CN209501185U - Device for recovering powder in a kind of calcined coke production process - Google Patents
Device for recovering powder in a kind of calcined coke production process Download PDFInfo
- Publication number
- CN209501185U CN209501185U CN201821675852.0U CN201821675852U CN209501185U CN 209501185 U CN209501185 U CN 209501185U CN 201821675852 U CN201821675852 U CN 201821675852U CN 209501185 U CN209501185 U CN 209501185U
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- China
- Prior art keywords
- dust
- calcined coke
- liquid
- production process
- liquid collecting
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- 239000011329 calcined coke Substances 0.000 title claims abstract description 26
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 20
- 239000000843 powder Substances 0.000 title claims abstract description 17
- 239000007788 liquid Substances 0.000 claims abstract description 70
- 230000007246 mechanism Effects 0.000 claims abstract description 65
- 239000007921 spray Substances 0.000 claims abstract description 54
- 239000000428 dust Substances 0.000 claims abstract description 45
- 238000005507 spraying Methods 0.000 claims abstract description 23
- 239000007787 solid Substances 0.000 claims description 16
- 238000005192 partition Methods 0.000 claims description 13
- 239000004743 Polypropylene Substances 0.000 claims description 7
- -1 polypropylene Polymers 0.000 claims description 7
- 229920001155 polypropylene Polymers 0.000 claims description 7
- 239000000945 filler Substances 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 4
- 238000001914 filtration Methods 0.000 claims description 3
- 238000002386 leaching Methods 0.000 claims 2
- 239000002699 waste material Substances 0.000 abstract description 7
- 230000008901 benefit Effects 0.000 abstract description 5
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 238000012856 packing Methods 0.000 description 7
- 238000010586 diagram Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000004615 ingredient Substances 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses device for recovering powder in a kind of calcined coke production process, including cabinet, the upper end of cabinet is equipped with dust inlet pipe, dust inlet pipe is connected with the first aspiration pump, the lower end of dust inlet pipe is equipped with filter chamber, and the lower end of cabinet is equipped with dust outlet pipe, and dust outlet pipe is connected with the second aspiration pump.Dust can be sprayed by two-stage spraying mechanism by having the advantage that, liquid after spray can be recycled processing, reduce the waste of useful component in dust, gas further progress is filtered simultaneously, qualified gas is discharged, prevent calcined coke dust escapes the pollution to result in waste of resources with environment, improves the economic benefit of calcined coke manufacturing enterprise, meets the theory of environmental protection and energy saving.
Description
Technical field
The utility model relates to device for recovering powder in a kind of calcined coke production process, belong to mechanical equipment technical field.
Background technique
Calcined coke product, which collects, is also easy to produce calcined coke dust in transmission process, escaping for calcined coke dust easily causes resource
Waste, affects the economic benefit of calcined coke manufacturing enterprise, meanwhile, calcined coke dust escapes the pollution for easily causing environment, no
Meet the present age energy-saving and environment-friendly theory.
Utility model content
Problem to be solved in the utility model is to go out the stable defect of wind effect product for edge, provides a kind of calcining
Device for recovering powder in burnt production process can spray dust by two-stage spraying mechanism, and the liquid after spray can be with
It is recycled, reduces the waste of useful component in dust, while filtering to gas further progress, qualified gas is discharged
Body, prevent calcined coke dust escapes the pollution to result in waste of resources with environment, improves the economic effect of calcined coke manufacturing enterprise
Benefit meets the theory of environmental protection and energy saving.
To solve the above-mentioned problems, the utility model uses following technical scheme:
The upper end of device for recovering powder in a kind of calcined coke production process, including cabinet, cabinet is equipped with dust inlet pipe, dust
Inlet pipe is connected with the first aspiration pump, and the lower end of dust inlet pipe is equipped with filter chamber, and the lower end of cabinet is equipped with dust outlet pipe, dust outlet pipe
It is connected with the second aspiration pump；
The top of the filter chamber is equipped with the first spraying mechanism, and the first liquid collecting mechanism is equipped with below the first spraying mechanism, the
The lower section of one liquid collecting mechanism is equipped with the second spraying mechanism, and the lower section of the second spraying mechanism, the second spraying mechanism is equipped with the second liquid collecting
Mechanism, the lower section of the second liquid collecting mechanism are equipped with deflector, and the lower section of deflector is equipped with filter mechanism.
