CN201793467U - Tank furnace used for producing basalt continuous filaments - Google Patents
Tank furnace used for producing basalt continuous filaments Download PDFInfo
- Publication number
- CN201793467U CN201793467U CN2010205006497U CN201020500649U CN201793467U CN 201793467 U CN201793467 U CN 201793467U CN 2010205006497 U CN2010205006497 U CN 2010205006497U CN 201020500649 U CN201020500649 U CN 201020500649U CN 201793467 U CN201793467 U CN 201793467U
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- melting
- tank
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- temperature bath
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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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Abstract
A tank furnace used for producing basalt continuous filaments relates to the technical field of design and manufacture of the tank furnace used for producing the basalt continuous filaments relates. A melting tank is arranged at the rear part of a tank furnace body; a constant temperature bath is arranged at the front part of the melting tank; a stabilization channel is formed at the front part of a constant temperature bath electrode; and a bubble removal operation channel is formed at the front part of the stabilization channel. The tank furnace adopts the working procedure as follows: basalt stones are put into the melting tank through two feed openings; and the stones dissolve into liquid material in the melting tank after being heated by a melting electrode through high temperature and being heated by two fluxing flames in the upper positions through high temperature in an auxiliary manner. The melting tank and the constant temperature bath are arranged in the tank furnace, so that feeding points for the melting tank are increased, and the flames above the feeding points can heat over against the stones directly in an auxiliary manner. The melting speed and the melting quantity of the tank furnace can be improved. Material can melt down completely in time. Melt can flow in a throat after a long path for clearing, bubble removing and uniform mixing. The high-quality wire drawing requirement can be achieved through a plurality of porous large bushings. A large amount of the energy consumption can be reduced, the product quality is improved, the manufacturing cost is lowered, and the production efficiency is improved. The practical problems of the prior device are solved.
Description
Technical field
The utility model relates to design and the manufacturing technology field of basalt continuous fiber production with tank furnace.
Background technology
In basalt continuous fiber is produced, generally use 200 hole bushing combination stove productions at present.Be that the basalt building stones directly carry out wire drawing production by the bushing hole after being melted.Since kiln to add warm spot few, there are the temperature difference in the body of heater top and the bottom, cause that the fusing amount is little, refining quality is low, can not satisfy the quantity-produced needs.Especially directly carry out wire drawing after the raw material fusing, because stock liquid stream range ability is very short, a large amount of bubbles can not get timely eliminating in the liquation so that cause, and very easily occur fracture of wire in the production, have both influenced product production, influence quality product again.Energy consumption is also big especially.
Summary of the invention
At above-mentioned situation, the purpose of this utility model provides a kind of feed points and is fluxed by flame, flow in location, the long path of liquation, temperature is even, bubble discharges the tank furnace of basalt continuous fiber production completely, to solve the practical problems that existing existing equipment exists.
Structure of the present utility model is as shown in drawings: at the rear portion of tank furnace body one melting pool is arranged, at the rear portion in molten bath one Waste gas outlet is arranged.Respectively there is an opening for feed Waste gas outlet both sides.Have the fusing rear electrode on the top of melting pool inner chamber, the bottom has wall electrode in the fusing.Have wall electrode tap hole in the fusing in the fusing on the wall electrode.Wall electrode top has the barricade brick in the fusing.One melting pool cover block is arranged at the top of melting pool.2 flame entrances are arranged on the melting pool cover block.The melting pool front portion is a temperature bath, and a pair of temperature bath electrode is arranged in the temperature bath.The temperature bath electrode is anterior, and stablizing path top has stable path cover block in order to stablize path, and stablizing has stable pathway electrode in the path.It is anterior for row steeps the operation path to stablize path, in row's bubble operation path polylith water conservancy diversion brick is installed, and the side of water conservancy diversion brick has locatees the flow liquid brick.Row's bubble operation path cover block is arranged at row's bubble operation path top.At row bubble operation path cover block, stablize on path cover block and the melting pool cover block and all have thermometer hole.Below row's bubble operation path a plurality of dog-holes are arranged.Row's bubble operation passage side has been worn the thermopair socket.Have thermopair in the thermocouple jack.Stablize path and have the globars socket, have globars in the globars socket with row's bubble operation path top.
Method of work of the present utility model is: the basalt building stones are put into the melting pool from 2 opening for feeds of melting pool side wall.Building stones are melted electrode heat and 2 places, top and flux and be melted into liquid material after the flame high temperature boosting in melting pool, liquation flows into temperature bath through the tap hole of melting pool battery lead plate.Again solution is carried out the constant temperature adjustment by the temperature bath electrode, flow into then and stablize path.Pathway electrode and boosting globars are further stable to melt temperature, composition is further even by stablizing again.Thereby flow in row's bubble operation path the walking path that has prolonged liquation through water conservancy diversion brick and location flow liquid brick then, the globars arranged of top rationally discharges in addition, make melt temperature more evenly, micro-bubble discharges fully.Guaranteed that the high quality liquation flows into a plurality of dog-holes and enters down the step wire-drawing process.
The utility model has increased melting pool feed points and feed point top flame and has directly carried out boosting over against building stones owing to be provided with melting pool and temperature bath.The burn-off rate and the fusing amount of tank furnace have been improved.Wall electrode, row's bubble operation path, water conservancy diversion brick and location flow liquid brick in the fusing of newly-increased band tap hole.Make material in time fully melt.Liquation can be grown and flow in the dog-hole after path clarification row bubble all mixes.Reach the high-quality stringy requirement of the big bushing of polylith porous.Reduced a large amount of energy consumptions, improved quality product, reduced production cost, improved production efficiency greatly.Be that a kind of energy satisfy to be produced basalt continuous fiber production tank furnace more than 2000 tons per year.
