CN214370153U - Side wall water-cooled wall adherence protection device based on thick and thin pulverized coal separation combustor - Google Patents
Side wall water-cooled wall adherence protection device based on thick and thin pulverized coal separation combustor Download PDFInfo
- Publication number
- CN214370153U CN214370153U CN202120006512.4U CN202120006512U CN214370153U CN 214370153 U CN214370153 U CN 214370153U CN 202120006512 U CN202120006512 U CN 202120006512U CN 214370153 U CN214370153 U CN 214370153U
- Authority
- CN
- China
- Prior art keywords
- secondary air
- burner
- air
- nozzle
- wall
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Images
Abstract
A side wall water-cooled wall adherence protection device based on a dense-dilute pulverized coal separation burner comprises adherence air nozzles which are respectively arranged on two sides of a front wall and a rear wall of a boiler of a coal-fired power plant, burners are arranged between the adherence air nozzles on the two sides of the front wall and the rear wall, and each burner comprises an outermost side burner adjacent to the adherence air nozzle and a plurality of middle area burners; a shutter type coal powder concentrator is arranged in a primary air pipe of the outermost burner, a primary air nozzle of the outermost burner is divided into a thick coal powder nozzle and a thin coal powder nozzle, one side of the boiler close to the burner in the middle area in the width direction of the boiler is the thick coal powder nozzle, one side of the boiler close to the left side wall or the right side wall of the boiler is the thin coal powder nozzle, and a coal powder pipeline of the outermost burner is introduced from the horizontal height direction of the primary air pipe and is connected with the primary air pipe through an elbow; the dense coal powder nozzle and the light coal powder nozzle can be adjusted by air distribution through independently arranged air door baffles. The utility model discloses can obviously improve side wall water-cooling wall adherence atmosphere.
Description
Technical Field
The utility model belongs to coal fired power plant boiler field, concretely relates to side wall water-cooling wall adherence protection device based on rich and weak buggy separation combustor.
Background
The burners of the front-back wall opposed firing boiler are arranged on the front wall and the back wall of the boiler, the middle areas of the left side wall and the right side wall of the boiler are easy to generate high-temperature corrosion, and the elevation of the high-temperature corrosion area is from the elevation of the lowest burner to the elevation of the over-fire air burner. If the water wall of the spiral tube ring of the left/right side wall of a certain 350MW supercritical unit in the area with the height between B, C layers of burners has the problem of high-temperature corrosion, the thickness of the lowest side of the part with the most serious wall thickness reduction of the water wall is about 1.2mm and is less than 1/5 of the original wall thickness; the high-temperature corrosion problem exists in the elevation range of the lower layer combustor to the upper layer combustor of two side walls of a certain 660MW supercritical unit, the wall thickness of the thinnest part is 5.7mm (the original design wall thickness is 7.5mm) when the thickness of the water wall is measured, the combination of a corrosion product layer on the water wall pipe and the water wall is not firm, the corrosion product layer can be easily removed by external force, and the outer wall of the water wall is dark black after the corrosion product falls off. When a 1000MW ultra-supercritical unit is shut down for maintenance, the wall thickness reduction of the water wall tubes on the two side walls is up to about 2mm, and the total number of 599 replaced tubes is 2000 m.
The high-temperature corrosion is mainly related to factors such as high sulfur content of the coal, strong reducing atmosphere near a water-cooled wall of a side wall, erosion of flue gas and pulverized coal airflow and the like. In order to solve the problem of high-temperature corrosion of water cooling walls on two side walls of a front-wall and rear-wall opposed combustion boiler, active protection and passive protection solutions are proposed by domestic boiler manufacturers, scientific research institutions and the like. The purpose of active protection is to improve the wall-attached reducing atmosphere of the water cooling walls on the two side walls by increasing the distance between the outermost side burner and the side walls, controlling the sulfur content of coal as fired, optimizing and adjusting the combustion test, modifying wall-attached air and the like; the passive protection is mainly implemented by corrosion-resistant spraying protection in high-temperature corrosion areas of water-cooled walls of two side walls. The combustion optimization adjustment test work comprises pulverized coal fineness adjustment and secondary air optimization of a combustor. When the fineness of the coal powder is controlled to be low, the coal powder is ignited and combusted in time, so that the coal powder which is not combusted completely can be prevented from being continuously combusted at the side wall, the oxygen at the side wall is consumed, and the reducing atmosphere at the water-cooled wall of the side wall is enhanced; the optimization of the secondary air of the combustor is mainly to enlarge the opening degree of the secondary air outside the combustor on the outermost side, so that the secondary air quantity outside the combustor on the outermost side is increased, the rotational flow strength is weakened, and the adherence atmosphere of a water wall of a side wall can be improved.
