CN104193164A - Equipment for producing andesite continuous fiber and method for producing continuous fiber through equipment - Google Patents
Equipment for producing andesite continuous fiber and method for producing continuous fiber through equipment Download PDFInfo
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- CN104193164A CN104193164A CN201410453123.0A CN201410453123A CN104193164A CN 104193164 A CN104193164 A CN 104193164A CN 201410453123 A CN201410453123 A CN 201410453123A CN 104193164 A CN104193164 A CN 104193164A
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- 239000000835 fiber Substances 0.000 title claims abstract description 68
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 22
- 238000002844 melting Methods 0.000 claims abstract description 73
- 230000008018 melting Effects 0.000 claims abstract description 73
- 238000010438 heat treatment Methods 0.000 claims abstract description 15
- 239000011521 glass Substances 0.000 claims abstract description 9
- 239000007788 liquid Substances 0.000 claims abstract description 8
- 239000000463 material Substances 0.000 claims abstract description 6
- 238000007493 shaping process Methods 0.000 claims description 57
- 238000000265 homogenisation Methods 0.000 claims description 36
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims description 29
- 238000005491 wire drawing Methods 0.000 claims description 15
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 14
- 238000002485 combustion reaction Methods 0.000 claims description 9
- 239000007789 gas Substances 0.000 claims description 8
- 238000007654 immersion Methods 0.000 claims description 7
- 238000000034 method Methods 0.000 claims description 7
- 239000003345 natural gas Substances 0.000 claims description 7
- 230000015572 biosynthetic process Effects 0.000 claims description 3
- 238000005265 energy consumption Methods 0.000 abstract description 7
- 238000011031 large-scale manufacturing process Methods 0.000 abstract 1
- 239000000156 glass melt Substances 0.000 description 12
- 101100194816 Caenorhabditis elegans rig-3 gene Proteins 0.000 description 6
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 6
- 239000003546 flue gas Substances 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 5
- 238000007380 fibre production Methods 0.000 description 5
- 239000006060 molten glass Substances 0.000 description 4
- 230000008901 benefit Effects 0.000 description 3
- 238000005352 clarification Methods 0.000 description 3
- 235000009508 confectionery Nutrition 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000010309 melting process Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 150000002829 nitrogen Chemical class 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000009738 saturating Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- CCEKAJIANROZEO-UHFFFAOYSA-N sulfluramid Chemical group CCNS(=O)(=O)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F CCEKAJIANROZEO-UHFFFAOYSA-N 0.000 description 1
Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/50—Glass production, e.g. reusing waste heat during processing or shaping
- Y02P40/57—Improving the yield, e-g- reduction of reject rates
Landscapes
- Glass Melting And Manufacturing (AREA)
Abstract
The invention discloses equipment for producing andesite continuous fiber and a method for producing continuous fiber through the equipment. The equipment comprises a feeding device, a heat exchange device, a heating device and a tank furnace, wherein the tank furnace includes a melting zone, a homogenizing zone, forming zones and a flue; a material outlet of the feeding device is communicated with the melting zone; the upper half part of the melting zone is communicated with the homogenizing zone; the flue is connected at the back of the forming zones; the heat exchange device is arranged at the top of the back end of the tank furnace; the heat exchange device is communicated with the flue; the at least two forming zones are arranged at the back of the homogenizing zone; at least two drain plates are arranged in the forming zones; and the heating device comprises an immersed burner, a sidewall burner and a crown burner. The equipment for producing andesite continuous fiber disclosed by the invention is simple in structure and low in cost, and is capable of melting much glass liquid within unit time and effectively improving production efficiency of the andesite continuous fiber for at least three times; the equipment improves production scale, saves energy consumption and realizes large-scale production of continuous fiber.
Description
Technical field
The present invention relates to a kind of continuous fibre production unit, particularly relate to a kind of equipment of producing andesite continuous fibre.
The invention still further relates to the method for the device fabrication continuous fibre that utilizes this production andesite continuous fibre.