Further, first liquid collecting mechanism is equipped with the first liquid outlet, and the first liquid outlet is connected with the first collecting tank, the
Two liquid collecting mechanisms are equipped with the second liquid outlet, and the second liquid outlet is connected with the second collecting tank.
Further, first spraying mechanism includes two-stage spray tube, setting of arranging above and below two-stage spray tube, two-stage spray
Several first spray heads are uniformly provided in shower pipe, first spray head is solid cone shaped, and first spray head sprays the liquid for being atomized into 25~85um
Drop.
Further, second spraying mechanism includes two-stage spray tube, setting of arranging above and below two-stage spray tube, two-stage spray
Several second spray heads are uniformly provided in shower pipe, second spray head is eddy current type, and second spray head sprays the liquid for being atomized into 70~120 um
Drop.
Further, first liquid collecting mechanism is identical with the structure of the second liquid collecting mechanism, and the second liquid collecting mechanism includes collection
Liquid plate and catch tray, catch tray interval are arranged, and channel is equipped between catch tray.
Further, the liquid collecting plate is covered on the top in channel, and the both ends of liquid collecting plate are separately positioned on two interval collection
The top of liquid disk, the shape of liquid collecting plate are the shapes of falling V, and liquid of the spray containing dust is facilitated to enter in catch tray.
Further, the deflector includes several deflectors being arranged successively, between two adjacent deflectors
Distance is 45~53mm, and the height of deflector is 300~340mm, and the shape of deflector is arc.
Further, the filter mechanism includes orifice filter arranged at the bottom, and orifice filter is equipped with several ventilations
Hole, the top of orifice filter are equipped with several partitions, and partition is in honeycomb, are filled with the solid filter packing of several layers in partition.
Further, the diameter of the solid filter packing is 40~50mm, and orifice filter and partition are by polypropylene material
It is made, solid filter packing is solid polypropylene filler.
The utility model is had the following technical effect that compared with prior art using above technical scheme
Dust can be sprayed by two-stage spraying mechanism, the liquid after spray can be recycled processing, reduce
The waste of useful component in dust, while gas further progress is filtered, qualified gas is discharged, prevents calcined coke dust
The pollution to result in waste of resources with environment is escaped, the economic benefit of calcined coke manufacturing enterprise is improved, meets the reason of environmental protection and energy saving
It reads.
The utility model is described in detail with reference to the accompanying drawings and examples.
Detailed description of the invention
Attached drawing 1 is the structural schematic diagram that device for recovering powder is produced in this practical embodiment；
Attached drawing 2 is the structural schematic diagram of filter chamber in the utility model embodiment；
Attached drawing 3 is the structural schematic diagram of filter mechanism in the utility model embodiment.
Specific embodiment
Embodiment 1, as shown in Figure 1 to Figure 3, device for recovering powder in a kind of calcined coke production process, including cabinet 1, case
The upper end of body 1 is equipped with dust inlet pipe 2, and dust inlet pipe 2 is connected with the first aspiration pump 3, and the lower end of dust inlet pipe 2 is equipped with filter chamber 4,
The lower end of cabinet 1 is equipped with dust outlet pipe 5, and dust outlet pipe 5 is connected with the second aspiration pump 6.
The top of the filter chamber 4 is equipped with the first spraying mechanism 41, is equipped with the first liquid collecting machine below the first spraying mechanism 41
Structure 42, the lower section of the first liquid collecting mechanism 42 are equipped with the second spraying mechanism 44, the second spraying mechanism 44, under the second spraying mechanism 44
Side is equipped with the second liquid collecting mechanism 43, and the lower section of the second liquid collecting mechanism 43 is equipped with deflector 45, and the lower section of deflector 45 is equipped with
Filter mechanism 46, the first liquid collecting mechanism 42 are equipped with the first liquid outlet 10, and the first liquid outlet 10 is connected with the first collecting tank 8, and second
Liquid collecting mechanism 43 is equipped with the second liquid outlet 11, and the second liquid outlet 11 is connected with the second collecting tank 9.
First spraying mechanism 41 includes two-stage spray tube, setting of arranging above and below two-stage spray tube, on two-stage spray tube
Several first spray heads 411 are uniformly provided with, first spray head 411 is solid cone shaped, and the ejection of first spray head 411 is atomized into 25~85um's
Droplet.
