CN202582151U

CN202582151U - Industrial furnace for smelting nonferrous metal

Info

Publication number: CN202582151U
Application number: CN 201220140638
Authority: CN
Inventors: 冯跃平; 冯笑; 冯与佳
Original assignee: MEISHAN ZHONGNENG ALUMINIUM CO Ltd
Current assignee: MEISHAN ZHONGNENG ALUMINIUM CO Ltd
Priority date: 2012-04-06
Filing date: 2012-04-06
Publication date: 2012-12-05
Anticipated expiration: 2022-04-06

Abstract

The utility model discloses an industrial furnace for smelting nonferrous metal. The industrial furnace for smelting the nonferrous metal comprises a furnace chamber (2), a feed barrel, a combustor (5) and a heat exchanger (9), a low temperature air pipeline (8) is connected between the heat exchanger (9) and a draught fan (7), a high temperature air pipeline (6) is connected between the heat exchanger (9) and the combustor (5), a furnace chamber furnace gas outlet (24) is manufactured in the furnace chamber (2), the feed barrel is a part of a heat exchange system, and the furnace chamber furnace gas outlet (24), the heat exchanger (9) and the feed barrel are connected into a whole through furnace gas pipelines. The feed barrel can preheat furnace materials (14) to be smelted by utilizing waste heat of waste furnace gas, the loading process can be carried out in an enclosed space, and therefore a great amount of heat loss inside the furnace is avoided when in loading, temperature of the waste furnace gas discharged into the atmosphere is greatly lowered, the furnace materials (14) to be smelted dissolves rapidly inside the furnace chamber (2), and the purposes of high efficiency, low energy consumption and low aluminum loss are achieved.

Description

Smelt the industrial furnace of non-ferrous metal

Technical field

The utility model relates to a kind of stove that is mainly used in metal smelting, particularly relates to a kind of furnace gas that gives up that utilizes and carries out repeatedly heat exchange, is the industrial furnace of the smelting non-ferrous metal of main furnace charge with waste aluminium alloy.

Background technology

Current, the year utilization of the waste and old non-ferrous metal of China is very huge, and the related industry of waste and old non-ferrous metal is occupied an important seat in national economy, and we can use the aluminium alloy of one of the most frequently used non-ferrous metal to describe as example.

For many years, along with the quick raising of rapid development of national economy, living standards of the people, the demand of China's waste aluminium alloy rapidly increases, and has reached year consumption in level more than 8,000,000 tons at present.The cost of waste aluminium alloy manufactured goods is except receiving non-processing factors such as waste recovery price influence; Also receive deeply processing factors such as energy consumption and aluminium damage in the smelting process great, directly influence; But not processing factors mainly by relation between market supply and demand decision, inhuman ability can about; Therefore, only on processing factors, make great efforts, could fundamentally find the outlet that reduces the waste aluminium alloy cost of goods manufactured.At present, the waste and old non-ferrous metal metallurgy technical merit of China is uneven, differs greatly with world level, sees from energy consumption, and slightly about 1/3rd, the heat utilization efficiency that has has only 1/4th even lower to the heat utilization efficiency of most of smelting furnaces; See that from the aluminium damage aluminium of mechanical aluminium decreases between 7 percent to 10, the aluminium of waste and old door-window section bar decreases between 12 6 percent to 1; This shows, in the face of like this huge melting consumption, energy-conservation with fall damage and become China's aluminium scrap and other smelting non-ferrous metal industries without doubt and be badly in need of the two great strategy property problems that solve at aspect such as reduce cost, improve productivity effect, enhance the competitiveness.

Energy consumption is meant energy that aluminium scrap consumed of every melting.Energy consumption just depends primarily on three aspect factor in the aluminium metallurgy process, and the one, body of heater is to the amount of heat of external radiation and conduction; The 2nd, the discharge capacity of waste gas from smelting furnace what and temperature height; The 3rd, in fill process, the heat in the burner hearth is through intensity size and the time length of charging aperture to external radiation and convection current.Because the building technology comparative maturity of China's smelting furnace; Generally can the gap of outer temperature of body of heater and environment temperature be controlled within 30 ℃; Body of heater is less relatively to the heat of external radiation and conduction, and therefore, cut down the consumption of energy, improve heat utilization efficiency must set about from above two aspect factors and three aspect factor; The discharge capacity of waste gas from smelting furnace is reduced and the temperature reduction, the intensity to external radiation and convection current in the fill process is reduced and the time shortening.

Aluminium decreases and is meant how many primary aluminum waste aluminium alloy per ton can be smelted into.The size that aluminium decreases depends on four aspect factors, the one, above the height of aluminium alloy melting temperature; The 2nd, the length of smelting time; The 3rd, in fusion process, waste aluminium alloy be expose on the aluminium liquid, or disappearance among aluminium liquid; The 4th, whether waste aluminium alloy directly contacts flame.Therefore, reduce aluminium and decrease, promptly avoid aluminium scrap oxidation and scaling loss in smelting furnace as far as possible with regard to reducing smelting temperature, shorten smelting time, prevent or reducing waste aluminium alloy and direct touch opportunity of flame and time.

The version of traditional smelting furnace is shown in figure 15, and this smelting furnace has advantage simple in structure, easy to use, cheap for manufacturing cost, but still has following shortcoming:

1) recovery utilization rate of conventional furnaces waste gas residual heat is low; Only for once; The discharge capacity that make to get into the waste gas from smelting furnace in the atmospheric environment is big high with waste heat supply temperature, adds that in fill process, to pass through charging aperture externally many with radiation and convection type dispersed heat, therefore; Need the more fuel of burning to carry out heat supplement in the conventional furnaces, caused the conventional furnaces energy consumption higher.

2) conventional furnaces does not have the function of preheating waste aluminium alloy; Except that fast through feeding cylinder the time, absorbing the minute quantity heat, receiving the small size intensification; The waste aluminium alloy temperature that gets in the burner hearth is low-down; And burner hearth is with the great amount of heat of having scattered and disappeared with radiation and convection type during charging, and the temperature in the smelting furnace descends serious; Be to realize the Way of Remelting Scrap Aluminium of equal parts, must the temperature of aluminum liquid in the burner hearth be raise, have in addition be raised to temperature far above 800 ℃; And need long-time heating; Owing to do not had preheating, temperature low by molten aluminium scrap, fusing time is also long again, and most of aluminium scraps all are positioned on the liquid aluminum in fusion process; Contact with oxygen easily, cause a large amount of oxidations; Behind each reinforced end, there are many aluminium scraps can't melt at all, have only directly to reheat, unfused like this aluminium scrap just directly contacts with flame, causes serious scaling loss; Just because of oxidation and scaling loss two aspect factors, directly caused the aluminium of conventional furnaces to decrease serious.

The utility model content

The industrial furnace of the smelting non-ferrous metal that the technical problem that the utility model will solve is a kind of efficient, low energy consumption, low aluminium decreases, thermal pollution is little.

For solving the problems of the technologies described above; A kind of industrial furnace of smelting non-ferrous metal of the utility model; Comprise burner hearth, be connected feeding cylinder on the burner hearth charging aperture of burner hearth, be connected burner on the burner hearth, be installed in the outer heat-exchange system of burner hearth, described heat-exchange system mainly is made up of heat exchanger, blower fan and air pipe line, between heat exchanger and blower fan, is interconnecting the Cryogenic air pipeline; Between heat exchanger and burner device, interconnecting the high temperature air pipeline; On burner hearth, be shaped on the burner hearth furnace gas export, feeding cylinder is the part of heat-exchange system, and the furnace gas pipeline is connected burner hearth furnace gas export, heat exchanger and feeding cylinder in aggregates.Described furnace gas is produced by fuel combustion, and temperature reduced after high-temperature furnace gas was passed to furnace wall and furnace charge with heat, became the low temperature furnace gas, and the low temperature furnace gas need discharge out of the furnace as waste gas; Described heat-exchange system is the integrated of useless burner gas residual heat recycle device; The function of said feeding cylinder still is the temporary transient storeroom and the preheating chamber of furnace charge fusion except that being the passage of furnace charge, and it can let the charging process in the space of sealing, carry out; Making does not almost have through radiation and convection type dispersed heat, and at this moment burner can be located at and close fiery state, thereby has avoided the flame scaling loss of when filling with substance; Make preheating, furnace charge fast instantizing after getting into burner hearth of higher temperature is arranged; Even there is few part furnace charge in time not dissolve, after burner was lighted a fire once more, this part furnace charge also can swim on the furnace charge solution face flickeringly; Receive the protection of furnace charge solution, exempt the heavy damage of oxidation and scaling loss.

Described a kind of industrial furnace of smelting non-ferrous metal; It is being connected first order furnace gas pipeline between burner hearth furnace gas export and heat exchanger or between burner hearth furnace gas export and the import of feeding cylinder furnace gas, correspondingly between heat exchanger and the import of feeding cylinder furnace gas or between heat exchanger and feeding cylinder furnace gas export, be connected second level furnace gas pipeline.The effect of described first order furnace gas pipeline is that the low temperature furnace gas is drawn in burner hearth, and delivers in the heat-exchange apparatus first time; The furnace gas pipeline effect of the described second level be with through the low temperature oven pneumatic transmission after the heat exchange for the first time in second time heat-exchange apparatus; When first order furnace gas pipeline was connected between burner hearth furnace gas export and the heat exchanger, second level furnace gas pipeline correspondingly was connected between heat exchanger and the import of feeding cylinder furnace gas; When first order furnace gas pipeline was connected between burner hearth furnace gas export and the import of feeding cylinder furnace gas, second level furnace gas pipeline correspondingly was connected between heat exchanger and the feeding cylinder furnace gas export.

