CN201793693U - Pulse combustion heat accumulation type metallic magnesium reducing furnace - Google Patents
Pulse combustion heat accumulation type metallic magnesium reducing furnace Download PDFInfo
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- CN201793693U CN201793693U CN201020545823XU CN201020545823U CN201793693U CN 201793693 U CN201793693 U CN 201793693U CN 201020545823X U CN201020545823X U CN 201020545823XU CN 201020545823 U CN201020545823 U CN 201020545823U CN 201793693 U CN201793693 U CN 201793693U
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Abstract
The utility model relates to a pulse combustion heat accumulation type metallic magnesium reducing furnace, which belongs to the technical field of nonferrous metal processing. The pulse combustion heat accumulation type metallic magnesium reducing furnace comprises a furnace top, a furnace body, a reducing tank, heat accumulation type burner nozzles, a smoke gas pipeline, an air pipeline and a coal gas pipeline, wherein the traditional continuous combustion control system is replaced through a pulse combustion heat accumulation type system, and three to four layers of heat accumulation type burner nozzles are uniformly arranged on the single side furnace wall in the furnace length direction. The utility model has the advantages that the pulse combustion control technology is used for improving the load regulation ratio of the burner nozzles, stabilizing the fuel gas spraying speed, improving the heat transfer efficiency, and realizing the precision control on the combustion atmosphere. Burners are arranged in the length direction of a hearth, the burning gas forms U-shaped flame in the width direction of the furnace, the convection heat exchange in the hearth can be increased, the uniformity of the temperature field can be enhanced, the consumption of the fuel can be reduced, and in addition, the service life of the reducing tank can be prolonged. The heat accumulation type combustion technology and the smoke gas coiling and suction effect generated by the siphon principle are utilized, the waste heat of the smoke gas is sufficiently utilized, the energy source can be saved to the furthest degree, and in addition, the pollutant discharge can be reduced.
Description
Technical field
The utility model belongs to technical field of nonferrous metal processing, particularly relates to a kind of pulse-combustion heat accumulating type metal magnesium reduction furnace, and the heat accumulating type high temperature reduction method of apply pulse combustion control technology is refined perpendicular jar of reduction furnace of magnesium.
Background technology
Domestic magnesium reducing furnace generally all adopts the form of continuous burning control, the adjusting of burner ratio is generally about 1: 4 under this pattern, when reduction furnace was in the intensification operating mode, burner was operated at full capacity, and gas flow rate, flame profile, thermo-efficiency all can reach optimum design geometry; But when reduction furnace is in the insulation operating mode, the burner flow is near its minimum flow rate, the thermal load minimum, gas flow rate reduces greatly, the length of flame does not reach requirement, cause reduction furnace middle part furnace temperature to be starkly lower than the two ends furnace temperature, do not reach the temperature uniformity requirement of technology, so present most of magnesium reducing furnace control poor effect.
Perpendicular jar of existing metal magnesium reduction furnace burner is along both sides headwall positioned opposite, flame reaches the high point of temperature and heat flux in distance burner spout a distance, peak flame temperature point temperature is too high, cause the furnace temperature inequality, and the feasible reduction jar excessive temperature differentials on the furnace superintendent direction that is arranged in stove centre and two ends, because temperature fluctuation is big, cause reduction jar easily loss; Along with the increase of reduction furnace installation reduction jar quantity, body of heater is longer, and continuous burning control can't realize the homogeneity of temperature field in furnace.
And horizontal jar of magnesium metal reduction ingle flame of tradition and flue gas climb over firebreak and enter burner hearth, from top to bottom through reduction jar, discharge burner hearth by inhaling fire hole very soon, funnel temperature up to 1000 ℃ about; Jar flat the crouching of reducing is fixed in the burner hearth, and the operation that the structure of this reduction jar and cloth jar mode extremely are not easy to input and output material is unfavorable for adopting mechanization means, has had a strong impact on production efficiency.
Summary of the invention
The purpose of this utility model is to provide a kind of pulse-combustion heat accumulating type metal magnesium reduction furnace, solved the defective of existing perpendicular jar metal magnesium reduction furnace, the apply pulse combustion control technology, improve the load regulation rate of burner, stablize the combustion gas spouting velocity, improve heat transfer efficiency, realize the accurate control of combustion atmosphere; Burner arranges that along the burner hearth length direction combustion gases form U type flame along the stove cross direction, increases the interior convective heat exchange of burner hearth, strengthens the homogeneity in temperature field, reduces the consumption of fuel, and improves the work-ing life of reduction jar; The flue gas of using regenerative combustion technology and utilizing siphon principle to produce entrainments effect, makes full use of fume afterheat, the discharging of the pollutent of save energy, and minimizing to greatest extent.
The utility model comprises furnace roof 1, body of heater 2, reduction jar 3, heat-accumulating burner 4, flue gas pipeline 5, airline 6, gaspipe line 7, pulse-combustion heat accumulating type Controlling System 8, substitute traditional continuous burning Controlling System with " pulse-combustion heat accumulating type Controlling System ", pulse-combustion heat accumulating type Controlling System 8 connects flue gas pipeline 5, airline 6 and gaspipe line 7, control the flame combustion state of heat-accumulating burner 4 by pilot piping gas flow and flow velocity, the assurance temperature field in furnace is uniform and stable: along evenly arranging heat-accumulating burner 4 on the one-sided furnace wall on the furnace superintendent direction, arrange layer 2-4 according to the furnace wall requirement for height, adjacent two row burners are one group, in succession as burner port and smoke outlet, burn and accumulation of heat, gas forms U type flame along the stove cross direction in burner hearth, strengthen the gas flow heat exchange; The airline 6 of burner and gaspipe line 7 meet pulse-combustion heat accumulating type Controlling System 8 I of controlling respectively on the same group, the upper left interface of II reversing valve, flue gas pipeline 5 meets pulse-combustion heat accumulating type Controlling System 8 I of controlling, the upper right interface of two reversing valves of II, the lower-left interface of the pulse-combustion heat accumulating type Controlling System 8 I reversing valves of controlling connects the gas entry of A group heat-accumulating burner 4, the bottom right interface connects the gas entry of B group heat-accumulating burner 4, the lower-left interface of the pulse-combustion heat accumulating type Controlling System 8 II reversing valves of controlling connects the gas inlet of A group heat-accumulating burner 4, and the bottom right interface connects the gas inlet of B group heat-accumulating burner 4; Pulse-combustion heat accumulating type Controlling System 8 is carried out automatic cycle commutation control and burst length control according to the signal of furnace temperature of being arranged on the body of heater 2 and furnace pressure proofing unit feedback by the PLC pre-set programs; Furnace roof 1 is formed by high-temp resistance prefabricated cover plate splice, and prefabricated cover plate substitutes traditional metal anchoring hook as weighting material with resistant to elevated temperatures ceramic anchored brick, carries out perforate according to reduction jar diameter and spacing on the prefabricated cover plate, and the width between centers of reduction jar is 650-850mm.
Described pulse-combustion heat accumulating type system 8 comprises furnace temperature and furnace pressure proofing unit, PLC central control system, executive device.Furnace temperature and furnace pressure proofing unit are arranged on the body of heater 2, connect the PLC central control system by compensating lead wire; Executive device is arranged in the gas line interface, is connected on the PLC central control system by cable; The PLC central control system is implemented to control to gas line by default PLC program according to the signal of body of heater furnace temperature and furnace pressure proofing unit feedback, carries out automatic cycle commutation control and burst length control.Pulse-combustion heat accumulating type system 8 adopts the mode of intermittent burning, use pulse modulation technology, realize the temperature control of reduction furnace by the dutycycle (being break make ratio: refer in a string ideal pulse sequence the ratio in the time length of positive pulse and total cycle of pulse) of regulating combustion time.
Described reduction jar 3 takes vertical mode to arrange in burner hearth, two rows are one group, the combustion channels that leaves 800-1250mm according to the flow velocity and the flow of combustion gas between every group of reduction jar, spray the zone of formed U type flame as burner, the mode of slagging tap is to slag tap in charging top, top, or slags tap in charging bottom, top.
Described heat-accumulating burner 4 is two heat-accumulating burners of space gas or air single regenerative burner.
