CN210426055U - Rock wool production kiln and rock wool production facility - Google Patents
Rock wool production kiln and rock wool production facility Download PDFInfo
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- CN210426055U CN210426055U CN201920820908.5U CN201920820908U CN210426055U CN 210426055 U CN210426055 U CN 210426055U CN 201920820908 U CN201920820908 U CN 201920820908U CN 210426055 U CN210426055 U CN 210426055U
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Abstract
The utility model provides a rock wool production kiln and rock wool production facility. The rock wool production kiln comprises a kiln body, a water cooling jacket, a spiral feeder, a vibrating feeder and a burner, wherein the water cooling jacket is wrapped on the outer wall of the kiln body, and the burner is installed at the bottom of the kiln body or on the side wall of the lower part of the kiln body. The immersed combustion mode is adopted, the fuel, the combustion-supporting gas and the raw materials are fully mixed and combusted, the fuel is directly sprayed into the raw materials, the heat transfer mode is improved, the melt is vigorously convected and stirred, the energy utilization rate is extremely high, and the energy utilization rate is 3 times that of a traditional kiln; the discharge amount of NOx is low, which is 2 times lower than that of the traditional kiln; small size and designed kiln area of 2-6m2The start and stop are convenient, large materials or powder can be melted, and the discharge amount can reach 30-100 t/d; the water-cooled furnace body is adopted, the service life of the furnace is long, the use of refractory materials is greatly reduced, and the dust emission is reduced by 10 times; and a CO treatment system is not needed, so that a large amount of equipment investment and operation cost are saved.
Description
Technical Field
The utility model relates to a rock wool production technical field, concretely relates to rock wool production kiln and rock wool production facility.
Background
At present, rock wool is mainly produced by a cupola furnace by using coke and ore raw materials. Not only is not environment-friendly, but also is contrary to the concept of low-carbon environment-friendly development due to the dependence on carbon. The Chinese government makes a commitment to the world solemn in the world climate congress of Copenhagen that the total carbon dioxide emission of the unit domestic production is reduced by 40% -45% in 2020 years and 2005. A new efficient and environment-friendly rock wool production technology is urgently needed. Although some existing carbon-free rock wool production processes adopt combustion modes of oxygen enrichment, pure oxygen and natural gas, the rock wool has a barrier effect on penetration of radiant heat, and the effect of melting and producing a large amount of glass through radiation of high-temperature pure oxygen flame is poor.
SUMMERY OF THE UTILITY MODEL
In order to overcome the defects of the prior art, the utility model aims at providing a rock wool production kiln and rock wool production equipment.
In order to achieve the above object, the technical solution of the present invention is: a rock wool production kiln comprising:
the furnace body is coated with a water cooling sleeve;
the spiral feeder is arranged at a first feeding port of the furnace body, and the first feeding port is positioned below the liquid level of melt in the furnace body during production;
the vibrating feeder is arranged at a second feeding port of the furnace body;
the burner is arranged at the bottom of the furnace body or on the side wall of the lower part of the furnace body, and a nozzle of the burner is immersed under the liquid level of the melt in the furnace body;
the flue is used for discharging waste gas in the furnace body during production and is arranged at the upper part of the furnace body;
and the material channel is used for discharging the melt in the furnace body.
Compared with the prior art, the utility model, adopt the submergence formula combustion mode, fuel and combustion-supporting gas and raw and other materials intensive mixing burning, the fuel is directly sprayed inside the raw materials, produce flame and burning in the raw materials and make the raw materials melt, the combustor is placed in the bottom of kiln, improved the heat transfer mode and produced violent convection stirring effect to the fuse-element, energy utilization is high, the super traditional kiln is more than 3 times; the discharge amount of NOx is low, which is 2 times lower than that of the traditional kiln; small size and designed kiln area of 2-6m2The start and stop are convenient, large materials or powder can be melted, and the discharge amount can reach 30-100 t/d; the water-cooled furnace body is adopted, the service life of the furnace is long, the use of refractory materials is greatly reduced, and the dust emission is reduced by 10 times; and a CO treatment system is not needed, so that a large amount of equipment investment and operation cost are saved.
