CN217511485U - Industrial steam quality improving device - Google Patents
Industrial steam quality improving device Download PDFInfo
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- CN217511485U CN217511485U CN202221414901.1U CN202221414901U CN217511485U CN 217511485 U CN217511485 U CN 217511485U CN 202221414901 U CN202221414901 U CN 202221414901U CN 217511485 U CN217511485 U CN 217511485U
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Abstract
The utility model discloses an industrial steam quality hoisting device, include: the two sides of the top end of the main tower are respectively provided with a main tower air inlet and a main tower air outlet; the bottom of the main tower is provided with a main tower drain outlet; the spiral separation module includes: a spiral separator, a central tube, and a separator; the spiral separating piece is spirally wound outside the central tube; the interior of the central tube is hollow, and two ends of the central tube are open; the top of the central pipe penetrates through the partition plate and is arranged at the top of the partition plate; an auxiliary tower air inlet is formed in the side wall of the bottom end of the auxiliary tower; an auxiliary tower air outlet is formed in the side wall of the top end of the auxiliary tower; the bottom of the auxiliary tower is provided with an auxiliary tower drain port; the tower separation assembly comprises: the supporting rod is arranged on the circular baffle; the annular baffle is fixedly connected with the inner wall of the auxiliary tower, and the support rod is fixedly connected with the circular baffle and the annular baffle; the sintered filter component is fixed at the top end of the interior of the auxiliary tower. The utility model provides a quality hoisting device can improve the dryness fraction and the cleanliness factor of steam, satisfies the production requirement.
Description
Technical Field
The utility model relates to a steam treatment equipment technical field, more specifically the utility model relates to an industrial steam quality hoisting device that says so.
Background
Along with the gradual maturity of the refined control process of industrial process, the requirement for gas quality in the steam use process is improved, and steam cleanliness and saturation are especially important in the technological process.
At present, the existing steam treatment equipment is single filtration or separation equipment, the dryness of the treated steam is low, a large amount of water and impurities are carried, the process requirement cannot be met, production process accidents can be caused due to the fact that the cleanliness and dryness of the steam are not in accordance with the requirement, terminal products are polluted, and great economic loss is caused by corrosion and scouring of process equipment.
Therefore, it is an urgent need to solve the above-mentioned problems by those skilled in the art to develop an industrial steam quality improving apparatus capable of improving dryness and cleanliness of steam.
SUMMERY OF THE UTILITY MODEL
In view of this, the utility model provides a can improve the industrial steam quality hoisting device of steam quality and cleanliness factor.
In order to realize the purpose, the utility model adopts the following technical scheme:
an industrial steam upgrading device comprising:
the two sides of the top end of the main tower are respectively provided with a main tower air inlet and a main tower air outlet; a main tower drain port is formed at the bottom of the main tower;
a spiral separation assembly disposed inside the main column; the spiral separation module comprises: a spiral separator, a central tube, and a separator; the spiral separating piece is spirally wound outside the central pipe, and a gap is reserved between the spiral separating piece and the inner wall of the main tower; the inner part of the central tube is hollow, and two ends of the central tube are open; the partition plate is arranged at the top of the main tower and is fixedly connected with the interior of the main tower; the partition board is inclined, the air inlet of the main tower is arranged below the partition board, and the air outlet of the main tower is arranged at the top of the partition board; the top of the central pipe penetrates through the partition plate, is arranged at the top of the partition plate and is fixedly connected with the partition plate;
the auxiliary tower is characterized in that an auxiliary tower air inlet is formed in the side wall of the bottom end of the auxiliary tower; an auxiliary tower air outlet is formed in the side wall of the top end of the auxiliary tower; the bottom of the auxiliary tower is provided with an auxiliary tower drain port; the auxiliary tower gas inlet is communicated with the main tower gas outlet through a gas connecting pipe;
the tower type separation assembly is arranged at the bottom end inside the auxiliary tower and is positioned above the air inlet of the auxiliary tower; the tower separation assembly comprises: the supporting device comprises a circular baffle, an annular baffle and a supporting rod; the auxiliary tower comprises a plurality of circular baffles, a plurality of supporting rods and a plurality of annular baffles, wherein the circular baffles and the plurality of annular baffles are arranged at intervals from bottom to top;
and the sintering filter assembly is fixed at the top end inside the auxiliary tower and is positioned below the air outlet of the auxiliary tower.
