CN115301431B - High-viscosity slurry atomization nozzle for inner wall of boiler tube of thermal power generating unit - Google Patents
High-viscosity slurry atomization nozzle for inner wall of boiler tube of thermal power generating unit Download PDFInfo
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- CN115301431B CN115301431B CN202211118734.0A CN202211118734A CN115301431B CN 115301431 B CN115301431 B CN 115301431B CN 202211118734 A CN202211118734 A CN 202211118734A CN 115301431 B CN115301431 B CN 115301431B
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- slurry
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- outlet channel
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Classifications
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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
Abstract
The application discloses a high-viscosity slurry atomization nozzle for the inner wall of a boiler tube of a thermal power unit, which comprises: a shell base, one end of which is a spraying end, wherein a conical cavity with caliber gradually increasing along the spraying direction is arranged in the spraying end; a slurry outlet channel and a gas 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 gas outlet channel is positioned at the periphery of the slurry outlet, and a plurality of gas outlets of the gas outlet channel are arranged on the cavity wall of the conical cavity; the air outlet channel is in a spiral shape in the injection end and is suitable for outwards injecting air flow which is scattered along the circle center in a rotating way through the air outlet; one end of the connecting rod penetrates through the slurry outlet channel to be fixedly connected with the shell base, and the other end of the connecting rod extends outwards from the slurry outlet; the baffle is connected to one end of the connecting rod extending 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 to 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 atomization spray head for the inner wall of a boiler tube of a thermal power generating unit.
Background
With the continuous development of industrial technology, many technical fields are used in spraying technology, for example, the spraying technology is used for carrying out appearance treatment on a metal piece, so that the metal piece is more attractive, or an oxidation resistant layer is sprayed on the surface of the metal piece, so as to improve the oxidation resistance of the surface of the metal piece.
The spraying of the antioxidation layer of the metal piece in the normal-temperature use environment is easy to realize, and the requirement of the antioxidation coating is not too high. However, for metal parts in high temperature service environments, the requirements for the slurry are relatively high, and a slurry containing metal powder is typically selected for spraying to form an oxidation resistant layer within and/or on the outer surface of the metal part. In order to obtain a good mixing effect of the slurry containing the metal powder, a solvent with high viscosity is required. The high viscosity solvent is required because the metal powder is easily precipitated in the low viscosity solvent, which may cause uneven mixing of the slurry and ultimately affect the quality of the sprayed oxidation resistant layer.
The existing spraying device comprises a slurry inlet pipeline and a slurry inlet pipeline which are coaxially arranged, wherein the slurry inlet pipeline is positioned at 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 from the gas outlet is flushed to the slurry flowing out from the slurry outlet, so that the slurry is sprayed outwards.
However, the spraying device is only limited to spraying a certain of slurry with stable properties and low viscosity, and aims at spraying high-viscosity slurry, so that the problems of poor atomization effect and uneven spraying effect when the slurry is sprayed out are solved.
Content of the application
Therefore, the application aims to overcome the defects of poor atomization effect and uneven spraying effect when the spraying device in the prior art sprays high-viscosity slurry, thereby providing the high-viscosity slurry atomization nozzle for the inner wall of the boiler tube of the thermal power generating unit.
In order to solve the technical problems, the technical scheme of the application is as follows:
a high-viscosity slurry atomization nozzle for the inner wall of a boiler tube of a thermal power generating unit comprises
The shell comprises a shell base, a shell cover and a shell, wherein one end of the shell base is a spraying end, and a conical cavity with caliber gradually increasing along the spraying direction is arranged in the spraying end; a pulp outlet channel and a gas outlet channel are arranged in the spraying end, a pulp outlet of the pulp outlet channel is arranged corresponding to the axis of the conical cavity, the gas outlet channel is positioned at the periphery of the pulp outlet, and a plurality of gas outlets of the gas outlet channel are formed in the cavity wall of the conical cavity; the air outlet channel is in a spiral shape in the spraying end and is suitable for outwards spraying air flow which is scattered along the circle center in a rotating way through the air outlet;
one end of the connecting rod penetrates through the slurry outlet channel to be fixedly connected with the shell base, and the other end of the connecting rod extends outwards from the slurry outlet;
the baffle is connected with one end of the connecting rod extending out of the slurry outlet and is blocked in the discharging direction of the slurry outlet so as to change the spraying direction of slurry.