Described a kind of industrial furnace of smelting non-ferrous metal, it is equipped with movable bell between the discharging opening of burner hearth charging aperture and feeding cylinder.Described movable bell can move between the discharging opening of burner hearth charging aperture and feeding cylinder or slide; When feeding, movable bell is removed, make the inner and feeding cylinder internal communication of burner hearth, get in the burner hearth to make things convenient for furnace charge; In other times, movable bell is the sealing of the burner hearth charging aperture of furnace roof, purpose be reduce heat-dissipating space with heat transfer space, guarantee temperature and furnace wall radiation intensity in the higher stove, ensure the abundant conversion of heat in burner hearth.

Described a kind of industrial furnace of smelting non-ferrous metal; Its burner hearth charging aperture is positioned on the furnace roof or furnace wall of burner hearth; The burner hearth furnace gas export is positioned on the furnace roof or furnace wall of burner hearth, and the burner hearth charging aperture is whole and burner hearth furnace gas export integral body is higher than the furnace charge solution face in the burner hearth.Said burner hearth charging aperture integral body and burner hearth furnace gas export integral body are meant all constituents that comprises burner hearth charging aperture and burner hearth furnace gas export, i.e. the whole profile of burner hearth charging aperture and burner hearth furnace gas export.

Described a kind of industrial furnace of smelting non-ferrous metal; Its feeding cylinder that docks with the burner hearth charging aperture of furnace roof is any in rectilinear feeding cylinder or oblique formula feeding cylinder, the bend formula feeding cylinder, and the feeding cylinder that docks with burner hearth charging aperture on the furnace wall is the side direction type feeding cylinder.Said bend formula feeding cylinder partly is made up of the elbow part of left end and the storing of right-hand member, and elbow part is that furnace charge gets into the passage in the burner hearth, and furnace charge in the storing part by preheating.

Described a kind of industrial furnace of smelting non-ferrous metal, the discharging opening end face of any feeding cylinder in its rectilinear feeding cylinder or oblique formula feeding cylinder, the bend formula feeding cylinder are higher than the furnace charge solution face 100cm～500cm in the burner hearth or are higher than the furnace roof face 0～400cm of burner hearth.Can guarantee that like this furnace charge fusion and the interior furnace charge liquid level of burner hearth in the feeding cylinder keep certain drop, make to have certain kinetic energy behind the furnace charge entering burner hearth fusion, can sink to rapidly, more in the high temperature furnace charge solution.

Described a kind of industrial furnace of smelting non-ferrous metal; On the bottom of the movable bell below its any feeding cylinder in rectilinear feeding cylinder or oblique formula feeding cylinder, bend formula feeding cylinder roller is installed; On the same furnace wall of burner hearth, be shaped on two fire doors, on the furnace wall in the middle of two fire doors, be shaped on the burner hearth furnace gas export.The effect of said roller is that the portable propelling bell moves; Said burner hearth furnace gas export is positioned in the middle of two fire doors on the burner hearth furnace wall, can collect the low temperature furnace gas better, reduces scattering and disappearing of furnace heat.

The industrial furnace of described any smelting non-ferrous metal, it is serially connected with the molecular sieve adsorption separator on Cryogenic air pipeline or high temperature air pipeline.Molecular sieve in the described molecular sieve adsorption separator can Chalk-dust filtering foreign material and absorbed portion nitrogen; Reach the total amount of minimizing combustion-supporting gas and the total displacement of waste gas from smelting furnace, the effect of the content ratio of raising oxygen in combustion-supporting gas, realize that finally fuel-efficient burning, burner hearth shortening heat time heating time, energy consumption and aluminium decrease the purpose that reduces.

The industrial furnace of described any smelting non-ferrous metal, it is on the other feeding cylinder outer wall of movable bell or be socketed with heat insulation sheath on the burner hearth charging aperture outer wall.Said heat insulation sheath effect is that the breach that will go out on burner hearth charging aperture or the feeding cylinder discharging opening blocks after movable bell shifts out between burner hearth charging aperture and the feeding cylinder discharging opening, scatters and disappears to prevent the heat in the burner hearth.

The industrial furnace of described any smelting non-ferrous metal; It is connected with third level furnace gas pipeline on terminal heat exchanger of second level furnace gas pipeline or feeding cylinder furnace gas export, described second level furnace gas pipeline end is the furnace gas outlet behind the furnace gas pipeline of the second level of flowing through; On third level furnace gas pipeline end, be connected with deduster, described third level furnace gas pipeline end is the furnace gas outlet behind the third level furnace gas pipeline of flowing through.Described third level furnace gas pipeline both can be used as heat exchanging pipe for the third time, also can be used as gas exhaust piping; When third level furnace gas pipeline is connected with deduster as gas exhaust piping, can carry out depositing dust to furnace gas and handle, reduce the pollution of furnace gas to environment.

Because the feeding cylinder of the utility model can utilize useless burner gas residual heat preheating furnace charge fusion, can let the charging process in the space of sealing, carry out; Thereby avoided a large amount of lost of when filling with substance furnace heat and greatly reduced the useless furnace gas temperature that is drained into atmosphere; Make preheating, temperature up to 300 ℃～furnace charge fusion fast instantizing after getting into burner hearth of 400 ℃; Even there is few part furnace charge in time not dissolve, after burner was lighted a fire once more, this part furnace charge also can swim on the furnace charge solution face flickeringly; Receive the protection of furnace charge solution, exempt the destruction of oxidation and scaling loss; Movable bell of the utility model and heat insulation sheath can play isolated and insulation effect simultaneously, can prevent that a large amount of of furnace heat scatter and disappear and the abundant conversion of guarantee heat in burner hearth; And the molecular sieve adsorption separator of the utility model can reach the total amount that reduces combustion-supporting gas and waste gas from smelting furnace total displacement, improve the content ratio of oxygen in combustion-supporting gas, realize fuel-efficient burning and burner hearth shortening heat time heating time; Therefore, make and the utlity model has the advantage that efficient, low energy consumption, low aluminium are decreased.Prove through practice of trial production; The utility model can decrease reduction by 1.5%～2% at the raising thermal efficiency about 30%, aluminium on the basis of conventional furnaces, aluminium scrap per ton processing can be practiced thrift 400 yuan～500 yuan costs; If by the annual 800 tons of Way of Remelting Scrap Aluminium amounts in the whole nation, its economic worth can reach more than 3,000,000,000 yuan.

Description of drawings

Below in conjunction with the accompanying drawing and the specific embodiment the utility model is done further detailed explanation.

Fig. 1 is the partial cutaway front view of the utility model embodiment one;

Fig. 2 is the partial cutaway front view of the utility model embodiment two;

Fig. 3 is the partial cutaway front view of the utility model embodiment three;

Fig. 4 is the partial cutaway front view of the utility model embodiment four;

Fig. 5 is the partial cutaway front view of the utility model embodiment five;

Fig. 6 is the partial cutaway front view of the utility model embodiment six;

Fig. 7 is the partial cutaway front view of the utility model embodiment seven;

Fig. 8 is the partial cutaway front view of the utility model embodiment eight;

Fig. 9 local fit structure master cutaway view that to be the movable bell of the utility model contact with feeding cylinder discharging opening end face closed allround with burner hearth charging aperture end face;

Figure 10 is the partial cutaway vertical view of the utility model Fig. 9;

Figure 11 is inserted in the burner hearth charging aperture of circular cross-section or the local fit structure master cutaway view that seals in the feeding cylinder for the movable bell of the utility model;

Figure 12 is the partial cutaway vertical view of the utility model Figure 11;

Figure 13 is inserted in the burner hearth charging aperture of square-section or the local fit structure master cutaway view that seals in the feeding cylinder for the movable bell of the utility model;

Figure 14 is the partial cutaway vertical view of the utility model Figure 13;

Figure 15 is the partial cutaway front view of the utility model background technology.

Identify among the figure: 1-burner hearth charging aperture, 2-burner hearth, 3-fire door, 4-mixer, 5-burner; 6-high temperature air pipeline, 7-blower fan, 8-Cryogenic air pipeline, 9-heat exchanger, 10-third level furnace gas pipeline; The 11-deduster, 12-first order furnace gas pipeline, 13-second level furnace gas pipeline, 14-furnace charge, the movable bell of 15-; The rectilinear feeding cylinder of 16-, the oblique formula feeding cylinder of 17-, 18-bend formula feeding cylinder, 19-side direction type feeding cylinder, 20-heat insulation sheath; 21-molecular sieve adsorption separator, the 22-furnace charge replenishes mouth, 23-conveyer, 24-burner hearth furnace gas export; The import of 25-feeding cylinder furnace gas, 26-feeding cylinder furnace gas export, the arrow on the pipeline is represented the flow direction of furnace gas, the arrow that pipeline is close to is represented the flow direction of air.