The beneficial effects of adopting the above technical scheme are that, the utility model discloses well steam gets into from the main tower air inlet, enters into the bottom of main tower along spiral separator, rises to the top of main tower along the center tube again, discharges from the main tower gas outlet, and spiral separator can drive steam rotatory decline in the main tower inside, makes the big liquid drop that has great inertial centrifugal force throw to main tower lateral wall and steam separation, and the liquid drop that separates descends along main tower lateral wall, discharges from the main tower drain trap; steam entering the auxiliary tower rises upwards in a curve shape from the outer side of the circular baffle and the middle of the annular baffle in sequence, water drops can be accumulated on the circular baffle, secondary steam-water separation is carried out on the steam, the steam obtained by separation is further filtered through moisture and impurities in the steam by the sintering and filtering assembly, and then the steam with the dryness and cleanliness meeting the requirements is obtained.
Preferably, the bottom end of the inside of the main tower and the bottom end of the inside of the auxiliary tower are both provided with a water tray, the edge of the water tray is provided with an inclined plate, and the inclined plate inclines towards the lower part of the outer side of the water tray. The water tray can be used for blocking steam, the steam can conveniently enter the central pipe, and the inclined plate is arranged to conveniently drop water on the top of the water tray along the inclined plate.
Preferably, a rectifying assembly is fixed inside the auxiliary tower and is arranged at the top of the tower type separation assembly; the rectifying assembly comprises a plurality of honeycomb core structural members which are arranged in a staggered and overlapped mode. A plurality of honeycomb core structures are arranged in a stacked and staggered mode, steam penetrates through the honeycomb core structures from bottom to top in sequence, the cross sections of the steam auxiliary towers are uniformly distributed, the pressure of the steam, caused by non-uniformity, on the silk screen can be reduced, and the service life of the silk screen can be effectively prolonged.
Preferably, a wire mesh is fixed inside the auxiliary tower and is disposed between the rectifying assembly and the sintered filtering assembly. The silk screen can intercept small molecule water and further separate steam.
Preferably, the auxiliary tower is divided into an upper part and a lower part at a position intermediate the mesh and the sintered filter assembly, and the upper part and the lower part are fixedly connected by a flange. The auxiliary tower is divided into two parts, so that the silk screen and the sintering filter component can be conveniently detached and replaced.
Preferably, the main tower air inlet and the main tower air outlet are symmetrically arranged along the central axis of the main tower; the main tower air inlet, the main tower air outlet and the auxiliary tower air outlet are located on the same horizontal plane, and the main tower air outlet connector and the auxiliary tower air outlet connector extend 15mm towards the inside of the main tower and the inside of the auxiliary tower. The interfaces of the air outlet of the main tower and the air outlet of the auxiliary tower extend into the main tower and the auxiliary tower, so that water drops on the inner wall of the main tower or the auxiliary tower can be prevented from entering the pipelines of the air outlet of the main tower and the air outlet of the auxiliary tower.
Preferably, the inclination angle of the spiral plate of the spiral separating piece is 30-40 degrees.
Preferably, the partition plate forms an included angle of 45 degrees with the horizontal plane.
Preferably, the distance between the central tube and the top of the main tower is larger than or equal to the size of the outer diameter of the central tube; the distance between the central pipe and the bottom of the main tower is more than or equal to 2 times of the external diameter of the central pipe.
Can know via foretell technical scheme, compare with prior art, the utility model discloses a provide an industrial steam quality hoisting device, its beneficial effect is:
(1) in the utility model, the secondary separation can be carried out on the steam through the spiral separation component and the tower type separation component, and a large amount of moisture in the steam can be separated;
(2) the steam after secondary separation enters the wire mesh, so that micromolecule water in the steam can be intercepted, and the steam can be removed from moisture and impurities in the steam after entering the sintering filtering component, so that the dryness and cleanliness of the steam are higher.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings required to be used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to the provided drawings without creative efforts.
Fig. 1 is a schematic structural diagram of the device provided by the present invention;
fig. 2 is a flow path diagram of steam inside the main tower provided by the present invention;
fig. 3 is a schematic structural diagram of a tower separation assembly provided by the present invention;
fig. 4 is a top view of a tower separation assembly provided by the present invention;
fig. 5 is a top view of a rectification assembly provided by the present invention;
fig. 6 is a front view of the rectifying assembly provided by the present invention.
Wherein, in the figure,
1-a main column;
11-main column inlet; 12-main column outlet; 13-main column drain;
2-a spiral separation module;
21-a helical separator; 22-a central tube; 23-a separator;
3-an auxiliary tower;
31-auxiliary column inlet; 32-auxiliary column outlet; 33-auxiliary column drain; 34-auxiliary column upper part; 35-the lower part of the auxiliary column;
4-gas connection pipe;
5-a tower separation assembly;
51-circular baffles; 52-an annular baffle; 53-support bars;
6-sintering the filter assembly;
7-a water tray;
71-an inclined plate;
8-a rectifying component;
81-honeycomb core structure;
9-silk screen.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative efforts all belong to the protection scope of the present invention.