However, the prior art has many problems in implementation, which mainly include: the corrosion-resistant spraying protection of the water-cooled wall is greatly influenced by a spraying process and a spraying material, and the spraying is required to be carried out again every 2-3 years; due to the coal market change and the operation pressure of coal-fired power plants, the proportion of the high-sulfur coal is large; in order to meet the requirements of the output of the coal mill and the load capacity of the unit, the fineness of the pulverized coal cannot be controlled to be thin; the opening degree of secondary air outside the outermost burner is maximum, the swirling strength is weakened to cause the reduction of the capacity of entrainment of high-temperature flue gas, and the ignition and stable combustion of pulverized coal are not facilitated; the added wall-adhering air nozzle is easy to be slag-bonded and burnt, and loses the wall-adhering air effect.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to above-mentioned prior art in the hedging combustion boiler side wall water-cooling wall high temperature corrosion problem, provide a side wall water-cooling wall adherence protection device based on dense and thin buggy separation combustor, guarantee under the prerequisite that the buggy surely burns, reduce the regional wall heat load of both sides wall, improve both sides wall water-cooling wall adherence atmosphere, and then the effectual water-cooling wall high temperature corrosion of avoiding.
In order to achieve the above object, the present invention provides the following technical solutions:
a side wall water-cooled wall adherence protection device based on a dense-dilute pulverized coal separation burner comprises adherence air nozzles which are respectively arranged on two sides of a front wall and a rear wall of a boiler of a coal-fired power plant, burners are arranged between the adherence air nozzles on the two sides of the front wall and the rear wall, and each burner comprises an outermost side burner adjacent to the adherence air nozzle and a plurality of other middle area burners; a shutter type coal powder concentrator is arranged in a primary air pipe of the outermost burner, a primary air nozzle of the outermost burner is divided into a thick coal powder nozzle and a thin coal powder nozzle, one side of the boiler close to the burner in the middle area in the width direction of the boiler is the thick coal powder nozzle, one side of the boiler close to the left side wall or the right side wall of the boiler is the thin coal powder nozzle, and a coal powder pipeline of the outermost burner is introduced from the horizontal height direction of the primary air pipe and is connected with the primary air pipe through an elbow; the dense coal powder nozzle and the light coal powder nozzle are provided with air distribution adjustment through air door baffles which are independently arranged.
Preferably, the outermost burner is a cyclone burner, and the burner air distribution is composed of primary air, inner secondary air, dense side outer secondary air and light side outer secondary air; the outer secondary air duct on the thick side and the outer secondary air duct on the thin side of the cyclone burner are semicircular air ducts which are separated by an outer secondary air duct partition plate; the nozzle of the outermost burner is respectively a primary air nozzle, an inner secondary air nozzle and an outer secondary air nozzle from inside to outside; the primary air nozzle is a circular nozzle, a middle partition plate is arranged in the nozzle, and the middle partition plate vertically divides the primary air nozzle into a thick coal powder nozzle and a thin coal powder nozzle which are semicircular; the air sources of the inner secondary air, the outer secondary air of the dense side and the outer secondary air of the light side of the outermost side combustor are taken from the air boxes; a fixed swirler is arranged in the inner secondary air duct of the outermost burner, and the swirl strength of the inner secondary air of the outermost burner is not adjustable; an inner secondary air adjusting rod is arranged on the burner panel of the outermost burner, and the inner secondary air quantity can be adjusted through the axial displacement of the inner secondary air adjusting rod along the burner.