Further, the calibers of the air outlets are the same.
Further, the connecting rod is a telescopic rod which can be telescopic along the spraying direction, and the baffle is connected to the telescopic part of the connecting rod.
Further, the air outlets are uniformly arranged at intervals along the circumferential direction of the spraying end.
Further, the air outlets are uniformly and sequentially arranged along the circumferential direction of the spraying end.
Further, a gas chamber and a slurry making chamber are also arranged in the shell base, and a slurry inlet and a gas inlet are arranged at the tail end of the shell base, which is opposite to the spraying end; the pulp inlet is communicated with the pulp outlet channel through the pulp making chamber, and the air inlet is communicated with a plurality of air outlet channels through the air chamber.
Further, the caliber of the slurry inlet is the same as that of the slurry 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; and the slurry sprayed from the slurry outlet is sprayed outwards from the gap after being reflected by striking the sputtering plane.
The technical scheme of the application has the following advantages:
1. according to the high-viscosity slurry atomization nozzle for the inner wall of the boiler tube of the thermal power generating unit, the baffle is connected to one end of the connecting rod extending out of the slurry outlet and is blocked in the discharging direction of the slurry outlet, slurry sprayed from the slurry outlet is impacted by the rotary airflow sprayed from the gas outlet, rotary-cut, the slurry is rapidly and uniformly stirred, the effect of transversely rotary-cut the slurry is achieved, and then the stirred slurry is impacted on the baffle again, so that the slurry is further atomized, a better atomization effect can be achieved on the high-viscosity slurry, the spraying is more uniform, and the spraying effect is better.
2. According to the high-viscosity slurry atomization spray head for the inner wall of the boiler tube of the thermal power generating unit, the connecting rod is the telescopic rod which can be telescopic along the spraying direction, the baffle is connected to the telescopic part of the connecting rod, the distance between the baffle and the slurry outlet can be adjusted through the telescopic of the connecting rod, and then the area of the sprayed circular ring is adjusted.
3. According to the high-viscosity slurry atomization nozzle for the inner wall of the boiler tube of the thermal power generating unit, the baffle is detachably connected to the connecting rod, and when the conical surface needs to be sprayed, the baffle is removed, so that the adaptability of the spraying shape of the high-viscosity slurry atomization nozzle for the inner wall of the boiler tube of the thermal power generating unit is improved.
4. The high-viscosity slurry atomization spray head for the inner wall of the boiler tube of the thermal power generating unit provided by the application has the advantages of simple structure, convenience in processing, convenience in cleaning, difficulty in blocking and low manufacturing cost.
Drawings
In order to more clearly illustrate the embodiments of the present application or the technical solutions in the prior art, the drawings that are needed in the description of the embodiments or the prior art will be briefly described, and it is obvious that the drawings in the description below are some embodiments of the present application, and other drawings can be obtained according to the drawings without inventive effort for a person skilled in the art.
FIG. 1 is a schematic diagram of the internal structure of a high-viscosity slurry atomizer for the inner wall of a boiler tube of a thermal power generating unit;
FIG. 2 is a left side view of the housing base of the present application;
FIG. 3 is a schematic representation of the effect of air flow on slurry in the present application.
Reference numerals illustrate:
1. a housing base; 2. a spray end; 21. a conical cavity; 22. a pulp outlet channel; 221. a slurry outlet; 23. an air outlet channel; 231. an air outlet; 3. a gas chamber; 4. tail end; 5. a connecting rod; 6. a baffle; 7. an air inlet; 8. a slurry inlet; 9. a pulping chamber.
Detailed Description
The following description of the embodiments of the present application will be made apparent and fully in view of the accompanying drawings, in which some, but not all embodiments of the application are shown. All other embodiments, which can be made by those skilled in the art based on the embodiments of the application without making any inventive effort, are intended to be within the scope of the application.
In the description of the present application, it should be noted that the directions or positional relationships indicated by the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", etc. are based on the directions or positional relationships shown in the drawings, are merely for convenience of describing the present application and simplifying the description, and do not indicate or imply that the devices or elements referred to must have a specific orientation, be configured and operated in a specific 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 explicitly specified and limited otherwise, the terms "mounted," "connected," and "connected" are to be construed broadly, and may be either fixedly connected, detachably connected, or integrally connected, for example; can be mechanically or electrically connected; can be directly connected or indirectly connected through an intermediate medium, and can be communication between two elements. The specific meaning of the above terms in the present application will be understood in specific cases by those of ordinary skill in the art.