Further, the burner includes:
the burner comprises a burner body, a burner cover and a burner cover, wherein the burner body comprises a nozzle panel, a gas chamber and a combustion-supporting gas chamber, a plurality of nozzles are uniformly arranged on the nozzle panel, the gas chamber and the combustion-supporting gas chamber are respectively distributed on two sides below the nozzle panel, and gas guide holes communicated with the nozzles from the gas chamber and the combustion-supporting gas chamber are formed in the nozzle panel;
the cooling water channel surrounds the periphery of the combustor body, a circle of semi-spacers are arranged in the cooling water channel, a water inlet and a water outlet of the cooling water channel are respectively located on two sides of the semi-spacers, and the water inlet and the water outlet are respectively distributed at two opposite ends of the combustor body.
Adopt above-mentioned preferred scheme, the rivers of heating produce the heat through the lateral wall and preheat gas and combustion air, have improved flame temperature and stability, reduce calorific loss.
Furthermore, the nozzle is a concave hemispherical groove, the gas guide holes communicated with the gas chamber and the combustion-supporting gas chamber are both linear, the two gas guide holes are arranged in a tangent manner with the nozzle, and the two gas guide holes are arranged in a diagonal manner at the opening of the inner wall of the nozzle.
By adopting the preferable scheme, at each nozzle, the fuel gas and the combustion-supporting gas are injected through opposite diagonal tangents to generate strong vortex mixing, so that the flame rotates upwards, and the upward penetrating power of the flame is improved.
Furthermore, the area of the bottom surface of the furnace body is less than 4m2The number of the burners is 2; the area of the bottom surface of the furnace body is 2m2On the basis of area, every 2m2Area, the number of said burners increases by 1.
By adopting the preferable scheme and adopting a reasonable number of combustors, the combustion efficiency is ensured, excessive flue gas generated by excessive combustion is prevented, and the emission is effectively reduced.
Further, the height of the first feeding port from the bottom surface of the furnace body is 15% -50% of the height of the liquid level of the melt in the furnace body during production.
By adopting the preferable scheme, the stable and orderly melting production can be ensured during normal production, and the fluctuation of the feeding in the small-space kiln to the combustion melting process is reduced.
Furthermore, the flue has an inclined part at the top of the furnace body, and a temperature measuring sensor is arranged at the upper part of the flue.
By adopting the preferable scheme, the inclined part can prevent the heat exchanger from being blocked, and the temperature sensor is arranged at the upper part of the flue, so that the temperature in the kiln can be detected more reliably.
Furthermore, an ignition rod is arranged on the combustor, and a flame detector is arranged on the ignition rod.
By adopting the preferable scheme, the combustor is provided with the ignition rod and the flame detection, and the self flame can be detected in real time in the ignition step.
Furthermore, the upper part of the side wall of the furnace body is provided with an openable furnace door, an ignition gun mechanism is arranged corresponding to the position of the furnace door, the ignition gun mechanism comprises an ignition gun, a telescopic mechanism and a swinging mechanism, the telescopic mechanism drives the ignition gun to move in a telescopic manner, and the swinging mechanism drives the telescopic mechanism and the ignition gun to swing together.
By adopting the preferable scheme, the structure of the burner can be simplified, and the kiln is ignited by a single external ignition gun, so that the configuration cost of the kiln is saved.
A rock wool production device comprises a rock wool production kiln, a fiberizer, a cotton collector and a curing furnace, wherein a material channel of the rock wool production kiln is communicated with the fiberizer, fibers blown by the fiberizer are pressed into rock wool fiber sheets through the cotton collector, and the rock wool fiber sheets are dried and cured into rock wool through the curing furnace.
The heat exchanger is communicated with a flue of the rock wool production kiln, and a heat circulation pipeline of the heat exchanger is also communicated with the curing furnace; the thermal circulation pipeline of the heat exchanger is also communicated with a raw material bin to be melted; the heat circulation pipeline of the heat exchanger is also communicated with a fuel gas supply pipeline and a combustion-supporting gas supply pipeline of the combustor.