Preferably, the outer secondary air duct of the dense side is at the same side with the dense coal powder nozzle, the outer secondary air volume of the dense side and the swirl strength thereof are adjusted through a dense side impeller type air door baffle plate which is arranged on the outermost side combustor in a tangential manner, a dense side outer secondary air door control lever is arranged on a combustor panel, the deflection angle of the outer secondary air door control lever of the dense side is adjusted, the dense side impeller type air door baffle plate is driven to rotate, the rotation angle of the dense side outer secondary air door control lever is changed, and the outer secondary air volume of the dense side and the swirl strength of the dense side outer secondary air are adjusted at the same time.
Preferably, the fresh-side outer secondary air duct is at the same side as the fresh coal nozzle, the fresh-side outer secondary air volume and the swirl strength thereof are adjusted through a fresh-side impeller type air door baffle arranged on the outermost burner in a tangential manner, a fresh-side outer secondary air door control lever is arranged on the burner panel, and the deflection angle of the fresh-side outer secondary air door control lever is adjusted to drive the fresh-side impeller type air door baffle to rotate so as to change the rotation angle thereof, so that the fresh-side outer secondary air volume and the fresh-side outer secondary air swirl strength are adjusted simultaneously.
Preferably, the louver type pulverized coal concentrator comprises a cavity formed by connecting a concentrator shell and a middle partition plate, and concentrating blades arranged in the cavity in a louver type mode.
Preferably, the middle area combustor is a cyclone combustor, the combustor air distribution is composed of primary air, central air, inner secondary air and outer secondary air, the inner secondary air duct and the outer secondary air duct are concentric annular channels, a pulverized coal pipeline of the middle area combustor is connected from the right below of a primary air pipe, and air sources of the central air, the inner secondary air and the outer secondary air are taken from an air box; a fixed swirler is arranged in an inner secondary air duct of the middle area combustor, and the swirling strength of inner secondary air of the middle area combustor is not adjustable; an inner secondary air adjusting rod is arranged on a burner panel of the middle area burner, and the inner secondary air can be adjusted by the inner secondary air adjusting rod along the axial displacement of the burner.
Preferably, the air volume and the swirl strength of the external secondary air of the middle area combustor are adjusted through an integral impeller type air door baffle arranged on the combustor in a tangential manner, and an external secondary air door operating lever is arranged on a combustor panel of the middle area combustor; the deflection angle of the outer secondary air door control lever is adjusted to drive the integral impeller type air door baffle to rotate, and the rotation angle of the integral impeller type air door baffle is changed, so that the outer secondary air quantity and the outer secondary air swirl strength are adjusted simultaneously.
Preferably, the wall-attached air nozzle is a circular nozzle, the wall-attached air is direct current air, and an air source of the wall-attached air nozzle is taken from a hot primary air main pipe.
Compared with the prior art, the utility model discloses following beneficial effect: be different from the ascending buggy concentration deviation of traditional cyclone burner buggy spout radial direction, the utility model discloses an elbow level introduces the buggy, add shutter formula buggy concentrator, and separate for dense buggy air current and light buggy air current with front and back wall offset combustion boiler outside burner buggy spout efflux horizontal direction, and set up the concentration alone, the air door baffle of light buggy air current carries out the air distribution and adjusts, make on not reducing the combustor heat load, do not influence the buggy and catch fire stable basis, the influence that boiler side wall water-cooling wall buggy erodees has been reduced, side wall department burning heat load has been reduced, be favorable to improving side wall water-cooling wall adherence atmosphere. The horizontal concentration separation of the pulverized coal nozzle of the outermost burner is combined with direct-current jet flow wall-attached air, so that the wall-attached atmosphere of the side wall water-cooled wall can be obviously improved, and the problem of high-temperature corrosion of the side wall water-cooled wall of the opposed firing boiler is solved.
