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US3918921A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for making granular hydrated alkali metal silicate

Assignee: PQ Corp
•
Filing: 1973-08-29
•
Granted: 1975-11-11
•
Expires: 1993-08-29
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Abstract

Abstract Readily soluble hydrated alkali metal silicate granules are prepared by a change in the spray drying process. The fine particles produced by spray drying are recycled through the spray dryer so that agglomerates are formed.

Inventors

  • 👤 Richard H Pierce

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-23 19:49
CPC Classifications
C; C01; C01B; C01B33/00; C01B33/20; C01B33/32; C01B33/325; B; B01; B01J; B01J2/00; B01J2/02; B01J2/04; C11; C11D; C11D11/00; C11D11/02; C11D3/00; C11D3/02; C11D3/04; C11D3/08

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 261 words
IN THE PROCESS FOR PRODUCING GRANULES CONSISTING ESSENTIALLY OF A PLURALITY OF HYDRATED AMORPHOUS ALKALI METAL SILICATE PARTUCLES BONDED TOGETHER AT TOUCHING SURFACES, HAVING AN SIO2/M2O MOL RATIO OF 1.2 TO 4.0/1.0. THE IMPROVEMENT WHEREBY SAID PRODUCT IS PRODUCED IN A CONTINUOUS SPRAY DRYING PROCESS WHICH RESULTS IN A PRODUCT HAVING 10 TO 30% EQUILIBRATED MOISTURE AND A TAMPED BULK DENSITY OF 20 TO 55 LBS/CU.FT. COMPRISING: A. MAINTAINING A SPRAY DRYER WITH A GAS INLET TEMPERATURE OF 250* TO 500*F AND GAS OUTLET TEMPERATURE OF 160* TO 250*F, B. INJECTING AN ATOMIZED AQUEOUS ALKALI METAL SILICATE SOLUTION INTO SAID SPRAY DRYER SO THAT APPARENTLY DRY PARTICLES ARE FORMED DURING THE PASSAGE THROUGH THE SPRAY DRYER, C. ENTRAINING SAID PARTICLES IN A GAS FLOWING AT 100 TO 250 FT/MIN, D. CONDUCTING SAID ENTRAINED PARTICLES THROUGH A COLLECTION SYSTEM WHEREIN THE PARTICLES HAVING A PARTICLE SIZE LARGER THAN ABOUT 100 MESH SEPARATE FROM THE FLOWING GAS BY GRAVITY BECAUSE THEY ARE TOO LARGE TO REMAIN ENTRAINED IN SAID GAS FLOW WHILE THE PARTICLES SMALLER THAN 100 MESH REMAIN ENTRAINED IN THE GAS FLOW, E. INJECTING THE GAS FLOW WITH SAID ENTRAINED SMALL PARTICLES SMALLER THAN 100 MESH INTO SPRAY DRYER AT A POINT ABOVE THE INJECTION POINT FOR THE ALKALI METAL SILICATE SOLUTION SO THAT THE FALLING PARTICLES ENCOUNTER SAID ATOMIZED ALKALI METAL SILICATE SOLUTION AND AGGLOMERATES ARE FORMED, AND A. MAINTAINING A SPRAY DRYER WITH A GAS INLET TEMPERATURE OF SOLUTION SUCH THAT THE SOLIDS UNJECTED INTO THE SPRAY DRYER ARE EQUAL TO THE PRODUCT SOLIDS REMOVED IN THE COLLECTION SYSTEM.
Claim 2
Dependent Claim 261 words
IN THE PROCESS FOR PRODUCING GRANULES CONSISTING ESSENTIALLY OF A PLURALITY OF HYDRATED AMORPHOUS ALKALI METAL SILICATE PARTUCLES BONDED TOGETHER AT TOUCHING SURFACES, HAVING AN SIO2/M2O MOL RATIO OF 1.2 TO 4.0/1.0. THE IMPROVEMENT WHEREBY SAID PRODUCT IS PRODUCED IN A CONTINUOUS SPRAY DRYING PROCESS WHICH RESULTS IN A PRODUCT HAVING 10 TO 30% EQUILIBRATED MOISTURE AND A TAMPED BULK DENSITY OF 20 TO 55 LBS/CU.FT. COMPRISING: A. MAINTAINING A SPRAY DRYER WITH A GAS INLET TEMPERATURE OF 250* TO 500*F AND GAS OUTLET TEMPERATURE OF 160* TO 250*F, B. INJECTING AN ATOMIZED AQUEOUS ALKALI METAL SILICATE SOLUTION INTO SAID SPRAY DRYER SO THAT APPARENTLY DRY PARTICLES ARE FORMED DURING THE PASSAGE THROUGH THE SPRAY DRYER, C. ENTRAINING SAID PARTICLES IN A GAS FLOWING AT 100 TO 250 FT/MIN, D. CONDUCTING SAID ENTRAINED PARTICLES THROUGH A COLLECTION SYSTEM WHEREIN THE PARTICLES HAVING A PARTICLE SIZE LARGER THAN ABOUT 100 MESH SEPARATE FROM THE FLOWING GAS BY GRAVITY BECAUSE THEY ARE TOO LARGE TO REMAIN ENTRAINED IN SAID GAS FLOW WHILE THE PARTICLES SMALLER THAN 100 MESH REMAIN ENTRAINED IN THE GAS FLOW, E. INJECTING THE GAS FLOW WITH SAID ENTRAINED SMALL PARTICLES SMALLER THAN 100 MESH INTO SPRAY DRYER AT A POINT ABOVE THE INJECTION POINT FOR THE ALKALI METAL SILICATE SOLUTION SO THAT THE FALLING PARTICLES ENCOUNTER SAID ATOMIZED ALKALI METAL SILICATE SOLUTION AND AGGLOMERATES ARE FORMED, AND A. MAINTAINING A SPRAY DRYER WITH A GAS INLET TEMPERATURE OF SOLUTION SUCH THAT THE SOLIDS UNJECTED INTO THE SPRAY DRYER ARE EQUAL TO THE PRODUCT SOLIDS REMOVED IN THE COLLECTION SYSTEM.
Claim 3
Dependent Claim 24 words
The process of claim 1 in which the alkali metal silicate solution is selected from a group consisting of sodium silicate and potassium silicate.
Claim 4
Dependent Claim 34 words
The process of claim 1 in which the velocity of the gas flowing through the collection system is 100 ft/min. and the product granules have a particle size range of 20 to 100 mesh.
Claim 5
Dependent Claim 34 words
The process of claim 1 in which the velocity of the gas flowing through the collection system is 200 ft/min. and the product granules have a particle size range of 10 to 80 mesh.
Claim 6
Dependent Claim 34 words
The process of claim 1 in which the velocity of the gas flowing through the collection system is 250 ft/min. and the product granules have a particle size range of 10 to 48 mesh.

References Cited (Backward Citations)

US1198203A Cited
US1517891A Cited
US2941947A Cited
US3208822A Cited
US3340018A Cited
US3714051A Cited
US3687640A Cited
US3748103A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-11-10 1979-05-12 1979-11-11 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-11-10 1983-05-12 1983-11-11 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-11-10 1987-05-12 1987-11-11 $7700.00 Window Closed / Lapsed

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