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Patent US4138235A successfully refreshed from Google Patents.
US4138235A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method of making flat glass with lower sulfur-containing emissions
Assignee: PPG Industries Inc
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Filing: 1977-05-31
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Granted: 1979-02-06
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Expires: 1997-05-31
Abstract
Abstract Conventional flat glass compositions are melted in a continuous melting process with lowered sulfur-containing emissions and with improved fining at high batch-to-cullet ratios by controlling the amount of SO3 included in the batch materials and cullet. This is accomplished while maintaining high throughputs and without using substitute fining agents. Preferably, the amount of carbon in the batch is maintained at a minimal level or eliminated.
Inventors
- 👤 Warren H. Turner
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-09 03:47
CPC Classifications
C; C03; C03C; C03C1/00; C03C1/004; C03C3/00; C03C3/04; C03C3/076; C03C3/083; C03C3/085; C03C3/087
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
316 words
In the continuous, large-scale method of melting soda-lime-silica glass wherein a pool of molten glass is maintained within an elongated furnace, and raw, unmelted glass batch materials and cullet, in a batch/cullet weight ratio of 70/30 to 100/0, are fed into the furnace at one end and melted glass is withdrawn at the opposite end and formed into a flat glass ribbon, wherein sources of Si, Na, K, Ca, Mg, Al, and Fe in the batch and cullet are proportioned to yield a final glass composition comprising, by weight: 6- 75percent SiO 2 12-16 percent Na 2 O 0-2 percent K 2 O 8-12 percent CaO 2-5 percent MgO 0-2 percent Al 2 O 3 0-0.7 percent Fe 2 O 3 and the interior of the furnace is maintained at sufficient temperatures and conditions to melt and react the batch and cullet to yield said glass composition, wherein the batch and cullet also include sources of sulfur, a portion of which is retained in the glass and additionally comprises 0.15 percent to 0.5 percent by weight of final glass composition as SO 3 and the remainder of which is volatilized and escapes from the pool of molten glass as gaseous products of reaction, said volatilization and escape of part of the sulfur serving as essentially the sole fining agent to reduce gaseous inclusions in the glass, said sulfur sources being provided in an amount and conditions being maintained in the furnace to induce sufficient volatilization of sulfur to fine the glass to a seed count of no more than one seed per square foot of formed glass ribbon, the improvement comprising: maintaining the input rate of sulfur from the batch and cullet being fed into the furnace at 1.20 to 2.25 times the weight of sulfur being withdrawn in the final glass composition, whereby sulfur-containing emissions from the furnace are minimized while maintaining sufficient fining action.
Claim 2
Dependent Claim
316 words
In the continuous, large-scale method of melting soda-lime-silica glass wherein a pool of molten glass is maintained within an elongated furnace, and raw, unmelted glass batch materials and cullet, in a batch/cullet weight ratio of 70/30 to 100/0, are fed into the furnace at one end and melted glass is withdrawn at the opposite end and formed into a flat glass ribbon, wherein sources of Si, Na, K, Ca, Mg, Al, and Fe in the batch and cullet are proportioned to yield a final glass composition comprising, by weight: 6- 75percent SiO 2 12-16 percent Na 2 O 0-2 percent K 2 O 8-12 percent CaO 2-5 percent MgO 0-2 percent Al 2 O 3 0-0.7 percent Fe 2 O 3 and the interior of the furnace is maintained at sufficient temperatures and conditions to melt and react the batch and cullet to yield said glass composition, wherein the batch and cullet also include sources of sulfur, a portion of which is retained in the glass and additionally comprises 0.15 percent to 0.5 percent by weight of final glass composition as SO 3 and the remainder of which is volatilized and escapes from the pool of molten glass as gaseous products of reaction, said volatilization and escape of part of the sulfur serving as essentially the sole fining agent to reduce gaseous inclusions in the glass, said sulfur sources being provided in an amount and conditions being maintained in the furnace to induce sufficient volatilization of sulfur to fine the glass to a seed count of no more than one seed per square foot of formed glass ribbon, the improvement comprising: maintaining the input rate of sulfur from the batch and cullet being fed into the furnace at 1.20 to 2.25 times the weight of sulfur being withdrawn in the final glass composition, whereby sulfur-containing emissions from the furnace are minimized while maintaining sufficient fining action.
Claim 3
Dependent Claim
37 words
The method of claim 1 wherein the amount of sulfur in the input stream of batch and cullet is no more than 2 times the weight content of sulfur in the glass being withdrawn from the furnace.
Claim 4
Dependent Claim
14 words
The method of claim 2 wherein the feed stream is essentially free of carbon.
Claim 5
Dependent Claim
26 words
The method of claim 3 wherein the source of SO 3 consists essentially of salt cake or gypsum and the SO 3 content of the cullet.
Claim 6
Independent Claim
16 words
The method of cliam 4 wherein the batch ingredients include sand, soda ash, limestone, and dolomite.
Claim 7
Independent Claim
16 words
The method of cliam 4 wherein the batch ingredients include sand, soda ash, limestone, and dolomite.
Claim 8
Dependent Claim
15 words
The method of claim 1 wherein the weight ratio of batch-to-cullet is at least 80/20.
Claim 9
Dependent Claim
14 words
The method of claim 1 wherein the feed stream is essentially free of carbon.
Claim 10
Dependent Claim
28 words
The method of claim 1 wherein the feed stream includes iron oxide and sufficient carbon to yield a ferrous/total iron ratio in the glass no greater than 0.35.
Claim 11
Dependent Claim
28 words
The method of claim 1 wherein the feed stream includes iron oxide and sufficient carbon to yield a ferrous/total iron ratio in the glass no greater than 0.30.
Claim 12
Dependent Claim
41 words
The method of claim 1 wherein the amount of sulfur in the input stream of batch and cullet is at least 1.2 times but no greater than 2.0 times the weight of sulfur in the glass being withdrawn from the furnace.
Claim 13
Dependent Claim
30 words
The method of claim 10 wherein the SO 3 content of the glass being withdrawn from the furnace is about 0.20 percent by weight to about 0.3 percent by weight.
Claim 14
Dependent Claim
26 words
The method of claim 1 wherein the source of SO 3 consists essentially of salt cake or gypsum and the SO 3 content of the cullet.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1982-02-05 | 1982-08-07 | 1983-02-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-02-05 | 1986-08-07 | 1987-02-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-02-05 | 1990-08-07 | 1991-02-06 | $7700.00 | Window Closed / Lapsed |