Drawings
FIG. 1 is a schematic structural view of an outermost burner of the present invention;
FIG. 2 is a schematic structural view of a middle zone burner of the present invention;
FIG. 3 is a schematic view of the arrangement structure of the sidewall water-cooled wall adherence protection device of the present invention;
FIG. 4 is a schematic view of the nozzle structure of the outermost burner of the present invention;
in the drawings: 1-front wall, 2-rear wall, 3-outermost burner, 4-middle zone burner, 5-primary air pipe, 6-louver type coal powder concentrator, 7-primary air nozzle, 8-dense coal powder nozzle, 9-weak coal powder nozzle, 10-left wall, 11-right wall, 12-coal powder pipeline, 13-elbow, 14-wall air nozzle, 15-dense side outer secondary air duct, 16-weak side outer secondary air duct, 17-outer secondary air duct baffle, 18-inner secondary air nozzle, 19-outer secondary air nozzle, 20-middle baffle, 21-air box, 22-concentrator shell, 23-concentrating blade, 24-dense side impeller type air door baffle, 25-dense side outer secondary air door control lever, 26-weak side impeller type air door baffle, 27-a fresh side outer secondary air door operating lever, 28-an inner secondary air duct, 29-an outer secondary air duct, 30-a fixed swirler, 31-a burner panel, 32-an inner secondary air adjusting lever, 33-an integral impeller type air door baffle and 34-an outer secondary air door operating lever.
Detailed Description
The present invention will be described in further detail with reference to the accompanying drawings.
The water-cooled wall high temperature corrosion problem to front and back wall offset combustion boiler, the utility model discloses side wall water-cooled wall adherence protection device based on dense and thin buggy separation combustor all is provided with the combustor including arranging adherence wind spout 14 in coal fired power plant boiler front wall 1 and 2 both sides of back wall respectively between the adherence wind spout 14 of front wall 1 and 2 both sides of back wall, the combustor includes 3 and arranges a plurality of middle zone combustor 4 between 3 with the adjacent outside combustor of adherence wind spout 14.
Referring to fig. 2, the middle area burner 4 of the present invention divides the air for combustion into primary air, central air, inner secondary air and outer secondary air. The primary air carries pulverized coal particles to form pulverized coal airflow, and the pulverized coal airflow sequentially enters the primary air pipe 5 of the combustor and the primary air nozzle 7 from a pulverized coal pipeline 12 right below the primary air pipe 5 of the middle-area combustor 4. The central air, the inner secondary air and the outer secondary air are taken from the air box 21, and the central air enters the hearth through a circular central air duct; the inner secondary air and the outer secondary air enter the hearth through concentric annular channels of the inner secondary air and the outer secondary air in the combustor. The inner secondary air and the outer secondary air are axial rotational flow air, annular backflow is formed in the near burner area, high-temperature flue gas is brought back to the near burner area, primary air is heated, pulverized coal is ignited, and flame stability is kept.
Referring to fig. 1 and 4, the outermost burner 3 divides the combustion air into primary air, inner secondary air, dense side outer secondary air, and weak side outer secondary air. The primary air carrying pulverized coal particles forms pulverized coal airflow, and flows through the outermost burner 3 corresponding to the pulverized coal pipeline 12, the primary air pipe 5 (including the louver type pulverized coal concentrator 6) and the primary air nozzle 7 to enter the hearth for combustion. The coal dust airflow enters the primary air pipe 5 from the outermost burner 3 corresponding to the coal dust pipeline 12. Because the outermost burner 3 is introduced from the horizontal height of the primary air pipe 5 corresponding to the pulverized coal pipeline 12 and is provided with a 90-degree elbow 13 for horizontal connection, after the pulverized coal airflow passes through the elbow 13, most pulverized coal particles are concentrated in the outer side wall area of the pipe under the action of centrifugal force to form concentration deviation, and the pulverized coal airflow passes through the elbow 13 and is divided into concentrated pulverized coal airflow and light pulverized coal airflow, wherein the concentrated pulverized coal airflow is close to the outer wall of the elbow, and the light pulverized coal airflow is close to the inner wall of the elbow. A shutter type coal dust concentrator 6 is arranged in a primary air pipe 5 of the outermost burner 3, the thick coal dust airflow and the thin coal dust airflow flow through the shutter type coal dust concentrator 6, and form two stable horizontal thick and thin coal dust airflows under the action of a concentrating blade 23, a thick side impeller type air door baffle 24 and a middle baffle plate 20, wherein the thick coal dust