Second spraying mechanism 44 includes two-stage spray tube, setting of arranging above and below two-stage spray tube, on two-stage spray tube
Several second spray heads 441 are uniformly provided with, second spray head 441 is eddy current type, and the ejection of second spray head 441 is atomized into 70~120 um's
Big drop.
First liquid collecting mechanism 42 is identical with the structure of the second liquid collecting mechanism 43, and the second liquid collecting mechanism 43 includes liquid collecting plate
47 and catch tray 49, the setting of the interval of catch tray 49 is equipped with channel 48 between catch tray 49, and liquid collecting plate 47 is covered on the upper of channel 48
Side, the both ends of liquid collecting plate 47 are separately positioned on the top of two interval catch trays 49, and the shape of liquid collecting plate 47 is the shape of falling V, convenient
Liquid of the spray containing dust enters in catch tray 49, and the liquid in catch tray 49 enters second by the second liquid outlet 11
Collecting tank 9, then the second collecting tank 9 is further recycled, it avoids wasting.
The deflector 45 includes several deflectors 451 being arranged successively, between two adjacent deflectors 451 away from
It is 300~340mm from the height for 45~53mm, deflector 451, the material of deflector 451 is superpower polypropylene, deflector
451 shape is arc.
The filter mechanism 46 includes orifice filter 461 arranged at the bottom, and orifice filter 461 is equipped with several ventilations
Hole, the top of orifice filter 461 are equipped with several partitions 462, and partition 462 is in honeycomb, and it is solid to be filled with several layers in partition 462
The diameter of filter packing 463, solid filter packing 463 is 40~50mm, and orifice filter 461 and partition 462 are by polypropylene material
It is made, solid filter packing 463 is solid polypropylene filler.
In use, dust is entered in filter chamber by dust inlet pipe 2, the first spraying mechanism first carries out the dust of entrance
It sprays, the liquid containing dust enters in the first liquid collecting mechanism after spray, then enters the first collection by the first liquid collecting mechanism
In slot, then the liquid in the first collecting tank is recycled, withdraws ingredient useful in dust, the dust run down is again
Second spraying mechanism sprays the dust of entrance, and the liquid after spray containing dust enters in the second liquid collecting mechanism, then
It is entered in the second collecting tank by the second liquid collecting mechanism, then the liquid in the second collecting tank is recycled, withdraw dust
In useful ingredient, then remaining dusty gas carries out water conservancy diversion by deflector, enters in filter mechanism, in filter mechanism
Further to being filtered in gas, remaining gas is discharged to by dust outlet pipe for orifice filter, partition, solid filter packing
In air, greatly reduce the harm to environment.
The above is the citing of the utility model preferred forms, wherein the part that do not address in detail is this field
The common knowledge of those of ordinary skill.The protection scope of the utility model is based on the contents of the claims, any to be based on this reality
The equivalent transformation carried out with novel technical inspiration, is also within the protection scope of the utility model.
Claims (9)
1. device for recovering powder in a kind of calcined coke production process, it is characterised in that: including cabinet (1), the upper end of cabinet (1) is set
Having dust inlet pipe (2), dust inlet pipe (2) is connected with the first aspiration pump (3), and the lower end of dust inlet pipe (2) is equipped with filter chamber (4),
The lower end of cabinet (1) is equipped with dust outlet pipe (5), and dust outlet pipe (5) is connected with the second aspiration pump (6)；
The top of the filter chamber (4) is equipped with the first spraying mechanism (41), and the first liquid collecting is equipped with below the first spraying mechanism (41)
The lower section of mechanism (42), the first liquid collecting mechanism (42) is equipped with the second spraying mechanism (44), the second spraying mechanism (44), the second spray
The lower section of mechanism (44) is equipped with the second liquid collecting mechanism (43), and the lower section of the second liquid collecting mechanism (43) is equipped with deflector (45), leads
The lower section for flowing mechanism (45) is equipped with filter mechanism (46).
2. device for recovering powder in a kind of calcined coke production process as described in claim 1, it is characterised in that: first collection
Liquid mechanism (42) is equipped with the first liquid outlet (10), and the first liquid outlet (10) is connected with the first collecting tank (8), the second liquid collecting mechanism
(43) the second liquid outlet (11) are equipped with, the second liquid outlet (11) is connected with the second collecting tank (9).
