CN216550283U - Reduce deposited dry coke quenching gas cooling device of incrustation scale - Google Patents
Reduce deposited dry coke quenching gas cooling device of incrustation scale Download PDFInfo
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- CN216550283U CN216550283U CN202220303659.4U CN202220303659U CN216550283U CN 216550283 U CN216550283 U CN 216550283U CN 202220303659 U CN202220303659 U CN 202220303659U CN 216550283 U CN216550283 U CN 216550283U
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Abstract
The utility model discloses a coke dry quenching gas cooling device for reducing scale deposit, relating to the technical field of coke dry quenching gas cooling devices and comprising: a main body; an air inlet seat; an air outlet seat; a rotating mechanism of a water tank seat and an arc fan is arranged; the cooling mechanism is provided with a conical seat and a conveying seat. According to the utility model, the generation of scale is reduced by arranging the rotating mechanism, cooling water enters the water tank seat through the water inlet pipe, the cooling water entering the water tank seat is contacted with the arc-shaped fan and impacts the arc-shaped fan, the arc-shaped fan is rotated through the rotating shaft under the impact influence, the arc-shaped fan rotates to stir water in the water tank seat, so that the generation of scale in the water tank seat is reduced, the cooling water in the first conveying pipe enters the conical seat along the inner wall of the conical seat, the cooling water in the second conveying pipe enters the conical seat along the inner wall of the second conveying pipe, and two types of cooling water form turbulent flow in the conical seat, so that the generation of scale in the conical seat is reduced.
Description
Technical Field
The utility model relates to the technical field of coke dry quenching gas cooling devices, in particular to a coke dry quenching gas cooling device capable of reducing scale deposition.
Background
The coke dry quenching refers to a coke quenching method for cooling red coke by inert gas, in the production process of coke dry quenching, a large amount of dust particles are mixed with circulating gas, and the coke dry quenching needs primary dust removal and secondary dust removal and dust removal treatment, wherein the primary dust removal and dust removal amount is large, the temperature is high, and the cooling treatment of a water cooling sleeve is needed.
At present dry quenching gaseous cooling device under long-time user state, the conveying pipeline of cooling water can be stained with the incrustation scale, and the incrustation scale is piled up and can be caused conveying pipeline's jam to influence the cooling effect, also need the shut down production to overhaul when conveying pipeline blocks up, influence production.
SUMMERY OF THE UTILITY MODEL
The present invention has been made to solve the above-mentioned problems occurring in the prior art, and an object of the present invention is to provide a dry quenching gas cooling apparatus that reduces scale deposition.
In order to achieve the purpose, the utility model provides the following technical scheme:
a dry quench gas cooling apparatus that reduces scale deposition, comprising:
a main body;
the air inlet seat is connected to one side of the outer wall of the main body;
the air outlet seat is positioned on one side, far away from the air inlet seat, of the outer wall of the main body;
the rotating mechanism is provided with a water tank seat and an arc-shaped fan, is arranged at the upper end of the main body and extends into the main body, and is used for increasing the flowing speed of water;
be provided with the cooling body of toper seat and transport seat, cooling body is located the bottom of main part and extends to the inside of main part for increase the cooling effect, the toper seat is located the inside of main part and is located the below of water tank seat.
As a still further scheme of the utility model: slewing mechanism is including water tank seat, inlet tube, axis of rotation and arc fan, the water tank seat sets up in the upper end of main part and extends to the inside of main part, the inlet tube sets up on the top of water tank seat and runs through to the inside of water tank seat, the axis of rotation sets up in the inside of water tank seat, and runs through to the below of main part from the inside top of water tank seat, the arc fan is located the inside of water tank seat and is located the outer wall of axis of rotation.
As a still further scheme of the utility model: cooling body is including first conveyer pipe, second conveyer pipe, transport seat, basin, outlet pipe and rotation leaf, the second conveyer pipe runs through to the upper end of toper seat from the bottom of water tank seat, first duct connections just extends to the upper end of toper seat in the bottom of water tank seat, first conveyer pipe is the annular setting in the outside of second conveyer pipe, go out the water piping connection in the bottom of main part, the basin sets up the inner wall bottom at the toper seat, the outer wall of second conveyer pipe and the outer wall of first conveyer pipe contact are connected to the transport seat, the inner wall that the rotation leaf is located the outlet pipe just sets up the bottom at the axis of rotation.