airflow is close to the burner 4 in the middle area along the width direction of the boiler, and the thin coal dust airflow is close to the side wall of the boiler. The thick coal powder air flow and the thin coal powder air flow respectively enter the hearth through a thick coal powder nozzle 8 and a thin coal powder nozzle 9. The inner secondary air, the outer secondary air on the dense side and the outer secondary air on the fresh side of the outermost burner 3 are taken from an air box 21, and the outer secondary air channel on the dense side and the outer secondary air channel on the fresh side are semicircular air channels which are separated by an outer secondary air channel partition plate 17. The secondary air outside the dense/light side is positioned at the same side of the dense/light coal powder nozzle, the secondary air quantity outside the dense/light side and the rotational flow intensity thereof are adjusted by a dense/light side impeller type air door baffle arranged in a tangential way on the burner, and a dense/light side outer secondary air door control lever is arranged on a burner panel. The impeller type air door baffle is driven to rotate by adjusting the deflection angle of the control lever of the secondary air door outside the dense/dilute side, and the rotation angle is changed, so that the secondary air quantity outside the dense/dilute side and the swirl strength of the secondary air outside the dense/dilute side are adjusted simultaneously. When the deflection angle of the secondary air door operating lever outside the thick/thin side is closed, the secondary air quantity outside the thick/thin side can be reduced, and the swirl intensity of the secondary air outside the thick/thin side can be increased; when the deflection angle of the secondary air door control lever outside the thick/thin side is opened to be large, the secondary air quantity outside the thick/thin side can be increased, and the swirling flow intensity of the secondary air outside the thick/thin side can be reduced.
Referring to fig. 3, pulverized coal burners of an opposed firing boiler are arranged on a front wall 1 and a rear wall 2 of the boiler, pulverized coal airflow is subjected to opposed firing, and the water-cooled wall middle areas of a left side wall 10 and a right side wall 11 of the boiler are affected by the pulverized coal airflow of the pulverized coal burners and the reducing atmosphere at the wall-attached position, so that the problem of high-temperature corrosion of the water-cooled wall in the areas is serious. In order to solve the problem of high-temperature corrosion of the water-cooled wall of the side wall, the combustion heat load at the position of the side wall needs to be reduced, and the oxygen content at the position of the wall-attached wall of the side wall needs to be increased. The utility model changes the coal powder nozzle of the outermost side combustor 3 of the front wall 1 and the rear wall 2 into the coal powder nozzle with horizontal shade separation, wherein the coal powder nozzle close to the left side wall 10 and the right side wall 11 is the light coal powder nozzle, which can reduce the combustion heat load of the side wall area, improve the wall adherence atmosphere of the side wall water wall, and combine with the direct current jet flow wall adherence wind, thereby avoiding the coal powder scouring of the side wall water wall and improving the wall adherence atmosphere of the side wall water wall; an adherence air nozzle 14 is arranged between the outermost burner 3 and the side wall, the adherence air nozzle 14 is a straight cylindrical round nozzle, hot air from a primary hot air main pipe enters the hearth through the adherence air nozzle 14, and a protective film is formed at the water wall of the side wall. The outermost side is separated horizontally by the coal powder nozzle of the outermost side combustor 3 and is additionally provided with wall-attached air, and the problem of high-temperature corrosion of the side wall water-cooled wall can be solved fundamentally through the combined action of the coal powder nozzle and the wall-attached air.
The primary air nozzle 7 of the outermost burner 3 is divided into a thick coal powder nozzle 8 and a thin coal powder nozzle 9 by a middle partition plate 20, and thick coal powder airflow and thin coal powder airflow respectively enter a hearth through the thick coal powder nozzle 8 and the thin coal powder nozzle 9 to be combusted. The concentration of the coal powder in the concentrated coal powder airflow is higher, the required ignition heat is less, and the concentration of the separated volatile matter is high, so that the ignition and stable combustion of the coal powder are facilitated; the concentration of the coal powder of the light coal powder airflow is low, and the air quantity is large. Because the light pulverized coal nozzles 9 are close to the side wall of the boiler, the influence of pulverized coal scouring on the water-cooled wall of the side wall is reduced, and the combustion heat load at the side wall is reduced.
