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US4087254A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for pelletizing wet siliceous particulates

Assignee: JM Huber Corp
•
Filing: 1975-03-07
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Granted: 1978-05-02
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Expires: 1995-03-07
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Abstract

Abstract An improved process for pelletizing siliceous materials produced in an aqueous medium is disclosed. The process comprises the improvement of filtering the aqueous medium in which the siliceous materials are produced or refined, forming a slurry of the filter cake obtained by filtration and thereafter introducing the slurry directly into a pelletizer. The pellets thus formed are dried and a portion thereof recycled to the pelletizer so that the solids content of the slurry has a predetermined solids content. The process obviates the need for an initial drying of the filter cake, reduces the drying of excess water at several steps and provides for the recycling and use of unsatisfactory materials.

Inventors

  • 👤 Robert B. Takewell

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 01:10
CPC Classifications
C; C09; C09C; C09C1/00; C09C1/28; C09C1/30; C09C1/3009; C09C1/3036; C09C1/40; C09C1/42; C09C3/00; C09C3/04; C09C3/045; C01; C01P; C01P2004/00; C01P2004/50; C01P2006/00; C01P2006/80; C01P2006/82

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 229 words
In a process for agglomerating finely divided siliceous particulates selected from the group consisting of clay, silica, and silicates wherein said finely divided particlates of said clay, silica, and silicates are produced in an aqueous medium and are filtered and introduced into a pelletizer to form agglomerates thereof, the improvement comprising: (a) producing finely divided particulates of clay, silica, and silicates in an aqueous medium; (b) filtering said aqueous medium to form a filter cake of said siliceous particulates; (c) preparing a slurry of said filter cake of said siliceous particulates, said slurry having a solids content in the range of from about 20 to 59% by weight solids; (d) introducing said filter cake slurry of said siliceous particulates and recycled dried siliceous pelletized particulates thereof into a pelletizer in an amount so that the slurry of siliceous particulate material to be pelletized has a solids content by weight percentage in the range of from about 60 to 80%; (e) pelletizing said slurry of said siliceous particulates; (f) drying said formed pellets to a moisture content of about 3 to 5%; (g) recycling at least a portion of the dried siliceous pellets produced by pelletizing said slurry to said pelletizer to form a portion of the particulate siliceous materials to be added to said filter cake slurry in said pelletizer; and (h) recovering the remainder of the siliceous pellets.
Claim 2
Dependent Claim 229 words
In a process for agglomerating finely divided siliceous particulates selected from the group consisting of clay, silica, and silicates wherein said finely divided particlates of said clay, silica, and silicates are produced in an aqueous medium and are filtered and introduced into a pelletizer to form agglomerates thereof, the improvement comprising: (a) producing finely divided particulates of clay, silica, and silicates in an aqueous medium; (b) filtering said aqueous medium to form a filter cake of said siliceous particulates; (c) preparing a slurry of said filter cake of said siliceous particulates, said slurry having a solids content in the range of from about 20 to 59% by weight solids; (d) introducing said filter cake slurry of said siliceous particulates and recycled dried siliceous pelletized particulates thereof into a pelletizer in an amount so that the slurry of siliceous particulate material to be pelletized has a solids content by weight percentage in the range of from about 60 to 80%; (e) pelletizing said slurry of said siliceous particulates; (f) drying said formed pellets to a moisture content of about 3 to 5%; (g) recycling at least a portion of the dried siliceous pellets produced by pelletizing said slurry to said pelletizer to form a portion of the particulate siliceous materials to be added to said filter cake slurry in said pelletizer; and (h) recovering the remainder of the siliceous pellets.

References Cited (Backward Citations)

US2024176A Cited
US2686161A Cited
GB695303A Cited
US3401017A Cited
US3387931A Cited
US3623858A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-05-01 1981-10-31 1982-05-02 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-05-01 1985-10-31 1986-05-02 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-05-01 1989-10-31 1990-05-02 $7700.00 Window Closed / Lapsed

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