Claims
- 1. A porous lightweight particulate aggregate comprising expanded and vitrified low alkalinity particles having a density of not more than about 60 g/dm.sup.3, a compression strength of from about 195 to about 275 Kg/cm.sup.2, a temperature resistance without undue fusion or deformation up to about 1250.degree. C. and an expansion ratio of up to about 15 times the original volume of said particles, said expanded and vitrified low alkalinity particles having been obtained by heating and firing dried particles of the composition comprising an alkali metal silicate having an M.sub.2 O/SiO.sub.2 ratio of from about 1:2 to about 1:4 wherein M is an alkali metal, from about 0.1 to about 50% by weight of said alkali metal silicate of silica, from about 0.1 to about 200% by weight of said alkali metal silicate of an alkaline earth metal silicate, and from about 0.1 to about 30% by weight of said alkali metal silicate of boric acid which upon firing produces a silicate-tetraborate glass.
- 2. The aggregate according to claim 1 wherein said alkali metal is sodium and said alkaline earth metal is calcium.
- 3. The aggregate according to claim 2 wherein said composition further comprises one or more additives selected from the group consisting of carbon, metal carbides and potassium oxide.
- 4. The aggregate according to claim 1 wherein said expanded and vitrified low alkalinity particles contain a large plurality of small pores evenly distributed throughout the body thereof.
- 5. The aggregate according to claim 1 wherein said expanded and vitrified low alkalinity particles are globe-like particles having a relatively large pore in the center thereof surrounded by a shell of material containing a large plurality of small pores evenly distributed throughout said shell.
- 6. A process for the manufacture of a porous light-weight particulate aggregate comprising expanded and vitrified low alkalinity particles having a density of not more than about 60 g/dm.sup.3, a compression strength of from about 195 to about 275 Kg/cm.sup.2, a temperature resistance without undue fusion or deformation up to about 1250.degree. C. and an expansion ratio of up to about 15 times the original volume of said particles, comprising:
- (a) dissolving an alkali metal silicate in water to form a solution of from about 35% to about 50% by weight of total solids, and kneading into said solution from about 0.1 to about 50% by weight of the alkali metal silicate of finely divided silica, from about 0.1 to about 200% by weight of the alkali metal silicate of a finely divided alkaline earth metal silicate and from about 0.1 to about 30% by weight of said alkali metal silicate of boric acid which upon firing produces a silicate-tetraborate glass, in order to obtain a homogeneous slurry;
- (b) partially drying the thus obtained slurry to produce a paste-like or solid mixture;
- (c) reducing said mixture to particles of a preselected size depending on the desired size of the finished aggregate;
- (d) heating said particles to a temperature of from about 100.degree. C. to about 700.degree. C. for a period of time of from about 0.1 second to about 5 minutes to remove the remaining water and expand the particles with the formation of a large plurality of pores therein;
- (e) firing said expanded particles at a temperature of from about 700.degree. C. to about 1500.degree. C. for a period of time of from about 5 seconds to about 1 minute to complete the expansion of the particles and produce vitrification thereof; and
- (f) slowly cooling said expanded and vitrified particles to room temperature.
- 7. The process according to claim 6 wherein from about 0.1 to about 400% by weight of carbon, based on the weight of said alkali metal silicate, is added to said slurry.
- 8. The process according to claim 7 wherein a blowing agent in an amount of from about 0.1 to about 30% by weight of said alkali metal silicate is added, whereby hollow particles having a large central pore surrounded by a hard porous shell are obtained.
- 9. The process according to claim 8 wherein said blowing agent is an organic blowing agent.
- 10. The process according to claim 9 wherein said organic blowing agent comprises wheat flour.
- 11. The process according to claim 8 wherein said blowing agent is potassium nitrate.
- 12. The process according to claim 6 wherein the heating of said particles is effected in a first stage under moist environmental conditions in which the temperature is raised from about 110.degree. to about 300.degree. C. and a second stage under dry conditions until a temperature of from about 300.degree. to about 700.degree. C. is reached, whereby a hollow particle having a relatively large central pore surrounded by a hard porous shell is obtained.
- 13. The process according to claim 12 wherein the moist environmental conditions are produced by contacting the particles with saturated steam.
- 14. The aggregate according to claim 3, wherein said carbon is present in an amount of from about 0.1 to about 400% by weight of said alkali metal silicate of finely divided carbon.
- 15. The aggregate according to claim 1 wherein said composition further comprises a blowing agent selected from the group consisting of a sulfur type blowing agent, an organic volatile solid finely divided blowing agent, or potassium nitrate.
- 16. The aggregate according to claim 1, wherein said composition to be heated and fired further comprises about 0.1 to about 30% by weight of said alkali metal silicate of potassium nitrate as a blowing agent.
- 17. The aggregate according to claim 1, wherein said composition consists essentially of said alkali metal silicate, said silica, said alkaline earth metal silicate and said boric acid.
- 18. The process according to claim 6, wherein said slurry consists essentially of said water, said alkali metal silicate, said silica, said alkaline earth metal silicate and said boric acid.
Priority Claims (1)
Number |
Date |
Country |
Kind |
160361 |
Aug 1975 |
MXX |
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Parent Case Info
This is a continuation of application Ser. No. 718,276, filed Aug. 27, 1976, now abandoned.
US Referenced Citations (1)
Number |
Name |
Date |
Kind |
3990901 |
Engstrom et al. |
Nov 1976 |
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Continuations (1)
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Number |
Date |
Country |
Parent |
718276 |
Aug 1976 |
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