CN204251504U - A kind of modified version basalt fibre hot melting furnace - Google Patents
A kind of modified version basalt fibre hot melting furnace Download PDFInfo
- Publication number
- CN204251504U CN204251504U CN201420720939.0U CN201420720939U CN204251504U CN 204251504 U CN204251504 U CN 204251504U CN 201420720939 U CN201420720939 U CN 201420720939U CN 204251504 U CN204251504 U CN 204251504U
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- CN
- China
- Prior art keywords
- melting furnace
- hot melting
- basalt fibre
- modified version
- sedimentation chamber
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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
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- Manufacture Of Alloys Or Alloy Compounds (AREA)
Abstract
The utility model relates to a kind of modified version basalt fibre hot melting furnace, comprise hot melting furnace body, filtering net is provided with in the middle part of hot melting furnace body, hot melting furnace body bottom portion middle position is provided with baffler, homogenize distribution cavity is formed between filtering net and baffler, arrange base plate bottom homogenize distribution cavity, arrange solution tank between base plate and baffler, solution tank two ends are communicated with left sedimentation chamber and right sedimentation chamber; Base plate is processed with and is set to leting slip a remark of integral structure; Periphery of leting slip a remark is provided with cooling chamber; Hot melting furnace body both sides are respectively arranged with the first heating electrode and the second heating electrode; Solution tank is provided with boosting electrode; The 3rd heating electrode is provided with in left sedimentation chamber; The 4th heating electrode is provided with in right sedimentation chamber.The utility model promotes basalt melting sources speed, ensures the homogeneity of basalt melt temperature, avoids crystalline polamer, realize basalt fibre and produce continuously, ensures quality product.
Description
Technical field
The utility model relates to basalt fibre production technical field, particularly a kind of modified version basalt fibre hot melting furnace.
Background technology
Basalt fibre is the base fiber raw material that a kind of over-all properties is very excellent, it is one of functional special fiber of state key development, there is the features such as intensity is high, acid and alkali-resistance, high temperature performance are good, fire resistance is superior, each field of military project civilian goods can be widely used in, wide market.In the production process of basalt fibre, basalt at high temperature melts, its fused solution has the features such as heat transfer is slow, large, the easy crystallization of thermograde, it is slow to there is basalt melting sources speed in existing production technology, non-uniform temperature easily forms the normal production that crystallization affects fiber, can only small-scale production be realized, be difficult to the industrialization realizing basalt fibre, define the production development of basalt fibre to a certain extent.
Based on above-mentioned analysis, design a kind of modified version basalt fibre hot melting furnace, promote basalt melting sources speed, ensure the homogeneity of basalt melt temperature, avoid crystalline polamer, realize basalt fibre and produce continuously, ensure quality product.
Utility model content
The purpose of this utility model is, for the existing hot melting furnace produced for basalt fibre, there is basalt melting sources speed slow, non-uniform temperature easily forms the technical problem that crystallization affects the normal production of fiber, a kind of modified version basalt fibre hot melting furnace is provided, solve the problems of the technologies described above, improve the continuous seepage of basalt fibre, improve production efficiency and product quality.
The utility model relates to a kind of modified version basalt fibre hot melting furnace, it is characterized in that, structure comprises hot melting furnace body (1), hot melting furnace body (1) middle part is provided with filtering net (2), hot melting furnace body (1) lower center position is provided with baffler (4), homogenize distribution cavity (3) is formed between filtering net (2) and baffler (4), homogenize distribution cavity (3) bottom arranges base plate (8), arrange solution tank (5) between base plate (8) and baffler (4), solution tank (5) two ends are communicated with left sedimentation chamber (6) and right sedimentation chamber (7);
Described base plate (8) is processed with let slip a remark (81) being set to integral structure;
Described (81) periphery of leting slip a remark is provided with cooling chamber (82);
Described cooling chamber (82) bottom is provided with condensed fluid collection pond (9);
Described hot melting furnace body (1) both sides are respectively arranged with the first heating electrode (11) and the second heating electrode (12);
Described solution tank (5) is provided with boosting electrode (51);
The 3rd heating electrode (61) is provided with in described left sedimentation chamber (6);
The 4th heating electrode (71) is provided with in described right sedimentation chamber (7).
