CN115301431A - High-viscosity slurry atomizing nozzle for inner wall of boiler pipe of thermal power generating unit - Google Patents
High-viscosity slurry atomizing nozzle for inner wall of boiler pipe of thermal power generating unit Download PDFInfo
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- CN115301431A CN115301431A CN202211118734.0A CN202211118734A CN115301431A CN 115301431 A CN115301431 A CN 115301431A CN 202211118734 A CN202211118734 A CN 202211118734A CN 115301431 A CN115301431 A CN 115301431A
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- slurry
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- thermal power
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- generating unit
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B7/00—Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas
- B05B7/02—Spray pistols; Apparatus for discharge
- B05B7/06—Spray pistols; Apparatus for discharge with at least one outlet orifice surrounding another approximately in the same plane
- B05B7/062—Spray pistols; Apparatus for discharge with at least one outlet orifice surrounding another approximately in the same plane with only one liquid outlet and at least one gas outlet
- B05B7/066—Spray pistols; Apparatus for discharge with at least one outlet orifice surrounding another approximately in the same plane with only one liquid outlet and at least one gas outlet with an inner liquid outlet surrounded by at least one annular gas outlet
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B12/00—Arrangements for controlling delivery; Arrangements for controlling the spray area
- B05B12/16—Arrangements for controlling delivery; Arrangements for controlling the spray area for controlling the spray area
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B13/00—Machines or plants for applying liquids or other fluent materials to surfaces of objects or other work by spraying, not covered by groups B05B1/00 - B05B11/00
- B05B13/06—Machines or plants for applying liquids or other fluent materials to surfaces of objects or other work by spraying, not covered by groups B05B1/00 - B05B11/00 specially designed for treating the inside of hollow bodies
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B7/00—Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas
- B05B7/02—Spray pistols; Apparatus for discharge
- B05B7/08—Spray pistols; Apparatus for discharge with separate outlet orifices, e.g. to form parallel jets, i.e. the axis of the jets being parallel, to form intersecting jets, i.e. the axis of the jets converging but not necessarily intersecting at a point
- B05B7/0807—Spray pistols; Apparatus for discharge with separate outlet orifices, e.g. to form parallel jets, i.e. the axis of the jets being parallel, to form intersecting jets, i.e. the axis of the jets converging but not necessarily intersecting at a point to form intersecting jets
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Abstract
The application discloses thermal power unit boiler pipe is high viscosity thick liquids atomizer for inner wall, and thermal power unit boiler pipe is high viscosity thick liquids atomizer for inner wall includes: one end of the shell base is a spraying end, and a conical cavity with the caliber gradually increasing along the spraying direction is arranged in the spraying end; a slurry outlet channel and an air outlet channel are arranged in the spraying end, a slurry outlet of the slurry outlet channel is arranged corresponding to the axis of the conical cavity, the air outlet channel is positioned at the periphery of the slurry outlet, and a plurality of air outlets of the air outlet channel are arranged on the wall of the conical cavity; the air outlet channel is spiral in the spraying end and is suitable for spraying air flow which is rotationally dispersed along the circle center outwards through the air outlet; one end of the connecting rod penetrates through the pulp outlet channel to be fixedly connected with the shell base, and the other end of the connecting rod extends outwards from the pulp outlet; and the baffle is connected to one end of the connecting rod, which extends out of the slurry outlet, and is blocked in the discharging direction of the slurry outlet so as to change the spraying direction of the slurry. Can realize better atomization effect on the high-viscosity slurry, so that the spraying is more uniform and the spraying effect is better.
Description
Technical Field
The application relates to the technical field of spray heads, in particular to a high-viscosity slurry atomizing spray head for the inner wall of a boiler tube of a thermal power generating unit.
Background
With the continuous development of industrial science and technology, a spraying technology is used in many technical fields, for example, the appearance of a metal part is treated by the spraying technology to make the metal part more beautiful, or an antioxidation layer is sprayed on the surface of the metal part to improve the antioxidation performance of the surface of the metal part.
The spraying of the anti-oxidation layer of the metal piece in the normal-temperature use environment is easy to realize, and the requirement on anti-oxidation coating is not high. However, for metal parts in high temperature environments, where the requirements for slurries are relatively high, slurries containing metal powders are often selected for spray application to form an oxidation resistant layer on the interior and/or exterior surfaces of the metal part. In order to obtain a good mixing effect of the metal powder-containing slurry, it is necessary to use a high viscosity solvent. The need to select a high viscosity solvent is due to the tendency of the metal powder to precipitate in a low viscosity solvent, which can result in non-uniform mixing of the slurry and ultimately affect the quality of the sprayed anti-oxidation layer.