Adopt above-mentioned preferred scheme, set submergence formula combustion method kiln, rock wool production efficiency is high, and the steady quality, the heat exchanger is fully synthesized the recycle with the flue gas heat, has practiced thrift energy resource consumption, reduction in production cost has reduced the pollutant discharge.
A production process of rock wool comprises the following steps,
the material preparation step: weighing the raw materials according to the material prescription, mixing well, and adding the raw materials into a bin of a spiral feeder and a vibratory feeder;
and (3) igniting: igniting the burner through an ignition system to enable the temperature in the kiln to reach a set temperature;
a material adding step: feeding materials simultaneously through a spiral feeder and a vibrating feeder, closing the vibrating feeder after the liquid level of the melt in the furnace reaches a set value, and adjusting the feeding amount through the spiral feeder to balance feeding and discharging so as to keep the melt in the furnace within a set liquid level range;
and (3) high-temperature melting temperature control step: controlling the furnace temperature to be kept within the range of 1100-1600 ℃ by adjusting the flow ratio of the fuel gas and the combustion-supporting gas of the combustor;
a fiber forming step: blowing the mixture into fibers through a fiberizer;
cotton collecting step: pressing the fibers into rock wool fibers with a certain thickness through a cotton collector;
and (3) curing: drying and curing the rock wool fiber with a certain thickness by a curing oven;
slicing: and (4) packaging the solidified rock wool slices according to the required specification to prepare a rock wool finished product.
By adopting the above preferred scheme, with the help of the immersed combustion mode, the flow ratio of the fuel gas and the combustion-supporting gas of the combustor adopts the double-cross amplitude limiting control, so that the air-fuel ratio is ensured to be kept stable during flow adjustment, the flow adjustment is not fluctuated, the quality of rock wool is more stable, and the production efficiency is high.
Further, the igniting step includes the steps of,
step A1: the ignition gun is pre-installed on an installation support outside the kiln, and a telescopic mechanism and a swinging mechanism are configured on the installation support; sequentially enabling an ignition gun to be close to the upper parts of the combustors to ignite the combustors;
step A2: after the last burner is ignited, the burner stays at the upper part of the burner, natural gas of the ignition gun is closed, outflow of combustion-supporting gas of the ignition gun is reserved, flame is continuously detected through a flame detector on the ignition gun, and the ignition is performed again if the flame is extinguished;
step A3: when the temperature of the kiln reaches above 850 ℃, the combustion-supporting gas of the ignition gun is closed, the kiln is withdrawn, and the kiln door is closed.
By adopting the preferable scheme, the burner is ignited by the external ignition gun, and the ignition gun can be started at any time when the kiln needs emergency heat preservation, so that the kiln can preserve heat.
Further, the igniting step includes the steps of,
step B1: the burner is provided with an ignition rod, and the ignition rod has a flame detection function; each burner is ignited through a respective ignition rod, flame is continuously detected, and if the flame is extinguished, the burner is ignited again;
step B2: when the temperature of the kiln reaches above 850 ℃, the flame detection function is waited, and the temperature of the kiln is detected through a temperature sensor.
By adopting the preferred scheme, each combustor is respectively and automatically provided with the ignition rod, so that the ignition stability and reliability are improved, and the flame of each combustor can be detected in real time.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to these drawings without creative efforts.
FIG. 1 is a schematic structural diagram of an embodiment of the present invention;
FIG. 2 is a schematic structural view of an embodiment of the burner of the present invention;
FIG. 3 is a sectional view of the structure taken along line A-A in FIG. 2;
fig. 4 is a process flow chart of rock wool production of the utility model.
Names of corresponding parts represented by numerals and letters in the drawings:
1-furnace body; 11-water cooling jacket; 12-a first feed inlet; 13-a second feed inlet; 14-flue; 15-material channel; 2-a burner; 21-a burner body; 211-a nozzle panel; 212-a nozzle; 213-air guide hole; 214-a gas chamber; 215-combustion gas chamber; 22-cooling water channel; 221-a water inlet; 222-a water outlet; 223-semi-septa.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative efforts belong to the protection scope of the present invention.