The thick coal powder nozzle 8 and the thin coal powder nozzle 9 are semicircular nozzles, the thick side outer secondary air duct 15 and the thin side outer secondary air duct 16 are semicircular annular air ducts, the thick side outer secondary air duct 15 is positioned at the same side as the thick coal powder nozzle 8, the thin side outer secondary air duct 16 is positioned at the same side as the thin coal powder nozzle 9, and the thick coal powder nozzle 8 and the thin coal powder nozzle 9 are respectively provided with a thick side outer secondary air door operating lever 25 and a thin side outer secondary air door operating lever 27. The thick and thin pulverized coal airflow is provided with different external secondary air quantity and external secondary air swirling flow strength, so that thick and thin pulverized coal airflow can be reasonably distributed and combusted. The outermost burner 3 is a horizontal rich-lean separation type burner, and the concentration deviation of coal powder in the rich coal powder airflow and the lean coal powder airflow is large, so that the swirling intensity of the outer secondary air can be independently adjusted according to the deviation of the coal powder concentration. The coal powder concentration in the coal powder airflow ejected by the concentrated coal powder nozzle 8 is higher, the corresponding external secondary air swirl strength is higher, the capacity of entraining high-temperature flue gas is enhanced, and the ignition and combustion of the concentrated coal powder airflow are facilitated; the coal powder concentration in the coal powder airflow sprayed out of the light coal powder nozzle 9 is low, the corresponding external secondary air swirl strength is low, the external secondary air quantity is large, the reduction of the combustion heat load of the side wall area is facilitated, and the oxygen quantity of the side wall area is increased. Furthermore, the separation of the concentration and the dilution of the pulverized coal airflow is realized by an elbow 13 on the pulverized coal pipeline and a shutter type pulverized coal concentrator 6 arranged in a primary air pipe 5, two streams of the concentration and the dilution are sprayed into a hearth from the horizontal direction, the concentrated pulverized coal airflow is sprayed into the hearth from one side far away from the side wall, and the dilute pulverized coal airflow is sprayed into the hearth from one side close to the side wall.
The above-described preferred embodiments of the present invention are not intended to limit the present invention, and it should be understood by those skilled in the art that the present invention can be modified and replaced by other simple modifications and replacements without departing from the spirit and principle of the present invention, and these modifications and replacements also fall within the protection scope of the appended claims.
Claims (8)
1. The utility model provides a side wall water-cooled wall adherence protection device based on rich and weak buggy separation combustor which characterized in that: the wall-attached air burner comprises wall-attached air nozzles (14) which are respectively arranged on two sides of a front wall (1) and a rear wall (2) of a boiler of a coal-fired power plant, burners are arranged between the wall-attached air nozzles (14) on the two sides of the front wall (1) and the rear wall (2), and each burner comprises an outermost side burner (3) adjacent to the wall-attached air nozzle (14) and a plurality of other middle area burners (4); a shutter type coal dust concentrator (6) is arranged in a primary air pipe (5) of the outermost burner (3), a primary air nozzle (7) of the outermost burner (3) is divided into a thick coal dust nozzle (8) and a thin coal dust nozzle (9), one side of the boiler close to the middle area burner (4) in the width direction is the thick coal dust nozzle (8), one side of the boiler close to a left side wall (10) or a right side wall (11) is the thin coal dust nozzle (9), a coal dust pipeline (12) of the outermost burner (3) is introduced from the horizontal height direction of the primary air pipe (5) and is connected with the primary air pipe (5) through an elbow (13); the dense coal powder nozzle (8) and the light coal powder nozzle (9) can be adjusted by air distribution through independently arranged air door baffles.
2. The side wall water-cooled wall adherence protection device based on the concentrated and diluted pulverized coal separation burner as claimed in claim 1, is characterized in that: the outermost burner (3) is a cyclone burner, and the burner air distribution is composed of primary air, inner secondary air, dense side outer secondary air and light side outer secondary air; the outer secondary air duct (15) at the thick side and the outer secondary air duct (16) at the thin side of the cyclone burner are semicircular air ducts which are separated by an outer secondary air duct partition plate (17); the nozzle of the outermost burner (3) is respectively a primary air nozzle (7), an inner secondary air nozzle (18) and an outer secondary air nozzle (19) from inside to outside; the primary air nozzle (7) is a circular nozzle, a middle partition plate (20) is arranged in the nozzle, and the primary air nozzle (7) is vertically divided into a semicircular thick coal nozzle (8) and a semicircular light coal nozzle (9) by the middle partition plate (20); the wind sources of the inner secondary wind, the outer secondary wind on the dense side and the outer secondary wind on the light side of the outermost burner (3) are taken from wind boxes (21); a fixed swirler (30) is arranged in an inner secondary air channel (28) of the outermost burner (3), and the swirl strength of inner secondary air of the outermost burner (3) is not adjustable; an inner secondary air adjusting rod (32) is arranged on a burner panel (31) of the outermost burner (3), and the inner secondary air quantity can be adjusted by the axial displacement of the inner secondary air adjusting rod (32) along the burner.