The specific embodiment

Embodiment one: as shown in Figure 1, the utility model mainly by burner hearth 2, be connected rectilinear feeding cylinder 16 on the burner hearth charging aperture 1, be connected fuel device 5 on the burner hearth 2 left end walls, be positioned at burner hearth 2 furnace bottoms mixer 4, be installed in burner hearth 2 outer heat-exchange systems and form; Described burner hearth charging aperture 1 is positioned at burner hearth 2 furnace roof right-hand members, on burner hearth 2 front side walls, is shaped on two fire doors 3 of furnace charge 14 liquid levels in a little higher than stove, on the front side wall in the middle of two fire doors 3, is shaped on burner hearth furnace gas export 24; Be shaped on feeding cylinder furnace gas import 25 in the upper end of rectilinear feeding cylinder 16, be shaped on feeding cylinder furnace gas export 26 in the lower end of rectilinear feeding cylinder 16; Described heat-exchange system mainly is made up of heat exchanger 9, blower fan 7, rectilinear feeding cylinder 16, Cryogenic air pipeline 8, high temperature air pipeline 6, first order furnace gas pipeline 12, second level furnace gas pipeline 13; Described Cryogenic air pipeline 8 is connecting heat exchanger 9 and blower fan 7; Described high temperature air pipeline 6 is connecting heat exchanger 9 and burner 5; Described first order furnace gas pipeline 12 is connecting burner hearth furnace gas export 24 and heat exchanger 9, and described second level furnace gas pipeline 13 is connecting the feeding cylinder furnace gas import 25 on heat exchanger 9 and the rectilinear feeding cylinder 16; On described Cryogenic air pipeline 8, be serially connected with molecular sieve adsorption separator 21; On the feeding cylinder furnace gas export 26 of rectilinear feeding cylinder 16, be connected with third level furnace gas pipeline 10, on third level furnace gas pipeline 10 ends, be connected with deduster 11; The movable bell 15 that the bottom has roller is installed between the discharging opening of rectilinear feeding cylinder 16 and burner hearth charging aperture 1.

As the fit structure of the discharging opening of movable bell 15 and rectilinear feeding cylinder 16 and burner hearth charging aperture 1 such as Fig. 9 with when shown in Figure 10; Cross sectional shape is that at this moment the discharging opening end face and burner hearth charging aperture 1 end face of circular or other shape can be socketed with the heat insulation sheath 20 in slit between sealing discharging opening end face and the burner hearth charging aperture 1 simultaneously by movable bell 15 closed allround on rectilinear feeding cylinder 16 outer walls on movable bell 15 sides; As the fit structure of the discharging opening of movable bell 15 and rectilinear feeding cylinder 16 and burner hearth charging aperture 1 such as Figure 11 with when shown in Figure 12; On the discharging opening end face of cross sectional shape, be shaped on half arc gap for circular rectilinear feeding cylinder 16; The right-hand member of movable bell 15 is the semi arch head that cooperates with the semi arch breach of rectilinear feeding cylinder 16 discharging opening end faces; The semi arch head of movable bell 15 can be inserted into through the semi arch breach of rectilinear feeding cylinder 16 discharging opening end faces in the rectilinear feeding cylinder 16; Come rectilinear feeding cylinder 16 endoporus and burner hearth charging aperture 1 endoporus are isolated, at this moment on other rectilinear feeding cylinder 16 outer walls of movable bell 15, be socketed with breach between sealing discharging opening end face and the burner hearth charging aperture 1, be shaped as the heat insulation sheath 20 of full circle ring or semicircular ring; As the fit structure of the discharging opening of movable bell 15 and rectilinear feeding cylinder 16 and burner hearth charging aperture 1 such as Figure 13 with when shown in Figure 14; With cross sectional shape is that the discharging opening left end of the rectilinear feeding cylinder 16 of rectangle is processed a breach; The right-hand member of the movable bell 15 of rectangle is inserted in the rectilinear feeding cylinder 16 through breach; Come rectilinear feeding cylinder 16 endoporus and burner hearth charging aperture 1 endoporus are isolated, the right-hand member by movable bell 15 in the charging process seals discharging opening left end breach.

During the heat-exchange system operation; Under the situation of movable bell 15 sealings; Produce great amount of heat during fuel combustion in the fuel device 5 and come furnace charge 14 solution and burner hearth 2 inwalls in the heating furnace; The combustion air of fuel is produced by blower fan 7, and combustion air at first is transported in the heat exchanger 9 through Cryogenic air pipeline 8, on through Cryogenic air pipeline 8 during the molecular sieve adsorption separator 21 of serial connection; The inner molecular sieves of molecular sieve adsorption separator 21 filter out part nitrogen in the combustion air and other dust foreign material, reduced the combustion air total amount with improved combustion air contain the oxygen ratio; In heat exchanger 9; The heat exchange first time of combustion air and the furnace gas that gives up from the useless furnace gas that transports in the burner hearth, through burner hearth furnace gas export 24 and first order furnace gas pipeline 12; Combustion air with low temperature when useless furnace gas temperature reduces is heated into the high temperature combustion air more than 400 ℃, and the high temperature combustion air is transported to burner 5 through high temperature air pipeline 6; In burner 5; Reduced useless nitrogen amount with improved the high temperature combustion air that contains the oxygen ratio help fuel more fully, burning quickly; More release heat makes burner hearth 2 inner intensifications, the also corresponding minimizing of useless furnace gas total amount that burning simultaneously produces quickly; The heat that is lost to atmosphere through useless furnace gas correspondingly reduces, and so not only energy-conservation, aluminium decreases and also can reduce; In burner hearth 2; The end product of fuel and the burning of high temperature combustion air is useless furnace gas; Useless furnace gas is transported to heat exchanger 9 through burner hearth furnace gas export 24 and first order furnace gas pipeline 12; After finishing the heat exchange first time of useless furnace gas, be transported in the rectilinear feeding cylinder 16, in rectilinear feeding cylinder 16, finish the heat exchange second time of furnace gas of giving up, after furnace charge 14 preheatings through second level furnace gas pipeline 13 and feeding cylinder furnace gas import 25; Temperature reduces once more, less than 200 ℃ useless furnace gases through feeding cylinder furnace gas export 26, third level furnace gas pipeline 10 and deduster 11, be discharged in the atmospheric environment.

When 14 solution of the furnace charge in the burner hearth 2 be elevated to about 800 ℃, in the time of need adding furnace charge 14 again; Fuel device 5 burn-outs; Movable bell 15 is opened automatically; Rectilinear feeding cylinder 16 and burner hearth 2 internal communication appear at breach between rectilinear feeding cylinder 16 discharging opening end faces and burner hearth charging aperture 1 end face by the right-hand member sealing of heat insulation sheath 20 or the movable bell 15 of rectangle thereupon, are preheating to furnace charge 14 rapid free fallings that 300 ℃～400 ℃, the furnace charge 14 solution faces in burner hearth 2 have 2m～3m drop this moment to furnace charge 14 solution; Movable then bell 15 automatically resets and closes; With convenient rectilinear feeding cylinder 16 next stove furnace charge 14 to be installed, under the stirring action of mixer 4, furnace charge 14 dissolves very soon or has few part furnace charge 14 to swim on the furnace charge 14 solution faces flickeringly.

Embodiment two: as shown in Figure 2, the utility model mainly by burner hearth 2, be connected rectilinear feeding cylinder 16 on the burner hearth charging aperture 1, be connected fuel device 5 on the burner hearth 2 left end walls, be positioned at burner hearth 2 furnace bottoms mixer 4, be installed in burner hearth 2 outer heat-exchange systems and form; Described burner hearth charging aperture 1 is positioned at burner hearth 2 furnace roof right-hand members, on burner hearth 2 front side walls, is shaped on two fire doors 3 of furnace charge 14 liquid levels in a little higher than stove, on the front side wall in the middle of two fire doors 3, is shaped on burner hearth furnace gas export 24; Be shaped on feeding cylinder furnace gas import 25 in the upper end of rectilinear feeding cylinder 16, be shaped on feeding cylinder furnace gas export 26 in the lower end of rectilinear feeding cylinder 16; Described heat-exchange system mainly is made up of heat exchanger 9, blower fan 7, rectilinear feeding cylinder 16, Cryogenic air pipeline 8, high temperature air pipeline 6, first order furnace gas pipeline 12, second level furnace gas pipeline 13; Described Cryogenic air pipeline 8 is connecting heat exchanger 9 and blower fan 7; Described high temperature air pipeline 6 is connecting heat exchanger 9 and burner 5; Described first order furnace gas pipeline 12 is connecting the feeding cylinder furnace gas import 25 on burner hearth furnace gas export 24 and the rectilinear feeding cylinder 16, and described second level furnace gas pipeline 13 is connecting the feeding cylinder furnace gas export 26 on heat exchanger 9 and the rectilinear feeding cylinder 16; On described Cryogenic air pipeline 8, be serially connected with molecular sieve adsorption separator 21; On heat exchanger 9, be connected with third level furnace gas pipeline 10, on third level furnace gas pipeline 10 ends, be connected with deduster 11; The movable bell 15 that the bottom has roller is installed between the discharging opening of rectilinear feeding cylinder 16 and burner hearth charging aperture 1.