In addition, the technical features of the different embodiments of the present application described below may be combined with each other as long as they do not collide with each other.
Examples
As shown in fig. 1 to 3, the embodiment provides a high-viscosity slurry atomization nozzle for the inner wall of a boiler tube of a thermal power generating unit, which comprises a shell base 1, a connecting rod 5 and a baffle 6.
One end of the shell base 1 is provided with a spraying end 2, and a conical cavity 21 with caliber gradually increasing along the spraying direction is arranged in the spraying end 2; a pulp outlet channel 22 and an air outlet channel 23 are arranged in the injection end 2, a pulp outlet 221 of the pulp 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 pulp 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 in a spiral shape in the spraying end 2, and is suitable for spraying air flow which is scattered along the circle center in a rotating way outwards through the air outlet 231, and the air outlet 231 deflects towards the axial direction of the pulp outlet 221, so that high-pressure air flow can be sprayed towards the pulp sprayed from the pulp outlet 221, and the pulp is subjected to rotary cutting. FIG. 3 is a schematic illustration of the effect of air flow on slurry.
One end of the connecting rod 5 passes through the slurry outlet passage 22 to be fixedly connected with the housing base 1, and the other end 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 to change the spraying direction of the slurry.
Because baffle 6 is connected at the one end that connecting rod 5 stretches out the thick liquid mouth 221 and keeps off in the play thick liquid direction of thick liquid mouth 221, from the thick liquid mouth 221 spun thick liquid is impacted, the rotary-cut by the rotatory air current of gas outlet 231 spun, thick liquid is evenly stirred fast, then, the thick liquid after stirring strikes baffle 6 again, makes the thick liquid obtain further atomizing, so, just so can realize better atomization effect to high viscosity thick liquid for the spraying is more even, and the spraying effect is better.
In addition, the high-viscosity slurry atomization 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 certainly applicable to spraying low-viscosity slurry, can be used for spraying pipelines, and can be widely applied to similar aspects needing spraying or pneumatic stirring in the food processing industry or other industrial fields, and the application range is wider.
For the shell base 1, a gas chamber 3 and a slurry making chamber 9 are also arranged in the shell base 1, and a slurry inlet 8 and a gas inlet 7 are arranged at the tail end 4 of the shell base 1, which is back to the spraying end 2; 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 pulp inlet 8 is communicated with the pulp outlet channel 22 through the pulp making chamber 9, and the apertures of the pulp inlet 8 and the pulp making chamber 9 are the same, so that the pulp blockage caused by diameter change is avoided; the gas inlet 7 communicates with a number of gas outlet channels 23 via gas chambers 3. As shown in fig. 1, in the present embodiment, the injection end 2 is independently formed, assembled on the housing base 1, and is a part of the housing base 1, and the injection end 2 is independently formed to facilitate processing.
For the air outlets 231, specifically, the apertures of the air outlets 231 are the same, so that the impact and the rotary cutting force of the high-pressure air flow sprayed 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 circumference of the spraying end 2, so that the slurry sprayed from the slurry outlet 221 is uniformly rotary-cut in all directions, and the stirring is more uniform, and of course, the air outlets 231 may be unevenly arranged, but the effect is not evenly arranged.