The existing spraying device comprises a slurry inlet pipeline and a gas inlet pipeline which are coaxially arranged, wherein the slurry inlet pipeline is positioned on the inner side of the gas inlet pipeline, the tail end of the slurry inlet pipeline is communicated with a slurry outlet, the slurry outlet is in a contracted shape, the tail end of the gas outlet pipeline is communicated with a gas outlet, and the tail end of the gas outlet is also in a contracted shape. The high-pressure gas sprayed out of the gas outlet rushes to the slurry flowing out of the slurry outlet, so that the slurry is sprayed out.
However, the spraying device is limited to spraying of a certain slurry with relatively stable property and relatively low viscosity, and has the problems of poor atomization effect and uneven spraying effect when the slurry is sprayed aiming at the spraying of the high-viscosity slurry.
Content of application
Therefore, the technical problem that this application will be solved lies in overcoming the spraying device among the prior art when the spraying high viscosity thick liquids, and atomization effect is poor, the inhomogeneous defect of spraying effect when thick liquids blowout to a high viscosity thick liquids atomizer is used to thermal power unit boiler pipe inner wall is provided.
In order to solve the technical problem, the technical scheme of the application is as follows:
a high-viscosity slurry atomizing nozzle for the inner wall of a boiler tube of a thermal power generating unit comprises
One end of the shell base is a spraying end, and a conical cavity with the caliber gradually increasing along the spraying direction is arranged in the spraying end; a slurry outlet channel and an air outlet channel are arranged in the spraying end, a slurry outlet of the slurry outlet channel is arranged corresponding to the axis of the conical cavity, the air outlet channel is positioned on the periphery of the slurry outlet, and a plurality of air outlets of the air outlet channel are formed in the wall of the conical cavity; the air outlet channel is spiral in the spraying end and is suitable for spraying air flow which is rotationally dispersed along the circle center outwards through the air outlet;
one end of the connecting rod penetrates through the pulp outlet channel to be fixedly connected with the shell base, and the other end of the connecting rod extends outwards from the pulp outlet;
and the baffle is connected to one end of the connecting rod, which extends out of the slurry outlet, and is blocked in the discharging direction of the slurry outlet so as to change the spraying direction of the slurry.
Furthermore, the calibers of the plurality of air outlets are the same.
Furthermore, the connecting rod is a telescopic rod which can be extended and retracted along the injection direction, and the baffle is connected to the extension and retraction part of the connecting rod.
Further, a plurality of the air outlets are evenly arranged at intervals along the circumferential direction of the injection end.
Furthermore, a plurality of the air outlets are uniformly and sequentially arranged along the circumferential direction of the injection end.
Furthermore, a gas chamber and a slurry making chamber are also arranged in the shell base, and a slurry inlet and a gas inlet are formed in the tail end of the shell base, which is back to the spraying end; the slurry inlet is communicated with the slurry outlet channel through the slurry making chamber, and the gas inlet is communicated with the gas outlet channels through the gas chamber.
Further, the size of the caliber of the pulp inlet is the same as that of the pulp making chamber.
Further, one surface of the baffle, facing the slurry outlet, is a sputtering plane, and a gap is formed between the sputtering plane and the spraying end; the slurry sprayed out of the slurry outlet impacts the sputtering plane to be reflected and then is sprayed out of the gap.
This application technical scheme has following advantage:
1. the application provides a thermal power generating unit boiler is high viscosity thick liquids atomizer for inside pipe wall, because the baffle is connected and is stretched out the one end of thick liquid mouth and keep off on the ejection of compact direction of thick liquid mouth at the connecting rod, from thick liquid mouth spun thick liquids by the rotatory air current impact from gas outlet spun, the rotary-cut, thick liquids are evenly stirred fast and are scattered, play the effect of horizontal rotary-cut thick liquids, then, the thick liquids after stirring and scattering strike the baffle again on, make thick liquids obtain further atomizing, so, just can realize better atomization effect to high viscosity thick liquids, make the spraying more even, the spraying effect is better.
2. The application provides a thermal power unit boiler is high viscosity thick liquids atomizer for inside pipe wall, connecting rod are along the telescopic link of injection direction telescopic, on the pars contractilis of connecting rod was connected to the baffle, the flexible adjustable fender of accessible connecting rod and the interval between the grout outlet, and then the area of the ring of adjustment spraying.