As a still further scheme of the utility model: the axis of rotation is connected with the rotation of water tank seat, the arc fan be the annular and be provided with a plurality of, the surface of arc fan is the cambered surface.
As a still further scheme of the utility model: the first conveying pipe is annularly provided with a plurality of, the position department that first conveying pipe and water tank seat contacted is provided with the opening.
As a still further scheme of the utility model: the second conveyer pipe respectively with water tank seat and toper seat fixed connection, the position department that the second conveyer pipe contacted with the inlet tube is provided with the opening, the position department that the second conveyer pipe contacted with the toper seat is provided with the opening, the transport seat is the inclined plane form, the diameter of axis of rotation is less than the diameter of second conveyer pipe.
As a still further scheme of the utility model: the conical seat is conical, the diameter of the upper end of the conical seat is smaller than that of the bottom end of the conical seat, and the rotating shaft penetrates through the inner portion of the water outlet pipe from the top end of the inner wall of the water tank seat.
Compared with the prior art, the utility model has the beneficial effects that:
1. the scale is reduced by arranging the rotating mechanism, cooling water enters the water tank seat through the water inlet pipe, the cooling water entering the water tank seat is contacted with the arc-shaped fan and impacts the arc-shaped fan, and is influenced by impact, the arc-shaped fan rotates through the rotating shaft, the arc-shaped fan rotates to stir water in the water tank seat, so that the scale generated in the water tank seat is reduced, the cooling water in the first conveying pipe enters the conical seat along the inner wall of the conical seat, the cooling water in the second conveying pipe enters the conical seat along the inner wall of the second conveying pipe, and two types of cooling water form turbulent flow in the conical seat, so that the scale generated in the conical seat is reduced;
2. realize gaseous abundant cooling and avoid the outlet pipe to be blockked up by the incrustation scale through setting up cooling body, the partial cooling water that gets into in the water tank seat gets into the toper seat through the first conveyer pipe of a plurality of, another partial cooling water gets into the toper seat through the second conveyer pipe in getting into the water tank seat, get into the partial cooling water of toper seat, get into first conveyer pipe through the transport seat, through first conveyer pipe, the setting of transport seat and second conveyer pipe, be convenient for get into the gas in the main part respectively with first conveyer pipe, transport seat and second conveyer pipe contact, thereby realize the function to gaseous abundant cooling, the water that gets into in the toper seat passes through outlet pipe discharge circulation and recycles, receive the axis of rotation and influence, the rotation leaf rotates along with the axis of rotation, from avoiding the outlet pipe to be blockked up by the incrustation scale.
Drawings
FIG. 1 is a schematic diagram of a dry quench gas cooling apparatus for reducing scale deposition;
FIG. 2 is a view of a dry quench gas cooling apparatus to reduce scale deposition;
fig. 3 is a view of a dry quenching gas cooling device to reduce scale deposition.
In the figure: 1. a main body; 2. an air inlet seat; 3. an air outlet seat; 4. a rotating mechanism; 401. a water tank base; 402. a water inlet pipe; 403. a rotating shaft; 404. an arc fan; 5. a cooling mechanism; 501. a first delivery pipe; 502. a second delivery pipe; 503. a conical seat; 504. a conveying seat; 505. a water outlet groove; 506. a water outlet pipe; 507. rotating the blades.
Detailed Description
Referring to fig. 1 to 3, in an embodiment of the present invention, a coke dry quenching gas cooling device for reducing scale deposition includes:
a main body 1;
the air inlet seat 2 is connected to one side of the outer wall of the main body 1;
the air outlet seat 3 is positioned on one side of the outer wall of the main body 1, which is far away from the air inlet seat 2;
a rotating mechanism 4 provided with a water tank seat 401 and an arc fan 404, the rotating mechanism 4 being provided at the upper end of the main body 1 and extending into the main body 1 for increasing the flow rate of water;
and the cooling mechanism 5 is provided with a conical seat 503 and a conveying seat 504, the cooling mechanism 5 is positioned at the bottom end of the main body 1 and extends to the inside of the main body 1 for increasing the cooling effect, and the conical seat 503 is positioned inside the main body 1 and is positioned below the water tank seat 401.