For the link 5 and the baffle 6, specifically, the link 5 is connected into the housing base 1 through the grout outlet 221, and the link 5 is provided coaxially with the grout outlet 221 and is a telescopic rod that is telescopic in the injection direction. The baffle 6 is connected to the telescopic part of the connecting rod 5, so that the size of the gap between the baffle 6 and the housing base 1 can be adjusted by means of the scalability of the connecting rod 5, and the size of the spraying circular ring area can be adjusted. When the connecting rod 5 is longer, the gap between the baffle 6 and the slurry outlet 221 is larger, the area of the sprayable ring is larger, and when the connecting rod 5 is shorter, the gap between the baffle 6 and the slurry outlet 221 is smaller, and the area of the sprayable ring is smaller. Moreover, the baffle 6 is detachably fixed on the connecting rod 5, and when the conical surface needs to be sprayed, only the baffle 6 needs to be removed, so that the slurry which is sprayed from the air outlet 231 and is subjected to rotary cutting by high-pressure air flow is directly sprayed on the conical surface. The baffle 6 is coaxially disposed with the slurry outlet 221, and the surface facing the slurry outlet 221 is a circular sputtering plane, however, it is also possible to dispose the baffle in other shapes such as triangle, square, etc. specifically according to actual needs; a gap is arranged between the sputtering plane of the baffle plate 6 and the spraying end 2; the slurry ejected from the slurry outlet 221 hits the sputtering plane, then is reflected and ejected outward from the gap onto the pipe wall to be sprayed. Of course, the shape of the baffle 6 is not limited to a flat plate shape, and may be a horn shape, and is specifically set according to actual needs, and is not specifically limited herein.
The working process of spraying the high-viscosity slurry atomization nozzle on the inner wall of the pipeline for the inner wall of the boiler tube of the thermal power generating unit is as follows:
the inner wall of a boiler tube of a thermal power generating unit integrally extends into a pipeline by using a high-viscosity slurry atomization nozzle, and the telescopic length of a connecting rod 5 is adjusted according to the size of the required spraying circular ring area;
feeding the slurry from the slurry inlet 8 into the slurry producing chamber 9 by high pressure and reaching the slurry outlet 221 along the slurry outlet passage 22 communicating with the slurry producing 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 outlet 231, and the gas sprayed out from each gas outlet 231 is matched together to form spiral gas flow as the gas outlet 231 is arranged in a deflection way towards the axis of the slurry outlet 221, and the slurry sprayed out from the slurry outlet 221 is rotary-cut, so that the slurry is rotary-cut;
the slurry after rotary cutting is collided on a baffle plate 6 with a certain distance from the front end of the slurry outlet 221, and is sprayed and atomized again;
the sprayed slurry is sprayed to the inner wall of the pipeline through a gap between the baffle 6 and the spraying end 2;
uniformly moving high-viscosity slurry atomization spray heads for the inner wall of a boiler tube of a thermal power unit in a pipeline to ensure that the high-viscosity slurry atomization spray heads for the inner wall of the boiler tube of the thermal power unit realize uniform spraying on all parts of the inner wall of the pipeline;
in addition, the following beneficial effects of the high-viscosity slurry atomization nozzle for the inner wall of the boiler tube of the thermal power generating unit in the embodiment are supplemented:
in the prior art, in order to obtain better atomization of the slurry, the slurry outlet 221 needs to be formed in a contracted shape to control the amount of the slurry sprayed, because if the amount of the slurry sprayed is relatively large, it may not be possible to obtain better atomization of all the slurry. However, in the high-viscosity slurry atomization nozzle for the inner wall of the boiler tube of the thermal power generating unit in the embodiment, due to the design of the baffle 6, the slurry with high viscosity can be well atomized outside the slurry outlet 221, so the slurry outlet 221 can be made into a flat tubular shape, compared with the contracted slurry outlet 221, the flat tubular slurry outlet 221 is not easy to be blocked, and therefore, the size of the high-viscosity slurry atomization nozzle for the inner wall of the boiler tube of the thermal power generating unit can be made smaller, so as to be suitable for spraying the inner wall of a small-size pipeline.
Moreover, as the air inlet 7 is connected with the high-pressure air inlet pipeline, the slurry inlet 8 is connected with the slurry inlet pipeline, so that the lengths of the high-pressure air inlet pipeline and the slurry inlet pipeline can be adjusted according to the needs, the propelling depth of the high-viscosity slurry atomizing nozzle for the inner wall of the boiler tube of the thermal power generating unit is increased, and the spraying device is suitable for spraying the inner wall of a longer pipeline.
It is apparent that the above examples are given by way of illustration only and are not limiting of the embodiments. Other variations or modifications of the above teachings will be apparent to those of ordinary skill in the art. It is not necessary here nor is it exhaustive of all embodiments. While still being apparent from variations or modifications that may be made by those skilled in the art are within the scope of the application.