3. The side wall water-cooled wall adherence protection device based on the concentrated and diluted pulverized coal separation burner as claimed in claim 2, is characterized in that: the outer secondary air duct (15) of the dense side is arranged at the same side of the dense coal powder nozzle (8), the outer secondary air volume of the dense side and the swirl strength of the outer secondary air volume of the dense side are adjusted through a dense side impeller type air door baffle (24) which is arranged on the outermost side combustor (3) in a tangential mode, an outer secondary air door control lever (25) of the dense side is arranged on a combustor panel, the deflection angle of the outer secondary air door control lever (25) of the dense side is adjusted, the impeller type air door baffle (24) of the dense side is driven to rotate, the rotation angle of the outer secondary air volume of the dense side and the swirl strength of the outer secondary air volume of the dense side are changed, and meanwhile the outer secondary air volume of the dense side and the swirl strength of the outer secondary air of the dense side are adjusted.
4. The side wall water-cooled wall adherence protection device based on the concentrated and diluted pulverized coal separation burner as claimed in claim 2, is characterized in that: the outer secondary air duct (16) of the light side is arranged at the same side of the light coal powder nozzle (9), the outer secondary air volume of the light side and the swirl strength of the outer secondary air volume of the light side are adjusted through a light side impeller type air door baffle (26) which is arranged on the outermost side combustor (3) in a tangential mode, an outer secondary air door control lever (27) of the light side is arranged on a combustor panel (31), the deflection angle of the outer secondary air door control lever (27) of the light side is adjusted to drive the outer secondary air door baffle (26) of the light side to rotate, the rotation angle of the outer secondary air duct of the light side is changed, and the outer secondary air volume of the light side and the swirl strength of the outer secondary air of the light side are adjusted at the same time.
5. The side wall water-cooled wall adherence protection device based on the concentrated and diluted pulverized coal separation burner as claimed in claim 1, is characterized in that: the louver type coal dust concentrator (6) comprises a cavity formed by connecting a concentrator shell (22) and a middle partition plate (20), and a louver type concentrating blade (23) arranged in the cavity.
6. The side wall water-cooled wall adherence protection device based on the concentrated and diluted pulverized coal separation burner as claimed in claim 1, is characterized in that: the middle area burner (4) is a cyclone burner, the air distribution of the burner consists of primary air, central air, inner secondary air and outer secondary air, the inner secondary air duct (28) and the outer secondary air duct (29) are concentric annular channels, a pulverized coal pipeline (12) of the middle area burner (4) is connected from the right below of a primary air pipe (5), and the air sources of the central air, the inner secondary air and the outer secondary air are taken from an air box (21); a fixed swirler (30) is arranged in an inner secondary air duct (28) of the middle area combustor (4), and the swirl strength of inner secondary air of the middle area combustor (4) is not adjustable; an inner secondary air adjusting rod (32) is arranged on a burner panel (31) of the middle area burner (4), and the inner secondary air quantity can be adjusted through the axial displacement of the inner secondary air adjusting rod (32) along the burner.
7. The side wall water-cooled wall adherence protection device based on the concentrated and diluted pulverized coal separation burner as claimed in claim 6, is characterized in that: the air volume and the rotational flow strength of the external secondary air of the middle area combustor (4) are adjusted through an integral impeller type air door baffle (33) which is arranged on the combustor in a tangential way, and an external secondary air door operating lever (34) is arranged on a combustor panel (31) of the middle area combustor (4); the deflection angle of an outer secondary air door control lever (34) is adjusted to drive the integral impeller type air door baffle (33) to rotate, and the rotation angle is changed, so that the outer secondary air quantity and the outer secondary air swirl strength are adjusted simultaneously.
