CN203010621U - Pulverized coal burner used for large upright reduction furnace - Google Patents

Pulverized coal burner used for large upright reduction furnace Download PDF

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Publication number
CN203010621U
CN203010621U CN 201220677361 CN201220677361U CN203010621U CN 203010621 U CN203010621 U CN 203010621U CN 201220677361 CN201220677361 CN 201220677361 CN 201220677361 U CN201220677361 U CN 201220677361U CN 203010621 U CN203010621 U CN 203010621U
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CN
China
Prior art keywords
coal
pulverized coal
burner
reduction furnace
coal dust
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.)
Expired - Fee Related
Application number
CN 201220677361
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Chinese (zh)
Inventor
张少军
杨沛胥
张伟东
雷振华
周寿山
闵建权
王超
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Kaitai Magnesium Co ltd
Original Assignee
Kaitai Magnesium Co ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Kaitai Magnesium Co ltd filed Critical Kaitai Magnesium Co ltd
Priority to CN 201220677361 priority Critical patent/CN203010621U/en
Application granted granted Critical
Publication of CN203010621U publication Critical patent/CN203010621U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model relates to a pulverized coal burner, in particular to a pulverized coal burner used for a large upright reduction furnace which adopts a plurality of channels to deliver pulverized coal and preheats igniting pulverized coal with high-temperature air as secondary air. The pulverized coal burner used for the large upright reduction furnace comprises a pulverized coal distributor, a pulverized coal channel, a turning connection pipe bundle, a burner shell and a coal-injection bundle are sequentially matched behind the pulverized coal distributor, a coal gas inlet is formed in the burner shell, and a coal gas delivery pipeline and a high-temperature air pipeline are respectively arranged on the inner side and the outer side of the pulverized coal channel (2). The pulverized coal burner used for the large upright reduction furnace is unique in structure, high-temperature air is used as secondary air, not only is the pulverized coal burner favorable for fire ignition and stable burning, but also the flame shape can be adjusted to be regular and reasonable so that the temperature field of the furnace is evenly distributed, and not only can burning efficiency of the pulverized coal be promoted, but also emission of NOx is reduced.

