CN1482429A - Cinker clew furnace - Google Patents
Cinker clew furnace Download PDFInfo
- Publication number
- CN1482429A CN1482429A CNA021354804A CN02135480A CN1482429A CN 1482429 A CN1482429 A CN 1482429A CN A021354804 A CNA021354804 A CN A021354804A CN 02135480 A CN02135480 A CN 02135480A CN 1482429 A CN1482429 A CN 1482429A
- Authority
- CN
- China
- Prior art keywords
- tear drop
- liquation
- flame
- melt pond
- cinker clew
- 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.)
- Granted
Links
Landscapes
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
- Vertical, Hearth, Or Arc Furnaces (AREA)
Abstract
The invention relates to an improved fused blocking furnace, which comprises a molten material tank and a water quenching feed box on the molten material tank side, wherein a high temperature molten liquid channel is arranged between the molten material tank and the droplet feed box, a molten droplet material nozzle is arranged on the bottom of the molten material box, a jet of flame circulation channel is arranged between the cavity of the molten material tank and the droplet feed box, a flame guiding deflector plate is arranged on the position corresponding to the jet flame circulation channel mouth in the molten material tank. The invention realizes simplified structure, fine design, high efficiency, low cost of manufacture and improved fused block product quality, thus the invention can be widely used in various fused blocks production in the ceramic industry.
Description
Technical field
The present invention relates to a kind of improved Cinker clew furnace.
Background technology
Frit is the flux commonly used of ceramic industry, and majority uses in ceramic glaze, can reduce the melt temperature of glaze, or improve the stability of some compositions, or improve internal performance, the external appearance characteristic of glaze layer, or the like, have application fields.In actual production, both the part glaze can be made frit, also whole glaze can be made frit and use.
The preparation of frit is usually adopted is that the raw material that needs are made frit is carried out the high-temperature fusion fusing, the fusion liquation of fusing is splashed into carry out shrend in the water again, can make frit.The making apparatus of frit has also passed through one and another evolution, simple device the earliest, less is a crucible, small-sized besides crucible Cinker clew furnace, and production scale is little, by hand stock, the row water intaking frit of quenching, environmental pollution is serious, commonly used leady raw materials in the frit especially, and labour intensity is big, production efficiency is low, produce frit quality and poor stability, it is self-produced personal to be applied to producer substantially, can not adapt to, satisfy extraneous a large amount of, long run supply.
Along with market and expanding economy, the production of frit is tending towards scale, specialization, and the specialty that forms frit produces producer, directly the extraneous various frits market of supply.Therefore, the making apparatus of frit has had very big leap, realized automation to a great extent, auto feed, fusion automatically, the automatic frit of quenching of fetching water of arranging, or the like, there is bigger melt pond to carry out melt, the liquation after the fusion enters the tear drop case through the high temperature solution passage,, directly fall in the cold water after the liquation tear drop mouth of tear drop box cavity bottom oozes.
At present, existing Cinker clew furnace, have only a liquation passage between the shrend tear drop case of its melt pond and melt pond one side, on the one hand, flow resistance is big, the temperature of the temperature in the tear drop case in the melt pond more seriously, when the liquation that fusion is good in the melt pond flow in the tear drop case, the fusion situation obviously descended, and flowability reduces greatly, not only influence production efficiency, also had a strong impact on the product quality of frit.Therefore, just the producer that has sets up the burning heat riser on the tear drop case, as aiming at the tear drop box cavity burner noz(zle) is set, is used for post bake, both made equipment complicated, increased the production management burden, increased production cost, effect is not very desirable again.
Summary of the invention
Technical problem to be solved by this invention is: provide a kind of simple in structure, and the production efficiency height, production cost is low, the Cinker clew furnace of frit good product quality.
Cinker clew furnace of the present invention, the shrend tear drop case that comprises melt pond and melt pond one side, be provided with the high temperature solution passage between melt pond and tear drop case, liquation tear drop mouth is arranged at tear drop box cavity bottom, is provided with flame injection stream circulation passage between its tear drop case cavity and melt pond cavity.
Flame injection stream circulation passage can directly make the high temperature melt flame in the melt pond be injected in the tear drop case, the temperature height, effective, make the liquation situation in liquation situation in the tear drop case and melt pond basic identical, mobile, therefore, the production efficiency height, the quality of frit product is good, and do not need to set up in addition other second heating apparatus, reduce administrative burden, reduce production costs, as removed the equipment cost of post bake and the combustion fuel cost of post bake etc. from.Simultaneously, just because of the setting of flame injection stream circulation passage, make the melt pond become one with the tear drop box-shaped in logical integral body, the operating condition unanimity in the inner chamber, stable, the flow resistance of liquation from the melt pond to shrend tear drop case is little, it is unimpeded to flow.
Among the present invention:
Flame injection stream circulation passage is located at the top of tear drop case cavity and melt pond cavity, and the liquation fluid " is walked " in the assurance bottom, and flame, hot gas " are walked " in top.