This kind of dry coke quenching gas cooling device is convenient for gaseous inside that gets into main part 1 through setting up air inlet seat 2, is convenient for reduce the production of incrustation scale through setting up slewing mechanism 4, is convenient for carry out abundant cooling to gaseous through setting up cooling body 5.
In fig. 2: slewing mechanism 4 is including water tank seat 401, inlet tube 402, axis of rotation 403 and arc fan 404, water tank seat 401 sets up in the upper end of main part 1 and extends to the inside of main part 1, inlet tube 402 sets up on the top of water tank seat 401 and runs through to the inside of water tank seat 401, axis of rotation 403 sets up in the inside of water tank seat 401, and run through to the below of main part 1 from the inside top of water tank seat 401, arc fan 404 is located the inside of water tank seat 401 and is located the outer wall of axis of rotation 403.
This kind of dry quenching gaseous cooling device, gaseous inside through the seat of admitting air 2 entering main part 1, meanwhile, the cooling water passes through the inside of inlet tube 402 entering water tank seat 401, the inside cooling water of entering water tank seat 401 contacts with arc fan 404 and strikes arc fan 404, receive the impact influence, arc fan 404 rotates through axis of rotation 403, arc fan 404 rotates and stirs the water in the water tank seat 401, thereby reduce the inside incrustation scale that produces of water tank seat 401.
In fig. 2-3: cooling mechanism 5 is including first conveyer pipe 501, second conveyer pipe 502, delivery seat 504, go out basin 505, outlet pipe 506 and rotation leaf 507, second conveyer pipe 502 runs through to the upper end of toper seat 503 from the bottom of water tank seat 401, first conveyer pipe 501 is connected at the bottom of water tank seat 401 and is extended to the upper end of toper seat 503, first conveyer pipe 501 is the annular setting in the outside of second conveyer pipe 502, outlet pipe 506 is connected the bottom at main part 1, go out basin 505 and set up the inner wall bottom at toper seat 503, delivery seat 504 is connected at the outer wall of second conveyer pipe 502 and is contacted with first conveyer pipe 501 outer wall, rotation leaf 507 is located the inner wall of outlet pipe 506 and sets up the bottom at the axis of rotation 403.
The partial cooling water entering the water tank seat 401 enters the conical seat 503 through the first delivery pipes 501, the other partial cooling water entering the water tank seat 401 enters the conical seat 503 through the second delivery pipes 502, the partial cooling water entering the conical seat 503 enters the first delivery pipes 501 through the delivery seats 504, and the gas entering the main body 1 is respectively contacted with the first delivery pipes 501, the delivery seats 504 and the second delivery pipes 502 through the first delivery pipes 501 and the delivery seats 504 and the second delivery pipes 502, so that the function of fully cooling the gas is realized.
In fig. 2: the rotating shaft 403 is rotatably connected with the water tank seat 401, a plurality of arc fans 404 are annularly arranged, and the surfaces of the arc fans 404 are arc surfaces.
This kind of dry quenching gaseous cooling device is convenient for the cooling water through setting up arc fan 404 and strikes arc fan 404 to make arc fan 404 rotate, stir the cooling water in water tank seat 401 through setting up arc fan 404.
In fig. 2-3: the first delivery pipe 501 is provided with a plurality of annular pipes, and a through opening is arranged at the position where the first delivery pipe 501 contacts the water tank base 401.
According to the coke dry quenching gas cooling device, the plurality of first conveying pipes 501 are arranged, so that cooling water in the water tank seat 401 can conveniently enter the conical seat 503 through the first conveying pipes 501, and the function of cooling gas is realized.