As shown in fig. 1, an embodiment of the present invention is: a rock wool production kiln comprising:
the furnace comprises a furnace body 1, wherein a water cooling jacket 11 is wrapped on the outer wall of the furnace body 1;
the spiral feeder is arranged at a first feeding port 12 of the furnace body 1, and the first feeding port 12 is positioned below the liquid level of melt in the furnace body during production;
the vibrating feeder is arranged at a second feeding port 13 of the furnace body 1;
the burner 2 is arranged at the bottom of the furnace body or on the side wall of the lower part of the furnace body, and a nozzle of the burner 2 is immersed under the liquid level of the melt in the furnace body;
a flue 14 for discharging exhaust gas in the furnace body at the time of production, which is provided at the upper part of the furnace body 1;
and the material channel 15 is used for discharging the melt in the furnace body, the material channel adopts an electric melting brick, and the discharging speed is adjusted by using a flashboard brick.
The beneficial effect of adopting above-mentioned technical scheme is: the submerged combustion mode is adopted, the fuel, the combustion-supporting gas and the raw materials are fully mixed and combusted, the fuel is directly sprayed into the raw materials, flame is generated in the raw materials and the raw materials are combusted to melt the raw materials, the combustor is placed at the bottom of the kiln, the heat transfer mode is improved, a violent convection stirring effect is generated on a melt, the energy utilization rate is extremely high, and the energy utilization rate is 3 times higher than that of a traditional kiln; the discharge amount of NOx is low, which is 2 times lower than that of the traditional kiln; small size and designed kiln area of 2-6m2The start and stop are convenient, large materials or powder can be melted, and the discharge amount can reach 30-100 t/d; the water-cooled furnace body is adopted, the service life of the furnace is long, the use of refractory materials is greatly reduced, and the dust emission is reduced by 10 times; without CO treatmentThe system saves a large amount of equipment investment and operation cost.
As shown in fig. 2 and 3, in other embodiments of the present invention, the burner 2 includes: the burner body 21 comprises a nozzle panel 211, a gas chamber 214 and a combustion-supporting gas chamber 215, wherein a plurality of nozzles 212 are uniformly arranged on the nozzle panel 211, the gas chamber 214 and the combustion-supporting gas chamber 215 are respectively distributed at two sides below the nozzle panel 211, and gas guide holes 213 which are respectively communicated with the nozzles 212 from the gas chamber 214 and the combustion-supporting gas chamber 215 are arranged on the nozzle panel 211; the cooling water channel 22 surrounds the periphery of the burner body 21, a circle of half spacers 223 are arranged in the cooling water channel 22, the water inlet 221 and the water outlet 222 of the cooling water channel 22 are respectively positioned at two sides of the half spacers 223, and the water inlet 221 and the water outlet 222 are respectively distributed at two opposite ends of the burner body 21. The combustion-supporting gas of the burner can adopt air, preheated air, oxygen enrichment or oxygen. The beneficial effect of adopting above-mentioned technical scheme is: the heated water flow generates heat through the side wall to preheat gas and combustion air, so that the flame temperature and stability are improved, and the heat loss is reduced.
As shown in fig. 2 and 3, in other embodiments of the present invention, the nozzle 212 is a concave hemispherical groove, the gas holes 213 connected to the gas chamber 214 and the gas holes 213 connected to the combustion supporting gas chamber 215 are both linear, and the two gas holes 213 are tangential to the nozzle 212, and the two gas holes 213 are diagonally disposed at the opening of the inner wall of the nozzle. The beneficial effect of adopting above-mentioned technical scheme is: at each nozzle, the fuel gas and the combustion-supporting gas are injected through opposite diagonal tangents, creating intense vortex mixing, thereby causing the flame to rotate upward, increasing the flame upward penetration.