During the heat-exchange system operation; Under the situation of movable bell 15 sealings; Produce great amount of heat during fuel combustion in the fuel device 5 and come furnace charge 14 solution and inboard wall of burner hearth in the heating furnace; The combustion air of fuel is produced by blower fan 7, and combustion air at first is transported in the heat exchanger 9 through Cryogenic air pipeline 8, on through Cryogenic air pipeline 8 during the molecular sieve adsorption separator 21 of serial connection; The inner molecular sieves of molecular sieve adsorption separator 21 filter out part nitrogen in the combustion air and other dust foreign material, reduced the combustion air total amount with improved combustion air contain the oxygen ratio; In heat exchanger 9; The give up heat exchange second time of furnace gas of combustion air and the useless furnace gas that transports through feeding cylinder furnace gas export 26 and second level furnace gas pipeline 13; Combustion air with low temperature when useless furnace gas temperature reduces is heated into the high temperature combustion air about 400 ℃, and the high temperature combustion air is transported to burner 5 through high temperature air pipeline 6; In burner 5; Reduced useless nitrogen amount with improved the high temperature combustion air that contains the oxygen ratio help fuel more fully, burning quickly; More release heat makes quickly in the burner hearth 2 and heats up, the also corresponding minimizing of useless furnace gas total amount that burning simultaneously produces; The heat that is lost to atmosphere through useless furnace gas correspondingly reduces, and so not only energy-conservation, aluminium decreases and also can reduce; In burner hearth 2; The end product of fuel and the burning of high temperature combustion air is useless furnace gas; Useless furnace gas is transported in the rectilinear feeding cylinder 16 through burner hearth furnace gas export 24, first order furnace gas pipeline 12 and feeding cylinder furnace gas import 25; After finish the heat exchange first time of useless furnace gas with furnace charges 14 in the rectilinear feeding cylinder 16, useless furnace gas is transported in the heat exchanger 9 through feeding cylinder furnace gas export 26 and second level furnace gas pipeline 13, heat exchanger 9 in and after combustion air finishes the heat exchange second time of the furnace gas that gives up; Temperature reduces once more, less than 200 ℃ useless furnace gases through third level furnace gas pipeline 10 and deduster 11, be discharged in the atmospheric environment.

When 14 solution of the furnace charge in the burner hearth 2 be elevated to about 800 ℃, in the time of need adding furnace charge 14 again; Fuel device 5 burn-outs; Movable bell 15 is opened automatically; Rectilinear feeding cylinder 16 and burner hearth 2 internal communication appear at breach between rectilinear feeding cylinder 16 discharging opening end faces and burner hearth charging aperture 1 end face by the right-hand member sealing of heat insulation sheath 20 or the movable bell 15 of rectangle thereupon, and the furnace charge 14 rapid free fallings that the furnace charge 14 solution faces about 400 ℃, in burner hearth 2 that are preheating to this moment have 2m～3m drop are to furnace charge 14 solution; Movable then bell 15 automatically resets and closes; With convenient rectilinear feeding cylinder 16 next stove furnace charge 14 to be installed, under the stirring action of mixer 4, furnace charge 14 dissolves very soon or has few part furnace charge 14 to swim on the furnace charge 14 solution faces flickeringly.

Embodiment three: as shown in Figure 3, the utility model mainly by burner hearth 2, be connected oblique formula feeding cylinder 17 on the burner hearth charging aperture 1, be connected fuel device 5 on the burner hearth 2 left end walls, be positioned at burner hearth 2 furnace bottoms mixer 4, be installed in burner hearth 2 outer heat-exchange systems and form; Described burner hearth charging aperture 1 is positioned at burner hearth 2 furnace roof right-hand members, on burner hearth 2 front side walls, is shaped on two fire doors 3 of furnace charge 14 liquid levels in a little higher than stove, on the front side wall in the middle of two fire doors 3, is shaped on burner hearth furnace gas export 24; Be shaped on feeding cylinder furnace gas import 25 in the upper end of oblique formula feeding cylinder 17, be shaped on feeding cylinder furnace gas export 26 in the lower end of oblique formula feeding cylinder 17; Described heat-exchange system mainly is made up of heat exchanger 9, blower fan 7, oblique formula feeding cylinder 17, Cryogenic air pipeline 8, high temperature air pipeline 6, first order furnace gas pipeline 12, second level furnace gas pipeline 13; Described Cryogenic air pipeline 8 is connecting heat exchanger 9 and blower fan 7; Described high temperature air pipeline 6 is connecting heat exchanger 9 and burner 5; Described first order furnace gas pipeline 12 is connecting burner hearth furnace gas export 24 and heat exchanger 9, and described second level furnace gas pipeline 13 is connecting the feeding cylinder furnace gas import 25 on heat exchanger 9 and the oblique formula feeding cylinder 17; On described Cryogenic air pipeline 8, be serially connected with molecular sieve adsorption separator 21; On the feeding cylinder furnace gas export 26 of oblique formula feeding cylinder 17, be connected with third level furnace gas pipeline 10, on third level furnace gas pipeline 10 ends, be connected with deduster 11; The movable bell 15 that the bottom has roller is installed between the discharging opening of oblique formula feeding cylinder 17 and burner hearth charging aperture 1.

As the fit structure of the discharging opening of movable bell 15 and oblique formula feeding cylinder 17 and burner hearth charging aperture 1 such as Fig. 9 with when shown in Figure 10; Cross sectional shape is that at this moment the discharging opening end face and burner hearth charging aperture 1 end face of circular or other shape can be socketed with the heat insulation sheath 20 in slit between sealing discharging opening end face and the burner hearth charging aperture 1 simultaneously by movable bell 15 closed allround on oblique formula feeding cylinder 17 outer walls on movable bell 15 sides; As the fit structure of the discharging opening of movable bell 15 and oblique formula feeding cylinder 17 and burner hearth charging aperture 1 such as Figure 11 with when shown in Figure 12; On the discharging opening end face of cross sectional shape, be shaped on half arc gap for circular oblique formula feeding cylinder 17; The right-hand member of movable bell 15 is the semi arch head that cooperates with the semi arch breach of oblique formula feeding cylinder 17 discharging opening end faces; The semi arch head of movable bell 15 can be inserted into through the semi arch breach of oblique formula feeding cylinder 17 discharging opening end faces in the oblique formula feeding cylinder 17; Come oblique formula feeding cylinder 17 endoporus and burner hearth charging aperture 1 endoporus are isolated, at this moment on other oblique formula feeding cylinder 17 outer walls of movable bell 15, be socketed with breach between sealing discharging opening end face and the burner hearth charging aperture 1, be shaped as the heat insulation sheath 20 of full circle ring or semicircular ring; As the fit structure of the discharging opening of movable bell 15 and oblique formula feeding cylinder 17 and burner hearth charging aperture 1 such as Figure 13 with when shown in Figure 14; With cross sectional shape is that the discharging opening left end of the oblique formula feeding cylinder 17 of rectangle is processed a breach; The right-hand member of the movable bell 15 of rectangle is inserted in the oblique formula feeding cylinder 17 through breach; Come oblique formula feeding cylinder 17 endoporus and burner hearth charging aperture 1 endoporus are isolated, the right-hand member by movable bell 15 in the charging process seals discharging opening left end breach.

During the heat-exchange system operation; Under the situation of movable bell 15 sealings; Produce great amount of heat during fuel combustion in the fuel device 5 and come furnace charge 14 solution and burner hearth 2 inwalls in the heating furnace; The combustion air of fuel is produced by blower fan 7, and combustion air at first is transported in the heat exchanger 9 through Cryogenic air pipeline 8, on through Cryogenic air pipeline 8 during the molecular sieve adsorption separator 21 of serial connection; The inner molecular sieves of molecular sieve adsorption separator 21 filter out part nitrogen in the combustion air and other dust foreign material, reduced the combustion air total amount with improved combustion air contain the oxygen ratio; In heat exchanger 9; The heat exchange first time of combustion air and the furnace gas that gives up from the useless furnace gas that transports in the burner hearth, through burner hearth furnace gas export 24 and first order furnace gas pipeline 12; Combustion air with low temperature when useless furnace gas temperature reduces is heated into the high temperature combustion air more than 400 ℃, and the high temperature combustion air is transported to burner 5 through high temperature air pipeline 6; In burner 5; Reduced useless nitrogen amount with improved the high temperature combustion air that contains the oxygen ratio help fuel more fully, burning quickly; More release heat makes quickly in the burner hearth 2 and heats up, the also corresponding minimizing of useless furnace gas total amount that burning simultaneously produces; The heat that is lost to atmosphere through useless furnace gas correspondingly reduces, and so not only energy-conservation, aluminium decreases and also can reduce; In burner hearth 2; The end product of fuel and the burning of high temperature combustion air is useless furnace gas; Useless furnace gas is transported to heat exchanger 9 through burner hearth furnace gas export 24 and first order furnace gas pipeline 12; After finishing the heat exchange first time of useless furnace gas, be transported in the oblique formula feeding cylinder 17, in oblique formula feeding cylinder 17, finish the heat exchange second time of furnace gas of giving up, after furnace charge 14 preheatings through second level furnace gas pipeline 13 and feeding cylinder furnace gas import 25; Temperature reduces once more, less than 200 ℃ useless furnace gases through feeding cylinder furnace gas export 26, third level furnace gas pipeline 10 and deduster 11, be discharged in the atmospheric environment.