The embodiment of the utility model discloses industry steam quality hoisting device, include:
the tower comprises a main tower 1, wherein a main tower air inlet 11 and a main tower air outlet 12 are respectively arranged on two sides of the top end of the main tower 1; the bottom of the main tower 1 is provided with a main tower drain opening 13;
the spiral separation component 2, the spiral separation component 2 is arranged inside the main tower 1; the spiral separation module 2 includes: a spiral separator 21, a center tube 22, and a partition 23; the spiral separating piece 21 is spirally wound outside the central tube 22, and a gap is reserved between the spiral separating piece 21 and the inner wall of the main tower 1; the center tube 22 is hollow and has openings at both ends; the partition plate 23 is arranged at the top of the main tower 1 and is fixedly connected with the interior of the main tower 1; the clapboard 23 is inclined, the main tower air inlet 11 is arranged below the clapboard 23, and the main tower air outlet 12 is arranged at the top of the clapboard 23; the top of the central tube 22 passes through the partition plate 23, is arranged on the top of the partition plate 23, and is fixedly connected with the partition plate 23;
an auxiliary tower air inlet 31 is arranged on the side wall of the bottom end of the auxiliary tower 3; an auxiliary tower air outlet 32 is arranged on the side wall of the top end of the auxiliary tower 3; the bottom of the auxiliary tower 3 is provided with an auxiliary tower drain port 33; the auxiliary tower gas inlet 31 is communicated with the main tower gas outlet 12 through a gas connecting pipe 4;
the tower type separation assembly 5 is arranged at the bottom end inside the auxiliary tower 3, and is positioned above the air inlet 31 of the auxiliary tower; the tower separation assembly 5 comprises: a circular baffle 51, an annular baffle 52 and a support rod 53; the circular baffles 51 and the annular baffles 52 are provided with a plurality of circular baffles 51 and a plurality of annular baffles 52 which are arranged from bottom to top at intervals, the annular baffles 52 are fixedly connected with the inner wall of the auxiliary tower 3, the support rods 53 are provided with a plurality of circular baffles and are uniformly distributed along the circumferential direction of the circular baffles 51, and the support rods 53 penetrate through the circular baffles 51 and the annular baffles 52 and are fixedly connected with the circular baffles 51 and the annular baffles 52;
and the sintered filter assembly 6 is fixed at the top end inside the auxiliary tower 3, and the sintered filter assembly 6 is positioned below the air outlet 32 of the auxiliary tower. The spiral separation component 2, the tower separation component 5 and the sintering and filtering component 6 are combined to realize the improvement of the steam quality, so that the dryness and cleanliness of the steam can reach the use standard. The circular baffle 51 and the annular baffle 52 are respectively one layer, the tower type separating piece 5 has at least 4 layers, and the thickness of each of the annular baffle 52 and the circular baffle 51 is 6 mm.
In order to further optimize the technical scheme, the bottom end inside the main tower 1 and the bottom end inside the auxiliary tower 3 are both provided with a water tray 7, the edge of the water tray 7 is provided with an inclined plate 71, and the inclined plate 71 inclines downwards outside the water tray 7. The water tray 7 is arranged to prevent steam from entering the main tower outlet 12 and the auxiliary tower outlet 32.
In order to further optimize the technical scheme, a rectifying assembly 8 is fixed inside the auxiliary tower 3, and the rectifying assembly 8 is arranged at the top of the tower type separation assembly 5; the fairing assembly 8 includes a plurality of honeycomb core structures 81, and the plurality of honeycomb core structures 81 are stacked in a staggered manner. The honeycomb core structure 81 is a plate-like structure having honeycomb holes on the surface, and a plurality of plate-like structures are stacked together. The honeycomb core structure 81 is made of 304 stainless steel, the height of a single plate-shaped structure is 30mm, the aperture of honeycomb holes is selected according to steam flow, the honeycomb holes are stacked in a multi-layer mode, and the total height is larger than the diameter of the auxiliary tower 3.
In order to further optimize the above technical solution, a wire mesh 9 is fixed inside the auxiliary tower 3, and the wire mesh 9 is disposed between the rectifying assembly 8 and the sintered filtering assembly 6. The sintering filter component 6 is a circular filter plate, is welded with the auxiliary tower 3, has the density of 0.5 micron, is made of 316L material, has the thickness selected according to the steam flow and the pressure, ensures that the steam pressure difference does not exceed 0.05Mpa, and has the specifications of 4 microns, 5 microns, 6 microns, 8 microns and 10 microns.