In other embodiments of the present invention, the burner has an outer dimension of 150mm (W) x 600mm (L) and an area of less than 4m on the bottom surface of the furnace body2The number of the burners is 2; the area of the bottom surface of the furnace body is 2m2On the basis of area, every 2m2Area, the number of said burners increases by 1. The beneficial effect of adopting above-mentioned technical scheme is: adopts a reasonable number of burners to ensure the combustion efficiency and preventExcessive flue gas generated by excessive combustion is prevented, and emission is effectively reduced.
In other embodiments of the present invention, in order to better improve the heating efficiency, burners are installed at the bottom of the furnace body and the side wall of the lower part of the furnace body at the same time to have an area of 4m2The furnace is taken as an example, the approximate size of the furnace is 2400mm in length, 1650mm in width and 2000mm in height, the melt liquid level in the furnace is 1000mm approximately during normal production, 2 burners are installed on the bottom surface of the furnace body, in addition, 1 burner is installed on the lower portion of the side wall of the furnace body opposite to the material channel, thus, vertical and horizontal dual heat convection stirring conduction is formed, the heat impact force of the burners on the side wall also promotes the melt to flow to the material channel end, the circulating residue of the melt in the furnace is reduced, and the production efficiency is improved.
In other embodiments of the present invention, the height of the first feeding port 12 from the bottom surface of the furnace body is 15% -50% of the height of the liquid level of the melt in the furnace body during production. The beneficial effect of adopting above-mentioned technical scheme is: the method ensures that the furnace can be stably and orderly melted and produced during normal production, and reduces the fluctuation of the combustion and melting process caused by feeding materials into the small-space kiln.
In other embodiments of the present invention, the flue has an inclined portion at the top of the furnace body, and the temperature measuring sensor is disposed on the upper portion of the flue. The beneficial effect of adopting above-mentioned technical scheme is: the inclined part can prevent the heat exchanger from being blocked, and the temperature sensor is arranged on the upper part of the flue and can more reliably detect the temperature in the kiln.
In other embodiments of the present invention, an ignition rod is disposed on the burner, and a flame detector is disposed on the ignition rod. The beneficial effect of adopting above-mentioned technical scheme is: the self-contained ignition rod and flame detection of the combustor are adopted, and the self flame can be detected in real time in the ignition step.
The utility model discloses an in other embodiments, furnace body lateral wall upper portion is equipped with open closed furnace gate, is equipped with burning torch mechanism corresponding to the furnace gate position, burning torch mechanism includes burning torch, telescopic machanism and swing mechanism, the telescopic machanism drive burning torch is flexible to be removed, swing mechanism drives telescopic machanism and burning torch are done the swing together. The beneficial effect of adopting above-mentioned technical scheme is: the structure of the burner can be simplified, and the kiln configuration cost is saved by igniting through a single external ignition gun.
A rock wool production device comprises a rock wool production kiln, a fiberizer, a cotton collector and a curing furnace, wherein a material channel of the rock wool production kiln is communicated with the fiberizer, fibers blown by the fiberizer are pressed into rock wool fiber sheets through the cotton collector, and the rock wool fiber sheets are dried and cured into rock wool through the curing furnace.
In other embodiments of the present invention, the heat exchanger is further included, a flue of the rock wool production kiln is communicated with the heat exchanger and the flue gas treatment system, and a thermal circulation pipeline of the heat exchanger is further communicated with the curing oven; the thermal circulation pipeline of the heat exchanger is also communicated with a raw material bin to be melted; the heat circulation pipeline of the heat exchanger is also communicated with a fuel gas supply pipeline and a combustion-supporting gas supply pipeline of the combustor. The beneficial effect of adopting above-mentioned technical scheme is: the integrated submerged combustion kiln has the advantages that rock wool production efficiency is high, quality is stable, the heat exchanger fully and comprehensively recycles heat of flue gas, energy consumption is saved, production cost is reduced, and pollution emission is reduced.
