CN103951168B - Be with the floatation glass production line melting furnaces molten tin bath with or without blocking atmosphere director - Google Patents
Be with the floatation glass production line melting furnaces molten tin bath with or without blocking atmosphere director Download PDFInfo
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- CN103951168B CN103951168B CN201410030194.XA CN201410030194A CN103951168B CN 103951168 B CN103951168 B CN 103951168B CN 201410030194 A CN201410030194 A CN 201410030194A CN 103951168 B CN103951168 B CN 103951168B
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- molten tin
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Abstract
Be with the floatation glass production line melting furnaces molten tin bath with or without blocking atmosphere director, it comprises melting furnaces molten tin bath body, it, also with or without blocking atmosphere director, is made up of acceleration tube (1), separator tube (2), vapor pipe (3), push-pull valve (4), aggregate bin (5), bottom plate (6) and flange (7) without blocking atmosphere director.Advantage of the present invention is: overcome that existing director easily blocks, glassy product loss, vacuum generator produce the deficiency such as tin liquor, exhaust pollution air in counter flow oxidation groove when clearing up, can accomplish that continuous long-time running is without blocking, cleaning cycle is long, and cleaning does not affect normal production, without features such as adverse currents, not polluted air.The long-term effect to molten tin bath gas flow guiding can be reached, have without blocking, easily cleaning, environmental protection, stannic oxide rate of recovery advantages of higher.
Description
Technical field
The present invention relates to floatation glass production line field, be specifically related to be with the floatation glass production line melting furnaces molten tin bath with or without blocking atmosphere director.
Background technology
Float glass tin bath shielding gas contains small amounts tin pollution molten tin bath, drops to cause defect on the sheet glass of soft state.The gas polluted can be derived molten tin bath by existing director, but 6 months will form local stoppages, affect water conservancy diversion effect; The float glass product degradation losses of 4 hours can be caused in scale removal process; Water conservancy diversion rear oxidation tin directly enters in the air, polluted air; Existing director uses vacuum generator simultaneously, and outlet obstruction can cause air inversion to enter molten tin bath, causes tin liquor severe oxidation.
Summary of the invention
Object of the present invention is exactly at present, and float glass tin bath shielding gas contains small amounts tin pollution molten tin bath, drops to cause defect on the sheet glass of soft state.The gas polluted can be derived molten tin bath by existing director, but 6 months will form local stoppages, affect water conservancy diversion effect; The float glass product degradation losses of 4 hours can be caused in scale removal process; Water conservancy diversion rear oxidation tin directly enters in the air, polluted air; Existing director uses vacuum generator simultaneously, and outlet obstruction can cause air inversion to enter molten tin bath, causes the deficiency of tin liquor severe oxidation, and provides band with or without the floatation glass production line melting furnaces molten tin bath of blocking atmosphere director.
The present invention includes melting furnaces molten tin bath body, it is also with or without blocking atmosphere director, without blocking atmosphere director by acceleration tube, separator tube, vapor pipe, push-pull valve, aggregate bin, bottom plate and flange composition, one end of acceleration tube communicates with the import of separator tube, the cross section of separator tube is greater than the cross section of acceleration tube, and acceleration tube is shorter in length than separator tube, the other end of acceleration tube is arranged on melting furnaces molten tin bath body by flange, the A outlet of separator tube communicates with the import of vapor pipe, one end of aggregate bin exports with the B of separator tube and communicates, push-pull valve open holes is had between the B outlet of aggregate bin and separator tube, push-pull valve is arranged in push-pull valve open holes, bottom plate is arranged on the other end of aggregate bin.
Advantage of the present invention is: overcome that existing director easily blocks, glassy product loss, vacuum generator produce the deficiency such as tin liquor, exhaust pollution air in counter flow oxidation groove when clearing up, can accomplish that continuous long-time running is without blocking, cleaning cycle is long, and cleaning does not affect normal production, without features such as adverse currents, not polluted air.The long-term effect to molten tin bath gas flow guiding can be reached, have without blocking, easily cleaning, environmental protection, stannic oxide rate of recovery advantages of higher.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
Embodiment
As shown in Figure 1, the present invention includes melting furnaces molten tin bath body, it is also with or without blocking atmosphere director, without blocking atmosphere director by acceleration tube 1, separator tube 2, vapor pipe 3, push-pull valve 4, aggregate bin 5, bottom plate 6 and flange 7 form, one end of acceleration tube 1 communicates with the import 2-1 of separator tube 2, the cross section of separator tube 2 is 9 times of acceleration tube 1, and acceleration tube 1 is shorter in length than separator tube 2, the other end of acceleration tube 1 is arranged on melting furnaces molten tin bath body by flange 7, the A of separator tube 2 exports 2-2 and communicates with the import of vapor pipe 3, one end of aggregate bin 5 exports 2-3 with the B of separator tube 2 and communicates, the B of aggregate bin 5 exports between 2-3 and separator tube 2 and has push-pull valve open holes, push-pull valve 4 is arranged in push-pull valve open holes, bottom plate 6 is arranged on the other end of aggregate bin 5.
