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Method for dust removal from solid-gas contact reactor

Assignee: Mitsubishi Heavy Industries Ltd
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Filing: 1982-03-12
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Granted: 1983-12-13
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Expires: 2002-03-12
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Abstract

Abstract A method for dust removal from a solid-gas contact reactor for dust-laden exhaust gases which includes a packing section composed of packings each having a plurality of passages formed in the flow direction of the gases to be handled. Jets of gas for cleaning use are issued from a bank of stationary or movable nozzles installed in the reactor against the face at the inlet end of the packing section so as to blow off economically and efficiently the dust and other particulate matter that have settled from the gases on the packing section and have grown or bridged as a deposit thereon. The distance from the nozzles to the face of the packing section to be cleaned ranges from 0.2 to 1.0 meter, and the gas jet velocity at the inlet of the same section ranges from 5 to 40 m/sec.

Inventors

  • 👤 Michio Hada
  • 👤 Yoshihiro Shiraishi
  • 👤 Masao Hino
  • 👤 Seto Toru

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 20:03
CPC Classifications
F; F28; F28G; F28G1/00; F28G1/16; F23; F23J; F23J3/00

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 196 words
A method for removing dust particles from the packings of a solid gas contact reactor of the parallel gas flow type which includes a housing having a packing section including packing having a plurality of passages formed in the flow direction of a gas passing therethrough, said packing having upper and lower surfaces to prevent inhibiting the flow of gas through said passages in the packing due to accumulation of dust particles thereon which comprises an externally supplied cleaning gas through said passsages at a gas flow velocity of from 15 to 30 meters per second at the inlet of said packing section by passing said gases through a plurality of nozzles mounted in a stationary or movable bank near the inlet at which the gas enters the packing section, said bank when movable being movable at substantially right angles to the flowing direction of the gas through said nozzles, the number of nozzles being such that the cleaning gas issuing therefrom covers said upper, the diameters of said nozzles being from 2 mm to 20 mm, said nozzles being located at a distance of from 0.2 to 1.0 meter from the upper of said packing.
Claim 2
Independent Claim 196 words
A method for removing dust particles from the packings of a solid gas contact reactor of the parallel gas flow type which includes a housing having a packing section including packing having a plurality of passages formed in the flow direction of a gas passing therethrough, said packing having upper and lower surfaces to prevent inhibiting the flow of gas through said passages in the packing due to accumulation of dust particles thereon which comprises an externally supplied cleaning gas through said passsages at a gas flow velocity of from 15 to 30 meters per second at the inlet of said packing section by passing said gases through a plurality of nozzles mounted in a stationary or movable bank near the inlet at which the gas enters the packing section, said bank when movable being movable at substantially right angles to the flowing direction of the gas through said nozzles, the number of nozzles being such that the cleaning gas issuing therefrom covers said upper, the diameters of said nozzles being from 2 mm to 20 mm, said nozzles being located at a distance of from 0.2 to 1.0 meter from the upper of said packing.
Claim 3
Dependent Claim 18 words
A method as in claim 1 wherein the gas velocity is from 15 to 25 meters per second.
Claim 4
Dependent Claim 15 words
A method as in claim 1 or 2 in which the cleaning gas is steam.
Claim 5
Dependent Claim 15 words
A method as in claim 1 or 2 in which the cleaning gas is air.
Claim 6
Independent Claim 166 words
An apparatus for dust removal from the packings of a solid-gas contact reaction fo the parallel gas flow type which includes a housing having a packing section including packing having a plurality of passages formed in the flow direction of a cleaning gas passing therethrough, said packing having upper and lower surfaces which comprises a plurality nozzle mounted in a stationary or movable bank near the inlet at which the cleaning gas enters the packing section, said bank when movable being movable at substantially right angles to the flowing direction of the gas through said nozzle, the number of nozzles being such that a cleaning gas issuing therefrom covers said upper, the diameter of said nozzles being from 2 mm to 20 mm, said nozzles being located at a distance of from 0.2 to 1.0 meter from the upper of said packing, and means operatively connected with said nozzles for passing a cleaning gas therethrough at a velocity of from 15 to 40 meters per second.
Claim 7
Independent Claim 166 words
An apparatus for dust removal from the packings of a solid-gas contact reaction fo the parallel gas flow type which includes a housing having a packing section including packing having a plurality of passages formed in the flow direction of a cleaning gas passing therethrough, said packing having upper and lower surfaces which comprises a plurality nozzle mounted in a stationary or movable bank near the inlet at which the cleaning gas enters the packing section, said bank when movable being movable at substantially right angles to the flowing direction of the gas through said nozzle, the number of nozzles being such that a cleaning gas issuing therefrom covers said upper, the diameter of said nozzles being from 2 mm to 20 mm, said nozzles being located at a distance of from 0.2 to 1.0 meter from the upper of said packing, and means operatively connected with said nozzles for passing a cleaning gas therethrough at a velocity of from 15 to 40 meters per second.
Claim 8
Dependent Claim 25 words
An apparatus as in claim 5 wherein the distance of the nozzles from the inlet of the packing section is from 0.3 to 0.8 meter.

References Cited (Backward Citations)

JPS5228460A Cited
US4102980A Cited
US4210427A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-12-12 1987-06-13 1987-12-13 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-12-12 1991-06-13 1991-12-13 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-12-12 1995-06-13 1995-12-13 $7700.00 Window Closed / Lapsed

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