As shown in fig. 4, a rock wool production process includes the following steps,
the material preparation step: weighing the raw materials according to the material prescription, mixing well, and adding the raw materials into a bin of a spiral feeder and a vibratory feeder;
and (3) igniting: igniting the burner through an ignition system to enable the temperature in the kiln to reach a set temperature;
a material adding step: feeding materials simultaneously through a spiral feeder and a vibrating feeder, closing the vibrating feeder after the liquid level of the melt in the furnace reaches a set value, and adjusting the feeding amount through the spiral feeder to balance feeding and discharging so as to keep the melt in the furnace within a set liquid level range;
and (3) high-temperature melting temperature control step: controlling the furnace temperature to be kept within the range of 1100-1600 ℃ by adjusting the flow ratio of the fuel gas and the combustion-supporting gas of the combustor;
a fiber forming step: blowing the mixture into fibers through a fiberizer;
cotton collecting step: pressing the fibers into rock wool fibers with a certain thickness through a cotton collector;
and (3) curing: drying and curing the rock wool fiber with a certain thickness by a curing oven;
slicing: and (4) packaging the solidified rock wool slices according to the required specification to prepare a rock wool finished product.
The beneficial effect of adopting above-mentioned technical scheme is: by means of an immersed combustion mode, the flow ratio of fuel gas and combustion-supporting gas of the combustor is controlled by double-cross amplitude limiting, the air-fuel ratio is guaranteed to be stable during flow adjustment, flow adjustment is not fluctuated, the quality of rock wool is more stable, and the production efficiency is high.
In other embodiments of the present invention, the igniting step comprises the steps of,
step A1: the ignition gun is pre-installed on an installation support outside the kiln, and a telescopic mechanism and a swinging mechanism are configured on the installation support; sequentially enabling an ignition gun to be close to the upper parts of the combustors to ignite the combustors;
step A2: after the last burner is ignited, the burner stays at the upper part of the burner, natural gas of the ignition gun is closed, outflow of combustion-supporting gas of the ignition gun is reserved, flame is continuously detected through a flame detector on the ignition gun, and the ignition is performed again if the flame is extinguished;
step A3: when the temperature of the kiln reaches above 850 ℃, the combustion-supporting gas of the ignition gun is closed, the kiln is withdrawn, and the kiln door is closed.
The beneficial effect of adopting above-mentioned technical scheme is: the burner is ignited by the external ignition gun, and the ignition gun can be started at any time when the kiln needs to be insulated emergently for heat insulation of the kiln.
In other embodiments of the present invention, the igniting step comprises the steps of,
step B1: the burner is provided with an ignition rod, and the ignition rod has a flame detection function; each burner is ignited through a respective ignition rod, flame is continuously detected, and if the flame is extinguished, the burner is ignited again;
step B2: when the temperature of the kiln reaches above 850 ℃, the flame detection function is waited, and the temperature of the kiln is detected through a temperature sensor.
The beneficial effect of adopting above-mentioned technical scheme is: each combustor is respectively provided with an ignition rod, so that the ignition stability and reliability are improved, and the flame of each combustor can be detected in real time.
The above embodiments are only for illustrating the technical conception and the features of the present invention, and the purpose thereof is to enable those skilled in the art to understand the contents of the present invention and implement the present invention, and the protection scope of the present invention can not be limited thereby, and all equivalent changes or modifications made according to the spirit of the present invention should be covered in the protection scope of the present invention.
Claims (10)
1. A rock wool production kiln, characterized by includes:
the furnace body is coated with a water cooling sleeve;
the spiral feeder is arranged at a first feeding port of the furnace body, and the first feeding port is positioned below the liquid level of melt in the furnace body during production;
the vibrating feeder is arranged at a second feeding port of the furnace body;
the burner is arranged at the bottom of the furnace body or on the side wall of the lower part of the furnace body, and a nozzle of the burner is immersed under the liquid level of the melt in the furnace body;
the flue is used for discharging waste gas in the furnace body during production and is arranged at the upper part of the furnace body;
and the material channel is used for discharging the melt in the furnace body.