Principle of work: acceleration tube 1 front end flange is connected to molten tin bath, flows into separator tube 2 with gas in the groove of stannic oxide by acceleration tube 1, and air-flow is at the speed of acceleration tube 1 apart from short, and granules of stannic oxide can not in this sedimentation.After air-flow enters separator tube, because cross section is 9 times of acceleration tube 1, gas velocity is very slow, and granules of stannic oxide in this sedimentation, and enters aggregate bin 6, and clean air enters air from vapor pipe 3.
Every half a year once closes push-pull valve 4, opens bottom plate 6, and take out stannic oxide and reclaim, period the present invention normally can play the functions such as water conservancy diversion.Close cover plate 6 after taking out stannic oxide, open push-pull valve 4, recover conventional state.
Claims (1)
1. band is with or without the floatation glass production line melting furnaces molten tin bath of blocking atmosphere director, it comprises melting furnaces molten tin bath body, it is characterized in that it also with or without blocking atmosphere director, without blocking atmosphere director by acceleration tube (1), separator tube (2), vapor pipe (3), push-pull valve (4), aggregate bin (5), bottom plate (6) and flange (7) composition, one end of acceleration tube (1) communicates with the import (2-1) of separator tube (2), the cross section of separator tube (2) is greater than acceleration tube (1), and acceleration tube (1) is shorter in length than separator tube (2), the other end of acceleration tube (1) is arranged on melting furnaces molten tin bath body by flange (7), A outlet (2-2) of separator tube (2) communicates with the import of vapor pipe (3), one end of aggregate bin (5) exports (2-3) with the B of separator tube (2) and communicates, push-pull valve open holes is had between B outlet (2-3) of aggregate bin (5) and separator tube (2), push-pull valve (4) is arranged in push-pull valve open holes, bottom plate (6) is arranged on the other end of aggregate bin (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410030194.XA CN103951168B (en) | 2014-01-23 | 2014-01-23 | Be with the floatation glass production line melting furnaces molten tin bath with or without blocking atmosphere director |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410030194.XA CN103951168B (en) | 2014-01-23 | 2014-01-23 | Be with the floatation glass production line melting furnaces molten tin bath with or without blocking atmosphere director |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103951168A CN103951168A (en) | 2014-07-30 |
| CN103951168B true CN103951168B (en) | 2015-11-11 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
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| CN201410030194.XA Active CN103951168B (en) | 2014-01-23 | 2014-01-23 | Be with the floatation glass production line melting furnaces molten tin bath with or without blocking atmosphere director |
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| CN (1) | CN103951168B (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104291554A (en) * | 2014-10-26 | 2015-01-21 | 蚌埠玻璃工业设计研究院 | Polluted gas discharge device for float glass tin baths |
| CN106145618A (en) * | 2015-04-22 | 2016-11-23 | 吴江南玻玻璃有限公司 | A kind of electronic glass that can reduce harmful gas emission oozes the control method of stannum amount |
| CN111470761B (en) * | 2020-03-31 | 2022-05-27 | 台玻安徽玻璃有限公司 | Float glass manufacturing device and float glass |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN200940114Y (en) * | 2006-08-03 | 2007-08-29 | 秦皇岛玻璃工业研究设计院 | Gas discharging device for float glass process tin cell |
| CN201704198U (en) * | 2010-07-01 | 2011-01-12 | 深圳市凯盛科技工程有限公司 | Protective gas flow guide device of tin bath |
| CN203095850U (en) * | 2012-12-22 | 2013-07-31 | 蚌埠玻璃工业设计研究院 | Novel tin-bath shielding gas cyclic utilization device |
| CN203715485U (en) * | 2014-01-23 | 2014-07-16 | 重庆万盛浮法玻璃有限公司 | Float glass production line melting furnace tin bath with non-clogging atmosphere deflector |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2008021023A1 (en) * | 2006-08-08 | 2008-02-21 | The Boc Group, Inc. | Tin bath atmospheric recycle system |
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2014
- 2014-01-23 CN CN201410030194.XA patent/CN103951168B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN200940114Y (en) * | 2006-08-03 | 2007-08-29 | 秦皇岛玻璃工业研究设计院 | Gas discharging device for float glass process tin cell |
| CN201704198U (en) * | 2010-07-01 | 2011-01-12 | 深圳市凯盛科技工程有限公司 | Protective gas flow guide device of tin bath |
| CN203095850U (en) * | 2012-12-22 | 2013-07-31 | 蚌埠玻璃工业设计研究院 | Novel tin-bath shielding gas cyclic utilization device |
| CN203715485U (en) * | 2014-01-23 | 2014-07-16 | 重庆万盛浮法玻璃有限公司 | Float glass production line melting furnace tin bath with non-clogging atmosphere deflector |
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| CN103951168A (en) | 2014-07-30 |
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