When 14 solution of the furnace charge in the burner hearth 2 be elevated to about 800 ℃, in the time of need adding furnace charge 14 again; Fuel device 5 burn-outs; Movable bell 15 is opened automatically; Oblique formula feeding cylinder 17 and burner hearth 2 internal communication appear at breach between oblique formula feeding cylinder 17 discharging opening end faces and burner hearth charging aperture 1 end face by the right-hand member sealing of heat insulation sheath 20 or the movable bell 15 of rectangle thereupon, are preheating to furnace charge 14 rapid free fallings that 300 ℃～400 ℃, the furnace charge 14 solution faces in burner hearth 2 have 2m～3m drop this moment to furnace charge 14 solution; Movable then bell 15 automatically resets and closes; With convenient oblique formula feeding cylinder 17 next stove furnace charge 14 to be installed, under the stirring action of mixer 4, furnace charge 14 dissolves very soon or has few part furnace charge 14 to swim on the furnace charge 14 solution faces flickeringly.

Embodiment four: as shown in Figure 4, the utility model mainly by burner hearth 2, be connected oblique formula feeding cylinder 17 on the burner hearth charging aperture 1, be connected fuel device 5 on the burner hearth 2 left end walls, be positioned at burner hearth 2 furnace bottoms mixer 4, be installed in burner hearth 2 outer heat-exchange systems and form; Described burner hearth charging aperture 1 is positioned at burner hearth 2 furnace roof right-hand members, on burner hearth 2 front side walls, is shaped on two fire doors 3 of furnace charge 14 liquid levels in a little higher than stove, on the front side wall in the middle of two fire doors 3, is shaped on burner hearth furnace gas export 24; Be shaped on feeding cylinder furnace gas import 25 in the upper end of oblique formula feeding cylinder 17, be shaped on feeding cylinder furnace gas export 26 in the lower end of oblique formula feeding cylinder 17; Described heat-exchange system mainly is made up of heat exchanger 9, blower fan 7, oblique formula feeding cylinder 17, Cryogenic air pipeline 8, high temperature air pipeline 6, first order furnace gas pipeline 12, second level furnace gas pipeline 13; Described Cryogenic air pipeline 8 is connecting heat exchanger 9 and blower fan 7; Described high temperature air pipeline 6 is connecting heat exchanger 9 and burner 5; Described first order furnace gas pipeline 12 is connecting the feeding cylinder furnace gas import 25 on burner hearth furnace gas export 24 and the oblique formula feeding cylinder 17, and described second level furnace gas pipeline 13 is connecting the feeding cylinder furnace gas export 26 on heat exchanger 9 and the oblique formula feeding cylinder 17; On described Cryogenic air pipeline 8, be serially connected with molecular sieve adsorption separator 21; On heat exchanger 9, be connected with third level furnace gas pipeline 10, on third level furnace gas pipeline 10 ends, be connected with deduster 11; The movable bell 15 that the bottom has roller is installed between the discharging opening of oblique formula feeding cylinder 17 and burner hearth charging aperture 1.Can

During the heat-exchange system operation; Under the situation of movable bell 15 sealings; Produce great amount of heat during fuel combustion in the fuel device 5 and come furnace charge 14 solution and inboard wall of burner hearth in the heating furnace; The combustion air of fuel is produced by blower fan 7, and combustion air at first is transported in the heat exchanger 9 through Cryogenic air pipeline 8, on through Cryogenic air pipeline 8 during the molecular sieve adsorption separator 21 of serial connection; The inner molecular sieves of molecular sieve adsorption separator 21 filter out part nitrogen in the combustion air and other dust foreign material, reduced the combustion air total amount with improved combustion air contain the oxygen ratio; In heat exchanger 9; The give up heat exchange second time of furnace gas of combustion air and the useless furnace gas that transports through feeding cylinder furnace gas export 26 and second level furnace gas pipeline 13; Combustion air with low temperature when useless furnace gas temperature reduces is heated into the high temperature combustion air about 400 ℃, and the high temperature combustion air is transported to burner 5 through high temperature air pipeline 6; In burner 5; Reduced useless nitrogen amount with improved the high temperature combustion air that contains the oxygen ratio help fuel more fully, burning quickly; More release heat makes quickly in the burner hearth 2 and heats up, the also corresponding minimizing of useless furnace gas total amount that burning simultaneously produces; The heat that is lost to atmosphere through useless furnace gas correspondingly reduces, and so not only energy-conservation, aluminium decreases and also can reduce; In burner hearth 2; The end product of fuel and the burning of high temperature combustion air is useless furnace gas; Useless furnace gas is transported in the oblique formula feeding cylinder 17 through burner hearth furnace gas export 24, first order furnace gas pipeline 12 and feeding cylinder furnace gas import 25; After finish the heat exchange first time of useless furnace gas with furnace charges 14 in the oblique formula feeding cylinder 17, useless furnace gas is transported in the heat exchanger 9 through feeding cylinder furnace gas export 26 and second level furnace gas pipeline 13, heat exchanger 9 in and after combustion air finishes the heat exchange second time of the furnace gas that gives up; Temperature reduces once more, less than 200 ℃ useless furnace gases through third level furnace gas pipeline 10 and deduster 11, be discharged in the atmospheric environment.

When 14 solution of the furnace charge in the burner hearth 2 be elevated to about 800 ℃, in the time of need adding furnace charge 14 again; Fuel device 5 burn-outs; Movable bell 15 is opened automatically; Oblique formula feeding cylinder 17 and burner hearth 2 internal communication appear at breach between oblique formula feeding cylinder 17 discharging opening end faces and burner hearth charging aperture 1 end face by the right-hand member sealing of heat insulation sheath 20 or the movable bell 15 of rectangle thereupon, and the furnace charge 14 rapid free fallings that the furnace charge 14 solution faces about 400 ℃, in burner hearth 2 that are preheating to this moment have 2m～3m drop are to furnace charge 14 solution; Movable then bell 15 automatically resets and closes; With convenient oblique formula feeding cylinder 17 next stove furnace charge 14 to be installed, under the stirring action of mixer 4, furnace charge 14 dissolves very soon or has few part furnace charge 14 to swim on the furnace charge 14 solution faces flickeringly.

Embodiment five: as shown in Figure 5, the utility model mainly by burner hearth 2, be connected bend formula feeding cylinder 18 on the burner hearth charging aperture 1, be connected fuel device 5 on the burner hearth 2 left end walls, be positioned at burner hearth 2 furnace bottoms mixer 4, be installed in burner hearth 2 outer heat-exchange systems and form; Described burner hearth charging aperture 1 is positioned at burner hearth 2 furnace roof right-hand members, on burner hearth 2 front side walls, is shaped on two fire doors 3 of furnace charge 14 liquid levels in a little higher than stove, on the front side wall in the middle of two fire doors 3, is shaped on burner hearth furnace gas export 24; Described bend formula feeding cylinder 18 partly is made up of the elbow part of left end and the storing of right-hand member; Left upper end at bend formula feeding cylinder 18 is shaped on feeding cylinder furnace gas import 25; Bottom righthand side at bend formula feeding cylinder 18 is shaped on feeding cylinder furnace gas export 26; Upper right side at bend formula feeding cylinder 18 is shaped on furnace charge additional mouthful 22, in the storing part of bend formula feeding cylinder 18 right-hand members, conveyer 23 is installed, and is placing furnace charge 14 on the conveyer 23; Described heat-exchange system mainly is made up of heat exchanger 9, blower fan 7, bend formula feeding cylinder 18, Cryogenic air pipeline 8, high temperature air pipeline 6, first order furnace gas pipeline 12, second level furnace gas pipeline 13; Described Cryogenic air pipeline 8 is connecting heat exchanger 9 and blower fan 7; Described high temperature air pipeline 6 is connecting heat exchanger 9 and burner 5; Described first order furnace gas pipeline 12 is connecting burner hearth furnace gas export 24 and heat exchanger 9, and described second level furnace gas pipeline 13 is connecting the feeding cylinder furnace gas import 25 on heat exchanger 9 and the bend formula feeding cylinder 18; On described Cryogenic air pipeline 8, be serially connected with molecular sieve adsorption separator 21; On the feeding cylinder furnace gas export 26 of bend formula feeding cylinder 18, be connected with third level furnace gas pipeline 10, on third level furnace gas pipeline 10 ends, be connected with deduster 11; The movable bell 15 that the bottom has roller is installed between the discharging opening of bend formula feeding cylinder 18 and burner hearth charging aperture 1.