In order to further optimize the above technical solution, the auxiliary tower 3 is divided into an auxiliary tower upper part 34 and an auxiliary tower lower part 35 at the middle position between the wire mesh 9 and the sintered filter assembly 6, and the auxiliary tower upper part 34 and the auxiliary tower lower part 35 are fixedly connected by a flange.
In order to further optimize the technical scheme, the main tower air inlet 11 and the main tower air outlet 12 are symmetrically arranged along the central axis of the main tower 1; the main tower air inlet 11, the main tower air outlet 12 and the auxiliary tower air outlet 32 are positioned on the same horizontal plane, and the interface of the main tower air outlet 12 and the interface of the auxiliary tower air outlet 32 both extend 15mm to the inside of the main tower 1 and the auxiliary tower 3. The diameter of the central tube 22 is the same as the diameter at the main column inlet 11; the main tower air inlet 11, the main tower air outlet 12 and the auxiliary tower air outlet 32 are located on the same horizontal plane, so that the main tower 1 and the auxiliary tower 3 can be conveniently installed under the condition that the original pipeline trend is not changed.
In order to further optimize the above solution, the angle of inclination of the spiral plate of the spiral separating element 21 is 30-40 °. The thickness of the spiral plate is 6mm, a steel plate is selected, and the distance between the spiral separating piece 21 and the inner wall of the main tower 1 is 1-2 mm.
In order to further optimize the above technical solution, the partition 23 forms an angle of 45 ° with the horizontal.
In order to further optimize the technical scheme, the distance between the central pipe 22 and the top of the main tower 1 is larger than or equal to the size of the outer diameter of the central pipe 22; the distance between the central tube 22 and the bottom of the main tower 1 is more than or equal to 2 times of the external diameter of the central tube 22.
The working principle is as follows:
the steam enters the inside of the main tower 1 from the main tower gas inlet 11, moves downwards along the spiral separating piece 21 until moving to the bottom of the main tower 1, enters the central pipe from the bottom of the central pipe 22 under the blockage of the water tray 7, is discharged from the top of the central pipe 22, is discharged from the main tower gas outlet 12 under the action of the partition plate 23, enters the auxiliary tower gas inlet 31 through the gas connecting pipe 4, then enters the inside of the auxiliary tower 3, then encounters the blockage of the circular baffle 51, moves upwards from the outer side of the circular baffle 51, encounters the annular baffle 52, continues to move upwards from the center of the annular baffle 52, then encounters the circular baffle 51, encounters the circular baffle 51 and the annular baffle 52 for multiple times, the steam bends upwards, and water drops are accumulated on the surfaces of the circular baffle 51 and the annular baffle 52, so that the separation of the steam is realized; the steam passing through the tower type separation assembly 5 passes through the rectifying assembly 8, the wire mesh 9 and the sintering filter assembly 6 in sequence and is finally discharged from the auxiliary tower air outlet.
The embodiments in the present description are described in a progressive manner, each embodiment focuses on differences from other embodiments, and the same and similar parts among the embodiments are referred to each other. The device disclosed by the embodiment corresponds to the method disclosed by the embodiment, so that the description is simple, and the relevant points can be referred to the method part for description.
The previous description of the disclosed embodiments is provided to enable any person skilled in the art to make or use the present invention. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the generic principles defined herein may be applied to other embodiments without departing from the spirit or scope of the invention. Thus, the present invention is not intended to be limited to the embodiments shown herein but is to be accorded the widest scope consistent with the principles and novel features disclosed herein.