Principle of work of the present utility model is:
1, " the pulse-combustion heat accumulating type system " that combine The pulse burning control technique and high-efficiency heat-accumulating technology is applied to metal magnesium reduction furnace, heat-accumulating burner all is under intensification operating mode and insulation operating mode operates at full capacity, guarantee gas flow rate, flame profile, thermo-efficiency reaches optimum design geometry, realize the unanimity of the length of flame under two kinds of operating modes, avoid reduction furnace middle part temperature on the low side, simultaneously, owing to can guarantee the combustion gas high flow rate, make heat-accumulating burner under the siphon principle effect, high-temperature flue gas in the burner hearth can be entrainmented burner into gas inlet and and air mixed, thereby improve the temperature that air is gone into the stokehold, reduce the burner hearth oxygen level, the final high-temperature and low-oxygen combustion of realizing increases fuel combustion efficiency.
2, adopt regenerative combustion technology, along evenly arranging two accumulation of heats of space gas or air single regenerative burner on the one-sided furnace wall on the furnace superintendent direction, adjacent two row burners are one group, in succession as burner and smoke outlet, the staggered burning and accumulation of heat, gas forms U type flame in burner hearth, strengthen the gas flow heat exchange, compare in perpendicular jar of existing reduction furnace, flame strengthens gas flow and heat exchange along the furnace superintendent direction no longer along the direct injection of knee wall passageway, promotes the stability of temperature field in furnace, improve a temperature field in the reduction jar jar, the thermal stresses that reduces to reduce jar and then reduced reduction jar distortion; Simultaneously, because burner is in staggered burning of stove cross direction and accumulation of heat, flame is the U type around reduction jar, and the combustion zone temperature is even, has prolonged reduction jar work-ing life.Thereby when having avoided in the past along the unified commutation of furnace superintendent, direct projection flame is poor in burner hearth middle part flame rigidity, and burner hearth middle part temperature is low, and near the burner spout time, gas intensity height causes temperature of combustion too high, causes the reduction jar premature oxidation scaling loss in the high temperature position.
Positively effect of the present utility model:
(1) load regulation rate of raising burner, strengthen the homogeneity of temperature field in furnace: the utility model is changed the insulation operating mode decline low-flow speed traditional form of continuous burning in the past, creatively adopt intermittent burning, reduce the mode of service life under the insulation operating mode, when being sprayed, burner all is in the state of operating at full capacity, thereby the length of flame of injection is consistent, guarantee that burner is operated in optimal combustion state: the combustion gas spouting velocity is fast, make and form negative pressure on every side, under the siphon principle effect, the high-temperature flue gas in the burner hearth entrainmented burner into gas inlet and and air fully mix, make fuel gas temperature and inner flue gas of the stove temperature approaching; Simultaneously, the U type flame of being realized by the burner unique arrangement has increased the convective heat exchange in the burner hearth, has improved the homogeneity of temperature field in furnace, thereby has improved the quality of finished product magnesium; Reduce high-temperature fuel gas the direct heat of heated object impacted, prolonged the reduction tank body work-ing life 1-2 doubly.
(2) can realize the accurate control of combustion atmosphere: at present traditional continuous burning control is stayed the surplus capacity of combustion air very big, does not reach the requirement of best energy-conservation and control excess oxygen content (or excess air coefficient).Adopt the pulse-combustion control mode, coal gas and the disposable desired value of adjusting to of air pressure after system puts into operation, only can be needed to keep these two pressure-stabilisations to get final product.Pressure measured and control want unit rate of flow much simple, can take full automatic control, also can take to control manually according to the practical situation of system.
(3) pulse combustion control system is simple and reliable, cheap: compare with continuous burning control, the instrument that participates in control in the pulse combustion control system significantly reduces, temperature sensor, global function partition type two-bit triplet reversing valve and robot control system(RCS) are only arranged, omitted a large amount of expensive Flow-rate adjustment (motor-driven control valve) mechanism.And because pulse-combustion control only needs two formula on-off control, topworks also becomes global function partition type two-bit triplet reversing valve (two position and four-way reversing valves) by original motor-driven control valve, has increased the reliability of system, has reduced the entire system cost.
(4) thermo-efficiency height, energy-saving and cost-reducing: the utility model adopts disperse direct combustion technology and special-purpose heat-accumulation combustor, and air and coal gas through the heat storage preheating uprise temperature by normal temperature before the burning, and it is more complete to burn, and can guarantee that fire box temperature is even; Adopt regenerative combustion technology fume afterheat can be used almost near the ultimate degree, reclaim flue gas latent heat to greatest extent, funnel temperature is reduced to below 150 ℃ by original 1000 ℃, and the waste heat recovery rate can reach 80%, be 1.3 times of conventional heat reclamation device, energy-saving and cost-reducing very obvious.