2. The rock wool production kiln of claim 1, wherein the burner comprises:
the burner comprises a burner body, a burner cover and a burner cover, wherein the burner body comprises a nozzle panel, a gas chamber and a combustion-supporting gas chamber, a plurality of nozzles are uniformly arranged on the nozzle panel, the gas chamber and the combustion-supporting gas chamber are respectively distributed on two sides below the nozzle panel, and gas guide holes communicated with the nozzles from the gas chamber and the combustion-supporting gas chamber are formed in the nozzle panel;
the cooling water channel surrounds the periphery of the combustor body, a circle of semi-spacers are arranged in the cooling water channel, a water inlet and a water outlet of the cooling water channel are respectively located on two sides of the semi-spacers, and the water inlet and the water outlet are respectively distributed at two opposite ends of the combustor body.
3. The kiln as claimed in claim 2, wherein the nozzle is a concave hemispherical groove, the gas holes connected to the gas chamber and the gas holes connected to the combustion gas chamber are both linear, and the two gas holes are arranged tangentially to the nozzle and diagonally to the opening of the inner wall of the nozzle.
4. The rock wool production kiln as claimed in claim 1, wherein the area of the bottom surface of the kiln body is less than 4m2The number of the burners is 2; the area of the bottom surface of the furnace body is 2m2On the basis of area, every 2m2Area, the number of said burners increases by 1.
5. The rock wool production kiln of claim 1, wherein the height of the first feeding port from the bottom surface of the furnace body is 15% -50% of the height of the liquid level of the melt in the furnace body during production.
6. The kiln for rock wool production according to claim 1, wherein the flue has an inclined portion at the top of the furnace body, and a temperature sensor is provided at the upper portion of the flue.
7. The rock wool production kiln as claimed in claim 1, wherein an ignition rod is arranged on the burner, and a flame detector is arranged on the ignition rod.
8. The kiln as claimed in claim 1, wherein the upper part of the side wall of the kiln body is provided with an openable and closable kiln door, the position corresponding to the kiln door is provided with an ignition gun mechanism, the ignition gun mechanism comprises an ignition gun, a telescopic mechanism and a swing mechanism, the telescopic mechanism drives the ignition gun to move telescopically, and the swing mechanism drives the telescopic mechanism and the ignition gun to swing together.
9. A rock wool production facility, characterized by that, including the rock wool production kiln of any one of claims 1-8, fiberizer, cotton collector and curing oven, the material channel of the rock wool production kiln communicates with the fiberizer, the fiber that the fiberizer blows is pressed into the rock wool fiber slice through the cotton collector, and then is cured into rock wool through the curing oven.
10. The rock wool production equipment as claimed in claim 9, further comprising a heat exchanger, wherein the flue of the rock wool production kiln is communicated with the heat exchanger and the flue gas treatment system, and the heat circulation pipeline of the heat exchanger is also communicated with the curing furnace; the thermal circulation pipeline of the heat exchanger is also communicated with a raw material bin to be melted; the heat circulation pipeline of the heat exchanger is also communicated with a fuel gas supply pipeline and a combustion-supporting gas supply pipeline of the combustor.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920820908.5U CN210426055U (en) | 2019-06-02 | 2019-06-02 | Rock wool production kiln and rock wool production facility |
| PCT/CN2019/119664 WO2020244165A1 (en) | 2019-06-02 | 2019-11-20 | Rock wool production kiln, device and process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920820908.5U CN210426055U (en) | 2019-06-02 | 2019-06-02 | Rock wool production kiln and rock wool production facility |
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| CN210426055U true CN210426055U (en) | 2020-04-28 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116835876A (en) * | 2023-07-07 | 2023-10-03 | 中国矿业大学(北京) | Solid waste fusion vitrification and fiberization system and method |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116835876A (en) * | 2023-07-07 | 2023-10-03 | 中国矿业大学(北京) | Solid waste fusion vitrification and fiberization system and method |
| CN116835876B (en) * | 2023-07-07 | 2024-08-06 | 中国矿业大学(北京) | Solid waste fusion vitrification and fiberization system and method |
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