A kind of bottom of pond structure producing ultra-clear glasses
Technical field
The present invention relates to a kind of glass production fields, and in particular to a kind of bottom of pond structure for producing ultra-clear glasses.
Background technique
Ultra-clear glasses are a kind of super transparent low iron glasses, it is a kind of high-quality, multifunctional novel high-grade glass kind,
Light transmittance is up to 91.5% or more, and ultra-clear glasses are in normal production, and there are the glass metals that two strands of loop directions are opposite in melting furnaces
Stream, one is the liquid streams that feeds intake before hot spot, and one is the molding liquid stream after hot spot, glass liquid stream is in cyclic process integrally to out
Card neck is mobile at material mouth, and existing ultra-clear glasses melting furnaces mostly use flat or bottom of pond structure with tilt stage, though such structure
So simple, convenient for construction, but rear portion pond is deeper, and glass flow layer thickness is thicker, and the clarification for being unfavorable for microbubble sheds, hot spot temperature
Degree is higher, is affected by reflux at clarification, glass metal quality can be caused to fluctuate widely when extraction has large change.
Summary of the invention
In order to overcome the shortcomings of the prior art among the above, the present invention uses a kind of discharge that can speed up microbubble,
Reduce hot(test)-spot temperature, have accelerate clarification, stop clarification and homogenization after glass metal reflux, stabilized glass liquid stream the characteristics of one
Kind produces the bottom of pond structure of ultra-clear glasses.
The purpose of the present invention is what is realized by following scheme: a kind of bottom of pond structure producing ultra-clear glasses, comprising: feed intake
At mouthful, at clarification, it is characterized in that being: successively increasing equipped with first step, second step, the on the right at the feeding port
Three steps, the 4th step, the right side of the 4th step are equipped with weir, are at reflux on the right of the weir.
Preferably, the second step middle position is equipped with bubbling device, and the bubbling device is in long strip, above
Longitudinal direction is furnished with multiple circular holes.
Preferably, depth is 1.5m at the feeding port.
Preferably, the first step, second step, third step, the 4th step each layer height be set as 0.1-
0.2m。
Preferably, depth is 0.7-1.1m at the clarification.
Preferably, the weir height is 0.5-0.75m.
A kind of bottom of pond structure producing ultra-clear glasses of the invention, it has the advantage that:
(1) glass metal homogenizing can be effectively improved and clarifying effect, the convection current situation of stabilized glass liquid improve glass product
Quality;
(2) fusion temperature is reduced, melting furnaces energy consumption is reduced, can realize higher melting rate in lesser kiln size,
Save the investment of melting furnaces;
(3) it reduces the stagnant area of glass metal and stops unhelpful reflux, keep the flow velocity and fluid layer thickness that liquid stream is stable in melting furnaces
Degree keeps refining quality unaffected when substantially going up and down extraction.
Specifically, 1, it is deep to different pond is arranged between clarification at dispensing port: ultra-clear glasses fusion temperature is high, glass
Transmitance is high, and the upper and lower level temperature difference is small, and bottom of pond temperature is higher, larger to the erosion of bottom of pond refractory material, therefore ultra-clear glasses pond deep one
As more common float glass pond it is deeper, deeper settling section is unfavorable for the discharge of microbubble in glass, in response to this problem, along glass
Different ponds depths are arranged according to different zones in glass flow direction, set 1.5m or so deeply for pond at feeding port before hot spot, lead to after hot spot
It crosses setting bottom of pond step and pond is lifted to 1m or so deeply in settling section, step is arranged 4 or so, and every step raises 100 ~
200mm or so, entire bottom of pond is left deep right shallow, and the deeper bottom of pond of left part extends batch in the residence time of height temperate zone, guarantees glass
The convection current of glass liquid is conducive to the fusing of batch, is conducive to improve melting rate, right part settling section uses shallow pool structure, reduces
Glass metal flow layer thickness, bubble efflux time shorten, and are more advantageous to the homogenizing of glass metal and the discharge of microbubble;
2, weir device is arranged: ultra-clear glasses will often replace calender according to service condition, and more replacements are arranged in channel
Number is more frequent, according to setting port number difference extraction fluctuating range between 20%-50%, causes glass metal quality significantly
Fluctuation, in response to this problem, is arranged weir in melting furnaces, by the way that the stream that weir changes glass liquid stream is rationally arranged in melting furnaces bottom of pond
It is dynamic, bottom of pond temperature can be reduced, the regurgitant volume of glass metal after clarification, homogenizing is reduced, weakens back-flow velocity, stable liquid stream is played and makees
With, to improve the quality of melting capacity and glass metal, melting furnaces energy consumption is reduced, it, can be preferably when extraction appearance is substantially gone up and down
Play the role of stabilized glass liquid liquid stream;
3, bubbling device is set: effectively blocking in bottom of pond retention layer non-molten batch material in melting furnaces after setting weir to going out
Card neck flows at material mouth, bubbling device is arranged in conjunction with weir, elongate in shape and circular hole enhance convection current for bottom of pond on bubbling device
Temperature of glass liquid improves, and largely reduces viscous layer, and bring no cofusing particle into high-temperature region and melted, and reduces calculus rate, can
Hot(test)-spot temperature is reduced, melting efficiency is improved, accelerates the clarification and homogenization of glass, as can be seen from the above the program has operation letter
Just, practical feature.
Detailed description of the invention
Fig. 1 is the schematic elevation view of structure of the invention.
Fig. 2 is schematic top plan view of the present invention.