Background technology
Andesite ore is the main ore of a kind of volcano slurry, has good chemical stability and thermostability.Andesite fusing is different from the batch melting process in glass production, there is no silicate reaction, and homogenizing clarification also has larger difference with glass production.The chemical composition change of the andesite in the same place of production is very little, and foreign matter content has fluctuation a little.The fiber of being made up of andesite has good performance: Heat stability is good, and use critical temperature large, corrosion resistance and good, tensile strength is high, and Young's modulus is high, good insulation preformance etc.Can be widely used in shipbuilding, automobile, space flight, aviation, the numerous areas such as building, application prospect is extensive.China has abundant andesite ore resource, but because andesite ore is a kind of infusibility material, melt diathermancy is poor, the features such as glass material property is shorter, and viscosity is large are only small-scale production at present, it is all generally electrically heated, and well heater is positioned at top, like this because heat is limited, and only heating is local, therefore the melting efficiency of andesite is not high, and then to make andesite continuous fibre can only be to produce in small tank furnace on a small scale, efficiency is very low, and cost is high.The degree of depth of melting area is superficial, and in the unit time, the glass metal of fusing is fewer, can not meet the requirement of producing andesite continuous fibre in enormous quantities.Therefore up to the present produce andesite continuous fibre and also there is no large-scale flame furnace.
Summary of the invention
The present invention completes in order to solve deficiency of the prior art, the object of this invention is to provide a kind of simple in structure, cost is low, unit time molten glass liquid is more, effectively improve andesite continuous fibre production efficiency more than at least three times, improve industrial scale, save energy consumption, realize the equipment of the production andesite continuous fibre of continuous fibre scale operation.
A kind of equipment of producing andesite continuous fibre of the present invention, comprise charging device, heat-exchanger rig, heating unit and be arranged at the charging device in front and the described heat-exchanger rig at rear between tank furnace, described tank furnace is melting area from front to back, homogenization zone, shaping area and flue, the discharge port of described charging device is communicated with described melting area, described melting area upper part is communicated with described homogenization zone, rear, described shaping area is connected with flue, the top, rear end of described tank furnace is provided with heat-exchanger rig, described heat-exchanger rig is communicated with described flue, rear, described homogenization zone is symmetrically arranged with at least two shaping areas, described shaping area is disposed with at least two bushings, described heating unit comprises the submersible burning device that is positioned at bottom, melting area, be positioned at the side wall burner on the sidewall of described melting area and be positioned on arch top, described melting area and be provided with towards the arch top of melting area burner.
A kind of equipment of producing andesite continuous fibre of the present invention can also be:
Described submersible burning device, side wall burner and arch top burner are pure oxygen combustor.
The evenly distributed gas jet that is furnished with at least two pure oxygen burnings on two side, each described shaping area, the gas jet position of described pure oxygen burning is higher than described shaping area inner melt liquid level.
The submersible burning device of bottom, described melting area is the natural air gun of pure oxygen immersion, and middle part, described melting area is provided with at least three natural air guns of pure oxygen immersion, and described arch top burner is pure oxygen rifle, and described side wall burner is pure oxygen combustion of natural gas rifle.
Described heat-exchanger rig is metallic recuperator, and described metallic recuperator is arranged at described flue top, and described metallic recuperator top is provided with chimney, and described chimney top is provided with adjustable plate.
In described tank furnace, be provided with weir, described weir tiling arranges bottom, described homogenization zone.
Bottom, described melting area is at least provided with row's bubbler, and described bubbler is parallel with described submersible burning device.
Between described homogenization zone and described shaping area, be communicated with by path, described shaping area respectively symmetry is positioned at described path both sides, and described shaping area number is even number.
Between described homogenization zone and described shaping area, be provided with glass separating device.
A kind of equipment of producing andesite continuous fibre of the present invention, comprise charging device, heat-exchanger rig, heating unit and be arranged at the charging device in front and the described heat-exchanger rig at rear between tank furnace, described tank furnace is melting area from front to back, homogenization zone, shaping area and flue, the discharge port of described charging device is communicated with described melting area, described melting area upper part is communicated with described homogenization zone, rear, described shaping area is connected with flue, the top, rear end of described tank furnace is provided with heat-exchanger rig, described heat-exchanger rig is communicated with described flue, rear, described homogenization zone is symmetrically arranged with at least two shaping areas, described shaping area is disposed with at least two bushings, described heating unit comprises the submersible burning device that is positioned at bottom, melting area, be positioned at the side wall burner on the sidewall of described melting area and be positioned on arch top, described melting area and be provided with towards the arch top of melting area burner.Like this, when enough andesites are dropped in tank furnace and enter melting area with charging device, arch top burner, side wall burner and lower submerged formula burner burn simultaneously, the evolution of heat simultaneously, can melt rapidly and in a large number andesite, make the overall tank furnace degree of depth can be very dark, the andesite amount that drops into fusing is huge, the comprehensive combustion heating in top sidepiece and bottom, the andesite of enormous amount is melted rapidly and carry out homogenizing, glass melt after homogenizing enters in the multiple shaping areas that are symmetricly set on rear, homogenization zone prepares andesite continuous fibre by multiple bushing wire drawings, the amount of glass melt producing due to the unit time is larger, therefore the advantage having is in terms of existing technologies: it can be realized extensive one-tenth completely and produce, save time, reduce costs, improve output capacity, energy-conservation energy consumption.