Further, described hot melting furnace body (1) is provided with the first turbine agitator (13).
Further, described baffler (4) is provided with the second turbine agitator (41).
Further, described filtering net (2) is provided with demountable structure.
Further, the cooling chamber (82) being arranged at let slip a remark (81) described in peripheral is interconnected.
Further, described cooling chamber (82) lower left quarter is communicated with the first nitrogen storage tank (8201).
Further, described cooling chamber (82) upper right quarter is communicated with the second nitrogen storage tank (8202).
Further, let slip a remark described in (81) be set to trapezoid groove structure wide at the top and narrow at the bottom.
Further, described homogenize distribution cavity (3) is connected with left sedimentation chamber (6).
Further, described homogenize distribution cavity (3) is connected with right sedimentation chamber (7).
The utility model relates to a kind of modified version basalt fibre hot melting furnace, and beneficial effect is:
1, the utility model increases at solution tank (5) boosting electrode (51), increase in left sedimentation chamber (6) and have the 3rd heating electrode (61), increase in right sedimentation chamber (7) and have the 4th heating electrode (71), this kind of project organization can effectively avoid the basalt solution being in molten state to produce crystallization before entering let slip a remark (81), causes fracture of wire phenomenon to occur.
2, the utility model is provided with baffler (4) at hot melting furnace body (1) lower center position, the basalt solution that baffler (4) can effectively limit in homogenize distribution cavity (3) directly enters let slip a remark (81), left sedimentation chamber (6) and right sedimentation chamber (7) is communicated with at solution tank (5) two ends, homogenize distribution cavity (3) is connected with right sedimentation chamber (7) with left sedimentation chamber (6), homogenize distribution cavity (3) be connected, the basalt solution being in molten state inputted by homogenize distribution cavity (3) first enters left sedimentation chamber (6) and right sedimentation chamber (7), solution tank (5) middle part is flowed to again by left sedimentation chamber (6) and right sedimentation chamber (7), and finally enter and let slip a remark in (81), this kind of project organization, make the crystal of impurity remaining in basalt solution or precipitation can obtain effective sedimentation in left sedimentation chamber (6) and right sedimentation chamber (7), the crystal of impurity and precipitation is avoided to enter let slip a remark (81), Improving The Quality of Products.
3, the utility model is respectively arranged with the first turbine agitator (13) and the second turbine agitator (41) in hot melting furnace body (1) and homogenize distribution cavity (3), this kind of project organization, basalt solution temperature homogeneity can be promoted, reduce crystal and separate out probability.
What 4, the utility model related to let slip a remark, and (81) periphery is provided with the cooling chamber (82) be interconnected, described cooling chamber (82) bottom is provided with condensed fluid collection pond (9), cooling chamber (82) lower left quarter is communicated with the first nitrogen storage tank (8201), cooling chamber (82) upper right quarter is communicated with the second nitrogen storage tank (8202), utilize this kind of project organization effectively to cool fast (81) outer wall of leting slip a remark, improve cooling efficiency and basalt fibre efficient attenuation.
Accompanying drawing explanation
Fig. 1 is a kind of modified version basalt fibre of the utility model hot melting furnace structural representation.
Embodiment
Accompanying drawings 1 pair of the utility model is described further.
A kind of modified version basalt fibre hot melting furnace, it is characterized in that, structure comprises hot melting furnace body (1), hot melting furnace body (1) middle part is provided with filtering net (2), hot melting furnace body (1) lower center position is provided with baffler (4), homogenize distribution cavity (3) is formed between filtering net (2) and baffler (4), homogenize distribution cavity (3) bottom arranges base plate (8), arrange solution tank (5) between base plate (8) and baffler (4), solution tank (5) two ends are communicated with left sedimentation chamber (6) and right sedimentation chamber (7);
Described base plate (8) is processed with let slip a remark (81) being set to integral structure;
Described (81) periphery of leting slip a remark is provided with cooling chamber (82);
Described cooling chamber (82) bottom is provided with condensed fluid collection pond (9);
Described hot melting furnace body (1) both sides are respectively arranged with the first heating electrode (11) and the second heating electrode (12);
Described solution tank (5) is provided with boosting electrode (51);
The 3rd heating electrode (61) is provided with in described left sedimentation chamber (6);
The 4th heating electrode (71) is provided with in described right sedimentation chamber (7).