(5) environment protecting is good: high-temperature flue gas entrainments effect and has not only saved the energy in regenerative combustion technology that the utility model uses and the burner hearth of realizing under the siphon principle effect, has reduced smoke discharge amount, and has greatly reduced SO in the flue gas
2, content of harmful gas such as NOx, guarantee that the flue gas that enters in the atmosphere can reach discharging standards, prevents contaminate environment.
Description of drawings
Fig. 1 is a structural representation of the present utility model.Wherein, furnace roof 1, body of heater 2, reduction jar 3, heat-accumulating burner 4
Fig. 2 is a fundamental diagram of the present utility model.Wherein, flue gas pipeline 5, airline 6, gaspipe line 7, pulse combustion control system 8
Embodiment
Referring to Fig. 1-Fig. 2, the utility model comprises furnace roof 1, body of heater 2, reduction jar 3, heat-accumulating burner 4, flue gas pipeline 5, airline 6, gaspipe line 7, pulse-combustion heat accumulating type Controlling System 8.Along evenly arranging heat-accumulating burner 4 on the one-sided furnace wall on the furnace superintendent direction, adjacent two row burners are one group, be positioned on the furnace wall of flame passageway correspondence position, arrange layer 2-4 according to the furnace wall requirement for height, all establish even number for every layer, to guarantee that per two burners control flame is the U type, in succession as burner and smoke outlet; The airline 6 of burner and gaspipe line 7 meet pulse-combustion heat accumulating type Controlling System 8 I of controlling respectively on the same group, the upper left interface of two reversing valves of II, flue gas pipeline 5 meets pulse-combustion heat accumulating type Controlling System 8 I of controlling respectively, the upper right interface of two reversing valves of II, the lower-left interface of the pulse-combustion heat accumulating type Controlling System 8 I reversing valves of controlling connects the gas entry of A group heat-accumulating burner 4, the bottom right interface connects the gas entry of B group heat-accumulating burner 4, the lower-left interface of the pulse-combustion heat accumulating type Controlling System 8 II reversing valves of controlling connects the gas inlet of A group heat-accumulating burner 4, the bottom right interface connects the gas inlet of B group heat-accumulating burner 4, pulse-combustion heat accumulating type Controlling System 8 is carried out automatic cycle commutation control and burst length control according to the signal of furnace temperature of being arranged on the body of heater 2 and furnace pressure proofing unit feedback by the PLC pre-set programs; Reduction jar 3 in the body of heater 2 vertically is hung on the furnace binding (not shown), two rows are one group, every row's quantity examination body of heater width is suitably adjusted, the combustion channels that leaves 800-1250mm according to the flow velocity and the flow of combustion gas between every group of reduction jar, the zone of spraying formed U type flame as burner.
The utility model principle of work is as shown in Figure 2: the space gas supply system comprises flue gas pipeline 5, airline 6, gaspipe line 7 and pulse-combustion heat accumulating type Controlling System 8, empty, coal gas is respectively put an autonomous channel, corresponding gas blower is set, the space gas interface that connects heat-accumulating burner 4 correspondences by pulse combustion control system 8 backs, reduction furnace adopts periodic breaks incendiary mode, when reduction furnace is in the intensification operating mode, burner combustion time lengthening, reduce break time, when reduction furnace is in the insulation operating mode, the burner combustion time reduces, break time, lengthening guaranteed that holding stage is 1/4 of the temperature rise period to the supply of coal gas and air, and burner all is in the state of operating at full capacity when spraying, thereby the length of flame of injection is consistent, and it is uniform and stable that temperature field in furnace keeps.When in one group of burner one when being listed in as burner combustion, another adjacent row then are used for smoke evacuation as smoke outlet.After a commutation cycle, by the switching of pulse-combustion heat accumulating type Controlling System 8, a former row burner that is used as burner combustion becomes smoke outlet and is used for discharging fume, and another row burner that was used for originally discharging fume is then as burner combustion.In the process of alternate combustion and smoke evacuation, the heat recuperation that the regenerator at burner rear portion is entrained with high-temperature flue gas also discharges to fuel and combustion air, in the process of fuel combustion, brings back to this part heat in the stove again; Simultaneously, heat-accumulating burner 4 is used siphon technology, the high-temperature flue gas in the burner hearth can be entrainmented burner into gas inlet and and air mixed, thereby improved the temperature that air is gone into the stokehold once more, reduce the oxygen level of burner hearth, finally realized high-temperature and low-oxygen combustion, increased fuel combustion efficiency.