Another object of the present invention is to provide one and utilizes that said structure is simple, cost is low, unit time molten glass liquid is more, effectively improve andesite continuous fibre production efficiency more than at least three times, improve industrial scale, save energy consumption, realize the method for the device fabrication continuous fibre of the production andesite continuous fibre of continuous fibre scale operation.
The method of the device fabrication continuous fibre of andesite continuous fibre is produced in utilization of the present invention, comprises the following steps:
A. charging: andesite material is delivered in tank furnace by charging device, falls in melting area;
B. heat fused: open be positioned at melting area bottom submersible burning device, be positioned at the side wall burner on the sidewall of melting area and be positioned at the arch top burner on arch top, melting area, make temperature in melting area be increased to the fusing point higher than andesite, andesite is molten into andesite liquation;
C. homogenizing: andesite liquation flows to homogenization zone and carries out homogenizing, and enters shaping area;
D. forming wire drawing: the andesite liquation after homogenizing leaks down to carry out wire drawing from the bushing in shaping area and forms continuous fibre;
E. reel and produce: below bushing, be provided with after coiler is reeled the continuous fibre of wire drawing formation and go out finished product.
By above-mentioned steps and utilize the equipment of the andesite continuous fibre of foregoing description, can cost low, unit time molten glass liquid is more, effectively improve andesite continuous fibre production efficiency more than at least three times, improve industrial scale, save energy consumption, realize continuous fibre scale operation.
Brief description of the drawings
A kind of apparatus embodiments schematic diagram of producing andesite continuous fibre of Fig. 1 the present invention.
A kind of equipment sectional view of producing andesite continuous fibre of Fig. 2 the present invention.
Figure number explanation
1 ... charging device 2 ... tank furnace 3 ... heat-exchanger rig
4 ... melting area 5 ... homogenization zone 6 ... shaping area
7 ... flue 8 ... bushing 9 ... submersible burning device
10 ... side wall burner 11 ... arch top burner 12 ... gas jet
13 ... chimney 14 ... adjustable plate 15 ... weir
16 ... bubbler 17 ... path 18 ... glass separating device
Embodiment
A kind ofly produce the equipment of andesite continuous fibre and utilize the method for this device fabrication continuous fibre to be described in further detail of the present invention below in conjunction with Fig. 1 to Fig. 2 of accompanying drawing.
A kind of equipment of producing andesite continuous fibre of the present invention, please refer to Fig. 1 to Fig. 2, comprise charging device 1, heat-exchanger rig 3, heating unit and be arranged at the charging device 1 in front and the described heat-exchanger rig 3 at rear between tank furnace 2, described tank furnace 2 is melting area 4 from front to back, homogenization zone 5 and shaping area 6 and flue 7, the discharge port of described charging device 1 is communicated with described melting area 4, described melting area 4 upper part are communicated with described homogenization zone 5, 6 rears, described shaping area are connected with flue 7, the top, rear end of described tank furnace 2 is provided with heat-exchanger rig 3, described heat-exchanger rig 3 is communicated with described flue 7, 5 rears, described homogenization zone are symmetrically arranged with at least two shaping areas 6, described shaping area 6 is disposed with at least two bushings 8, described heating unit comprises the submersible burning device 9 that is positioned at 4 bottoms, melting area, be positioned at the side wall burner 10 on 4 sidewalls of described melting area and be positioned on 4 arch tops, described melting area and be provided with towards the arch top of melting area 4 burner 11.Particularly, charging device 1 is for to the interior input andesite of tank furnace 2 raw material, 3 of heat-exchanger rigs are that the flue-gas temperature of avoiding tank furnace 2 to produce the heat in tank furnace 2 and extraneous heat exchange is too high, and heating unit is for heating and make it be molten into glass melt the andesite in melting area 4.Tank furnace 2 is large tank furnace used 2, and size is more much larger than current continuous fibre tank furnace 2.Melting area 4 is for melting andesite, homogenization zone 5 is for the andesite glass melt of homogenizing fusing, the effect of shaping area 6 is that forming wire drawing forms continuous fibre, melting area 4 upper part are communicated with homogenization zone 5, make in the glass melt after fusing relatively clear saturating part enter homogenization zone 5 and carry out homogenizing, after homogenizing, enter shaping area 6 moulding, flue 7 effects that connect at 6 rears, shaping area are that the flue gas in melting area 4, homogenization zone 5 and shaping area 6 in tank furnace 2 is discharged again.The heat-exchanger rig 3 on tank furnace 2 tops, for reducing the temperature of discharge flue gas, is convenient to carry out flue gas processing, reaches national environmental protection emission request.Like this, when enough andesites are dropped into and enter melting area 4 in tank furnace 2 with charging device 1, arch top burner 11, side wall burner 10 and lower submerged formula burner 9 burn simultaneously, the evolution of heat simultaneously, can melt rapidly and in a large number andesite, make overall tank furnace 2 degree of depth can be very dark, the andesite amount that drops into fusing is huge, the comprehensive combustion heating in top sidepiece and bottom, the andesite of enormous amount is melted rapidly and carry out homogenizing, glass melt after homogenizing enters in the multiple shaping areas 6 that are symmetricly set on 5 rears, homogenization zone prepares andesite continuous fibre by multiple bushing 8 wire drawings, the amount of glass melt producing due to the unit time is larger, therefore the advantage having is in terms of existing technologies: it can be realized extensive one-tenth completely and produce, save time, reduce costs, improve output capacity, save energy consumption.In addition, bushing most preferably is the evenly distributed bottom, shaping area that is arranged in, and production efficiency is high like this, and glass melt good flowing properties, and continuous fibre conforming product rate is high, good evenness.And submersible burning device, side wall burner and arch top burner comparative optimization be evenly distributed on described melting area arch top, melting area sidewall and bottom, described melting area, or be equidistantly arranged as multiple row or come arch top, melting area, melting area sidewall and bottom, described melting area more.Like this, after burning, port coverage is large, and flame temperature is high, and flame temperature is more or less the same everywhere, and bath surface can be heated equably, continuous fibre better quality.Shaping area is elongated rectangular shape shape, and described bushing is also elongated rectangular shape shape.Bushing is arranged in a row along shaping area length direction.
A kind of equipment of producing andesite continuous fibre of the present invention, please refer to Fig. 1 to Fig. 2, on the basis of previously described technical scheme, can be specifically: described submersible burning device 9, side wall burner 10 and arch top burner 11 are pure oxygen combustor.The all burners that use in the equipment of whole production andesite continuous fibre are like this pure oxygen combustor, like this, do not need to consider the problem of the nitrogen discharge that uses air burner, because contain 70% nitrogen in air, this nitrogen can not consume in combustion processes again, need to discharge, if but direct discharge may have the problem of contaminate environment, is sufficient combustion and use the advantage of pure oxygen combustor, thermal value efficiency is high, energy-conserving and environment-protective simultaneously, environmental sound.Further preferred technical scheme is the evenly distributed gas jet 12 that is furnished with at least two pure oxygen burnings on 6 two sides, each described shaping area, and gas jet 12 positions of described pure oxygen burning are higher than described shaping area 6 inner melt liquid levels.Like this, glass melt in shaping area 6 is further heated, avoids, because glass melt is long the solidifying of the interior flowing time in large-scale homogenization zone 5 and shaping area 6, further ensureing the production efficiency of andesite continuous fibre, improve yield rate, ensure the temperature requirement of wire drawing andesite continuous fibre.The submersible burning device 9 that can also be 4 bottoms, described melting area is the natural air gun of pure oxygen immersion, 4 middle parts, described melting area are provided with at least three natural air guns of pure oxygen immersion, described arch top burner 11 is pure oxygen rifle, and described side wall burner 10 is pure oxygen combustion of natural gas rifle.The natural air gun of pure oxygen immersion is submersible burning, the natural air gun of pure oxygen and Sweet natural gas mixed firing.And arch top burner 11 is pure oxygen rifle, pure oxygen rifle scope is larger, as long as pure oxygen burning, its fuel can be that Sweet natural gas can be also heavy oil or other fuel.Side wall burner 10 is pure oxygen combustion of natural gas rifle, and its fuel is Sweet natural gas.Efficiency of combustion is higher like this.
A kind of equipment of producing andesite continuous fibre of the present invention, please refer to Fig. 1 to Fig. 2, on the basis of previously described technical scheme, can also be: described heat-exchanger rig 3 is metallic recuperator, described metallic recuperator is arranged at described flue 7 tops, described metallic recuperator top is provided with chimney 13, and described chimney 13 tops are provided with adjustable plate 14.Chimney 13 is for all flue gas is discharged, and adjustable plate 14 is for regulating the opening aperture at chimney 13 tops, and then the speed that regulates flue gas to flow out, final for regulating the pressure in tank furnace 2.
A kind of equipment of producing andesite continuous fibre of the present invention, please refer to Fig. 1 to Fig. 2, on the basis of previously described technical scheme, can also be: in described tank furnace 2, be provided with weir 15, described weir 15 tilings arrange 5 bottoms, described homogenization zone.It is better that weir 15 makes homogenization zone 5 homo-effects like this, and more upper strata homo-effect is better in homogenization zone 5, glass melt best homo-effect is delivered to shaping area 6 wire drawings and forms continuous fibre.Can also be: 4 bottoms, described melting area are at least provided with row's bubbler 16, and described bubbler 16 is parallel with described submersible burning device 9.Blast pressurized gas by bubbler 16 to melting area 4, the one, play certain stirring action, improve the temperature of liquation, force fusing, the 2nd, accelerate to eliminate the bubble in liquation, accelerate the speed of clarification.Can also be to be communicated with by path 17 between described homogenization zone 5 and described shaping area 6, described shaping area 6 respectively symmetry be positioned at described path 17 both sides, and described shaping area 6 numbers are even number.Glass melt after the 5 homogenizing clarifications of homogenization zone enters respectively in each shaping area 6 by each path 17 simultaneously like this, form as far as possible many continuous tows from the wire-drawing shape that leaks down of the multiple bushings 8 in each shaping area 6, and then ensure to produce a large amount of continuous fibres simultaneously.Certainly shaping area 6 can be four, six, eight or more even number, as long as even number is arranged on 5 rears, homogenization zone symmetrically.The quantity of shaping area 6 is more, and the scale that becomes to produce continuous fibre is larger.Can also be to be provided with glass separating device 18 between described homogenization zone 5 and described shaping area 6.
The method of the device fabrication continuous fibre that utilizes previously described production andesite continuous fibre of the present invention, please refer to Fig. 1 to Fig. 2, comprises the following steps:
A. charging: andesite material is delivered in tank furnace 2 by charging device 1, falls in melting area 4;
B. heat fused: open be positioned at 4 bottoms, melting area submersible burning device 9, be positioned at the side wall burner 10 on 4 sidewalls of melting area and be positioned at the arch top burner 11 on 4 arch tops, melting area, make the interior temperature in melting area 4 be increased to the fusing point higher than andesite, andesite is molten into andesite liquation;
C. homogenizing: andesite liquation flows to homogenization zone 5 and carries out homogenizing, and enters shaping area 6;
D. forming wire drawing: the andesite liquation after homogenizing leaks down to carry out wire drawing from the bushing 8 in shaping area 6 and forms continuous fibre;
E. reel and produce: below bushing 8, be provided with after coiler is reeled the continuous fibre of wire drawing formation and go out finished product.
By above-mentioned steps and utilize the equipment of the andesite continuous fibre of foregoing description, can cost low, unit time molten glass liquid is more, effectively improve andesite continuous fibre production efficiency more than at least three times, improve industrial scale, save energy consumption, realize continuous fibre scale operation.
Above-mentionedly only several specific embodiments in the present invention are illustrated; but can not serve as protection scope of the present invention; every equivalence variation of having done according to the design spirit in the present invention or modification or equal proportion zoom in or out etc., all should think and fall into protection scope of the present invention.