8. The side wall water-cooled wall adherence protection device based on the concentrated and diluted pulverized coal separation burner as claimed in claim 1, is characterized in that: the wall-attached air nozzle (14) is a circular nozzle, the wall-attached air is direct current air, and the air source of the wall-attached air nozzle is taken from a hot primary air main pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202120006512.4U CN214370153U (en) | 2021-01-04 | 2021-01-04 | Side wall water-cooled wall adherence protection device based on thick and thin pulverized coal separation combustor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202120006512.4U CN214370153U (en) | 2021-01-04 | 2021-01-04 | Side wall water-cooled wall adherence protection device based on thick and thin pulverized coal separation combustor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN214370153U true CN214370153U (en) | 2021-10-08 |
Family
ID=77953838
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202120006512.4U Active CN214370153U (en) | 2021-01-04 | 2021-01-04 | Side wall water-cooled wall adherence protection device based on thick and thin pulverized coal separation combustor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN214370153U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115888963A (en) * | 2022-09-19 | 2023-04-04 | 山东大学 | Coal pulverizer entry primary air volume governing system |
| WO2023160032A1 (en) * | 2022-02-25 | 2023-08-31 | 西安热工研究院有限公司 | Direct-current burner primary air chamber and method for preventing boiler slagging and high-temperature corrosion |
-
2021
- 2021-01-04 CN CN202120006512.4U patent/CN214370153U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2023160032A1 (en) * | 2022-02-25 | 2023-08-31 | 西安热工研究院有限公司 | Direct-current burner primary air chamber and method for preventing boiler slagging and high-temperature corrosion |
| CN115888963A (en) * | 2022-09-19 | 2023-04-04 | 山东大学 | Coal pulverizer entry primary air volume governing system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101725969B (en) | Low-NOx pulverized coal burner | |
| CN112709985A (en) | Side wall water-cooled wall adherence protection device based on horizontal shade separation | |
| CN209978093U (en) | System for controlling temperature of boiler burner of coal-fired power plant to avoid burning loss | |
| CN112032711A (en) | Stable combustion burner based on temperature control of precombustion chamber and operation method thereof | |
| CN214370153U (en) | Side wall water-cooled wall adherence protection device based on thick and thin pulverized coal separation combustor | |
| CN107477572A (en) | Using the center feeding rotational flow coal dust burner of separation Secondary Air bilayer jet | |
| CN201606876U (en) | Low-NOx coal burner | |
| CN101629718A (en) | Low-nitrogen-oxide multi-tube axial eddy pulverized-coal burner | |
| CN112902154A (en) | Over-fire air system with controllable steam temperature deviation and CO concentration at two sides of opposed firing boiler | |
| CN201215311Y (en) | Adjustable bias jet DC coal burner | |
| CN107504480A (en) | A kind of industrial coal powder boiler with center feeding rotational flow coal dust burner | |
| CN214840783U (en) | Concentrated type double-air-regulation rotational flow low-nitrogen combustor provided with central air | |
| CN104121579A (en) | Boiler provided with dual-register pulverized coal burner on top | |
| CN215174993U (en) | Air quantity and rotational flow double-regulation burner | |
| CN202024323U (en) | Powder fuel combustor | |
| CN100585276C (en) | Side direction multilevel open type igniting center powder feeding vortex combustor of small oil mass gasification combustion | |
| CN204176635U (en) | The boiler of two tune wind coal burner overhead | |
| CN211694854U (en) | W flame boiler low-nitrogen combustion and slagging-proof flue gas recirculation system | |
| CN202024324U (en) | Powder fuel combustor | |
| CN203731402U (en) | A dual-air-regulating pulverized coal burner for an industrial pulverized coal boiler | |
| CN107355807A (en) | W type flame boiler air distribution mode optimization methods | |
| CN105910107A (en) | Concentric axial flow low nitrogen oxide sleeve combustor | |
| CN111121007A (en) | W flame boiler low-nitrogen combustion and slagging-proof flue gas recirculation system | |
| CN214664372U (en) | Over-fire air system for controlling steam temperature deviation and CO concentration of opposed firing boiler | |
| CN212430847U (en) | Coal fired power plant direct current burner suitable for coal-mixed combustion |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |