein: the steel plate net is made of stainless steel materials, and the thickness of the steel plate net is 0.7mm-1.0 mm.
9. The activated carbon flue gas purification system adsorption layer flue gas outlet expanded steel of any one of claims 1 to 7, wherein: the diamond holes are stretching holes manufactured by a stretching process.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920822325.6U CN210138571U (en) | 2019-06-03 | 2019-06-03 | Activated carbon flue gas purification system adsorbed layer exhanst gas outlet steel screen |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920822325.6U CN210138571U (en) | 2019-06-03 | 2019-06-03 | Activated carbon flue gas purification system adsorbed layer exhanst gas outlet steel screen |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210138571U true CN210138571U (en) | 2020-03-13 |
Family
ID=69734170
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920822325.6U Active CN210138571U (en) | 2019-06-03 | 2019-06-03 | Activated carbon flue gas purification system adsorbed layer exhanst gas outlet steel screen |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN210138571U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110075663A (en) * | 2019-06-03 | 2019-08-02 | 威海浩洋机械制造有限公司 | Active carbon flue gas purification system adsorption layer exhanst gas outlet expanded metal lath |
-
2019
- 2019-06-03 CN CN201920822325.6U patent/CN210138571U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110075663A (en) * | 2019-06-03 | 2019-08-02 | 威海浩洋机械制造有限公司 | Active carbon flue gas purification system adsorption layer exhanst gas outlet expanded metal lath |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202725003U (en) | Compound type multifunctional ammonia desulphurization device | |
| CN201855651U (en) | Smoke adsorbing and purifying device | |
| CN102908867B (en) | Active coke smoke purifying device for optimizing air-flow distribution | |
| CN109772097B (en) | Activated carbon method flue gas purification device and flue gas purification method | |
| CN104826489B (en) | A kind of combined desulfurization and denitration fluidized bed plant based on activated carbon and low temperature catalyst | |
| CN109806723A (en) | A kind of cross-flow type activated coke moving bed sintering flue gas purifying tower | |
| CN103230724B (en) | New cross-convective flue gas purification absorption tower | |
| CN112675698B (en) | A separate chamber turbulent bed desulfurization, denitrification and dust removal device and its process | |
| CN210138571U (en) | Activated carbon flue gas purification system adsorbed layer exhanst gas outlet steel screen | |
| CN106110829A (en) | The airflow distribution device of activated coke flue gas adsorption tower | |
| CN102423604A (en) | Combined flue gas desulfurization and denitrification device | |
| CN201295585Y (en) | Flowing type organic waste gas treatment device integrating adsorption and desorption | |
| CN203315990U (en) | Cross flow type twin-stage moving bed active coke exhaust gas integration purifying tower | |
| CN206730794U (en) | Activated coke integrated purifying desulfurizer | |
| CN206688512U (en) | A kind of gas cleaning module for loaded particles catalyst or adsorbent | |
| CN203264529U (en) | Cross flow-convection flue gas purification and adsorption tower | |
| CN205965495U (en) | Removing device of many pollutants of dry process integration desorption | |
| CN202860367U (en) | Air distribution device of activated coke flue gas adsorption tower | |
| CN210495900U (en) | High-efficient single-tower desulfurization is dust removal defogging device in coordination | |
| CN208711431U (en) | An electrostatic photocatalytic mercury removal and dust removal device | |
| CN215086187U (en) | A multistage ammonia purification tower that spouts for flue gas active coke method degree of depth SOx/NOx control | |
| CN103768892B (en) | Radial Cross-flow Moving Bed Reactor for Removing Hydrogen Sulfide by Temperature Swing Adsorption | |
| CN106669359A (en) | Adsorption device for combined movable bed | |
| CN107754551A (en) | Activated coke smoke eliminator | |
| WO2018119812A1 (en) | Activated carbon adsorption tower and gas purification device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |