US4336235A
Expired / Lapsed
US
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Process for the manufacture of sodium silicate
Assignee: Produits Chimiques Ugine Kuhlmann
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Filing: 1980-06-20
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Granted: 1982-06-22
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Expires: 2000-06-20
Abstract
Abstract The present invention comprises a process for the manufacture of a sodium silicate solution in a continuous manner from a silicon dioxide-containing material, comprising continuously adding to a reaction zone a stream of said silicon dioxide-containing material and a stream of a sodium hydroxide-sodium carbonate solution, reacting said silicon dioxide-containing material and said sodium hydroxide-sodium carbonate at a temperature and pressure and for a time sufficient to form a sodium silicate solution, and recovering said sodium silicate solution from the reaction zone.
Inventors
- 👤 Jean Deabriges
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 07:55
CPC Classifications
C; C01; C01B; C01B33/00; C01B33/20; C01B33/32
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
91 words
A process for the manufacture of a sodium silicate solution in a continuous manner from a silicon dioxide-containing material, comprising continuously adding to a reaction zone a stream of said silicon dioxide-containing material and a stream of a sodium hydroxide-sodium carbonate solution, reacting said silicon dioxide-containing material and said sodium hydroxide-sodium carbonate at a temperature of from about 225° to 245° C. and pressure of from about 27 to 32 bars for a time of from about 20 to 35 minutes, and recovering said sodium silicate solution from the reaction zone.
Claim 2
Dependent Claim
91 words
A process for the manufacture of a sodium silicate solution in a continuous manner from a silicon dioxide-containing material, comprising continuously adding to a reaction zone a stream of said silicon dioxide-containing material and a stream of a sodium hydroxide-sodium carbonate solution, reacting said silicon dioxide-containing material and said sodium hydroxide-sodium carbonate at a temperature of from about 225° to 245° C. and pressure of from about 27 to 32 bars for a time of from about 20 to 35 minutes, and recovering said sodium silicate solution from the reaction zone.
Claim 3
Dependent Claim
36 words
The process of claims 1 or 2 wherein the sodium hydroxide-sodium carbonate solution contains NaOH in a concentration of 180 to 230 grams/liter and Na 2 CO 3 in a concentration of 15 to 20 grams/liter.
Claim 4
Dependent Claim
36 words
The process of claim 1 wherein the silicon dioxide containing material is quartz sand which is placed into suspension with a portion of said sodium hydroxide-sodium carbonate solution prior to being added to said reaction zone.
Claim 5
Dependent Claim
33 words
The process of claim 3 wherein the remainder of said sodium hydroxide-sodium carbonate solution is heated to a temperature of about 250° to 280° C. prior to being added to said reaction zone.
Claim 6
Dependent Claim
20 words
The process of claim 4 wherein the weight ratio of SiO 2 /total NaOH being reacted is from about 1.7-2.6.
Claim 7
Dependent Claim
142 words
A process for the manufacture of a sodium silicate solution in a continuous manner comprising forming a suspension of quartz sand having a grain size below 1 mm in a portion of a solution of sodium hydroxide-sodium carbonate containing 180 to 230 grams/liter of NaOH and 15 to 20 grams/liter of Na 2 CO 3 , heating the remainder of said sodium hydroxide-sodium carbonate solution to a temperature of 250° to 280° C., continuously adding a stream of said quartz sand suspension and a stream of said heated solution to a reaction zone to form a reaction mixture, maintaining said reaction zone at a pressure of 27 to 32 bars and the reaction mixture at a temperature of 225° to 245° C., and recovering a sodium silicate solution from said reaction zone after the reaction has continued for 20 to 35 minutes.
Claim 8
Dependent Claim
142 words
A process for the manufacture of a sodium silicate solution in a continuous manner comprising forming a suspension of quartz sand having a grain size below 1 mm in a portion of a solution of sodium hydroxide-sodium carbonate containing 180 to 230 grams/liter of NaOH and 15 to 20 grams/liter of Na 2 CO 3 , heating the remainder of said sodium hydroxide-sodium carbonate solution to a temperature of 250° to 280° C., continuously adding a stream of said quartz sand suspension and a stream of said heated solution to a reaction zone to form a reaction mixture, maintaining said reaction zone at a pressure of 27 to 32 bars and the reaction mixture at a temperature of 225° to 245° C., and recovering a sodium silicate solution from said reaction zone after the reaction has continued for 20 to 35 minutes.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1985-06-21 | 1985-12-21 | 1986-06-22 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-06-21 | 1989-12-21 | 1990-06-22 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-06-21 | 1993-12-21 | 1994-06-22 | $7700.00 | Window Closed / Lapsed |