Flame injection stream circulation passage and high temperature solution passage can be two passages of isolating mutually up and down, also can be a passage that communicates up and down, during a passage, the liquation flow export place in melt pond should establish liquation and flow out the control striker plate, the striker plate upper end is higher than the liquation liquid level, avoiding the molten surface floating thing in the melt pond to enter the tear drop case, guarantee quality, the purity of frit product, is the liquation passage below the striker plate.Have the structure of striker plate better, because striker plate does not have laminating of body of wall for independently, the striker plate after high temperature corrosion is convenient to change.
In the tear drop case, be provided with flame guiding reflecting plate in the road junction all corresponding to the flame injection stream, guarantee to make to obtain elevated temperature heat environmental effect preferably in the tear drop case.The far infrared carborundum plate that we preferably make flame spray towards liquation, far infrared carborundum plate good in thermal property helps improving thermal environment performance and thermal technology's operating mode of tear drop case.The high-quality performance of far infrared carborundum plate gains universal acceptance, and product is directly buied.
On the tear drop case, establish independently chimney, be convenient to control the thermal technology's operating mode situation in the tear drop case, be beneficial to and realize best production control.
The melt pond is same as the melt pond of the melten glass of glass industry, among the present invention, other conventional common-sense situation such as relevant melt pond, tear drop case is as combustion chamber, smoke evacuation chimney, deslagging, reinforced, tear drop, shrend etc., the general knowledge technical situation carries out or adjusts getting final product routinely, is not repeated.
Cinker clew furnace of the present invention is simple in structure, design ingenious, the production efficiency height, production cost is low, the frit good product quality is beneficial to and applies.
Description of drawings
Fig. 1, one embodiment of the invention cross section structure schematic diagram.
A-A schematic cross-section among Fig. 2, Fig. 1.
Fig. 3, another embodiment of the present invention cross section structure schematic diagram.
Among the figure: 1, body of wall 2, melt pond cavity 3, melt pond 4,9 fusion liquations 5,14, flame injection stream circulation passage 6,15, liquation passage 7, tear drop mouth 8, striker plate 10, tear drop case 11, tear drop case cavity 12, reflecting plate 13, chimney 16, divider wall.
The specific embodiment
The invention will be further described in conjunction with the foregoing description accompanying drawing.
As shown in Figure 1, 2, Cinker clew furnace of the present invention, the shrend tear drop case 10 that comprises melt pond 3 and melt pond one side, 10 in melt pond 3 and tear drop case are provided with high temperature solution passage 6, liquation tear drop mouth 7 is arranged at tear drop box cavity 11 bottoms, tear drop case cavity 11 and 2 of melt pond cavitys are provided with flame injection stream circulation passage 5, and flame injection stream circulation passage 5 is located at the top of tear drop case cavity 11 and melt pond cavity 2, bottom stream liquation.Flame injection stream circulation passage 5 and high temperature solution passage 6 communicate up and down, and the liquation flow export place in melt pond 3 is provided with liquation and flows out control striker plate 8, and striker plate 8 upper ends are higher than liquation 4 liquid levels, are liquation passage 6 below.In the tear drop case 10, be provided with the far infrared carborundum flame guiding reflecting plate 12 that flame is sprayed towards liquation in the road junction all corresponding to the flame injection stream, tear drop case 10 is provided with independently chimney 13.
As shown in Figure 3, the flame injection stream circulation passage 14 of Cinker clew furnace and high temperature solution passage 15 are isolated up and down mutually by divider wall 16, other same Fig. 1.
During application, the frit batching is melt into liquation and flow to the tear drop case from the liquation passage in the melt pond, carry out shrend again the water cooling pond below the tear drop mouth drips to and make the frit product.The free-standing chimneies of flame injection stream circulation passage, flame guiding reflecting plate, tear drop case etc. have all played good adjustment, regulating action to the thermal technology's operating mode in the tear drop case cavity, have improved the production run situation significantly.
Claims (7)
1, a kind of Cinker clew furnace, the shrend tear drop case that comprises melt pond and melt pond one side, be provided with the high temperature solution passage between melt pond and tear drop case, liquation tear drop mouth is arranged at tear drop box cavity bottom, it is characterized in that being provided with flame injection stream circulation passage between tear drop case cavity and melt pond cavity.
2, Cinker clew furnace according to claim 1 is characterized in that flame injection stream circulation passage is located at the top of tear drop case cavity and melt pond cavity.
3, Cinker clew furnace according to claim 2 is characterized in that flame injection stream circulation passage and high temperature solution passage two passages for isolating mutually up and down.
4, Cinker clew furnace according to claim 2, it is characterized in that flame injection stream circulation passage and high temperature solution passage communicate up and down, the liquation flow export place in melt pond is provided with liquation and flows out the control striker plate, and the striker plate upper end is higher than the liquation liquid level, is the liquation passage below.
5,, it is characterized in that being provided with flame guiding reflecting plate in the road junction all corresponding to the flame injection stream in the tear drop case according to the described Cinker clew furnace of the arbitrary claim of claim 1-4.
6, Cinker clew furnace according to claim 5 is characterized in that flame guiding reflecting plate is the far infrared carborundum plate that flame is sprayed towards liquation.
7, Cinker clew furnace according to claim 5 is characterized in that the tear drop case is provided with independently chimney.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNB021354804A CN100410195C (en) | 2002-09-13 | 2002-09-13 | Cinker clew furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNB021354804A CN100410195C (en) | 2002-09-13 | 2002-09-13 | Cinker clew furnace |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1482429A true CN1482429A (en) | 2004-03-17 |
CN100410195C CN100410195C (en) | 2008-08-13 |
Family
ID=34146166
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CNB021354804A Expired - Fee Related CN100410195C (en) | 2002-09-13 | 2002-09-13 | Cinker clew furnace |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN100410195C (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106855355A (en) * | 2015-12-09 | 2017-06-16 | 中国计量学院 | A kind of melting furnace of utilization biomass fuel heating fusing aluminium ingot |
CN111825336A (en) * | 2020-06-15 | 2020-10-27 | 广东三水大鸿制釉有限公司 | Frit preparation method and device |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4185984A (en) * | 1978-02-06 | 1980-01-29 | Union Carbide Corporation | Process for producing glass in a rotary furnace |
JPS5917052B2 (en) * | 1980-11-06 | 1984-04-19 | セントラル硝子株式会社 | glass melting kiln |
US4654068A (en) * | 1981-07-30 | 1987-03-31 | Ppg Industries, Inc. | Apparatus and method for ablating liquefaction of materials |
US4932035A (en) * | 1987-05-30 | 1990-06-05 | Sorg Gmbh & Co. Kg | Discontinuous glass melting furnace |
IT1292024B1 (en) * | 1997-05-28 | 1999-01-25 | Balzaretti Modigliani Spa | PROCESS AND DEVICE FOR THE RECYCLING OF WASTE IN A PRODUCTION OF MINERAL FIBERS |
CN2570276Y (en) * | 2002-09-14 | 2003-09-03 | 刘持强 | Fused block furnace |
-
2002
- 2002-09-13 CN CNB021354804A patent/CN100410195C/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106855355A (en) * | 2015-12-09 | 2017-06-16 | 中国计量学院 | A kind of melting furnace of utilization biomass fuel heating fusing aluminium ingot |
CN106855355B (en) * | 2015-12-09 | 2019-10-22 | 中国计量大学 | A kind of melting furnace heating fusing aluminium ingot using biomass fuel |
CN111825336A (en) * | 2020-06-15 | 2020-10-27 | 广东三水大鸿制釉有限公司 | Frit preparation method and device |
Also Published As
Publication number | Publication date |
---|---|
CN100410195C (en) | 2008-08-13 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US5116399A (en) | Glass melter with front-wall oxygen-fired burner process | |
CN100341805C (en) | Method for auxiliary heating to glass-melting furnace using top-mounted oxygen fuel nozzle | |
CN107522387A (en) | Melting furnaces for TFT glass | |
US20210017063A1 (en) | Gradient fining tank for refining foamy molten glass and a method of using the same | |
CN85108670A (en) | Improvement about glass melter and the refractory materials that in this glass melter, uses | |
CN107686226A (en) | Melting furnaces for borosilicate glass | |
CN103011580B (en) | A kind of high-strength glass fibre pool kiln wiredrawing method and device thereof | |
CN109081599B (en) | Kiln for producing basalt fibers | |
CN1052463C (en) | Channel for carrying molten glass | |
Beerkens | Analysis of elementary process steps in industrial glass melting tanks-Some ideas on innovations in industrial glass melting | |
CN110590125A (en) | End-fired glass melting furnace | |
CN1482429A (en) | Cinker clew furnace | |
CN2570276Y (en) | Fused block furnace | |
CN205088093U (en) | High -efficient optical glass melting tank | |
CN205662448U (en) | Dispersion tympanic bulla submerged combustion glass melting furnace | |
CN108751674B (en) | Glass melting furnace and method for melting glass | |
CN104341088B (en) | Spray nozzle brick for oxy-fuel combustion spray gun, manufacturing method and spray gun and melting furnace with spray nozzle brick | |
CN215828616U (en) | Horseshoe flame glass kiln and float glass production system | |
CN105152520B (en) | A kind of high effective optical glass melting pond | |
CN2563153Y (en) | Heat exchanging type double vault longitudinal flame small glass shell pool furnace | |
CN209081713U (en) | A kind of stained glass coloring furnace | |
CN218290723U (en) | Small flat glass furnace | |
CN200961119Y (en) | Ores smelting furnace for producing basalt continuous fibre | |
CN201534816U (en) | Oxy-fuel spray gun combusting natural gas | |
CN108892363A (en) | A kind of stained glass coloring furnace |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
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: 20080813 Termination date: 20110913 |