CN104944765A - Device capable of realizing wiredrawing of basalt continuous fiber - Google Patents
Device capable of realizing wiredrawing of basalt continuous fiber Download PDFInfo
- Publication number
- CN104944765A CN104944765A CN201510304570.4A CN201510304570A CN104944765A CN 104944765 A CN104944765 A CN 104944765A CN 201510304570 A CN201510304570 A CN 201510304570A CN 104944765 A CN104944765 A CN 104944765A
- Authority
- CN
- China
- Prior art keywords
- room
- heater
- wire drawing
- melt
- horizontal
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Crystals, And After-Treatments Of Crystals (AREA)
Abstract
The invention discloses a device capable of realizing wiredrawing of basalt continuous fiber. The device comprises a front chamber, a furnace body and a wiredrawing chamber, wherein the front chamber is communicated with the furnace body, and the furnace body is communicated with the wiredrawing chamber; at least two horizontal launders correspondingly distributed up and down, and a collector arranged below the horizontal launders and used for collecting melt flowing out of the horizontal launders are arranged in the furnace body. With arrangement of the at least two horizontal launders correspondingly distributed up and down in the furnace body, melt can form small waterfalls between the horizontal launders correspondingly distributed up and down, so that uniform mixing of the melt can be realized, volatile gas can be released better, the advantages of low energy consumption, high efficiency and environmental friendliness can be realized, basalt continuous fiber with stable quality can be obtained conveniently, and an obvious industrial application value can be realized.
Description
Technical field
The present invention relates to a kind of device realizing basalt continuous fiber wire drawing, belong to ceramic technical field of processing equipment.
Background technology
Basalt fibre is a kind of novel inorganic environment-friendly and green high performance fibre material, be widely used in many aspects such as fibre reinforced composites, friction materials, shipbuilding materials, lagging material, automobile industry, high temperature filtration fabric and protection fields, China is classified as basalt fibre as one of four large fibers that China gives priority to.
And to there is following problem in existing basalt continuous fiber production unit do not solved well, i.e. the Homogeneous phase mixing of effective fusing of refractory oxide in basalt, melt, melt center volatile gases can not discharge very well and in melt, the enrichment of rich ferriferous oxide causes platinum base alloy to be let slip a remark inefficacy etc.As Chinese patent CN200810195980.X discloses a kind of tank furnace producing basalt continuous fiber, its body of heater is made up of melting pool and material road, connected by non-invasive dog-hole between melting pool and material road, melting area and homogenization zone is divided in melting pool, burner is arranged vertically at furnace roof, arrange at melting area burner and feed-pipe interval, form the strong melting range of uniform feeding, homogeneous heating.Distinguish three directions in melting pool homogenizing and arrange material road, step-by-step arrangement burning burner in material road, ensure melt temperature in material road, in each material road, be evenly arranged more than 12 wire-drawing shape districts is bushing supply basalt molten mass, in melting pool afterbody Ji Geliao road, afterbody arranges discharging device, can carry out fused solution emissions operation in operational process when fused solution accumulates impurity for a long time or changes raw material variety.Although which solves effective fusing and the melt Homogeneous phase mixing problem of refractory oxide in basalt, but there is energy consumption defect more greatly and not environmentally in the combustion type that this device adopts, and well can not discharge volatile gases, easily cause the enrichment of rich ferriferous oxide in melt that the platinum in wire-drawing shape district or platinum base alloy are let slip a remark inefficacy.
Summary of the invention
For prior art above shortcomings, the object of this invention is to provide a kind ofly can realize melt Homogeneous phase mixing, volatile gases can be discharged very well, less energy-consumption and the device realizing basalt continuous fiber wire drawing of environmental protection.
For achieving the above object, the present invention adopts following technical scheme:
Realize a device for basalt continuous fiber wire drawing, comprising: cup, body of heater and wire drawing room, be all connected between described cup with described body of heater and between described body of heater with described wire drawing room; It is characterized in that, in described body of heater, be provided with at least two and the horizontal chute of up and down corresponding distribution, and being arranged on below horizontal chute, going out the collector of melt for collecting horizontal flow concentrated flow.Make melt form cascade one by one between the horizontal chute of corresponding distribution up and down, fully can discharge volatile element before inflow collector, and realize fully mixing.
As a kind of preferred version, electric heater is equipped with in the below of each horizontal chute and the bottom of described collector, the viscosity gradient variation tendency of melt in depth profile is reduced, to prevent the rich iron cpd depositing crystalline of large proportion, and then improves the wire drawing quality of fiber.
As a kind of embodiment, described cup comprises crucible and inclined flow passage, is respectively arranged with combustion gas head above described crucible and inclined flow passage, and the bottom of described inclined flow passage is provided with electric heater, effectively can improve heats with two kinds of type of heating, and reduce energy consumption.
As a kind of preferred version, the inside of described inclined flow passage is rugged oblique runner, makes melt realize fully mixing, and help to remove the volatile gases in melt with turbulization.
As a kind of embodiment, described wire drawing room comprises room and lower room, and described upper room is connected with collector, and described lower room is connected with upper room.
As a kind of preferred version, the outside of room is provided with outside induction heater, to realize producing joule heating under high-frequency electromagnetic field action on described; On described room sidewall in be provided with inert material floor, for the heating efficiency improving outside induction heater, be beneficial to the high-melting-point complex oxide in fused basalt.
As a kind of preferred version, be provided with ultrasonic unit above room on described, to shake melt, realize further homogenizing vitreum, and accelerate the melting of high-melting-point complex oxide.
As a kind of preferred version, the both sides of described lower room are provided with electric discharge wall, the below of described electric discharge wall is provided with sheet cooling duct, for keeping moist wire drawing environment.
As a kind of embodiment, also comprise side room, be provided with side runner in the inside in described side room, described side runner is connected with collector, and described side runner is provided with the opening for being communicated with wire drawing room.
As a kind of preferred version, be provided with electric heater in the bottom of described side runner.
Relative to prior art, the present invention by arranging at least two and the horizontal chute of corresponding distribution up and down in body of heater, melt can be made between the horizontal chute of corresponding distribution up and down to form cascade one by one, make melt fully can discharge volatile element before inflow collector, and realize fully mixing.Especially, when arranging electric heater in each below of horizontal chute and the bottom of collector, the viscosity gradient variation tendency of melt in depth profile can be made to reduce, to prevent the rich iron cpd depositing crystalline of large proportion, and then improving the wire drawing quality of fiber.In addition, the present invention can not only realize melt Homogeneous phase mixing, volatile gases can be discharged very well, but also have that energy consumption is low, efficiency is high and the advantage such as environmental protection, be conducive to obtaining stay-in-grade basalt continuous fiber, there is obvious industrial application value.
Accompanying drawing explanation
It is a kind of partial cross structural representation realizing the device of basalt continuous fiber wire drawing provided by the invention shown in Fig. 1;
It is a kind of cross-sectional view realizing the device of basalt continuous fiber wire drawing provided by the invention shown in Fig. 2;
It is the partial cross structural representation of wire drawing room of the present invention shown in Fig. 3;
In figure: 1-cup; 11-metal material storing cavity; 12-feed-pipe; 13-crucible; 14-fixture block; 15-inclined flow passage; 16-combustion gas head; 17-electric heater; 2-body of heater; The horizontal chute of 21-; 22-collector; 23-electric heater; 24-thermofin; 25-regulating course; 26-opening; 3-wire drawing room; The upper room of 31-; Room under 32-; 33-lets slip a remark; 34-fin shield pipeline; 35-discharges wall; 36-positive and negative electrode; The outside induction heater of 37-; 38-thermofin; 39-ultrasonic element; 310-opening; 4-side room; 41-side runner; 42-step; 43-electric heater; 44-opening.
Embodiment
Below with reference to accompanying drawing of the present invention, carry out clear, complete description and discussion to the technical scheme in the embodiment of the present invention, obviously, as described herein is only a part of example of the present invention, is not whole examples.
Shown in composition graphs 1 and Fig. 2:
A kind of device realizing basalt continuous fiber wire drawing that the present embodiment provides, comprising: cup 1, body of heater 2, wire drawing room 3 and 4 four, side room part.
In cup 1: feed-pipe 12 is connected with metal material storing cavity 11 by fixture block 14, basalt raw material enters metal material storing cavity 11 by feed-pipe 12, its effect is transported and stores raw mineral materials, then basalt raw material melts under the heating of combustion gas 16 in crucible 13, a combustion gas 16 preferred Sweet natural gas oxygen heater, heat is higher.When crucible 13 temperature is raised to about 1100 DEG C, the basalt material temperature in crucible, close to 1000 DEG C, starts to soften.Along with the further rising of temperature, basalt raw material starts fusing, and when crucible temperature is raised to 1300 DEG C, the basalt raw material in crucible is close to its temperature of fusion 1260 DEG C, and basalt melting sources becomes melt to flow into inclined flow passage 15.Above inclined flow passage 15 and bottom be respectively equipped with combustion gas 16 and electric heater 17, the former is for direct heating melt, and the latter is used for heating inclined flow passage 15, makes melt temperature continue to be elevated to 1400 DEG C; In rugged multizone inclined flow passage 15, turbulization makes melt fully mix, and removes the volatile gases in melt; Described inclined flow passage 15 is preferably made up of erosion-resisting material.Cup 1 outermost layer is thermofin, and use lagging material to make, centre is provided with regulating course, uses stupalith to make.
In body of heater 2: melt enters in the horizontal chute 21 distributed up and down body of heater 2 from cup 1, make melt between the horizontal chute of corresponding distribution up and down, form waterfall shape flowing, realize fully to discharge volatile element before inflow collector 22, and realize fully mixing; The electric heater 23 arranged below horizontal chute 21 can keep melt temperature.Be arranged on collector 22 below horizontal chute for collecting the melt flowed out through horizontal chute 21; When the bottom at collector 22 arranges electric heater 23, the viscosity gradient variation tendency of melt in depth profile can be made to reduce, to prevent the rich iron cpd depositing crystalline of large proportion, and then can melt quality be improved, ensure the wire drawing quality of fiber.Described collector 22 is made up of the most erosion-resisting material, such as: chromium ceramic.Body of heater 2 outermost layer is thermofin 24, and use lagging material to make, centre is provided with regulating course 25, uses stupalith to make.
Shown in composition graphs 2 and Fig. 3:
In wire drawing room 3: first the melt in collector 22 flows into the opening 310 of the upper room 31 of wire drawing room 3 by its bottom opening 26, upper room 31 utilizes fire-resistant (1950 DEG C-2100 DEG C) pottery by electromagnetic resistance to strong wearing and tearing, heat shock resistance to make, this is provided with outside induction heater 37 outside room 31, realize producing joule heating under high-frequency electromagnetic field action, be provided with inert material graphite linings in sidewall for the efficiency improving outside induction heating, be beneficial to the high-melting-point complex oxide in fused basalt; Above upper room 31, be provided with ultrasonic element 39 and positive and negative electrode 36, for concussion melt, realize further homogenizing melt, and accelerate the melting of high-melting-point complex oxide.32 pairs, the lower room be connected with upper room 31 melt condition viscosity, two side bottoms are provided with electric discharge wall 35, lower room 32 utilizes high-quality metal-ceramic material to make, bottom is provided with the bushing of the pottery of porous, wherein be inlaid with platinum or platinum base alloy lets slip a remark 33, below electric discharge wall 35, be provided with sheet cooling duct 34, inside have water coolant for keeping moist wire drawing environment, basalt continuous fiber being stablized shaping; Sheet cooling duct 34 material is the TiNi material of porous.The outermost layer of wire drawing room 3 is thermofin 38, and use lagging material to make, centre is provided with regulating course, uses stupalith to make.
Shown in composition graphs 1 and Fig. 2:
A side room 4 is respectively had in body of heater 2 both sides; all be connected with collector 22; side runner 41 is provided with in side room 4; step 42 is provided with in the inlet location of side runner 41; electric heater 43 is provided with in the bottom of side runner 41; the electric current of the kilo-ampere produced by low voltage (6V); to produce joule heating; keep melt temperature; and the multiple openings 44 (there is shown two) be provided with on side runner 41 for being communicated with wire drawing room; each opening 44 can be communicated with a wire drawing room 3, thus works while realizing multiple wire drawing room, to meet large-scale production requirement.
Finally be necessary described hereinly be; the foregoing is only the present invention's preferably embodiment; but protection scope of the present invention is not limited thereto; anyly be familiar with those skilled in the art in the technical scope that the present invention discloses; the change that can expect easily or replacement, all should be encompassed within protection scope of the present invention.
Claims (10)
1. realize a device for basalt continuous fiber wire drawing, comprising: cup, body of heater and wire drawing room, be all connected between described cup with described body of heater and between described body of heater with described wire drawing room; It is characterized in that: in described body of heater, be provided with at least two and the horizontal chute of up and down corresponding distribution, and being arranged on below horizontal chute, going out the collector of melt for collecting horizontal flow concentrated flow.
2. device according to claim 1, is characterized in that: be equipped with electric heater in the below of each horizontal chute and the bottom of described collector.
3. device according to claim 1, is characterized in that: described cup comprises crucible and inclined flow passage, is respectively arranged with combustion gas head above described crucible and inclined flow passage, and the bottom of described inclined flow passage is provided with electric heater.
4. device according to claim 3, is characterized in that: the inside of described inclined flow passage is rugged oblique runner.
5. device according to claim 1, is characterized in that: described wire drawing room comprises room and lower room, and described upper room is connected with collector, and described lower room is connected with upper room.
6. device according to claim 5, is characterized in that: the outside of room is provided with outside induction heater on described, on described room sidewall in be provided with inert material floor.
7. the device according to claim 5 or 6, is characterized in that: be provided with ultrasonic unit above room on described.
8. device according to claim 5, is characterized in that: the both sides of described lower room are provided with electric discharge wall, and the below of described electric discharge wall is provided with sheet cooling duct.
9. device according to claim 1, is characterized in that: also comprise side room, is provided with side runner in the inside in described side room, and described side runner is connected with collector, and described side runner is provided with the opening for being communicated with wire drawing room.