Claims (6)
1. a pulse-combustion heat accumulating type metal magnesium reduction furnace comprises furnace roof, body of heater, reduction jar, heat-accumulating burner, flue gas pipeline, airline, gaspipe line; It is characterized in that pulse-combustion heat accumulating type system (8) substitutes the continuous burning Controlling System, pulse-combustion heat accumulating type Controlling System (8) connects flue gas pipeline (5), airline (6) and gaspipe line (7); Along evenly arranging heat-accumulating burner (4) on the one-sided furnace wall on the body of heater length direction, arrange the 3-4 layer according to the furnace wall requirement for height, adjacent two row burners are one group, airline of burner (6) and gaspipe line (7) meet pulse-combustion heat accumulating type Controlling System (8) I of controlling respectively on the same group, the upper left interface of II reversing valve, flue gas pipeline (5) meets pulse-combustion heat accumulating type Controlling System (8) I of controlling, the upper right interface of two reversing valves of II, the lower-left interface of pulse-combustion heat accumulating type Controlling System (8) the I reversing valve of controlling connects the gas entry of A group heat-accumulating burner (4), the bottom right interface connects the gas entry of B group heat-accumulating burner (4), the lower-left interface of pulse-combustion heat accumulating type Controlling System (8) the II reversing valve of controlling connects the gas inlet of A group heat-accumulating burner (4), and the bottom right interface connects the gas inlet of B group heat-accumulating burner (4).
2. reduction furnace as claimed in claim 1 is characterized in that, described reduction jar (3) takes vertical mode to arrange in burner hearth, and two rows are one group.
3. reduction furnace as claimed in claim 1 is characterized in that, heat-accumulating burner (4) is two heat-accumulating burners of space gas or air single regenerative burner.
4. reduction furnace as claimed in claim 1 is characterized in that, described pulse-combustion heat accumulating type system (8) comprises furnace temperature and furnace pressure proofing unit, PLC central control system, executive device, PLC central control system; Furnace temperature and furnace pressure proofing unit are arranged on the body of heater (2), connect the PLC central control system by compensating lead wire, and executive device is arranged in the gas line interface, is connected on the PLC central control system by cable.
5. reduction furnace as claimed in claim 1 is characterized in that, furnace roof (1) is formed by high-temp resistance prefabricated cover plate splice.
6. reduction furnace as claimed in claim 5, it is characterized in that, prefabricated cover plate substitutes traditional metal anchoring hook as weighting material with resistant to elevated temperatures ceramic anchored brick, carries out perforate according to reduction jar diameter and between centers on the prefabricated cover plate, and the width between centers of reduction jar is 650-850mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201020545823XU CN201793693U (en) | 2010-09-28 | 2010-09-28 | Pulse combustion heat accumulation type metallic magnesium reducing furnace |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201020545823XU CN201793693U (en) | 2010-09-28 | 2010-09-28 | Pulse combustion heat accumulation type metallic magnesium reducing furnace |
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| CN201793693U true CN201793693U (en) | 2011-04-13 |
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| CN201020545823XU Expired - Fee Related CN201793693U (en) | 2010-09-28 | 2010-09-28 | Pulse combustion heat accumulation type metallic magnesium reducing furnace |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110068229A (en) * | 2019-04-11 | 2019-07-30 | 赛能杰高新技术股份有限公司 | A method of improving recuperative heater efficiency of combustion |
| CN113864795A (en) * | 2021-09-22 | 2021-12-31 | 龙游超晟科技有限公司 | Organic waste gas treatment system capable of treating explosion limit |
-
2010
- 2010-09-28 CN CN201020545823XU patent/CN201793693U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110068229A (en) * | 2019-04-11 | 2019-07-30 | 赛能杰高新技术股份有限公司 | A method of improving recuperative heater efficiency of combustion |
| CN113864795A (en) * | 2021-09-22 | 2021-12-31 | 龙游超晟科技有限公司 | Organic waste gas treatment system capable of treating explosion limit |
| CN113864795B (en) * | 2021-09-22 | 2024-04-02 | 浙江超晟科技有限公司 | Organic waste gas treatment system for treating explosion limit |
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Legal Events
| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110413 Termination date: 20120928 |