Claims (6)
1. The utility model provides a thermal power unit boiler tube high viscosity thick liquids atomizer for inner wall which characterized in that includes:
a shell base (1), one end of which is provided with a spraying end (2), wherein a conical cavity (21) with caliber gradually increasing along the spraying direction is arranged in the spraying end (2); a pulp outlet channel (22) and an air outlet channel (23) are arranged in the spraying end (2), a pulp outlet port (221) of the pulp 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 pulp outlet port (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 in a spiral shape in the injection end (2) and is suitable for externally spraying air flow which is scattered along the circle center in a rotating way through the air outlet (231); the shell base (1) is internally provided with a gas chamber (3) and a slurry making chamber (9), and the tail end (4) of the shell base (1) facing away from the injection end (2) is provided with a slurry inlet (8) and a gas inlet (7); the pulp inlet (8) is communicated with the pulp outlet channels (22) through the pulp making chamber (9), and the air inlet (7) is communicated with a plurality of air outlet channels (23) through the air chamber (3);
one end of the connecting rod (5) penetrates through the slurry outlet channel (22) to be fixedly connected with the shell base (1), and the other end of the connecting rod extends outwards from the slurry outlet (221);
the baffle plate (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; one surface 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) is sprayed outwards from the gap after being reflected by striking the sputtering plane.
2. The high-viscosity slurry atomization nozzle for the inner wall of a boiler tube of a thermal power generating unit according to claim 1, wherein the apertures of the plurality of air outlets (231) are the same.
3. The high-viscosity slurry atomization nozzle for the inner wall of a boiler tube of a thermal power generating unit according to claim 1, wherein a plurality of the air outlets (231) are uniformly arranged at intervals along the circumferential direction of the injection end (2).
4. A high viscosity slurry atomizer for an inner wall of a boiler tube of a thermal power generating unit according to claim 1, wherein a plurality of said air outlets (231) are axially offset towards said slurry outlet (221).
5. The high-viscosity slurry atomization nozzle for the inner wall of a boiler tube of a thermal power generating unit according to claim 1, wherein the connecting rod (5) is a telescopic rod which is telescopic along the spraying direction, and the baffle plate (6) is connected to a telescopic part of the connecting rod (5).
6. The high-viscosity slurry atomization nozzle for the inner wall of a boiler tube of a thermal power generating unit according to claim 1, wherein the caliber sizes of the slurry inlet (8) and the slurry manufacturing 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 CN115301431A (en) | 2022-11-08 |
| CN115301431B true 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 (27)
| 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 |
| 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 |
| 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 | 斯普瑞喷雾系统(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 | 喷雾系统公司 | 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 |
| 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 |
| 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 |
| 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 |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3801967B2 (en) * | 2001-08-28 | 2006-07-26 | 株式会社いけうち | NOZZLE AND METHOD OF INJECTING FLUID TO INTERNAL PERIPHERAL SURFACE BY NOZZLE |
| US7014808B2 (en) * | 2002-03-05 | 2006-03-21 | The Coca-Cola Company | Method and apparatus for coating the interior surface of a straw |
| US8448441B2 (en) * | 2007-07-26 | 2013-05-28 | General Electric Company | Fuel nozzle assembly for a gas turbine engine |
| DE102015006484A1 (en) * | 2015-05-22 | 2016-11-24 | Sata Gmbh & Co. Kg | Nozzle arrangement for a spray gun, in particular paint spray gun and spray gun, in particular paint spray gun |
| CN204994473U (en) * | 2015-08-03 | 2016-01-27 | 上海爱农机电设备有限公司 | Portable superfine atomizing machine |
| DE102015221151B3 (en) * | 2015-10-29 | 2016-10-27 | Areva Gmbh | Sampling vessel and sampling system and related operating procedures |
| US11453017B2 (en) * | 2019-10-09 | 2022-09-27 | Spraying Systems Co. | Liquid slurry spraying system |
-
2022
- 2022-09-14 CN CN202211118734.0A patent/CN115301431B/en active Active
Patent Citations (27)
| 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 |
| 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 |
| 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 | 斯普瑞喷雾系统(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 | 喷雾系统公司 | 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 |
| 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 |
| 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 |
| 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 (1)
| Title |
|---|
| 蒸汽喷射加热技术与设备的进展及在造纸行业的应用;黄鸿;戴拓;;中华纸业(10);14-20 * |
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