3. The application provides a high viscosity thick liquids atomizer for boiler tube inner wall of thermal power unit, baffle can dismantle to be connected on the connecting rod, when needs spraying conical surface, take off the baffle can, and then improved the adaptability of the spraying shape of high viscosity thick liquids atomizer for boiler tube inner wall of thermal power unit.
4. The application provides a high viscosity thick liquids atomizer for thermal power unit boiler pipe inner wall, simple structure, processing is convenient, and it is convenient to wash, difficult jam, low in manufacturing cost.
Drawings
In order to more clearly illustrate the detailed description of the present application or the technical solutions in the prior art, the drawings used in the detailed description or the prior art description will be briefly described below, and it is obvious that the drawings in the following description are some embodiments of the present application, and other drawings can be obtained by those skilled in the art without creative efforts.
Fig. 1 is a schematic view of an internal structure of a high-viscosity slurry atomizing nozzle for an inner wall of a boiler tube of a thermal power generating unit according to the present application;
FIG. 2 is a left side view of the housing base of the present application;
FIG. 3 is a schematic illustration of the action of gas flow on the slurry in the present application.
Description of the reference numerals:
1. a housing base; 2. a spray end; 21. a tapered cavity; 22. a slurry outlet channel; 221. a pulp outlet; 23. an air outlet channel; 231. an air outlet; 3. a gas chamber; 4. a tail end; 5. a connecting rod; 6. a baffle plate; 7. an air inlet; 8. a pulp inlet; 9. a pulp making chamber.
Detailed Description
The technical solutions of the present application will be described clearly and completely with reference to the accompanying drawings, and it is to be understood that the described embodiments are only a part of the embodiments of the present application, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present application.
In the description of the present application, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of description and simplicity of description, and do not indicate or imply that the device or element being referred to must have a particular orientation, be constructed and operated in a particular orientation, and thus, should not be construed as limiting the present application. Furthermore, the terms "first," "second," and "third" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
In the description of the present application, it should be noted that, unless otherwise explicitly stated or limited, the terms "mounted," "connected," and "connected" are to be construed broadly, and may be, for example, a fixed connection, a detachable connection, or an integral connection; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present application can be understood in a specific case by those of ordinary skill in the art.
In addition, the technical features mentioned in the different embodiments of the present application described below may be combined with each other as long as they do not conflict with each other.
Examples
As shown in fig. 1 to 3, the present embodiment provides a high viscosity slurry atomizer for an inner wall of a boiler tube of a thermal power generating unit, which includes a housing base 1, a connecting rod 5 and a baffle 6.
One end of the shell base 1 is a spraying end 2, and a conical cavity 21 with the caliber gradually increased along the spraying direction is arranged in the spraying end 2; a slurry outlet channel 22 and an air outlet channel 23 are arranged in the spraying end 2, a slurry outlet 221 of the slurry outlet channel 22 is arranged corresponding to the axis of the conical cavity 21, the air outlet channel 23 is positioned at the periphery of the slurry outlet 221, and a plurality of air outlets 231 of the air outlet channel 23 are arranged on the cavity wall of the conical cavity 21; the air outlet channel 23 is spiral in the spraying end 2, and is adapted to spray air flow which is rotationally dispersed along the circle center outwards through the air outlet 231, and the air outlet 231 deflects towards the axial direction of the slurry outlet 221, so that the high-pressure air flow can be sprayed towards the slurry sprayed from the slurry outlet 221 to perform rotary cutting on the slurry. Fig. 3 is a schematic diagram of the effect of the gas flow on the slurry.
One end of the connecting rod 5 passes through the slurry outlet channel 22 and is fixedly connected with the casing base 1, and the other end of the connecting rod extends outwards from the slurry outlet 221. The baffle 6 is connected to one end of the connecting rod 5 extending out of the slurry outlet 221 and is blocked in the discharging direction of the slurry outlet 221 so as to change the spraying direction of the slurry.
Because baffle 6 is connected in the one end that connecting rod 5 stretches out grout outlet 221 and is kept off in the play thick liquid direction of grout outlet 221, from grout outlet 221 spun thick liquids by the rotatory air current impact of spout 231 from gas outlet, the rotary-cut, thick liquids are evenly stirred fast and are dispersed, then, thick liquids after stirring disperse again bump on baffle 6, make thick liquids obtain further atomizing, so, just so, can realize better atomization effect to high viscosity thick liquids, make the spraying more even, the spraying effect is better.