10. device according to claim 9, is characterized in that: be provided with electric heater in the bottom of described side runner.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510304570.4A CN104944765A (en) | 2015-06-04 | 2015-06-04 | Device capable of realizing wiredrawing of basalt continuous fiber |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510304570.4A CN104944765A (en) | 2015-06-04 | 2015-06-04 | Device capable of realizing wiredrawing of basalt continuous fiber |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN104944765A true CN104944765A (en) | 2015-09-30 |
Family
ID=54159905
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510304570.4A Pending CN104944765A (en) | 2015-06-04 | 2015-06-04 | Device capable of realizing wiredrawing of basalt continuous fiber |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104944765A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106766897A (en) * | 2017-01-24 | 2017-05-31 | 山东佳元重工机械有限公司 | The electric induction furnace of continuous production high temperature rock/mineral wool raw materials liquation |
| CN106766896A (en) * | 2017-01-24 | 2017-05-31 | 山东佳元重工机械有限公司 | The continuous electric induction furnace for preparing rock/mineral wool raw materials liquation |
| CN112279518A (en) * | 2020-10-30 | 2021-01-29 | 武汉理工大学 | Low-temperature sintered microcrystalline glass bonding agent for diamond grinding wheel and preparation method and application thereof |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6647747B1 (en) * | 1997-03-17 | 2003-11-18 | Vladimir B. Brik | Multifunctional apparatus for manufacturing mineral basalt fibers |
| CN204661545U (en) * | 2015-06-04 | 2015-09-23 | 上海工程技术大学 | A kind of basalt continuous fiber wire-drawing frame |
-
2015
- 2015-06-04 CN CN201510304570.4A patent/CN104944765A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6647747B1 (en) * | 1997-03-17 | 2003-11-18 | Vladimir B. Brik | Multifunctional apparatus for manufacturing mineral basalt fibers |
| CN204661545U (en) * | 2015-06-04 | 2015-09-23 | 上海工程技术大学 | A kind of basalt continuous fiber wire-drawing frame |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106766897A (en) * | 2017-01-24 | 2017-05-31 | 山东佳元重工机械有限公司 | The electric induction furnace of continuous production high temperature rock/mineral wool raw materials liquation |
| CN106766896A (en) * | 2017-01-24 | 2017-05-31 | 山东佳元重工机械有限公司 | The continuous electric induction furnace for preparing rock/mineral wool raw materials liquation |
| CN112279518A (en) * | 2020-10-30 | 2021-01-29 | 武汉理工大学 | Low-temperature sintered microcrystalline glass bonding agent for diamond grinding wheel and preparation method and application thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107699711B (en) | Copper smelting method | |
| CN201250173Y (en) | Stepped refiner bottom structure of large-scale float glass melting furnace | |
| WO2018090867A1 (en) | System and method for preparing titanium slag | |
| CN103011580B (en) | A kind of high-strength glass fibre pool kiln wiredrawing method and device thereof | |
| CN102992581B (en) | Large thermal power combination tank furnace for producing basalt continuous fibers | |
| CN201330217Y (en) | All-electric melting combination kiln for drawing long fibers of basalt | |
| CN104944765A (en) | Device capable of realizing wiredrawing of basalt continuous fiber | |
| CN204661545U (en) | A kind of basalt continuous fiber wire-drawing frame | |
| CN206014696U (en) | A kind of glass fiber drawing furnace | |
| CN101788229A (en) | Multifunctional smelting furnace | |
| CN208362171U (en) | A kind of energy saving kiln | |
| CN104293396B (en) | A kind of overflow type iron bath molten slag bath and Slagoff method thereof | |
| CN201334426Y (en) | Compound electrode of 12t high borosilicate glass electric melting furnace | |
| CN102901350B (en) | Metal melting furnace | |
| CN202808558U (en) | Basalt fiber tank furnace | |
| CN205088093U (en) | High -efficient optical glass melting tank | |
| CN204097327U (en) | Basalt continuous fiber wire drawing electric smelter | |
| CN105152520B (en) | A kind of high effective optical glass melting pond | |
| CN202945143U (en) | Tank furnace for producing basalt continuous filament with annular output of 5000 tons | |
| CN203782029U (en) | All-electric melting furnace for producing mineral wool | |
| CN209288279U (en) | A kind of plasma preparation nano material preheating diversion pipe | |
| CN209242906U (en) | A kind of gas refining melting furnace for continuous production cylinder of quartz glass | |
| JP2016204257A (en) | Glass melting plant | |
| CN207918667U (en) | A kind of glass melting device | |
| CN206709604U (en) | The environmentally friendly electric induction furnace of continuous production high temperature rock/mineral wool raw materials liquation |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20150930 |
|
| WD01 | Invention patent application deemed withdrawn after publication |