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US3638400A Expired / Lapsed US ⏱️ 0.0 years remaining

Separation of alkali-rich dust from cement kilns

Assignee: FLSmidth and Co AS
•
Filing: 1969-02-14
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Granted: 1972-02-01
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Expires: 1989-02-14
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Abstract

Abstract The alkali content of cement clinker is controlled by recycling a fraction of dust having a particle size larger than 5 to 15 microns recovered from the exhaust gas of the cement kiln cooled to below the precipitation temperature of the alkali.

Inventors

  • 👤 Thorbjorn Heilmann

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-09 08:20
CPC Classifications
C; C04; C04B; C04B7/00; C04B7/36; C04B7/60; F; F27; F27B; F27B7/00; F27B7/20; F27B2007/2091; F27B7/32; F27B7/3205; F27B2007/3247

Claims Analysis

Total Claims: 3
Claim 1
Independent Claim 77 words
The method according to claim 1 in which separation of alkalies and entrained solids from said gas is effected by electrostatic precipitation and which includes recovering from at least a part of said solids formed in said second zone a fraction having a particle size of less than from about 5 to about 15 microns, and recycling at least a portion of the remainder fraction of said solids from the second precipitation zone to said burning zone.
Claim 2
Dependent Claim 55 words
The method according to claim 1 which includes recovering the solids formed in the second zone, separating from at least a part of said solids a fraction having a particle size of less than from about 5 to about 15 microns, and recycling at least a portion of the remainder fraction to said first zone.
Claim 3
Dependent Claim 232 words
A plant for making cement clinker comprising a rotary kiln for burning cement raw materials thereby producing an exhaust gas containing alkalies vaporized from the raw materials, gas discharge means for discharging gas into the atmosphere means for contacting said exhaust gas with raw materials being fed to said kiln to heat said materials and to cool the exhaust gas to a temperature sufficiently low to cause solidification of the vaporized alkalies therein, two groups of means for separating solidified alkalies from said gas interposed between said contacting means and said gas discharge means, means for conveying said gas successively through said separating means, means for fractionating the solids separated from said gas in the first group of separating means into two fractions one of which has a particle size less than from about 5 to about 15 microns, means for recycling at least a portion of the other fraction to the kiln, and said gas discharge means being operatively constructed and arranged fro discharging said gas into the atmosphere from said second group of separating means, and said two groups of means for separating solidified alkalies from said gas being operatively constructed and arranged for effecting the separation of solidified alkalies and entrained solids from said gas in said two groups of means without passing the cooled gas through a layer of the raw materials being fed to said rotary kiln.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1975-01-31 1975-08-02 1976-02-01 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1979-01-31 1979-08-02 1980-02-01 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1983-01-31 1983-08-02 1984-02-01 $7700.00 Window Closed / Lapsed

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