As the fit structure of the discharging opening of movable bell 15 and bend formula feeding cylinder 18 and burner hearth charging aperture 1 such as Fig. 9 with when shown in Figure 10; Cross sectional shape is that at this moment the discharging opening end face and burner hearth charging aperture 1 end face of circular or other shape can be socketed with the heat insulation sheath 20 in slit between sealing discharging opening end face and the burner hearth charging aperture 1 simultaneously by movable bell 15 closed allround on bend formula feeding cylinder 18 outer walls on movable bell 15 sides; As the fit structure of the discharging opening of movable bell 15 and bend formula feeding cylinder 18 and burner hearth charging aperture 1 such as Figure 11 with when shown in Figure 12; On the discharging opening end face of cross sectional shape, be shaped on half arc gap for circular bend formula feeding cylinder 18; The right-hand member of movable bell 15 is the semi arch head that cooperates with the semi arch breach of bend formula feeding cylinder 18 discharging opening end faces; The semi arch head of movable bell 15 can be inserted into through the semi arch breach of bend formula feeding cylinder 18 discharging opening end faces in the bend formula feeding cylinder 18; Come bend formula feeding cylinder 18 endoporus and burner hearth charging aperture 1 endoporus are isolated, at this moment on other bend formula feeding cylinder 18 outer walls of movable bell 15, be socketed with breach between sealing discharging opening end face and the burner hearth charging aperture 1, be shaped as the heat insulation sheath 20 of full circle ring or semicircular ring; As the fit structure of the discharging opening of movable bell 15 and bend formula feeding cylinder 18 and burner hearth charging aperture 1 such as Figure 13 with when shown in Figure 14; With cross sectional shape is that the discharging opening left end of the bend formula feeding cylinder 18 of rectangle is processed a breach; The right-hand member of the movable bell 15 of rectangle is inserted in the bend formula feeding cylinder 18 through breach; Come bend formula feeding cylinder 18 endoporus and burner hearth charging aperture 1 endoporus are isolated, the right-hand member by movable bell 15 in the charging process seals discharging opening left end breach.

During the heat-exchange system operation; Under the situation of movable bell 15 sealings; Produce great amount of heat during fuel combustion in the fuel device 5 and come furnace charge 14 solution and inboard wall of burner hearth in the heating furnace; The combustion air of fuel is produced by blower fan 7, and combustion air at first is transported in the heat exchanger 9 through Cryogenic air pipeline 8, on through Cryogenic air pipeline 8 during the molecular sieve adsorption separator 21 of serial connection; The inner molecular sieves of molecular sieve adsorption separator 21 filter out part nitrogen in the combustion air and other dust foreign material, reduced the combustion air total amount with improved combustion air contain the oxygen ratio; In heat exchanger 9; The heat exchange first time of combustion air and the furnace gas that gives up from the useless furnace gas that transports in the burner hearth, through burner hearth furnace gas export 24 and first order furnace gas pipeline 12; Combustion air with low temperature when useless furnace gas temperature reduces is heated into the high temperature combustion air more than 400 ℃, and the high temperature combustion air is transported to burner 5 through high temperature air pipeline 6; In burner 5; Reduced useless nitrogen amount with improved the high temperature combustion air that contains the oxygen ratio help fuel more fully, burning quickly; More release heat makes quickly in the burner hearth 2 and heats up, the also corresponding minimizing of useless furnace gas total amount that burning simultaneously produces; The heat that is lost to atmosphere through useless furnace gas correspondingly reduces, and so not only energy-conservation, aluminium decreases and also can reduce; In burner hearth 2; The end product of fuel and the burning of high temperature combustion air is useless furnace gas; Useless furnace gas is transported to heat exchanger 9 through burner hearth furnace gas export 24 and first order furnace gas pipeline 12; After finishing the heat exchange first time of useless furnace gas, be transported in the bend formula feeding cylinder 18, in bend formula feeding cylinder 18, finish the heat exchange second time of furnace gas of giving up, after furnace charge 14 preheatings through second level furnace gas pipeline 13 and feeding cylinder furnace gas import 25; Temperature reduces once more, less than 200 ℃ useless furnace gases through feeding cylinder furnace gas export 26, third level furnace gas pipeline 10 and deduster 11, be discharged in the atmospheric environment.

When 14 solution of the furnace charge in the burner hearth 2 be elevated to about 800 ℃, in the time of need adding furnace charge 14 again; Fuel device 5 burn-outs; Movable bell 15 is opened automatically; Bend formula feeding cylinder 18 and burner hearth 2 internal communication; Appear at breach between bend formula feeding cylinder 18 discharging opening end faces and burner hearth charging aperture 1 end face by the right-hand member sealing of the movable bell 15 of heat insulation sheath 20 or rectangle thereupon; After being preheating to 300 ℃～400 ℃ furnace charge 14 this moment and being transmitted the elbow part that device 23 is transported to bend formula feeding cylinder 18,2m～rapid free falling of 3m drop is arranged to furnace charge 14 solution with the 14 solution faces of the furnace charge from burner hearth 2 in, movable then bell 15 automatically resets and closes, to make things convenient for bend formula feeding cylinder 18 through the additional mouth of furnace charge 22 next stove furnace charge 14 to be installed; Under the stirring action of mixer 4, furnace charge 14 dissolves very soon or has few part furnace charge 14 to swim on the furnace charge 14 solution faces flickeringly.

Embodiment six: as shown in Figure 6, the utility model mainly by burner hearth 2, be connected bend formula feeding cylinder 18 on the burner hearth charging aperture 1, be connected fuel device 5 on the burner hearth 2 left end walls, be positioned at burner hearth 2 furnace bottoms mixer 4, be installed in burner hearth 2 outer heat-exchange systems and form; Described burner hearth charging aperture 1 is positioned at burner hearth 2 furnace roof right-hand members, on burner hearth 2 front side walls, is shaped on two fire doors 3 of furnace charge 14 liquid levels in a little higher than stove, on the front side wall in the middle of two fire doors 3, is shaped on burner hearth furnace gas export 24; Described bend formula feeding cylinder 18 partly is made up of the elbow part of left end and the storing of right-hand member; Left upper end at bend formula feeding cylinder 18 is shaped on feeding cylinder furnace gas import 25; Bottom righthand side at bend formula feeding cylinder 18 is shaped on feeding cylinder furnace gas export 26; Upper right side at bend formula feeding cylinder 18 is shaped on furnace charge additional mouthful 22, in the storing part of bend formula feeding cylinder 18 right-hand members, conveyer 23 is installed, and is placing furnace charge 14 on the conveyer 23; Described heat-exchange system mainly is made up of heat exchanger 9, blower fan 7, bend formula feeding cylinder 18, Cryogenic air pipeline 8, high temperature air pipeline 6, first order furnace gas pipeline 12, second level furnace gas pipeline 13; Described Cryogenic air pipeline 8 is connecting heat exchanger 9 and blower fan 7; Described high temperature air pipeline 6 is connecting heat exchanger 9 and burner 5; Described first order furnace gas pipeline 12 is connecting the feeding cylinder furnace gas import 25 on burner hearth furnace gas export 24 and the bend formula feeding cylinder 18, and described second level furnace gas pipeline 13 is connecting the feeding cylinder furnace gas export 26 on heat exchanger 9 and the bend formula feeding cylinder 18; On described Cryogenic air pipeline 8, be serially connected with molecular sieve adsorption separator 21; On heat exchanger 9, be connected with third level furnace gas pipeline 10, on third level furnace gas pipeline 10 ends, be connected with deduster 11; The movable bell 15 that the bottom has roller is installed between the discharging opening of bend formula feeding cylinder 18 and burner hearth charging aperture 1.

During the heat-exchange system operation; Under the situation of movable bell 15 sealings; Produce great amount of heat during fuel combustion in the fuel device 5 and come furnace charge 14 solution and inboard wall of burner hearth in the heating furnace; The combustion air of fuel is produced by blower fan 7, and combustion air at first is transported in the heat exchanger 9 through Cryogenic air pipeline 8, on through Cryogenic air pipeline 8 during the molecular sieve adsorption separator 21 of serial connection; The inner molecular sieves of molecular sieve adsorption separator 21 filter out part nitrogen in the combustion air and other dust foreign material, reduced the combustion air total amount with improved combustion air contain the oxygen ratio; In heat exchanger 9; The give up heat exchange second time of furnace gas of combustion air and the useless furnace gas that transports through feeding cylinder furnace gas export 26 and second level furnace gas pipeline 13; Combustion air with low temperature when useless furnace gas temperature reduces is heated into the high temperature combustion air about 400 ℃, and the high temperature combustion air is transported to burner 5 through high temperature air pipeline 6; In burner 5; Reduced useless nitrogen amount with improved the high temperature combustion air that contains the oxygen ratio help fuel more fully, burning quickly; More release heat makes quickly in the burner hearth 2 and heats up, the also corresponding minimizing of useless furnace gas total amount that burning simultaneously produces; The heat that is lost to atmosphere through useless furnace gas correspondingly reduces, and so not only energy-conservation, aluminium decreases and also can reduce; In burner hearth 2; The end product of fuel and the burning of high temperature combustion air is useless furnace gas; Useless furnace gas is transported in the bend formula feeding cylinder 18 through burner hearth furnace gas export 24, first order furnace gas pipeline 12 and feeding cylinder furnace gas import 25; After finish the heat exchange first time of useless furnace gas with furnace charges 14 in the bend formula feeding cylinder 18, useless furnace gas is transported in the heat exchanger 9 through feeding cylinder furnace gas export 26 and second level furnace gas pipeline 13, heat exchanger 9 in and after combustion air finishes the heat exchange second time of the furnace gas that gives up; Temperature reduces once more, less than 200 ℃ useless furnace gases through third level furnace gas pipeline 10 and deduster 11, be discharged in the atmospheric environment.