Description of drawings
Fig. 1 is the utility model structural representation
6-barricade brick 7-stablizes path 8-and stablizes in the pathway electrode 9-water conservancy diversion brick 10-location flow liquid brick 11-dog-hole 12-row bubble operation path 13-thermopair socket 14-temperature bath 15-opening for feed 16-melting pool inner chamber 17-melting pool 18-Waste gas outlet 19-fusing rear electrode 20-fusing wall electrode 22-temperature bath electrode 23-globars socket in the wall electrode tap hole 21-fusing
Fig. 2 is three cover block structural representations in the utility model
1-flame entrance 2-melting pool cover block 3-thermometer hole 4-stablizes path cover block 5-row bubble operation path cover block
Embodiment
Structure of the present utility model is as shown in drawings: at the rear portion of tank furnace body one melting pool 17 is arranged, a Waste gas outlet 18 is arranged at the rear portion in molten bath.Respectively there is an opening for feed 15 the Waste gas outlet both sides.Have fusing rear electrode 19 on the top of melting pool inner chamber 16, the bottom has wall electrode 21 in the fusing.Have wall electrode tap hole 20 in the fusing in the fusing on the wall electrode.Wall electrode top has barricade brick 6 in the fusing.One melting pool cover block 2 is arranged at the top of melting pool.2 flame entrances 1 are arranged on the melting pool cover block.The melting pool front portion is a temperature bath 14, and a pair of temperature bath electrode 22 is arranged in the temperature bath.The temperature bath electrode is anterior, and stablizing path top has stable path cover block 4 in order to stablize path 7, and stablizing has stable pathway electrode 8 in the path.It is anterior for row steeps operation path 12 to stablize path, in row's bubble operation path polylith water conservancy diversion brick 9 is installed, and the side of water conservancy diversion brick has locatees flow liquid brick 10.Row's bubble operation path cover block 5 is arranged at row's bubble operation path top.At row bubble operation path cover block, stablize on path cover block and the melting pool cover block and all have thermometer hole 3.Below row's bubble operation path a plurality of dog-holes 11 are arranged.There is thermopair socket 13 row's bubble operation path side.Have thermopair in the thermocouple jack.Stablize path and arrange bubble operation path top and have globars socket 23.Have globars in the globars socket.
Claims (1)
1. basalt continuous fiber production tank furnace, it is characterized in that: a melting pool (17) is arranged at the rear portion of tank furnace body, respectively there is an opening for feed (15) the Waste gas outlet both sides, have fusing rear electrode (19) on the top of melting pool inner chamber (16), the bottom has wall electrode (21) in the fusing, 2 flame entrances (1) are arranged on the melting pool cover block, the melting pool front portion is temperature bath (14), a pair of temperature bath electrode (22) is arranged in the temperature bath, the temperature bath electrode is anterior for stablizing path (7), stablize stable pathway electrode (8) is arranged in the path, it is anterior for arranging bubble operation path (12) to stablize path, in the row bubble operation path polylith water conservancy diversion brick (9) is installed, the side of water conservancy diversion brick has location flow liquid brick (10), a plurality of dog-holes (11) is arranged below row's bubble operation path, there is thermopair socket (13) row's bubble operation path side, have thermopair in the thermocouple jack, stablize path and have globars socket (23), have globars in the globars socket with row's bubble operation path top.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205006497U CN201793467U (en) | 2010-08-19 | 2010-08-19 | Tank furnace used for producing basalt continuous filaments |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205006497U CN201793467U (en) | 2010-08-19 | 2010-08-19 | Tank furnace used for producing basalt continuous filaments |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201793467U true CN201793467U (en) | 2011-04-13 |
Family
ID=43848386
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010205006497U Expired - Fee Related CN201793467U (en) | 2010-08-19 | 2010-08-19 | Tank furnace used for producing basalt continuous filaments |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201793467U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102992581A (en) * | 2012-11-06 | 2013-03-27 | 中材科技股份有限公司 | Large thermal power combination tank furnace for producing basalt continuous fibers |
| CN103951157A (en) * | 2014-04-02 | 2014-07-30 | 东南大学 | Tank furnace for mass production of continuous basalt fibers and heating method |
| CN113277706A (en) * | 2021-04-12 | 2021-08-20 | 姚树飞 | Special multi-bushing plate tank furnace for producing pure basalt fibers |
-
2010
- 2010-08-19 CN CN2010205006497U patent/CN201793467U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102992581A (en) * | 2012-11-06 | 2013-03-27 | 中材科技股份有限公司 | Large thermal power combination tank furnace for producing basalt continuous fibers |
| CN102992581B (en) * | 2012-11-06 | 2015-03-25 | 中材科技股份有限公司 | Large thermal power combination tank furnace for producing basalt continuous fibers |
| CN103951157A (en) * | 2014-04-02 | 2014-07-30 | 东南大学 | Tank furnace for mass production of continuous basalt fibers and heating method |
| CN103951157B (en) * | 2014-04-02 | 2016-05-18 | 东南大学 | A kind of tank furnace for continuous basalt fiber large-scale production and heating means |
| CN113277706A (en) * | 2021-04-12 | 2021-08-20 | 姚树飞 | Special multi-bushing plate tank furnace for producing pure basalt fibers |
| CN113277706B (en) * | 2021-04-12 | 2024-01-05 | 姚树飞 | Special multi-bushing tank furnace for producing pure basalt fibers |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110413 Termination date: 20130819 |