CN204693432U

CN204693432U - A kind of low nitrogen type of furnace of single body of heater bilateral-firing

Info

Publication number: CN204693432U
Application number: CN201520353463.6U
Authority: CN
Inventors: 李延新
Original assignee: Individual
Current assignee: Individual
Priority date: 2015-05-27
Filing date: 2015-05-27
Publication date: 2015-10-07
Anticipated expiration: 2025-05-27

Abstract

The utility model relates to a kind of low nitrogen type of furnace of single body of heater bilateral-firing, comprises body of heater, burner and stove tail, and described burner and stove tail are positioned at the two ends of the body of heater of the low nitrogen type of furnace, and burner and stove tail one end of body of heater are respectively provided with a burner.Further, the flame that ejects of the flame that ejects of described furnace head burner and described stove tail burner is independent of one another.The flame that described furnace head burner ejects is the slender type flame along the burning of burner hearth axis; The flame that described stove tail burner ejects is the rotary outer shroud flame pressing close to furnace wall.The equipment of the single body of heater bilateral-firing that the utility model proposes, can Simplified flowsheet, improve production capacity, reduce equipment manufacturing cost and production cost, also can reduce produce in combustion process nitrogen discharged simultaneously, thus realize the best object that low-cost energy-saving reduces discharging.

Description

A kind of low nitrogen type of furnace of single body of heater bilateral-firing

Technical field

The utility model relates to field of combustion equipment, particularly, relate to a kind of can single body of heater bilateral-firing burning kiln, boiler etc. optimize the low nitrogen type of furnace.

Background technology

Be conventionally used to the kiln that rubbish, dangerous solid waste, mud etc. burn, secondary combustion chamber must be equipped with carry out incineration tail gas to realize qualified discharge, therefore huge, the disposable input of equipment of system and production cost all very high.

For the kiln (see Fig. 1) that rubbish, dangerous solid waste, mud etc. burn, tail gas can take away a large amount of unburnt granular material and a large amount of toxic and harmful when material loading end is discharged, tail gas must be sent into after secondary combustion chamber burns in order to the qualified discharge of tail gas and discharge again, therefore huge, the equipment manufacturing cost of system and operating cost all higher.Meanwhile, because fuel and air are all provided by a burner, the vigorous combustion under high-temperature oxygen-enriched environment generates a large amount of NO, causes the nitrogen discharged also higher of tail gas.

The technical scheme of the single body of heater bilateral-firing that the utility model proposes, can Simplified flowsheet, improve production capacity, reduce equipment manufacturing cost and production cost, also can reduce produce in combustion process nitrogen discharged simultaneously, thus realize the best object that low-cost energy-saving reduces discharging.

Utility model content

The utility model provides a kind of low nitrogen type of furnace of single body of heater bilateral-firing, technical problem to be solved is the problem that the tail gas existed in traditional combustion process can take away a large amount of unburnt granular material and a large amount of toxic and harmful when material loading end is discharged, also significantly can reduce discharging nitric oxide simultaneously.

The technical scheme that the utility model solves the problems of the technologies described above is as follows:

The low nitrogen type of furnace of a kind of single body of heater bilateral-firing of the present utility model, comprise the body of heater of the low nitrogen type of furnace, burner and stove tail, described burner (7) and stove tail (8) are positioned at the two ends of the furnace body (1) of the low nitrogen type of furnace, the center of described stove burner end face is provided with furnace head burner, and the center of the end face of described stove tail is provided with stove tail burner.

Further, the flame that sprays of the flame of described furnace head burner ejection and described stove tail burner is independent of one another.

Further, the body of heater of the described low nitrogen type of furnace is hollow cylindrical structure, and the flame of described furnace head burner ejection is the slender type flame along the burning of burner hearth axis; The flame of described stove tail burner ejection is the rotary outer shroud flame pressing close to furnace wall.

Further, be provided with exhanst gas outlet near the body of heater upper end of burner, be provided with discharging opening near the body of heater lower end of burner, the bottom of described stove tail is provided with charging aperture, and described exhanst gas outlet and charging aperture are positioned at the head and the tail two ends of body of heater.

The beneficial effects of the utility model are: the technical scheme of the single body of heater bilateral-firing that the utility model proposes, can Simplified flowsheet, improve production capacity, reduce equipment manufacturing cost and production cost, also can reduce produce in combustion process nitrogen discharged simultaneously, thus realize the best object of low-cost energy-saving reduction of discharging.

Accompanying drawing explanation

Fig. 1 is traditional kiln schematic diagram;

Fig. 2 is the utility model bilateral-firing low nitrogen kiln schematic diagram;

Detailed description of the invention

Be described principle of the present utility model and feature below in conjunction with accompanying drawing, example, only for explaining the utility model, is not intended to limit scope of the present utility model.