3. device for recovering powder in a kind of calcined coke production process as described in claim 1, it is characterised in that: first spray
Leaching mechanism (41) includes two-stage spray tube, and setting of arranging above and below two-stage spray tube is uniformly provided with several first on two-stage spray tube
Spray head (411), first spray head (411) are solid cone shaped, and first spray head (411) sprays the drop for being atomized into 25~85um.
4. device for recovering powder in a kind of calcined coke production process as described in claim 1, it is characterised in that: second spray
Leaching mechanism (44) includes two-stage spray tube, and setting of arranging above and below two-stage spray tube is uniformly provided with several second on two-stage spray tube
Spray head (441), second spray head (441) are eddy current type, and second spray head (441) sprays the drop for being atomized into 70~120 um.
5. device for recovering powder in a kind of calcined coke production process as described in claim 1, it is characterised in that: first collection
Liquid mechanism (42) is identical with the structure of the second liquid collecting mechanism (43), and the second liquid collecting mechanism (43) includes liquid collecting plate (47) and catch tray
(49), catch tray (49) interval is arranged, and is equipped with channel (48) between catch tray (49).
6. device for recovering powder in a kind of calcined coke production process as claimed in claim 5, it is characterised in that: the liquid collecting plate
(47) it is covered on the top of channel (48), the both ends of liquid collecting plate (47) are separately positioned on the top of two intervals catch tray (49),
The shape of liquid collecting plate (47) is the shape of falling V, and liquid of the spray containing dust is facilitated to enter in catch tray (49).
7. device for recovering powder in a kind of calcined coke production process as described in claim 1, it is characterised in that: the flow guiding machine
Structure (45) includes several deflectors (451) being arranged successively, and the distance between two adjacent deflectors (451) are 45~
53mm, the height of deflector (451) are 300~340mm, and the shape of deflector (451) is arc.
8. device for recovering powder in a kind of calcined coke production process as described in claim 1, it is characterised in that: the filter
Structure (46) includes orifice filter arranged at the bottom (461), and orifice filter (461) is equipped with several ventholes, orifice filter
(461) top is equipped with several partitions (462), and partition (462) is in honeycomb, is filled with the solid mistake of several layers in partition (462)
It filters filler (463).
9. device for recovering powder in a kind of calcined coke production process as claimed in claim 8, it is characterised in that: the solid mistake
The diameter for filtering filler (463) is 40~50mm, and orifice filter (461) and partition (462) are made of polypropylene material, solid mistake
Filtering filler (463) is solid polypropylene filler.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821675852.0U CN209501185U (en) | 2018-10-16 | 2018-10-16 | Device for recovering powder in a kind of calcined coke production process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821675852.0U CN209501185U (en) | 2018-10-16 | 2018-10-16 | Device for recovering powder in a kind of calcined coke production process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209501185U true CN209501185U (en) | 2019-10-18 |
Family
ID=68192369
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821675852.0U Active CN209501185U (en) | 2018-10-16 | 2018-10-16 | Device for recovering powder in a kind of calcined coke production process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209501185U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114100271A (en) * | 2021-11-11 | 2022-03-01 | 扬州杰嘉工业固废处置有限公司 | Purification treatment device and method for hazardous waste storage waste gas |
| CN114307463A (en) * | 2021-12-27 | 2022-04-12 | 北京华源泰盟节能设备有限公司 | Large-temperature-difference spray tower |
-
2018
- 2018-10-16 CN CN201821675852.0U patent/CN209501185U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114100271A (en) * | 2021-11-11 | 2022-03-01 | 扬州杰嘉工业固废处置有限公司 | Purification treatment device and method for hazardous waste storage waste gas |
| CN114307463A (en) * | 2021-12-27 | 2022-04-12 | 北京华源泰盟节能设备有限公司 | Large-temperature-difference spray tower |
| CN114307463B (en) * | 2021-12-27 | 2023-08-18 | 北京华源泰盟节能设备有限公司 | Large-temperature-difference spray tower |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 262737 No. 006067, Huanghe West Street, Binhai Economic Development Zone, Weifang City, Shandong Province Patentee after: China carbon energy (Shandong) Co., Ltd Address before: 262737 Binhai Economic Development Zone, Weifang City, Shandong Province Patentee before: China carbon energy (Shandong) Co., Ltd |