Description

Large-scale vertical reduction furnace coal burner
Technical field
The utility model relates to a kind of coal burner, especially relates to a kind of employing multichannel pulverized coal conveying, and high temperature air is as the large-scale vertical reduction furnace coal burner of the pre-thermal ignition coal dust of Secondary Air.
Background technology
At present, China is to the metallurgy stove, especially the uniformity requirement of the burner hearth internal temperature field of magnesium metal smelting industry large-scale vertical reduction furnace used is very high, because the temperature conditions of method for smelting magnesium by hot technique is controlled at 1200 ℃ of left and right, and the reduction tank adopts the external heat inner vacuum, so inhomogeneous temperature field is very large to the damage of high-temperature steel alloy reduction tank, the shared cost proportion of the consumption of reduction tank is also larger.The most enterprises of China use thermal reduction legal system magnesium technique, and former magnesium output is the first in the world, but most metals magnesium-smelting plant man is just simple based on method for smelting magnesium by hot technological process and equipment, the small investment of founding the factory, technical difficulty is little, and for the uniformity in reduction furnace temperature field, the profound problems such as the consumption that reduces fuel and Decrease production cost is lacked thinking.Owing to reducing the quantity of tank and the difference of arranging at reduction furnace burner hearth internal memory, almost do not have for the designed burner of reduction furnace for smelting metal magnesium specially, the inhomogeneities of fire box temperature field has caused the average magnesium producing rate of reduction tank can not maintain higher level always, and the damage ratio to steel alloy reduction tank is more serious, utilization rate to fuel is lower, greatly increase production cost, seriously hindered making constant progress of China's method for smelting magnesium by hot technology.
Summary of the invention
The purpose of this utility model is to overcome the deficiencies in the prior art, provide a kind of structure unique, adopt high temperature air as Secondary Air, steady combustion both had been conducive to catch fire, can regulate again flame profile rule rationally makes the fire box temperature field evenly distribute, can not only improve the efficiency of combustion of coal dust, and reduce the large-scale vertical reduction furnace coal burner of the discharging of NOx.
The utility model is realized in the following way:
Large-scale vertical reduction furnace coal burner, it is characterized in that: it is combined with successively the coal dust passage after comprising a pulverized coal distributor, pulverized coal distributor, turns to the tube connector group, burner housing and coal injection pipe group, be provided with gas entry on burner housing, be respectively equipped with gas pipeline and high temperature air conveyance conduit in inboard and the outside of coal dust passage;
Be combined with a plurality of described coal dust passages after described pulverized coal distributor, at the vertical direction of described each coal dust passage, manual pulverized coal valve be housed all;
Described gas pipeline is wrapped up by a plurality of coal dust passages, and a plurality of coal dust passages are arranged outside gas pipeline ringwise;
Described high temperature air conveyance conduit is in the outside of the annular space of a plurality of coal dust passages formation, is surrounded by two different shells of diameter to form.
The utility model has following effect:
1) structure is unique: pulverized coal distributor is installed at the pipeline section position at pulverized coal conveying straight up, due to coal dust gravitate and speed perpendicular to ground facing up, the coal dust amount that can guarantee to enter each conveyance conduit is identical, has solved the problem of layering in the coal dust course of conveying.Coal dust is carried through being divided into a plurality of coal dust passages after pulverized coal distributor, and a plurality of coal dust passages are equipped with at vertical direction the coal dust amount that a manual pulverized coal valve can be regulated the flow of a wind and flow velocity and carry separately, can realize effectively and accurately to the adjusting of load.A plurality of coal dust passages enter reduction furnace through circular array after turning to the tube connector group by horizontal direction, coal gas is by being inputed to reduction furnace by the gas passage of a plurality of coal dust passage parcels, the outside of a plurality of coal dust passages is surrounded by the different shell of two-layer diameter and forms a circular passage, high temperature air as Secondary Air thus passage input to reduction furnace in the furnace wall crust place of reduction furnace level.
2) the utility model adopts adjustable multichannel input coal dust and can input simultaneously coal gas, by the high temperature air of temperature up to 1000 ℃ as the pre-thermal ignition coal dust of Secondary Air, steady combustion both had been conducive to catch fire, can regulate again flame profile rule rationally makes the fire box temperature field evenly distribute, the efficiency of combustion of the coal dust that not only improves, and reduced the discharging of NOx.
3) the utility model adopts the dual-purpose configuration of adjustable multichannel coal dust gas, coal gas but also can also realize mixed combustion by combusting coal fines not only can burn, and the high temperature air that adopts can effectively improve the efficiency of combustion of coal dust as the pre-thermal ignition coal dust of Secondary Air, has reduced the discharging of NOx.Uniformity of Temperature Field is being required use this burner can effectively protect steel alloy reduction tank on higher magnesium smelting large-scale vertical reduction furnace; improve the efficiency of combustion of fuel; the magnesium amount that goes out of unit mass raw material obviously increases, and greatly reduces production cost, has improved the competitiveness of enterprise.
Description of drawings
Fig. 1 is structural representation of the present utility model;
Fig. 2 is that the utility model Fig. 1 is along the cutaway view of A-A.
The specific embodiment
A kind of large-scale vertical reduction furnace coal burner, as illustrated in fig. 1 and 2, it comprise one be combined with successively coal dust passage 2 after pulverized coal distributor, pulverized coal distributor 1 are installed in the pipeline section position of pulverized coal conveying straight up, turn to tube connector group 4, burner housing 6 and coal injection pipe group 7, be provided with gas entry 5 on burner housing 6, be respectively equipped with gas pipeline 9 and high temperature air conveyance conduit 8 in inboard and the outside of coal dust passage 2.
Be combined with a plurality of described coal dust passages 2 after described pulverized coal distributor 1, at the vertical direction of described each coal dust passage 2, manual pulverized coal valve 3 be housed all.
Described gas pipeline 9 is by the logical 2 roads parcels of a plurality of coal dusts, and a plurality of coal dust passages 2 are arranged ringwise in gas pipeline 9 outsides.
Described high temperature air conveyance conduit 8 is in the outside of the annular space of a plurality of coal dust passages 2 formation, is surrounded by two different shells of diameter to form.
As shown in Figure 1: wind entrainments coal dust and enters during pulverized coal distributor 1 is assigned to minor diameter coal dust distributing pipe group 2 uniformly in straight up direction, and this mode has effectively overcome traditional level and distributed coal dust because being subjected to gravity to cause the shortcoming of distributing inequality.On each root pipeline of coal dust distributing pipe group, manual pulverized coal valve 3 is housed all, thereby flow that can be by a wind of each coal dust distributing pipe of this valve fine adjustment when change appears in furnace load and flow velocity and the coal dust amount of carrying are effectively controlled the uniformity of fire box temperature field.Coal dust distributing pipe group is by turning to tube connector group 4 to be changed into the coal injection pipe group 7 of horizontal direction by vertical direction, so that the more effective burner hearth that sprays into, turn to simultaneously the tube connector group a plurality of power transportation pipes of coal injection pipe group by annular arrangement, and at gas pipeline 9 of annular intermediate arrangement, realized the function that coal dust gas is dual-purpose.The shell 6 that is provided with one deck housing and burner in the outside of coal injection pipe group has formed an annular space, up to the high temperature airs of 1000 ℃ as Secondary Air thus passage spray into burner hearth, the thermal ignition coal dust burns rapidly coal dust in advance.
Found out by above-mentioned, the rationally distributed compact conformation of the utility model, can guarantee not only to have improved the efficiency of combustion of coal dust under the uniform prerequisite in fire box temperature field, but also reduce the discharging of NOx, be worth promoting the use of in the industry in metal metallurgy smelting field especially method for smelting magnesium by hot.

