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US4812149A Expired / Lapsed US ⏱️ 0.0 years remaining

Hot inert gas purging for filter blowback process

Assignee: Westinghouse Electric Co LLC
•
Filing: 1987-12-03
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Granted: 1989-03-14
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Expires: 2007-12-03
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Abstract

Abstract A filter cleaning process for filters for separating particulates from a hot gas stream using hollow, tubular filter elements. Blowback and hot purge gas systems provide for cleaning of the filter elements and maintenance of the blowback system clear of the solids or condensation products that might form during separation. The process is especially useful in filtering solids from a hot, corrosive gaseous stream, such as a zirconium tetrachloride process gaseous stream, where the gas stream contains gaseous constituents that are subject to condensation directly to a solid during separation of the particulates and prior to discharge from the filtering apparatus.

Inventors

  • 👤 Rodney L. Griffin
  • 👤 David F. Ciliberti
  • 👤 Thomas E. Lippert

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 16:50
CPC Classifications
B; B01; B01D; B01D46/00; B01D46/42; B01D46/4263; B01D46/24; B01D46/2403; B01D46/2407; B01D46/56; B01D46/58; B01D46/66; B01D46/70; B01D46/71; C; C01; C01B; C01B25/00; C01B25/02; C01B25/027; C01G; C01G23/00; C01G23/02; C01G23/022; C01G23/024; C01G25/00; C01G25/04; B01D2273/00; B01D2273/20

Claims Analysis

Total Claims: 17
Claim 1
Independent Claim 136 words
In a process for filtering particulate materials from a hot gas stream of the type which contain gaseous constituents that have a condensation temperature and are subject to condensation or solids formation during separation of the particulate material through cooling of the gas stream, and in which ceramic filter and blowback gas ports and blowback conduits are utilized for cleaning said filter, and in which a purge gas flow which continually exits through the blowback gas ports is utilized; the improved method which comprises: preheating said purge gas flow to above the condensation temperature of said component of the gas stream which component is subject to condensation or solids formation during the separation of the particulate material through cooling of the gas stream, whereby condensation in the blowback gas ports and blowback conduits is substantially avoided.
Claim 2
Dependent Claim 136 words
In a process for filtering particulate materials from a hot gas stream of the type which contain gaseous constituents that have a condensation temperature and are subject to condensation or solids formation during separation of the particulate material through cooling of the gas stream, and in which ceramic filter and blowback gas ports and blowback conduits are utilized for cleaning said filter, and in which a purge gas flow which continually exits through the blowback gas ports is utilized; the improved method which comprises: preheating said purge gas flow to above the condensation temperature of said component of the gas stream which component is subject to condensation or solids formation during the separation of the particulate material through cooling of the gas stream, whereby condensation in the blowback gas ports and blowback conduits is substantially avoided.
Claim 3
Dependent Claim 13 words
The process of claim 1, wherein said purge gas is above 350° C.
Claim 4
Dependent Claim 15 words
The process of claim 1, wherein an inert gas is utilized as said purge gas.
Claim 5
Dependent Claim 18 words
The process of claim 1, wherein said gas stream contains a gaseous chloride of a group IV-B metal.
Claim 6
Dependent Claim 13 words
The process of claim 4, wherein said gas stream is principally zirconium tetrachloride.
Claim 7
Dependent Claim 16 words
The process of claim 3, wherein the ceramic in said ceramic filter is principally silicon carbide.
Claim 8
Dependent Claim 13 words
The process of claim 2, wherein said gas stream is principally titanium tetrachloride.
Claim 9
Dependent Claim 13 words
The process of claim 2, wherein said gas stream is principally elemental phosphorus.
Claim 10
Dependent Claim 17 words
The process of claim 5, wherein said purge gas is nitrogen which is heated above 450° C.
Claim 11
Dependent Claim 102 words
In a process for filtering particulate materials from a gas stream having a temperature of at least 450° C. said gas stream being of the type which contain at least one gaseous constituent that is subject to condensation or solids formation during separation of the particulate material through cooling of the gas stream and in which a ceramic filter and blowback gas ports are utilized, and utilizing a pulse of blowback gas for cleaning said filter and a purge gas flow which continually exits through the blowback gas ports; the improved method which comprises: preheating said purge gas to above 450° C.
Claim 12
Dependent Claim 102 words
In a process for filtering particulate materials from a gas stream having a temperature of at least 450° C. said gas stream being of the type which contain at least one gaseous constituent that is subject to condensation or solids formation during separation of the particulate material through cooling of the gas stream and in which a ceramic filter and blowback gas ports are utilized, and utilizing a pulse of blowback gas for cleaning said filter and a purge gas flow which continually exits through the blowback gas ports; the improved method which comprises: preheating said purge gas to above 450° C.
Claim 13
Dependent Claim 21 words
The process of claim 10, wherein said gas stream constituent that is subject to condensation or solids formation is zirconium tetrachloride.
Claim 14
Dependent Claim 11 words
The process of claim 11, wherein said purge gas is nitrogen.
Claim 15
Dependent Claim 21 words
The process of claim 10, wherein said gas stream constituent which is subject to condensation or solids formation is titanium tetrachloride.
Claim 16
Dependent Claim 21 words
The process of claim 10, wherein said gas stream constituent which is subject to condensation, or solids formation is elemental phosphorous.
Claim 17
Dependent Claim 12 words
The process of claim 10, wherein said blowback gas is not preheated.

References Cited (Backward Citations)

US24954A Cited
USRE24954E Cited
US2721626A Cited
US3325979A Cited
SU507337A1 Cited
US4343631A Cited
US4735635A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1992-03-13 1992-09-12 1993-03-14 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1996-03-13 1996-09-12 1997-03-14 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2000-03-13 2000-09-12 2001-03-14 $7700.00 Window Closed / Lapsed

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