Claims (9)
1. An industrial steam quality improving device, comprising:
the device comprises a main tower (1), wherein a main tower air inlet (11) and a main tower air outlet (12) are respectively arranged on two sides of the top end of the main tower (1); a main tower drain opening (13) is formed in the bottom of the main tower (1);
a spiral separation assembly (2), the spiral separation assembly (2) being disposed inside the main column (1); the spiral separation module (2) comprises: a spiral separator (21), a central tube (22) and a partition (23); the spiral separating piece (21) is spirally wound outside the central pipe (22), and a gap is reserved between the spiral separating piece (21) and the inner wall of the main tower (1); the interior of the central tube (22) is hollow, and two ends of the central tube are open; the clapboard (23) is arranged at the top of the main tower (1) and is fixedly connected with the inside of the main tower (1); the partition plate (23) is inclined, the main tower air inlet (11) is arranged below the partition plate (23), and the main tower air outlet (12) is arranged at the top of the partition plate (23); the top of the central pipe (22) penetrates through the partition plate (23), is arranged on the top of the partition plate (23), and is fixedly connected with the partition plate (23);
the auxiliary tower (3), the side wall of the bottom end of the auxiliary tower (3) is provided with an auxiliary tower air inlet (31); an auxiliary tower air outlet (32) is formed in the side wall of the top end of the auxiliary tower (3); an auxiliary tower drain opening (33) is formed in the bottom of the auxiliary tower (3); the auxiliary tower gas inlet (31) is communicated with the main tower gas outlet (12) through a gas connecting pipe (4);
the tower type separation assembly (5) is arranged at the bottom end inside the auxiliary tower (3), and is positioned above the air inlet (31) of the auxiliary tower; the tower separation assembly (5) comprises: a circular baffle plate (51), an annular baffle plate (52) and a support rod (53); the circular baffle plates (51) and the annular baffle plates (52) are arranged in a plurality, the circular baffle plates (51) and the annular baffle plates (52) are arranged from bottom to top at intervals, the annular baffle plates (52) are fixedly connected with the inner wall of the auxiliary tower (3), a plurality of support rods (53) are arranged and uniformly distributed along the circumferential direction of the circular baffle plates (51), and the support rods (53) penetrate through the circular baffle plates (51) and the annular baffle plates (52) and are fixedly connected with the circular baffle plates (51) and the annular baffle plates (52);
and the sintered filter component (6) is fixed at the top end inside the auxiliary tower (3), and is positioned below the air outlet (32) of the auxiliary tower (6).
2. An industrial steam quality improving device according to claim 1, characterized in that the bottom end inside the main tower (1) and the bottom end inside the auxiliary tower (3) are provided with water trays (7), the edge of the water tray (7) is provided with an inclined plate (71), and the inclined plate (71) inclines downwards outside the water tray (7).
3. The industrial steam quality improving device according to claim 1, characterized in that a rectifying component (8) is fixed inside the auxiliary tower (3), and the rectifying component (8) is arranged at the top of the tower-type separation component (5); the rectifying assembly (8) comprises a plurality of honeycomb core structural members (81), and the honeycomb core structural members (81) are arranged in a staggered and overlapped mode.
4. An industrial steam quality improving device according to claim 3, characterized in that a wire mesh (9) is fixed inside the auxiliary tower (3), and the wire mesh (9) is arranged between the rectifying assembly (8) and the sintering filter assembly (6).
5. An industrial steam quality improving device according to claim 4, characterized in that the auxiliary tower (3) is divided into an upper auxiliary tower part (34) and a lower auxiliary tower part (35) at the middle position of the wire mesh (9) and the sintered filter assembly (6), and the upper auxiliary tower part (34) and the lower auxiliary tower part (35) are fixedly connected through a flange.
6. An industrial steam quality upgrading device according to claim 1, characterized in that the main tower air inlet (11) and main tower air outlet (12) are arranged symmetrically along the central axis of the main tower (1); the main tower air inlet (11), the main tower air outlet (12) and the auxiliary tower air outlet (32) are located on the same horizontal plane, and the interface of the main tower air outlet (12) and the interface of the auxiliary tower air outlet (32) extend 15mm to the inside of the main tower (1) and the inside of the auxiliary tower (3).
7. An industrial steam upgrading device according to claim 1, wherein the angle of inclination of the spiral plates of the spiral separating member (21) is 30 ° -40 °.
8. An industrial steam quality enhancement device according to claim 1 or 7, wherein the partition (23) is angled at 45 ° to the horizontal.
9. An industrial steam upgrading device according to claim 1, characterized in that the distance of the central pipe (22) from the top of the main column (1) is greater than or equal to the outer diameter of the central pipe (22); the distance between the central pipe (22) and the bottom of the main tower (1) is more than or equal to 2 times of the outer diameter of the central pipe (22).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202221414901.1U CN217511485U (en) | 2022-06-07 | 2022-06-07 | Industrial steam quality improving device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202221414901.1U CN217511485U (en) | 2022-06-07 | 2022-06-07 | Industrial steam quality improving device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN217511485U true CN217511485U (en) | 2022-09-30 |
Family
ID=83391127
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202221414901.1U Active CN217511485U (en) | 2022-06-07 | 2022-06-07 | Industrial steam quality improving device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN217511485U (en) |
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2022
- 2022-06-07 CN CN202221414901.1U patent/CN217511485U/en active Active
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