Claims (4)

1. large-scale vertical reduction furnace coal burner, it is characterized in that: it is combined with successively coal dust passage (2) after comprising a pulverized coal distributor (1), pulverized coal distributor (1), turns to tube connector group (4), burner housing (6) and coal injection pipe group (7), be provided with gas entry (5) on burner housing (6), be respectively equipped with gas pipeline (9) and high temperature air conveyance conduit (8) in inboard and the outside of coal dust passage (2).
2. large-scale vertical reduction furnace coal burner as claimed in claim 1, it is characterized in that: be combined with a plurality of described coal dust passages (2) after described pulverized coal distributor (1), at the vertical direction of described each coal dust passage (2), manual pulverized coal valve (3) be housed all.
3. large-scale vertical reduction furnace coal burner as claimed in claim 1 or 2 is characterized in that: described gas pipeline (9) is by a plurality of coal dusts logical (2) roads parcel, and a plurality of coal dust passages (2) are arranged ringwise in gas pipeline (9) outside.
4. large-scale vertical reduction furnace coal burner as claimed in claim 1 or 2 is characterized in that: described high temperature air conveyance conduit (8) is in the outside of the annular space that a plurality of coal dust passages (2) form, and is surrounded by two different shells of diameter to form.
CN 201220677361 2012-12-11 2012-12-11 Pulverized coal burner used for large upright reduction furnace Expired - Fee Related CN203010621U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201220677361 CN203010621U (en) 2012-12-11 2012-12-11 Pulverized coal burner used for large upright reduction furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201220677361 CN203010621U (en) 2012-12-11 2012-12-11 Pulverized coal burner used for large upright reduction furnace

Publications (1)

Publication Number Publication Date
CN203010621U true CN203010621U (en) 2013-06-19

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CN 201220677361 Expired - Fee Related CN203010621U (en) 2012-12-11 2012-12-11 Pulverized coal burner used for large upright reduction furnace

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102944016A (en) * 2012-12-11 2013-02-27 开泰镁业有限公司 Pulverized coal burner of large-scale vertical reducing furnace

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102944016A (en) * 2012-12-11 2013-02-27 开泰镁业有限公司 Pulverized coal burner of large-scale vertical reducing furnace

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Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20130619

Termination date: 20161211

CF01 Termination of patent right due to non-payment of annual fee