Preferably, as improvement, described hot melting furnace body (1) is provided with the first turbine agitator (13).
Preferably, as improvement, described baffler (4) is provided with the second turbine agitator (41).
Preferably, as improvement, described filtering net (2) is provided with demountable structure.
Preferably, as improvement, described in be arranged at let slip a remark (81) peripheral cooling chamber (82) be interconnected.
Preferably, as improvement, described cooling chamber (82) lower left quarter is communicated with the first nitrogen storage tank (8201).
Preferably, as improvement, described cooling chamber (82) upper right quarter is communicated with the second nitrogen storage tank (8202).
Preferably, as improvement, described in let slip a remark (81) be set to trapezoid groove structure wide at the top and narrow at the bottom.
Preferably, as improvement, described homogenize distribution cavity (3) is connected with left sedimentation chamber (6).
Preferably, as improvement, described homogenize distribution cavity (3) is connected with right sedimentation chamber (7).
Compared with prior art, the utility model increases at solution tank (5) boosting electrode (51), increase in left sedimentation chamber (6) and have the 3rd heating electrode (61), increase in right sedimentation chamber (7) and have the 4th heating electrode (71), this kind of project organization can effectively avoid the basalt solution being in molten state to produce crystallization before entering let slip a remark (81), causes fracture of wire phenomenon to occur.
The utility model is provided with baffler (4) at hot melting furnace body (1) lower center position, the basalt solution that baffler (4) can effectively limit in homogenize distribution cavity (3) directly enters let slip a remark (81), left sedimentation chamber (6) and right sedimentation chamber (7) is communicated with at solution tank (5) two ends, homogenize distribution cavity (3) is connected with right sedimentation chamber (7) with left sedimentation chamber (6), homogenize distribution cavity (3) be connected, the basalt solution being in molten state inputted by homogenize distribution cavity (3) first enters left sedimentation chamber (6) and right sedimentation chamber (7), solution tank (5) middle part is flowed to again by left sedimentation chamber (6) and right sedimentation chamber (7), and finally enter and let slip a remark in (81), this kind of project organization, make the crystal of impurity remaining in basalt solution or precipitation can obtain effective sedimentation in left sedimentation chamber (6) and right sedimentation chamber (7), the crystal of impurity and precipitation is avoided to enter let slip a remark (81), Improving The Quality of Products.
The utility model is respectively arranged with the first turbine agitator (13) and the second turbine agitator (41) in hot melting furnace body (1) and homogenize distribution cavity (3), and this kind of project organization can promote basalt solution temperature homogeneity, reduces crystal and separates out probability.
What the utility model related to let slip a remark, and (81) periphery is provided with the cooling chamber (82) be interconnected, described cooling chamber (82) bottom is provided with condensed fluid collection pond (9), cooling chamber (82) lower left quarter is communicated with the first nitrogen storage tank (8201), cooling chamber (82) upper right quarter is communicated with the second nitrogen storage tank (8202), utilize this kind of project organization effectively to cool fast (81) outer wall of leting slip a remark, improve cooling efficiency and basalt fibre efficient attenuation.
The utility model in use, enter basalt raw material in hot melting furnace body (1) rapid melting under the heat effect of the first heating electrode (11) and the second heating electrode (12), in melting process, first turbine agitator (13) is to the raw material Keep agitation entered in hot melting furnace body (1), make raw material internal temperature homogeneous, material solution after fusing enters homogenize distribution cavity (3) after filter screen (2) filters, second turbine agitator (41) stirs the material solution entering homogenize distribution cavity (3), solution is mixed more even, under the buffer action of baffler (4), basalt solution directly enters left sedimentation chamber (6) and right sedimentation chamber (7) by homogenize distribution cavity (3), remaining impurity and the crystal of precipitation are in left sedimentation chamber (6) and right sedimentation chamber (7) after further sedimentation, the basalt solution being in molten state enters let slip a remark (81) via solution tank (5), and be connected on drawing wire machine via let slip a remark (81), carry out fiber draw, in drawing process, the first nitrogen storage tank (8201) and the second nitrogen storage tank (8202) is utilized to cool to cooling chamber (82) input liquid nitrogen (81) outer wall of leting slip a remark.