Claims (10)
1. produce the equipment of andesite continuous fibre for one kind, it is characterized in that: comprise charging device, heat-exchanger rig, heating unit and be arranged at the charging device in front and the described heat-exchanger rig at rear between tank furnace, described tank furnace is melting area from front to back, homogenization zone, shaping area and flue, the discharge port of described charging device is communicated with described melting area, described melting area upper part is communicated with described homogenization zone, rear, described shaping area is connected with flue, the top, rear end of described tank furnace is provided with heat-exchanger rig, described heat-exchanger rig is communicated with described flue, rear, described homogenization zone is symmetrically arranged with at least two shaping areas, described shaping area is disposed with at least two bushings, described heating unit comprises the submersible burning device that is positioned at bottom, melting area, be positioned at the side wall burner on the sidewall of described melting area and be positioned on arch top, described melting area and be provided with towards the arch top of melting area burner.
2. a kind of equipment of producing andesite continuous fibre according to claim 1, is characterized in that: described submersible burning device, side wall burner and arch top burner are pure oxygen combustor.
3. a kind of equipment of producing andesite continuous fibre according to claim 2, it is characterized in that: the evenly distributed gas jet that is furnished with at least two pure oxygen burnings on two side, each described shaping area, the gas jet position of described pure oxygen burning is higher than described shaping area inner melt liquid level.
4. a kind of equipment of producing andesite continuous fibre according to claim 2, it is characterized in that: the submersible burning device of bottom, described melting area is the natural air gun of pure oxygen immersion, middle part, described melting area is provided with at least three natural air guns of pure oxygen immersion, described arch top burner is pure oxygen rifle, and described side wall burner is pure oxygen combustion of natural gas rifle.
5. a kind of equipment of producing andesite continuous fibre according to claim 1, it is characterized in that: described heat-exchanger rig is metallic recuperator, described metallic recuperator is arranged at described flue top, and described metallic recuperator top is provided with chimney, and described chimney top is provided with adjustable plate.
6. want a kind of equipment of producing andesite continuous fibre described in 1 to 5 any claim according to right, it is characterized in that: in described tank furnace, be provided with weir, described weir tiling arranges bottom, described homogenization zone.
7. want a kind of equipment of producing andesite continuous fibre described in 1 to 5 any claim according to right, it is characterized in that: bottom, described melting area is at least provided with row's bubbler, and described bubbler is parallel with described submersible burning device.
8. want a kind of equipment of producing andesite continuous fibre described in 1 to 5 any claim according to right, it is characterized in that: between described homogenization zone and described shaping area, be communicated with by path, described shaping area respectively symmetry is positioned at described path both sides, and described shaping area number is even number.
9. want a kind of equipment of producing andesite continuous fibre described in 1 to 5 any claim according to right, it is characterized in that: between described homogenization zone and described shaping area, be provided with glass separating device.
10. utilize any one method of producing the device fabrication continuous fibre of andesite continuous fibre in claim 1 to 5, comprise the following steps:
A. charging: andesite material is delivered in tank furnace by charging device, falls in melting area;
B. heat fused: open be positioned at melting area bottom submersible burning device, be positioned at the side wall burner on the sidewall of melting area and be positioned at the arch top burner on arch top, melting area, make temperature in melting area be increased to the fusing point higher than andesite, andesite is molten into andesite liquation;
C. homogenizing: andesite liquation flows to homogenization zone and carries out homogenizing, and enters shaping area;
D. forming wire drawing: the andesite liquation after homogenizing leaks down to carry out wire drawing from the bushing in shaping area and forms continuous fibre;
E. reel and produce: below bushing, be provided with after coiler is reeled the continuous fibre of wire drawing formation and go out finished product.
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| CN201410453123.0A CN104193164A (en) | 2014-09-05 | 2014-09-05 | Equipment for producing andesite continuous fiber and method for producing continuous fiber through equipment |
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| CN201410453123.0A CN104193164A (en) | 2014-09-05 | 2014-09-05 | Equipment for producing andesite continuous fiber and method for producing continuous fiber through equipment |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108858721A (en) * | 2018-06-21 | 2018-11-23 | 青岛联合冶金研究院有限公司 | Utilize the system of hot molten slag production insulation board |
| CN109133579A (en) * | 2018-08-17 | 2019-01-04 | 中材科技股份有限公司 | A kind of material path structure |
| CN116969674A (en) * | 2023-09-22 | 2023-10-31 | 中国耀华玻璃集团有限公司 | Float color glass and preparation method and application thereof |
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| CN109133579B (en) * | 2018-08-17 | 2020-09-22 | 中材科技股份有限公司 | Material channel structure |
| CN116969674A (en) * | 2023-09-22 | 2023-10-31 | 中国耀华玻璃集团有限公司 | Float color glass and preparation method and application thereof |
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