Embodiment 1

As shown in Figure 2, a kind of low nitrogen kiln of single body of heater bilateral-firing, comprise body of heater 1, burner 7 and stove tail 8, described burner 7 and stove tail 8 are positioned at the two ends of the furnace body 1 of the low nitrogen type of furnace, the end face center of described burner 7 is provided with furnace head burner 2, and the end face center of described stove tail 8 is provided with the stove tail burner 9 be oppositely arranged with burner 2.The flame that the flame of described furnace head burner 2 ejection and described stove tail burner 9 spray is independent of one another.The body of heater 1 of the described low nitrogen type of furnace is the flame that the wherein said furnace head burner 2 of hollow cylindrical structure sprays is the slender type flame burnt along burner hearth axis; The flame of described stove tail burner 9 ejection is the rotary outer shroud flame pressing close to furnace wall.Be provided with exhanst gas outlet 6 near the body of heater upper end of described burner 7, be provided with discharging opening 5 near the body of heater lower end of described burner 7, the bottom of described stove tail 8 is provided with charging aperture 4, and described exhanst gas outlet 6 and charging aperture 4 are positioned at the head and the tail two ends of body of heater.

When kiln work described in the utility model, the elongated flame of oxygen debt burning sprays in kiln by furnace head burner 2, provide the high temperature incineration district in kiln, because internal flame is in the fired state of severe depletion of oxygen, thus there is strong NO reduction atmosphere, thus drastically reduce the area the generation of fuel NO.

The low temperature outer shroud flame of high power coefficient of excess air is sprayed into kiln by the stove tail burner 9 being meanwhile positioned at kiln afterbody, the temperature reducing internal flame when flame envelope converges mutually with internal flame supplements again the oxygen needed for internal flame burning, and define the outer shroud flame of adherent spiral backflow, thus make to be filled with flame in kiln, low-temperature burning state can reduce the generation of oxynitrides effectively in addition.

Material enters stove from the charging aperture being positioned at kiln tail, slowly enters high temperature incineration district after the dehydration of drying district, and finally discharge from the discharging opening being positioned at kiln hood, the material of powdery is then discharged from exhanst gas outlet simultaneously.Because charging aperture and gas outlet are positioned at the two ends of kiln, no matter be therefore that the burning that large granular materials or powder material all have to pass through whole furnace superintendent could discharge body of heater, thus all combustibles and the whole after-flame of gas can be reached, various toxic and harmful is through the innoxious object of high temperature incineration.Eliminate the secondary combustion chamber that conventional incinerators must be equipped with, greatly simplified burning process, decrease and disposablely purchase machine expense and operating cost.

In addition, because both sides spray into internal flame in stove and flame envelope reverse movement each other, coordinated by the difference of segmentation flame and two ends flame intensity and coefficient of excess air, can at a large amount of nitrogen oxides reduction of internal flame combustion phases of long distance, reduce flame temperature at the combustion phases of adherent spiral flame envelope, thus reduce the generation of nitrogen oxide.

Finally it should be noted that the utility model also extends to other combustion field, the burner hearth of the smoke evacuation of every side, bidirectional arrangements burner, and the combustion system of flame and outer shroud flame move toward one another, all should within protection of the present utility model.

The foregoing is only preferred embodiment of the present utility model, not in order to limit the utility model, all within spirit of the present utility model and principle, any amendment done, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.

Claims

1. the low nitrogen type of furnace of a single body of heater bilateral-firing, comprise the body of heater (1) of the low nitrogen type of furnace, burner (7) and stove tail (8) two parts, described burner (7) and stove tail (8) are positioned at the two ends of the furnace body (1) of the low nitrogen type of furnace, it is characterized in that, the center of described burner (7) is provided with furnace head burner (2), and the center of described stove tail (8) is provided with stove tail burner (9).

2. the low nitrogen type of furnace of single body of heater bilateral-firing according to claim 1, is characterized in that, the flame that described furnace head burner (2) sprays and the flame that described stove tail burner (9) sprays independent of one another.

3. the low nitrogen type of furnace of single body of heater bilateral-firing according to claim 2, it is characterized in that, the furnace body (1) of the described low nitrogen type of furnace is hollow cylindrical structure, and the flame that described furnace head burner (2) sprays is the slender type flame along the burning of burner hearth axis; The flame that described stove tail burner (9) sprays is the rotary outer shroud flame pressing close to furnace wall.

4. according to the low nitrogen type of furnace of described single body of heater bilateral-firing arbitrary in claim 1-3, it is characterized in that, exhanst gas outlet (6) is provided with near the furnace body upper end of the low nitrogen type of furnace of described burner (7), be provided with discharging opening (5) near body of heater (1) lower end of described burner (7), the furnace wall lower portion of furnace body near described stove tail (8) is provided with charging aperture (4).