In addition, the high-viscosity slurry atomizing nozzle for the inner wall of the boiler tube of the thermal power generating unit provided by the embodiment is convenient for spraying high-viscosity slurry, is also suitable for spraying low-viscosity slurry, can be used for spraying pipelines, can be widely applied to similar related aspects needing spraying or pneumatic stirring in the food processing industry or other industrial fields, and has a wide application range.
For the shell base 1, the shell base 1 is also internally provided with a gas chamber 3 and a slurry making chamber 9, and the tail end 4 of the shell base 1, which is back to the spraying end 2, is provided with a slurry inlet 8 and an air inlet 7; the slurry inlet 8 is communicated with a slurry pipeline (not shown), and the gas inlet 7 is communicated with a high-pressure gas pipeline (not shown); the slurry inlet 8 is communicated with the slurry outlet channel 22 through the slurry making chamber 9, and the diameters of the slurry inlet 8 and the slurry making chamber 9 are the same, so that slurry blockage caused by diameter change is avoided; the gas inlet 7 communicates with several gas outlet channels 23 via the gas chamber 3. As shown in fig. 1, in the present embodiment, the injection end 2 is formed separately and assembled on the housing base 1, and is a part of the housing base 1, and the injection end 2 is formed separately for easy processing.
As for the air outlets 231, specifically, the apertures of the air outlets 231 are the same, so that the impact and rotary cutting force of the high-pressure air flow ejected from each air outlet 231 on the slurry are the same, which is beneficial to the uniformity of slurry mixing. Furthermore, the plurality of air outlets 231 are uniformly spaced along the circumferential direction of the spraying end 2, so that the slurry sprayed from the slurry outlet 221 is uniformly and rotationally cut in all directions, and is uniformly dispersed, and of course, the slurry can be non-uniformly arranged, and only the effect is not uniformly arranged.
As for the connecting rod 5 and the baffle 6, specifically, the connecting rod 5 is connected into the casing base 1 through the slurry outlet 221, and the connecting rod 5 is a telescopic rod which is coaxially arranged with the slurry outlet 221 and is telescopic along the injection direction. The baffle 6 is connected with the telescopic part of the connecting rod 5, so that the size of a gap between the baffle 6 and the shell base 1 can be adjusted by means of the scalability of the connecting rod 5, and the size of the area of the spraying circular ring can be adjusted. When the connecting rod 5 is long, the gap between the baffle 6 and the slurry outlet 221 is large, the area of the circular ring which can be sprayed is large, and when the connecting rod 5 is short, the gap between the baffle 6 and the slurry outlet 221 is small, and the area of the circular ring which can be sprayed is small. Moreover, the baffle 6 is detachably fixed on the connecting rod 5, and when the conical surface needs to be sprayed, the baffle 6 is only required to be taken down, so that the slurry rotationally cut by the high-pressure airflow sprayed out from the air outlet 231 is directly sprayed on the conical surface. In addition, the baffle 6 and the slurry outlet 221 are coaxially arranged, and one surface facing the slurry outlet 221 is a circular sputtering plane, but of course, the baffle can also be in other shapes such as a triangle, a square and the like, and the baffle can be specifically arranged according to actual needs; a gap is arranged between the sputtering plane of the baffle 6 and the spraying end 2; the slurry sprayed from the slurry outlet 221 hits the sputtering plane, then is reflected and sprayed out from the gap to the pipe wall to be sprayed. Of course, the shape of the baffle 6 is not limited to a flat plate shape, and may also be a horn shape, and is specifically provided according to actual needs, and is not specifically limited herein.