In fig. 2-3: the second delivery pipe 502 is respectively fixedly connected with the water tank base 401 and the conical base 503, a through hole is arranged at the position where the second delivery pipe 502 is contacted with the water inlet pipe 402, a through hole is arranged at the position where the second delivery pipe 502 is contacted with the conical base 503, the delivery base 504 is in an inclined plane shape, and the diameter of the rotating shaft 403 is smaller than that of the second delivery pipe 502.
According to the coke dry quenching gas cooling device, the second conveying pipe 502 is arranged, so that cooling water in the water tank seat 401 can conveniently enter the conical seat 503 through the second conveying pipe 502, and turbulent flow is formed between the cooling water entering the conical seat 503 through the first conveying pipe 501 and the cooling water entering the conical seat 503 through the second conveying pipe 502 through the conical seat 503, so that scale generated in the conical seat 503 is reduced.
In fig. 2-3: the conical seat 503 is conical, the diameter of the upper end of the conical seat 503 is smaller than that of the bottom end of the conical seat 503, and the rotating shaft 403 penetrates from the top end of the inner wall of the water tank seat 401 to the inside of the water outlet pipe 506.
According to the coke dry quenching gas cooling device, the rotating shaft 403 is arranged to facilitate the rotating shaft 403 to rotate so as to enable the rotating blades 507 to rotate, and the rotating blades 507 rotate to avoid water outlet pipe 506 blockage caused by scale accumulation.
The working principle of the utility model is as follows: when the gas cooling device is used, gas generated by a dry quenching blast furnace is filtered, the filtered gas enters the inside of the main body 1 through the air inlet seat 2, meanwhile, cooling water enters the inside of the water tank seat 401 through the water inlet pipe 402, the cooling water entering the inside of the water tank seat 401 is contacted with the arc-shaped fan 404 and impacts the arc-shaped fan 404, the arc-shaped fan 404 is influenced by the impact, the arc-shaped fan 404 rotates through the rotating shaft 403, the arc-shaped fan 404 rotates to stir water in the water tank seat 401, so that scale produced in the water tank seat 401 is reduced, partial cooling water entering the water tank seat 401 enters the conical seat 503 through the plurality of first conveying pipes 501, the other partial cooling water entering the water tank seat 401 enters the conical seat through the second conveying pipe 502, partial cooling water entering the conical seat 503 enters the first conveying pipe 501 through the conveying seat 504, and passes through the arrangement of the first conveying pipe 501, the conveying seat 504 and the second conveying pipe 502, be convenient for get into the interior gas of main part 1 respectively with first conveyer pipe 501, carry seat 504 and the contact of second conveyer pipe 502, thereby realize the function to gaseous full cooling, the cooling water in the first conveyer pipe 501 gets into in the toper seat 503 along the inner wall of toper seat 503, the cooling water in the second conveyer pipe 502 gets into in the toper seat 503 along the inner wall of second conveyer pipe 502, two kinds of cooling water form the turbulent flow in toper seat 503, thereby reduce the inside incrustation scale that produces of toper seat 503, the water that gets into in the toper seat 503 passes through outlet pipe 506 and discharges the circulation and recycle, receive axis of rotation 403 to rotate the influence, rotating blade 507 rotates along with axis of rotation 403 rotates and rotates, from avoiding outlet pipe 506 to be blockked up by the incrustation scale.
The above description is only for the preferred embodiment of the present invention, but the scope of the present invention is not limited thereto, and any person skilled in the art should be considered to be within the scope of the present invention, and the technical solutions and the utility model concepts of the present invention are equivalent to or changed within the scope of the present invention.
Claims (7)
1. A coke dry quenching gas cooling apparatus for reducing scale deposits, comprising:
a main body (1);
the air inlet seat (2), the air inlet seat (2) is connected to one side of the outer wall of the main body (1);
the air outlet seat (3) is positioned on one side, far away from the air inlet seat (2), of the outer wall of the main body (1);
the rotating mechanism (4) is provided with a water tank seat (401) and an arc-shaped fan (404), and the rotating mechanism (4) is arranged at the upper end of the main body (1), extends into the main body (1) and is used for increasing the flowing speed of water;
the cooling mechanism (5) is provided with a conical seat (503) and a conveying seat (504), the cooling mechanism (5) is located at the bottom end of the main body (1) and extends into the main body (1) for increasing the cooling effect, and the conical seat (503) is located inside the main body (1) and is located below the water tank seat (401).
