US4256502A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method of preparing cement clinker from carboniferous shale
Assignee: Lafarge Conseils et Etudes
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Filing: 1979-06-12
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Granted: 1981-03-17
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Expires: 1999-06-12
Abstract
Abstract The invention is related to a method and an installation for preparing cement clinker from carboniferous shale or from any other mineral substance capable of releasing a certain amount of calorific power. According to this novel method, raw material constituted in part by previously calcined carboniferous shale and in part by additive substances which may contain limestone and clay, is submitted to clinkerization. The additive substances are at least partially decarbonated prior to their admixture with the shale.
Inventors
- 👤 Jean-Pierre Lovichi
- 👤 Bernard LeBras
- 👤 Robert Guyot
- 👤 Francois Guilmin
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 23:05
CPC Classifications
C; C04; C04B; C04B7/00; C04B7/24; C04B7/30; C04B7/36; C04B7/43; C04B7/44; Y; Y02; Y02P; Y02P40/00; Y02P40/10
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
319 words
In a method of preparing cement clinker from a mineral raw material capable of releasing calorific energy, such as carboniferous shale, in an installation comprising: a rotary clinkerization kiln associated to a clinker cooler; an exchanger column connected to said kiln and including a plurality of superimposed exchanger cyclones and an exchanger precalcinator, and; a raw material treating column connected to said kiln and including a plurality of superimposed treating cyclones which comprise, from top to bottom, at least one first, one second, one third and one fourth treating cyclone, said treating column further comprising a treating calcinator, the improvement comprising the steps of: (a) feeding said exchanger column only with additive substances adapted to be used in combination with said raw material for making said clinker, and partially decarbonating said additive substances in said exchanger column prior to introducing said substances into said kiln, and introducing into said exchanger column the gases issuing from said cooler; (b) feeding the gases issuing from said cooler into said exchanger column through said exchanger precalcinator; (c) feeding said treating column with said raw material by introducing the same into a flow path leading from the fourth treating cyclone to said treating calcinator; (d) feeding fumes issuing from said kiln into said third treating cyclone, (e) injecting a portion of the solid matter issuing from said second cyclone into a gas flow path leading from said second cyclone to said first cyclone; (f) injecting the remaining solid matter issuing from said second cyclone into said flow path connecting said fourth treating cyclone to said treating calcinator, (g) injecting the fumes issuing from said treating calcinator into a flow path through which said fumes issuing from the kiln are fed into said third treating cyclone; (h) feeding at least a portion of the solid matter issuing from said fourth treating cyclone and the solid matter issuing from said treating calcinator into said kiln.
Claim 2
Dependent Claim
319 words
In a method of preparing cement clinker from a mineral raw material capable of releasing calorific energy, such as carboniferous shale, in an installation comprising: a rotary clinkerization kiln associated to a clinker cooler; an exchanger column connected to said kiln and including a plurality of superimposed exchanger cyclones and an exchanger precalcinator, and; a raw material treating column connected to said kiln and including a plurality of superimposed treating cyclones which comprise, from top to bottom, at least one first, one second, one third and one fourth treating cyclone, said treating column further comprising a treating calcinator, the improvement comprising the steps of: (a) feeding said exchanger column only with additive substances adapted to be used in combination with said raw material for making said clinker, and partially decarbonating said additive substances in said exchanger column prior to introducing said substances into said kiln, and introducing into said exchanger column the gases issuing from said cooler; (b) feeding the gases issuing from said cooler into said exchanger column through said exchanger precalcinator; (c) feeding said treating column with said raw material by introducing the same into a flow path leading from the fourth treating cyclone to said treating calcinator; (d) feeding fumes issuing from said kiln into said third treating cyclone, (e) injecting a portion of the solid matter issuing from said second cyclone into a gas flow path leading from said second cyclone to said first cyclone; (f) injecting the remaining solid matter issuing from said second cyclone into said flow path connecting said fourth treating cyclone to said treating calcinator, (g) injecting the fumes issuing from said treating calcinator into a flow path through which said fumes issuing from the kiln are fed into said third treating cyclone; (h) feeding at least a portion of the solid matter issuing from said fourth treating cyclone and the solid matter issuing from said treating calcinator into said kiln.
Claim 3
Dependent Claim
57 words
The method of claim 1, further comprising the steps of: (a) injecting the solid matter issuing from said first treating cyclone into a flow of cool air fed into said second treating cyclone, and (b) injecting the solid matter issuing from said third treating cyclone into a flow of cool air fed into said fourth treating cyclone.
Claim 4
Independent Claim
29 words
The method of any of claims 1 and 2, comprising the further step of injecting fuel into said flow path connecting said fourth treating cyclone to said treating calcinator.
Claim 5
Independent Claim
30 words
The method of any of claims 1 to 3, comprising the further step of feeding the fumes issuing from said first and second treating cyclones into a two-stage heat exchanger.
References Cited (Backward Citations)
US3973980A
Cited
US4045162A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1984-03-16 | 1984-09-15 | 1985-03-17 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-03-16 | 1988-09-15 | 1989-03-17 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-03-16 | 1992-09-15 | 1993-03-17 | $7700.00 | Window Closed / Lapsed |