Wherein: 1, first step, 2, second step, 3, third step, the 4, the 4th step, 5, be bubbled, 6, weir, 7, feed intake
At mouthful, 8, at clarification.
Specific embodiment
It is as depicted in figs. 1 and 2: a kind of bottom of pond structure producing ultra-clear glasses, comprising: at feeding port 8 at 7, clarification,
Be characterized in being: 7 the right is successively increased equipped with first step 1, second step 2, third step 3, at the feeding port
Four steps 4, the right side of the 4th step 4 are equipped with weir 6, are described second 8 at clarification on the right of the weir 6
2 middle position of rank is equipped with bubbling device 5, and the bubbling device 5 is in long strip, is longitudinally furnished with multiple circular holes above, described
At feeding port 7 depth be 1.5m, the first step 1, second step 2, third step 3, the 4th step 4 each layer height
It is set as 0.1-0.2m, 8 depth are 0.7-1.1m at the clarification, and 6 height of weir is 0.5-0.75m.
Embodiment 1
This programme is implemented, and please refers to Fig. 1 and Fig. 2.
1, structure composition, 7 is will form the liquid stream that feeds intake before hot spot at the feeding port of bottom of pond, and bottom of pond is caused to fluctuate liquid stream wave
It is dynamic, the other is the hot spot molding liquid stream at clarification later, this programme using at the feeding port of bottom of pond 7 the right setting the
One step 1 is highly 0.1m, and it is highly 0.1m that second step 2, which is arranged, in the right of first step 1, successively the right side of second step 2
Third step 3 is arranged in side, is highly 0.1m, and it is highly 0.1m, at the 4th that the 4th step 4, which is arranged, in the right of third step 3
A weir 6 is arranged in the right of rank 4, and 6 height of weir is 0.75m, and 8 depth are 1.1m at clarification, and 7 depth are at feeding port
1.5m, it is preferred that multiple grooves are laterally arranged in 6 surface of weir, convenient for mitigating the big minor swing of reflux amplitude, in second step 2
Upper setting bubbling device, bubbling device 5 is in long strip, is longitudinally furnished with multiple circular holes above, and this programme is such, manufacture ultrawhite
The raw material of glass is entered by raw material dispensing 7 carries out heating and melting in kiln pond, charging can produce glass metal original in pond
Raw liquid stream, melting not sufficient feed particles can be because of the rank of first step 1, second step 2, third step 3, the 4th step 4
Trapezoidal shape and bubbling device 5 etc. continue to melt, and the glass metal after hot spot can cross each step, bubbling device 5 and weir 6, into
Enter at clarification 8,8 liquid stream can occur again because of the relationship of production extraction at clarification, and weir 6 changes the stream of glass liquid stream
It is dynamic, bottom of pond temperature can be reduced, the regurgitant volume of glass metal after clarification, homogenizing is reduced, weakens back-flow velocity, stable liquid stream is played and makees
With, to improve the quality of melting capacity and glass metal, melting furnaces energy consumption is reduced, it, can be preferably when extraction appearance is substantially gone up and down
Play the role of stabilized glass liquid liquid stream.
Embodiment 2
This programme is implemented, and please refers to Fig. 1 and Fig. 2.
Structure composition, 7 is will form the liquid stream that feeds intake before hot spot at the feeding port of bottom of pond, cause bottom of pond fluctuation liquid stream fluctuation,
The other is the molding liquid stream at clarification, this programme are arranged first using at the feeding port of bottom of pond 7 the right to hot spot later
Step 1 is highly 0.2m, and it is highly 0.2m that second step 2, which is arranged, in the right of first step 1, successively the right of second step 2
Third step 3 is set, is highly 0.2m, it is highly 0.2m, in the 4th step that the 4th step 4, which is arranged, in the right of third step 3
A weir 6 is arranged in 4 the right, and 6 height of weir is 0.5m, and depth is 0.7m at clarification, and 7 depth are 1.5m at feeding port, excellent
Choosing, multiple grooves are laterally arranged in 6 surface of weir, and convenient for mitigating the big minor swing of reflux amplitude, drum is arranged on second step 2
Bulb apparatus, bubbling device 5 is in long strip, is longitudinally furnished with multiple circular holes above, this programme be it is such, manufacture the original of ultra-clear glasses
Material is entered by raw material dispensing 7 carries out heating and melting in kiln pond, charging can generate liquid stream to glass metal original in pond, melts
Change not sufficient feed particles can because first step 1, second step 2, third step 3, the 4th step 4 stairstepping and drum
Bulb apparatus 5 etc. continues to melt, and the glass metal after hot spot can cross each step, bubbling device 5 and weir 6, enters at clarification
8,8 can be because liquid stream occur again in the relationship of production extraction at clarification, weir 6 changes the flowing of glass liquid stream, can reduce
Bottom of pond temperature reduces the regurgitant volume of glass metal after clarification, homogenizing, weakens back-flow velocity, play the role of stable liquid stream, to improve
The quality of melting capacity and glass metal reduces melting furnaces energy consumption, when extraction appearance is substantially gone up and down, can preferably play stable glass
The effect of glass liquid liquid stream.
Finally, it should be noted that above embodiments are only to illustrate the present invention and not limit technology described in the invention
Scheme;Therefore, although this specification is referring to above-mentioned each embodiment, the present invention has been described in detail, this
Field it is to be appreciated by one skilled in the art that still can modify to the present invention or equivalent replacement;And all do not depart from this
The technical solution and its improvement of the spirit and scope of invention, should all cover within the scope of the claims of the present invention.