In use, the first heating electrode (11) and the second heating electrode (12) heat the basalt raw material entered in hot melting furnace body (1), impel rapid melting; 3rd heating electrode (61) and the 4th heating electrode (71) carry out heat supplement to left sedimentation chamber (6) and right sedimentation chamber (7) to the material solution entering left sedimentation chamber (6) and right sedimentation chamber (7) respectively, ensure that it is in the temperature levels of requirement; Boosting electrode (51) heats the basalt solution in solution tank (5), ensures that it is in the temperature levels of requirement.
As described above, can complete application of the present utility model.
The above; be only the utility model preferably embodiment; but protection domain of the present utility model is not limited thereto; anyly be familiar with those skilled in the art in the technical scope that the utility model discloses; be equal to according to the technical solution of the utility model and utility model design thereof and replace or change, all should be encompassed within protection domain of the present utility model.
Claims (10)
1. a modified version basalt fibre hot melting furnace, it is characterized in that, structure comprises hot melting furnace body (1), hot melting furnace body (1) middle part is provided with filtering net (2), hot melting furnace body (1) lower center position is provided with baffler (4), homogenize distribution cavity (3) is formed between filtering net (2) and baffler (4), homogenize distribution cavity (3) bottom arranges base plate (8), arrange solution tank (5) between base plate (8) and baffler (4), solution tank (5) two ends are communicated with left sedimentation chamber (6) and right sedimentation chamber (7);
Described base plate (8) is processed with let slip a remark (81) being set to integral structure;
Described (81) periphery of leting slip a remark is provided with cooling chamber (82);
Described cooling chamber (82) bottom is provided with condensed fluid collection pond (9);
Described hot melting furnace body (1) both sides are respectively arranged with the first heating electrode (11) and the second heating electrode (12);
Described solution tank (5) is provided with boosting electrode (51);
The 3rd heating electrode (61) is provided with in described left sedimentation chamber (6);
The 4th heating electrode (71) is provided with in described right sedimentation chamber (7).
2. modified version basalt fibre hot melting furnace according to claim 1, is characterized in that, described hot melting furnace body (1) is provided with the first turbine agitator (13).
3. modified version basalt fibre hot melting furnace according to claim 1, is characterized in that, described baffler (4) is provided with the second turbine agitator (41).
4. modified version basalt fibre hot melting furnace according to claim 1, is characterized in that, described filtering net (2) is provided with demountable structure.
5. modified version basalt fibre hot melting furnace according to claim 1, is characterized in that, described in be arranged at let slip a remark (81) peripheral cooling chamber (82) be interconnected.
6. modified version basalt fibre hot melting furnace according to claim 1, is characterized in that, described cooling chamber (82) lower left quarter is communicated with the first nitrogen storage tank (8201).
7. modified version basalt fibre hot melting furnace according to claim 1, is characterized in that, described cooling chamber (82) upper right quarter is communicated with the second nitrogen storage tank (8202).
8. modified version basalt fibre hot melting furnace according to claim 1, is characterized in that, described in let slip a remark (81) be set to trapezoid groove structure wide at the top and narrow at the bottom.
9. modified version basalt fibre hot melting furnace according to claim 1, is characterized in that, described homogenize distribution cavity (3) is connected with left sedimentation chamber (6).
10. modified version basalt fibre hot melting furnace according to claim 1, is characterized in that, described homogenize distribution cavity (3) is connected with right sedimentation chamber (7).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420720939.0U CN204251504U (en) | 2014-11-27 | 2014-11-27 | A kind of modified version basalt fibre hot melting furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420720939.0U CN204251504U (en) | 2014-11-27 | 2014-11-27 | A kind of modified version basalt fibre hot melting furnace |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204251504U true CN204251504U (en) | 2015-04-08 |
Family
ID=52955831
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420720939.0U Expired - Fee Related CN204251504U (en) | 2014-11-27 | 2014-11-27 | A kind of modified version basalt fibre hot melting furnace |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204251504U (en) |
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2014
- 2014-11-27 CN CN201420720939.0U patent/CN204251504U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150408 Termination date: 20171127 |
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| CF01 | Termination of patent right due to non-payment of annual fee |