Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Sodium Hydroxide | HCID 14798 | — |
| Reactant | Sodium Silicate | HCID 23266 | — |
| Reactant | Silica | HCID 24261 | — |
| Solvent | Water | HCID 962 | — |
| Product | Sodium orthosilicate | HCID 26051 | — |
Reaction Steps
A process for producing amorphous sodium silicates having a water content of 0.3 to 6% by weight and an SiO2 /Na2O molar ratio of (1.9 to 2.8) : 1 from a waterglass solution containing at least 20% by weight of solids, the water-glass solution is obtained by reacting quartz sand with sodium hydroxide solution at an SiO2 /Na2O molar ratio of (2.0 to 2.8) : 1 at temperatures of 180 to 240° C. and pressures of 10 to 30 bar. This waterglass solution is treated in a spray-drying zone with hot air at 200 to 300° C. for a residence time of 10 to 20 seconds and at a temperature of the exit gas leaving the spray-drying zone of 90° to 130° C., to form a pulverulent amorphous sodium silicate having a water content (determined as the loss on ignition at 700° C.) of 15 to 23% by weight and a bulk density of more than 300 g/l. The pulverulent sodium silicate is introduced into an obliquely arranged rotary kiln fitted with devices for moving solids and treated therein with flue gas in countercurrent at temperatures from 250° up to 500° C. for 1 to 60 minutes. The rotary kiln is here insulated in such a way that its outside wall temperature is less than 60° C. Finally, the amorphous sodium silicate emerging from the rotary kiln is comminuted by means of a mechanical crusher to grain sizes of 0.1 to 12 mm.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US05229095 |
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| Source dataset | uspto-grants-1993_07 |
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| ORD ID | ord-242d1381df234e2b91b0f083955faa90 |
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| Source note | uspto-grants-1993_07 |
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