The working process of spraying the inner wall of the pipeline by using the high-viscosity slurry atomizing nozzle for the inner wall of the boiler pipe of the thermal power generating unit is as follows:
integrally extending the inner wall of a boiler tube of a thermal power generating unit into a pipeline by using a high-viscosity slurry atomizing nozzle, and adjusting the telescopic length of a connecting rod 5 according to the area of a required spraying ring;
the slurry is sent into the slurry making chamber 9 from the slurry inlet 8 by high pressure and reaches the slurry outlet 221 along the slurry outlet channel 22 communicated with the slurry making chamber 9;
high-pressure gas is introduced into the gas chamber 3 from the gas inlet 7 and is finally sprayed out from the gas outlets 231, the gas outlets 231 are arranged in a deflected mode towards the axis of the slurry outlet 221, the gas sprayed out from the gas outlets 231 are matched together to form spiral gas flow, slurry sprayed out from the slurry outlet 221 is rotationally cut, and the slurry is rotationally cut;
the rotary-cut slurry is collided to the baffle 6 which is at a certain distance from the front end of the slurry outlet 221, and then is sprayed and atomized again;
the sprayed and atomized slurry is sprayed to the inner wall of the pipeline through a gap between the baffle 6 and the spraying end 2;
uniformly moving the high-viscosity slurry atomizing nozzle for the inner wall of the boiler pipe of the thermal power generating unit in the pipeline, so that the high-viscosity slurry atomizing nozzle for the inner wall of the boiler pipe of the thermal power generating unit can uniformly spray all positions on the inner wall of the pipeline;
in addition, supplementary explanation follows the beneficial effect of the high viscosity thick liquids atomizer for the inner wall of the boiler tube of the thermoelectric generator group in this embodiment:
in the prior art, in order to achieve better atomization of the slurry, the slurry outlet 221 needs to be made in a contracted shape to control the amount of the slurry to be sprayed, because if the amount of the slurry to be sprayed is relatively large, all the slurry may not be well atomized. However, in the high-viscosity slurry atomizing nozzle for the inner wall of the boiler tube of the thermal power generating unit in this embodiment, due to the design of the baffle 6, the high-viscosity slurry can be well atomized outside the slurry outlet 221, so that the slurry outlet 221 can be made into a straight tubular shape, and compared with the contracted slurry outlet 221, the straight tubular slurry outlet 221 is not easily blocked, and thus, the size of the high-viscosity slurry atomizing nozzle for the inner wall of the boiler tube of the thermal power generating unit can be made smaller to adapt to spraying of the inner wall of a small-sized pipeline.
Moreover, because air inlet 7 is connected with the high-pressure air inlet pipeline, advances thick liquid pipeline is connected to thick liquid mouth 8, in this way, just can adjust the high-pressure air inlet pipeline as required and advance the length of thick liquid pipeline, increases the propulsive degree of depth of high viscosity thick liquids atomizer for thermal power unit boiler pipe inner wall to the spraying of adaptation longer pipeline inner wall.
It should be understood that the above examples are only for clarity of illustration and are not intended to limit the embodiments. Other variations and modifications will be apparent to persons skilled in the art in light of the above description. And are neither required nor exhaustive of all embodiments. And obvious variations or modifications of this invention are intended to be covered by the scope of the invention as expressed herein.
Claims (8)
1. The utility model provides a thermal power generating unit boiler pipe inner wall is with high viscosity thick liquids atomizer which characterized in that includes:
the device comprises a shell base (1), wherein one end of the shell base is a spraying end (2), and a conical cavity (21) with the caliber gradually increased along the spraying direction is arranged in the spraying end (2); a slurry outlet channel (22) and an air outlet channel (23) are arranged in the spraying end (2), a slurry outlet (221) of the slurry outlet channel (22) is arranged corresponding to the axis of the conical cavity (21), the air outlet channel (23) is positioned on the periphery of the slurry outlet (221), and a plurality of air outlets (231) of the air outlet channel (23) are formed in the cavity wall of the conical cavity (21); the air outlet channel (23) is spiral in the spraying end (2) and is suitable for spraying air flow which is rotationally dispersed along the circle center outwards through the air outlet (231);
one end of the connecting rod (5) penetrates through the pulp outlet channel (22) to be fixedly connected with the shell base (1), and the other end of the connecting rod extends outwards from the pulp outlet (221);
and the baffle (6) is connected to one end, extending out of the slurry outlet (221), of the connecting rod (5) and is blocked in the discharging direction of the slurry outlet (221) so as to change the spraying direction of the slurry.
2. The thermal power generating unit boiler tube inner wall atomizing nozzle according to claim 1, wherein the plurality of air outlets (231) have the same aperture size.
3. The thermal power generating unit boiler tube inner wall atomizing nozzle according to claim 1, characterized in that a plurality of the gas outlets (231) are evenly spaced along a circumferential direction of the injection end (2).
4. The thermal power generating unit boiler tube inner wall atomizing nozzle according to claim 1, wherein a plurality of the gas outlets (231) are deflected in an axial direction of the slurry outlet (221).
5. The thermal power generating unit boiler tube inner wall atomizing nozzle for high viscosity slurry according to claim 1, characterized in that the connecting rod (5) is a telescopic rod which is telescopic in the spraying direction, and the baffle plate (6) is connected to the telescopic part of the connecting rod (5).
6. The thermal power generating unit boiler pipe inner wall atomizing nozzle for the high-viscosity slurry according to any one of claims 1 to 5, characterized in that a face of the baffle plate (6) facing the slurry outlet (221) is a sputtering plane, and a gap is formed between the sputtering plane and the spraying end (2); the slurry sprayed from the slurry outlet (221) impacts the sputtering plane to be reflected and then is sprayed out from the gap.