2. The coke dry quenching gas cooling device for reducing scale deposition as claimed in claim 1, wherein the rotating mechanism (4) comprises a water tank base (401), a water inlet pipe (402), a rotating shaft (403) and an arc fan (404), the water tank base (401) is arranged at the upper end of the main body (1) and extends to the inside of the main body (1), the water inlet pipe (402) is arranged at the top end of the water tank base (401) and penetrates to the inside of the water tank base (401), the rotating shaft (403) is arranged in the water tank base (401) and penetrates to the lower part of the main body (1) from the top end of the inside of the water tank base (401), and the arc fan (404) is arranged in the water tank base (401) and is arranged at the outer wall of the rotating shaft (403).
3. The coke dry quenching gas cooling device for reducing scale deposition as claimed in claim 2, wherein the cooling mechanism (5) comprises a first delivery pipe (501), a second delivery pipe (502), a delivery seat (504), a water outlet groove (505), a water outlet pipe (506) and a rotating blade (507), the second delivery pipe (502) penetrates from the bottom end of the water tank seat (401) to the upper end of the conical seat (503), the first delivery pipe (501) is connected to the bottom end of the water tank seat (401) and extends to the upper end of the conical seat (503), the first delivery pipe (501) is annularly arranged outside the second delivery pipe (502), the water outlet pipe (506) is connected to the bottom end of the main body (1), the water outlet groove (505) is arranged at the bottom end of the inner wall of the conical seat (503), the delivery seat (504) is connected to the outer wall of the second delivery pipe (502) and is in contact with the outer wall of the first delivery pipe (501), the rotating blade (507) is positioned on the inner wall of the water outlet pipe (506) and is arranged at the bottom end of the rotating shaft (403).
4. The coke dry quenching gas cooling device for reducing scale deposition as claimed in claim 2, wherein the rotating shaft (403) is rotatably connected with the water tank base (401), the arc fan (404) is provided with a plurality of ring-shaped fans, and the surface of the arc fan (404) is arc-shaped.
5. A coke dry quenching gas cooling device to reduce scale deposition as claimed in claim 3, characterized in that the first duct (501) is provided in a ring shape with several openings where the first duct (501) contacts the water tank base (401).
6. The coke dry quenching gas cooling device for reducing scale deposition as claimed in claim 3, wherein the second delivery pipe (502) is fixedly connected with the water tank seat (401) and the conical seat (503), respectively, a through hole is arranged at the position where the second delivery pipe (502) is contacted with the water inlet pipe (402), a through hole is arranged at the position where the second delivery pipe (502) is contacted with the conical seat (503), the delivery seat (504) is in a slope shape, and the diameter of the rotating shaft (403) is smaller than that of the second delivery pipe (502).
7. The coke dry quenching gas cooling device for reducing scale deposition as claimed in claim 3, wherein the conical seat (503) is conical, the diameter of the upper end of the conical seat (503) is smaller than the diameter of the bottom end of the conical seat (503), and the rotating shaft (403) penetrates from the top end of the inner wall of the water tank seat (401) to the inside of the water outlet pipe (506).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202220303659.4U CN216550283U (en) | 2022-02-15 | 2022-02-15 | Reduce deposited dry coke quenching gas cooling device of incrustation scale |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202220303659.4U CN216550283U (en) | 2022-02-15 | 2022-02-15 | Reduce deposited dry coke quenching gas cooling device of incrustation scale |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN216550283U true CN216550283U (en) | 2022-05-17 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202220303659.4U Active CN216550283U (en) | 2022-02-15 | 2022-02-15 | Reduce deposited dry coke quenching gas cooling device of incrustation scale |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN216550283U (en) |
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2022
- 2022-02-15 CN CN202220303659.4U patent/CN216550283U/en active Active
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