When 14 solution of the furnace charge in the burner hearth 2 be elevated to about 800 ℃, in the time of need adding furnace charge 14 again; Fuel device 5 burn-outs; Movable bell 15 is opened automatically; Bend formula feeding cylinder 18 and burner hearth 2 internal communication; Appear at breach between bend formula feeding cylinder 18 discharging opening end faces and burner hearth charging aperture 1 end face by the right-hand member sealing of the movable bell 15 of heat insulation sheath 20 or rectangle thereupon; After being preheating to furnace charge 14 about 400 ℃ this moment and being transmitted the elbow part that device 23 is transported to bend formula feeding cylinder 18,2m～rapid free falling of 3m drop is arranged to furnace charge 14 solution with the 14 solution faces of the furnace charge from burner hearth 2 in, movable then bell 15 automatically resets and closes, to make things convenient for bend formula feeding cylinder 18 through the additional mouth of furnace charge 22 next stove furnace charge 14 to be installed; Under the stirring action of mixer 4, furnace charge 14 dissolves very soon or has few part furnace charge 14 to swim on the furnace charge 14 solution faces flickeringly.

Embodiment seven: as shown in Figure 7, the utility model mainly by burner hearth 2, be connected side direction type feeding cylinder 19 on the burner hearth charging aperture 1, be connected fuel device 5 on burner hearth 2 headwalls, be positioned at burner hearth 2 furnace bottoms mixer 4, be installed in burner hearth 2 outer heat-exchange systems and form; Described burner hearth charging aperture 1 is positioned at the right-hand member wall upper end of burner hearth 2, on burner hearth 2 front side walls, is shaped on two fire doors 3 of furnace charge 14 liquid levels in a little higher than stove, on the front side wall in the middle of two fire doors 3, is shaped on the burner hearth furnace gas export; Be shaped on the furnace gas import in the upper end of side direction type feeding cylinder 19, be shaped on furnace gas export in the lower end of side direction type feeding cylinder 19; Described heat-exchange system mainly is made up of heat exchanger 9, blower fan 7, side direction type feeding cylinder 19, Cryogenic air pipeline 8, high temperature air pipeline 6, first order furnace gas pipeline 12, second level furnace gas pipeline 13; Described Cryogenic air pipeline 8 is connecting heat exchanger 9 and blower fan 7; Described high temperature air pipeline 6 is connecting heat exchanger 9 and burner 5; Described first order furnace gas pipeline 12 is connecting burner hearth furnace gas export and heat exchanger 9, and described second level furnace gas pipeline 13 is connecting the furnace gas import on heat exchanger 9 and the side direction type feeding cylinder 19; On described Cryogenic air pipeline 8, be serially connected with molecular sieve adsorption separator 21; On the furnace gas export of side direction type feeding cylinder 19, be connected with third level furnace gas pipeline 10, on third level furnace gas pipeline 10 ends, be connected with deduster 11; Between the discharging opening of side direction type feeding cylinder 19 and burner hearth charging aperture 1, vertical movable bell 15 is installed.

As the fit structure of the discharging opening of movable bell 15 and side direction type feeding cylinder 19 and burner hearth charging aperture 1 such as Fig. 9 with when shown in Figure 10; Cross sectional shape is that at this moment the discharging opening end face and burner hearth charging aperture 1 end face of circular or other shape can be socketed with the heat insulation sheath 20 in slit between sealing discharging opening end face and the burner hearth charging aperture 1 simultaneously by movable bell 15 closed allround on side direction type feeding cylinder 19 outer walls on movable bell 15 sides; As the fit structure of the discharging opening of movable bell 15 and side direction type feeding cylinder 19 and burner hearth charging aperture 1 such as Figure 11 with when shown in Figure 12; On the discharging opening end face of cross sectional shape, be shaped on half arc gap for circular side direction type feeding cylinder 19; The right-hand member of movable bell 15 is the semi arch head that cooperates with the semi arch breach of side direction type feeding cylinder 19 discharging opening end faces; The semi arch head of movable bell 15 can be inserted in the side direction type feeding cylinder 19 through the semi arch breach of side direction type feeding cylinder 19 discharging opening end faces; Come side direction type feeding cylinder 19 endoporus and burner hearth charging aperture 1 endoporus are isolated, at this moment on other side direction type feeding cylinder 19 outer walls of movable bell 15, be socketed with breach between sealing discharging opening end face and the burner hearth charging aperture 1, be shaped as the heat insulation sheath 20 of full circle ring or semicircular ring; As the fit structure of the discharging opening of movable bell 15 and side direction type feeding cylinder 19 and burner hearth charging aperture 1 such as Figure 13 with when shown in Figure 14; With cross sectional shape is that the discharging opening left end of the side direction type feeding cylinder 19 of rectangle is processed a breach; The right-hand member of the movable bell 15 of rectangle is inserted in the side direction type feeding cylinder 19 through breach; Come side direction type feeding cylinder 19 endoporus and burner hearth charging aperture 1 endoporus are isolated, the right-hand member by movable bell 15 in the charging process seals discharging opening left end breach.

During the heat-exchange system operation; Under the situation of movable bell 15 sealings; Produce great amount of heat during fuel combustion in the fuel device 5 and come furnace charge 14 solution and burner hearth 2 inwalls in the heating furnace; The combustion air of fuel is produced by blower fan 7, and combustion air at first is transported in the heat exchanger 9 through Cryogenic air pipeline 8, on through Cryogenic air pipeline 8 during the molecular sieve adsorption separator 21 of serial connection; The inner molecular sieves of molecular sieve adsorption separator 21 filter out part nitrogen in the combustion air and other dust foreign material, reduced the combustion air total amount with improved combustion air contain the oxygen ratio; In heat exchanger 9; The heat exchange first time of combustion air and the furnace gas that gives up from the useless furnace gas that transports in the burner hearth, through burner hearth furnace gas export 24 and first order furnace gas pipeline 12; Combustion air with low temperature when useless furnace gas temperature reduces is heated into the high temperature combustion air more than 400 ℃, and the high temperature combustion air is transported to burner 5 through high temperature air pipeline 6; In burner 5; Reduced useless nitrogen amount with improved the high temperature combustion air that contains the oxygen ratio help fuel more fully, burning quickly; More release heat makes quickly in the burner hearth 2 and heats up, the also corresponding minimizing of useless furnace gas total amount that burning simultaneously produces; The heat that is lost to atmosphere through useless furnace gas correspondingly reduces, and so not only energy-conservation, aluminium decreases and also can reduce; In burner hearth 2; The end product of fuel and the burning of high temperature combustion air is useless furnace gas; Useless furnace gas is transported to heat exchanger 9 through burner hearth furnace gas export 24 and first order furnace gas pipeline 12; After finishing the heat exchange first time of useless furnace gas, furnace gas pipeline 13 and feeding cylinder furnace gas import 25 are transported in the side direction type feeding cylinder 19 through the second level, in side direction type feeding cylinder 19, finish the heat exchange second time of furnace gas of giving up, with after furnace charge 14 preheatings; Temperature reduces once more, less than 200 ℃ useless furnace gases through feeding cylinder furnace gas export 26, third level furnace gas pipeline 10 and deduster 11, be discharged in the atmospheric environment.

When 14 solution of the furnace charge in the burner hearth 2 be elevated to about 800 ℃, in the time of need adding furnace charge 14 again; Fuel device 5 burn-outs; Movable bell 15 is opened automatically; Side direction type feeding cylinder 19 and burner hearth 2 internal communication appear at breach between side direction type feeding cylinder 19 discharging opening end faces and burner hearth charging aperture 1 end face by the right-hand member sealing of heat insulation sheath 20 or the movable bell 15 of rectangle thereupon, are preheating to furnace charge 14 rapid free fallings that 300 ℃～400 ℃, the furnace charge 14 solution faces in burner hearth 2 have 1m～3m drop this moment to furnace charge 14 solution; Movable then bell 15 automatically resets and closes; To make things convenient for side direction type feeding cylinder 19 next stove furnace charge 14 to be installed, under the stirring action of mixer 4, furnace charge 14 dissolves very soon or has few part furnace charge 14 to swim on the furnace charge 14 solution faces flickeringly.

Present embodiment burner hearth charging aperture 1 can be on the sustained height with fire door 3.