7. The thermal power generating unit boiler tube inner wall atomizing nozzle for the thermal power generating unit boiler tube as claimed in claim 6, characterized in that a gas chamber (3) and a slurry making chamber (9) are further provided in the casing base (1), and a slurry inlet (8) and a gas inlet (7) are provided at a tail end (4) of the casing base (1) facing away from the injection end (2); the pulp inlet (8) is communicated with the pulp outlet channel (22) through the pulp making chamber (9), and the gas inlet (7) is communicated with the gas outlet channels (23) through the gas chamber (3).
8. The thermal power generating unit boiler tube inner wall atomizing nozzle for the thermal power generating unit boiler tube as claimed in claim 7, wherein the size of the slurry inlet (8) and the size of the slurry making chamber (9) are the same.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202211118734.0A CN115301431B (en) | 2022-09-14 | 2022-09-14 | High-viscosity slurry atomization nozzle for inner wall of boiler tube of thermal power generating unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202211118734.0A CN115301431B (en) | 2022-09-14 | 2022-09-14 | High-viscosity slurry atomization nozzle for inner wall of boiler tube of thermal power generating unit |
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| Publication Number | Publication Date |
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| CN115301431A true CN115301431A (en) | 2022-11-08 |
| CN115301431B CN115301431B (en) | 2023-08-15 |
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| CN202211118734.0A Active CN115301431B (en) | 2022-09-14 | 2022-09-14 | High-viscosity slurry atomization nozzle for inner wall of boiler tube of thermal power generating unit |
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Citations (34)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA300636A (en) * | 1930-05-27 | A. Heath Forrest | Oil burning method and apparatus | |
| GB1365294A (en) * | 1971-10-13 | 1974-08-29 | Engineering Developments Birmi | Apparatus for effecting aerobic degradation by aeration |
| EP0028088A1 (en) * | 1979-10-25 | 1981-05-06 | Sumitomo Light Metal Industries Limited | Method, apparatus and spray nozzle for coating the inner surface of long tubes of small diameter |
| US4335677A (en) * | 1979-10-25 | 1982-06-22 | Sumitomo Light Metal Industries, Ltd. | Coating of the inner surface of tubes |
| US4702420A (en) * | 1985-02-01 | 1987-10-27 | Ransburg-Gema Ag | Spray gun for coating material |
| EP0367985A2 (en) * | 1988-11-07 | 1990-05-16 | Nordson Corporation | Nozzle attachment for an adhesive spray gun |
| GB9026542D0 (en) * | 1990-12-06 | 1991-01-23 | Itw Ltd | An improved automatic spraygun |
| CN2369089Y (en) * | 1999-04-09 | 2000-03-15 | 岳林清 | High performance apparatus for dust collecting and desulfurizing flue gas |
| US20030168772A1 (en) * | 2002-03-05 | 2003-09-11 | Sevugan Palaniappan | Method and apparatus for coating the interior surface of a straw |
| CN1485142A (en) * | 2002-08-19 | 2004-03-31 | 伊利诺斯器械工程公司 | Spray gun with improved atomization |
| US20040227016A1 (en) * | 2001-08-28 | 2004-11-18 | Shuichi Yagi | Nozzle and method of jetting fluid into inner peripheral surface of conduct by the nozzle |
| JP2006082023A (en) * | 2004-09-16 | 2006-03-30 | Toto Ltd | Composite structure formation system and formation method |
| CN201124077Y (en) * | 2007-11-04 | 2008-10-01 | 丁有农 | Atomized spray head for wet desulfurization and dust elimination |
| US20090223054A1 (en) * | 2007-07-26 | 2009-09-10 | Nyberg Ii Charles Richard | Fuel nozzle for a gas turbine engine and method of fabricating the same |