Embodiment eight: as shown in Figure 8, the utility model mainly by burner hearth 2, be connected side direction type feeding cylinder 19 on the burner hearth charging aperture 1, be connected fuel device 5 on burner hearth 2 headwalls, be positioned at burner hearth 2 furnace bottoms mixer 4, be installed in burner hearth 2 outer heat-exchange systems and form; Described burner hearth charging aperture 1 is positioned at the right-hand member wall upper end of burner hearth 2, on burner hearth 2 front side walls, is shaped on two fire doors 3 of furnace charge 14 liquid levels in a little higher than stove, on the front side wall in the middle of two fire doors 3, is shaped on the burner hearth furnace gas export; Be shaped on the furnace gas import in the upper end of side direction type feeding cylinder 19, be shaped on furnace gas export in the lower end of side direction type feeding cylinder 19; Described heat-exchange system mainly is made up of heat exchanger 9, blower fan 7, side direction type feeding cylinder 19, Cryogenic air pipeline 8, high temperature air pipeline 6, first order furnace gas pipeline 12, second level furnace gas pipeline 13; Described Cryogenic air pipeline 8 is connecting heat exchanger 9 and blower fan 7; Described high temperature air pipeline 6 is connecting heat exchanger 9 and burner 5; Described first order furnace gas pipeline 12 is connecting the feeding cylinder furnace gas import 25 on burner hearth furnace gas export and the side direction type feeding cylinder 19, and described second level furnace gas pipeline 13 is connecting the feeding cylinder furnace gas export 26 of heat exchanger 9 and side direction type feeding cylinder 19; On described Cryogenic air pipeline 8, be serially connected with molecular sieve adsorption separator 21; On heat exchanger 9, be connected with third level furnace gas pipeline 10, on third level furnace gas pipeline 10 ends, be connected with deduster 11; Between the discharging opening of side direction type feeding cylinder 19 and burner hearth charging aperture 1, vertical movable bell 15 is installed.

During the heat-exchange system operation; Under the situation of movable bell 15 sealings; Produce great amount of heat during fuel combustion in the fuel device 5 and come furnace charge 14 solution and inboard wall of burner hearth in the heating furnace; The combustion air of fuel is produced by blower fan 7, and combustion air at first is transported in the heat exchanger 9 through Cryogenic air pipeline 8, on through Cryogenic air pipeline 8 during the molecular sieve adsorption separator 21 of serial connection; The inner molecular sieves of molecular sieve adsorption separator 21 filter out part nitrogen in the combustion air and other dust foreign material, reduced the combustion air total amount with improved combustion air contain the oxygen ratio; In heat exchanger 9; The give up heat exchange second time of furnace gas of combustion air and the useless furnace gas that transports through feeding cylinder furnace gas export 26 and second level furnace gas pipeline 13; Combustion air with low temperature when useless furnace gas temperature reduces is heated into the high temperature combustion air about 400 ℃, and the high temperature combustion air is transported to burner 5 through high temperature air pipeline 6; In burner 5; Reduced useless nitrogen amount with improved the high temperature combustion air that contains the oxygen ratio help fuel more fully, burning quickly; More release heat makes quickly in the burner hearth 2 and heats up, the also corresponding minimizing of useless furnace gas total amount that burning simultaneously produces; The heat that is lost to atmosphere through useless furnace gas correspondingly reduces, and so not only energy-conservation, aluminium decreases and also can reduce; In burner hearth 2; The end product of fuel and the burning of high temperature combustion air is useless furnace gas; Useless furnace gas is transported in the side direction type feeding cylinder 19 through burner hearth furnace gas export 24, first order furnace gas pipeline 12 and feeding cylinder furnace gas import 25; After finish the heat exchange first time of useless furnace gas with furnace charges 14 in the side direction type feeding cylinder 19, useless furnace gas is transported in the heat exchanger 9 through feeding cylinder furnace gas export 26 and second level furnace gas pipeline 13, heat exchanger 9 in and after combustion air finishes the heat exchange second time of the furnace gas that gives up; Temperature reduces once more, less than 200 ℃ useless furnace gases through third level furnace gas pipeline 10 and deduster 11, be discharged in the atmospheric environment.

When 14 solution of the furnace charge in the burner hearth 2 be elevated to about 800 ℃, in the time of need adding furnace charge 14 again; Fuel device 5 burn-outs; Movable bell 15 is opened automatically; Side direction type feeding cylinder 19 and burner hearth 2 internal communication appear at breach between side direction type feeding cylinder 19 discharging opening end faces and burner hearth charging aperture 1 end face by the right-hand member sealing of heat insulation sheath 20 or the movable bell 15 of rectangle thereupon, are preheating to furnace charge 14 rapid free fallings that furnace charge 14 solution about 400 ℃, in burner hearth 2 have 1m～3m drop this moment to furnace charge 14 solution; Movable then bell 15 automatically resets and closes; To make things convenient for side direction type feeding cylinder 19 next stove furnace charge 14 to be installed, under the stirring action of mixer 4, furnace charge 14 dissolves very soon or has few part furnace charge 14 to swim on the furnace charge 14 solution faces flickeringly.

Certainly, the utility model is not limited to above embodiment, the furnace gas of the utility model feeding cylinder import and export can to turn upside down in the position or left-right and front-back relatively, side by side; The utility model fire door 3 can be used as burner hearth charging aperture 1; The molecular sieve adsorption separator 21 of the utility model can be that 21 parallel connections of at least two cover molecular sieve adsorption separators are used; The utility model heat insulation sheath 20 also can be socketed in burner hearth charging aperture 1 outer wall; The utility model roller, third level furnace gas pipeline 10 and deduster 11 also can be selected for use according to circumstances; The utility model can also be applied to materials such as processed glass, pottery and indivedual ferrous metal except that being applied to processing aluminum materials material and other non-ferrous metals; The utility model can be obtained positive effect energy-conservation, that reduce discharging, reduce cost has relied on the booster action of mixer 4 to a certain extent, but also only under the utility model version, the booster action of mixer 4 can be obtained bigger effect.

Claims

1. industrial furnace of smelting non-ferrous metal; Comprise burner hearth (2), be connected feeding cylinder on the burner hearth charging aperture (1) of burner hearth (2), be connected burner (5) on the burner hearth (2), be installed in the outer heat-exchange system of burner hearth (2); Described heat-exchange system mainly is made up of heat exchanger (9), blower fan (7) and air pipe line; Between heat exchanger (9) and blower fan (7), interconnecting Cryogenic air pipeline (8); Between heat exchanger (9) and burner (5), interconnecting high temperature air pipeline (6); It is characterized in that: on burner hearth (2), be shaped on burner hearth furnace gas export (24), feeding cylinder is the part of heat-exchange system, and the furnace gas pipeline is connected burner hearth furnace gas export (24), heat exchanger (9) in aggregates with feeding cylinder.

2. a kind of industrial furnace of smelting non-ferrous metal according to claim 1; It is characterized in that: between burner hearth furnace gas export (24) and heat exchanger (9) or between burner hearth furnace gas export (24) and feeding cylinder furnace gas import (25), be connected first order furnace gas pipeline (12), correspondingly between heat exchanger (9) and feeding cylinder furnace gas import (25) or between heat exchanger (9) and feeding cylinder furnace gas export (26), be connected second level furnace gas pipeline (13).

3. a kind of industrial furnace of smelting non-ferrous metal according to claim 2 is characterized in that: movable bell (15) is installed between the discharging opening of burner hearth charging aperture (1) and feeding cylinder.

4. a kind of industrial furnace of smelting non-ferrous metal according to claim 3; It is characterized in that: burner hearth charging aperture (1) is positioned on the furnace roof or furnace wall of burner hearth (2); Burner hearth furnace gas export (24) is positioned on the furnace roof or furnace wall of burner hearth (2), and burner hearth charging aperture (1) is whole and burner hearth furnace gas export (24) integral body is higher than furnace charge (14) the solution face in the burner hearth (2).

5. a kind of industrial furnace of smelting non-ferrous metal according to claim 4; It is characterized in that: the feeding cylinder that docks with the burner hearth charging aperture (1) of furnace roof is any in rectilinear feeding cylinder (16) or oblique formula feeding cylinder (17), the bend formula feeding cylinder (18), and the feeding cylinder that docks with burner hearth charging aperture (1) on the furnace wall is side direction type feeding cylinder (19).

6. a kind of industrial furnace of smelting non-ferrous metal according to claim 5 is characterized in that: the discharging opening end face of any feeding cylinder in rectilinear feeding cylinder (16) or oblique formula feeding cylinder (17), the bend formula feeding cylinder (18) is higher than furnace charge (14) the solution face 100cm～500cm in the burner hearth (2) or is higher than the furnace roof face 0～400cm of burner hearth (2).

7. a kind of industrial furnace of smelting non-ferrous metal according to claim 6; It is characterized in that: on the bottom of the movable bell (15) of any feeding cylinder below in rectilinear feeding cylinder (16) or oblique formula feeding cylinder (17), bend formula feeding cylinder (18) roller is installed; On the same furnace wall of burner hearth (2), be shaped on two fire doors (3), on the furnace wall in the middle of two fire doors (3), be shaped on burner hearth furnace gas export (24).

8. according to the industrial furnace of claim 1,2,3,4,5,6 or 7 described any smelting non-ferrous metals, it is characterized in that: on Cryogenic air pipeline (8) or high temperature air pipeline (6), be serially connected with molecular sieve adsorption separator (21).

9. according to the industrial furnace of claim 3,4,5,6 or 7 described any smelting non-ferrous metals, it is characterized in that: on the other feeding cylinder outer wall of movable bell (15) or be socketed with heat insulation sheath (20) on burner hearth charging aperture (1) outer wall.

10. a kind of industrial furnace of smelting non-ferrous metal according to claim 9 is characterized in that: on Cryogenic air pipeline (8) or high temperature air pipeline (6), be serially connected with molecular sieve adsorption separator (21).