| CN101992160A (en) * | 2009-08-27 | 2011-03-30 | 斯普瑞喷雾***(上海)有限公司 | Two-fluid nozzle device with large adjustment ratio and large adjustment ratio method thereof |
| CN103846172A (en) * | 2012-11-28 | 2014-06-11 | 山东中烟工业有限责任公司青岛卷烟厂 | External mixing type double-medium atomizing nozzle |
| CN104540597A (en) * | 2012-08-17 | 2015-04-22 | 喷雾***公司 | Full cone air-assisted spray nozzle assembly |
| CN104874515A (en) * | 2015-05-26 | 2015-09-02 | 江苏大学 | Low-frequency ultrasonic secondary atomizing spraying head controlled in electromagnetic mode |
| CN106513224A (en) * | 2016-12-28 | 2017-03-22 | 广州荣鑫容器有限公司 | Pop can inner wall spray system |
| CN107081055A (en) * | 2017-04-17 | 2017-08-22 | 山东大学 | A kind of eddy flow combined type SCR static mixers |
| CN107214007A (en) * | 2017-07-04 | 2017-09-29 | 深圳市德瑞茵精密科技有限公司 | A kind of air gun and its atomizer of sprayed with adhesive coating |
| CN207342923U (en) * | 2017-05-09 | 2018-05-11 | 湖州博川环保科技有限公司 | The core atomizer of water mist dust-removing |
| US20180133727A1 (en) * | 2015-05-22 | 2018-05-17 | Sata Gmbh & Co. Kg | Nozzle arrangement for a spray gun |
| CN108114971A (en) * | 2017-12-20 | 2018-06-05 | 郑州艾莫弗信息技术有限公司 | Xun Huan head-on collision mixed type earth prosthetic device in a kind of |
| US20180207654A1 (en) * | 2015-08-03 | 2018-07-26 | Airofog Machinery Co., Ltd. | Portable Ultrafine Nebulizer |
| US20180246233A1 (en) * | 2015-10-29 | 2018-08-30 | Framatome Gmbh | Sample container, sampling system, nuclear power plant and corresponding operating method |
| CN109876950A (en) * | 2019-04-01 | 2019-06-14 | 安徽省农业科学院土壤肥料研究所 | A kind of atomizer |
| WO2019119244A1 (en) * | 2017-12-18 | 2019-06-27 | 深圳市大疆创新科技有限公司 | Centrifugal swing disc, spraying device and unmanned aerial vehicle |
| CN212596510U (en) * | 2020-05-11 | 2021-02-26 | 江苏顺晟新材料科技有限公司 | Colored slurry atomization spraying device |
| US20210107017A1 (en) * | 2019-10-09 | 2021-04-15 | Spraying Systems Co. | Liquid slurry spraying system |
| CN113600391A (en) * | 2021-08-26 | 2021-11-05 | 华能国际电力股份有限公司 | Shot blasting-spraying device for inner wall of steel pipe |
| CN215088174U (en) * | 2021-03-31 | 2021-12-10 | 罗邦初 | Spiral air flow channel electric spray gun |
| WO2022034372A1 (en) * | 2020-08-10 | 2022-02-17 | A. Raymond Et Cie | Consumption optimized nozzle assembly |
| CN218048471U (en) * | 2022-09-14 | 2022-12-16 | 华能国际电力股份有限公司 | High-viscosity slurry atomizing nozzle for inner wall of boiler pipe of thermal power generating unit |
-
2022
- 2022-09-14 CN CN202211118734.0A patent/CN115301431B/en active Active
Patent Citations (34)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA300636A (en) * | 1930-05-27 | A. Heath Forrest | Oil burning method and apparatus | |
| GB1365294A (en) * | 1971-10-13 | 1974-08-29 | Engineering Developments Birmi | Apparatus for effecting aerobic degradation by aeration |
| EP0028088A1 (en) * | 1979-10-25 | 1981-05-06 | Sumitomo Light Metal Industries Limited | Method, apparatus and spray nozzle for coating the inner surface of long tubes of small diameter |
| US4335677A (en) * | 1979-10-25 | 1982-06-22 | Sumitomo Light Metal Industries, Ltd. | Coating of the inner surface of tubes |
| US4702420A (en) * | 1985-02-01 | 1987-10-27 | Ransburg-Gema Ag | Spray gun for coating material |
| EP0367985A2 (en) * | 1988-11-07 | 1990-05-16 | Nordson Corporation | Nozzle attachment for an adhesive spray gun |
| GB9026542D0 (en) * | 1990-12-06 | 1991-01-23 | Itw Ltd | An improved automatic spraygun |
| CN2369089Y (en) * | 1999-04-09 | 2000-03-15 | 岳林清 | High performance apparatus for dust collecting and desulfurizing flue gas |
| US20040227016A1 (en) * | 2001-08-28 | 2004-11-18 | Shuichi Yagi | Nozzle and method of jetting fluid into inner peripheral surface of conduct by the nozzle |
| US20030168772A1 (en) * | 2002-03-05 | 2003-09-11 | Sevugan Palaniappan | Method and apparatus for coating the interior surface of a straw |
| CN1485142A (en) * | 2002-08-19 | 2004-03-31 | 伊利诺斯器械工程公司 | Spray gun with improved atomization |
| JP2006082023A (en) * | 2004-09-16 | 2006-03-30 | Toto Ltd | Composite structure formation system and formation method |
| US20090223054A1 (en) * | 2007-07-26 | 2009-09-10 | Nyberg Ii Charles Richard | Fuel nozzle for a gas turbine engine and method of fabricating the same |
| CN201124077Y (en) * | 2007-11-04 | 2008-10-01 | 丁有农 | Atomized spray head for wet desulfurization and dust elimination |
| CN101992160A (en) * | 2009-08-27 | 2011-03-30 | 斯普瑞喷雾***(上海)有限公司 | Two-fluid nozzle device with large adjustment ratio and large adjustment ratio method thereof |
| CN104540597A (en) * | 2012-08-17 | 2015-04-22 | 喷雾***公司 | Full cone air-assisted spray nozzle assembly |
| CN103846172A (en) * | 2012-11-28 | 2014-06-11 | 山东中烟工业有限责任公司青岛卷烟厂 | External mixing type double-medium atomizing nozzle |
| US20180133727A1 (en) * | 2015-05-22 | 2018-05-17 | Sata Gmbh & Co. Kg | Nozzle arrangement for a spray gun |
| CN104874515A (en) * | 2015-05-26 | 2015-09-02 | 江苏大学 | Low-frequency ultrasonic secondary atomizing spraying head controlled in electromagnetic mode |
| US20180207654A1 (en) * | 2015-08-03 | 2018-07-26 | Airofog Machinery Co., Ltd. | Portable Ultrafine Nebulizer |
| US20180246233A1 (en) * | 2015-10-29 | 2018-08-30 | Framatome Gmbh | Sample container, sampling system, nuclear power plant and corresponding operating method |
| CN106513224A (en) * | 2016-12-28 | 2017-03-22 | 广州荣鑫容器有限公司 | Pop can inner wall spray system |
| CN107081055A (en) * | 2017-04-17 | 2017-08-22 | 山东大学 | A kind of eddy flow combined type SCR static mixers |
| CN207342923U (en) * | 2017-05-09 | 2018-05-11 | 湖州博川环保科技有限公司 | The core atomizer of water mist dust-removing |
| CN107214007A (en) * | 2017-07-04 | 2017-09-29 | 深圳市德瑞茵精密科技有限公司 | A kind of air gun and its atomizer of sprayed with adhesive coating |
| WO2019119244A1 (en) * | 2017-12-18 | 2019-06-27 | 深圳市大疆创新科技有限公司 | Centrifugal swing disc, spraying device and unmanned aerial vehicle |
| CN108114971A (en) * | 2017-12-20 | 2018-06-05 | 郑州艾莫弗信息技术有限公司 | Xun Huan head-on collision mixed type earth prosthetic device in a kind of |
| CN109876950A (en) * | 2019-04-01 | 2019-06-14 | 安徽省农业科学院土壤肥料研究所 | A kind of atomizer |
| US20210107017A1 (en) * | 2019-10-09 | 2021-04-15 | Spraying Systems Co. | Liquid slurry spraying system |
| CN212596510U (en) * | 2020-05-11 | 2021-02-26 | 江苏顺晟新材料科技有限公司 | Colored slurry atomization spraying device |
| WO2022034372A1 (en) * | 2020-08-10 | 2022-02-17 | A. Raymond Et Cie | Consumption optimized nozzle assembly |
| CN215088174U (en) * | 2021-03-31 | 2021-12-10 | 罗邦初 | Spiral air flow channel electric spray gun |
| CN113600391A (en) * | 2021-08-26 | 2021-11-05 | 华能国际电力股份有限公司 | Shot blasting-spraying device for inner wall of steel pipe |
| CN218048471U (en) * | 2022-09-14 | 2022-12-16 | 华能国际电力股份有限公司 | High-viscosity slurry atomizing nozzle for inner wall of boiler pipe of thermal power generating unit |
Non-Patent Citations (3)
| Title |
|---|
| 张小明;郭根喜;陶启友;黄小华;胡昱;: "高压射流水下洗网机旋转的瞬态射流打击力研究" * |
| 张小明;郭根喜;陶启友;黄小华;胡昱;: "高压射流水下洗网机旋转的瞬态射流打击力研究", 现代制造工程, no. 05, pages 21 - 25 * |
| 黄鸿;戴拓;: "蒸汽喷射加热技术与设备的进展及在造纸行业的应用", 中华纸业, no. 10, pages 14 - 20 * |
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