US4670054A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Heat processing of particulate material
Assignee: Owens Corning Fiberglas Technology Inc
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Filing: 1986-01-17
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Granted: 1987-06-02
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Expires: 2006-01-17
Abstract
Abstract Apparatus and method for the heat processing of granular materials by the counterflow of the granular material and preheated particulate heat exchange media through a processing drum rotatable about an inclined axis. The hot media is imtimately mixed with the granular material internally of the drum to heat the material and to cool the media. Various arrangements are disclosed to recover the heat imparted to the material, or to utilize the media for successive heating operations, or to recover waste heat from other related heat processing operations or to utilize the material as preheated by the media.
Inventors
- 👤 Charles M. Hohman
- 👤 Mark A. Propster
- 👤 Stephen Seng
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 08:42
CPC Classifications
C; C03; C03B; C03B3/00; C03B3/02; C03B3/023; C03B1/00; C03B1/02; F; F27; F27D; F27D13/00; Y; Y02; Y02P; Y02P40/00; Y02P40/50
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
223 words
A process for manufacturing cement comprising the steps of: (a) flowing raw cement batch, in series, through (1) a dehydration drum in which the batch is heated to a dehydration temperature of about 300° F., (2) a calcining drum in which the dehydrated batch is calcined at a temperature of about 1800° F., (3) a clinker kiln is which the calcined batch is heated to about 2650° F., and (4) a cooling drum in which the clinkers are cooled to about 300° F., each of said drums being rotatable about an inclined longitudinal axis and the batch flowing downwardly through each of the drums; (b) preheating a particulate heat transfer media in a preheating apparatus to a temperature in excess of 300° F.; (c) flowing particulate heat transfer media upwardly through each of the drums (1), (2) and (4) in a direction countercurrent to the batch flow therethrough, the media being introduced into the drum (1) at the preheat temperature, the media issuing from the drum (1) being introduced into the drum (4) to be heated by the hot clinkers introduced therein from the clinker kiln, the media issuing from the drum (4) is introduced into the calcining drum (2) and the media issuing from the calcining drum (2) is returned to the preheating apparatus for preheating in accordance with step (b) above.
Claim 2
Dependent Claim
223 words
A process for manufacturing cement comprising the steps of: (a) flowing raw cement batch, in series, through (1) a dehydration drum in which the batch is heated to a dehydration temperature of about 300° F., (2) a calcining drum in which the dehydrated batch is calcined at a temperature of about 1800° F., (3) a clinker kiln is which the calcined batch is heated to about 2650° F., and (4) a cooling drum in which the clinkers are cooled to about 300° F., each of said drums being rotatable about an inclined longitudinal axis and the batch flowing downwardly through each of the drums; (b) preheating a particulate heat transfer media in a preheating apparatus to a temperature in excess of 300° F.; (c) flowing particulate heat transfer media upwardly through each of the drums (1), (2) and (4) in a direction countercurrent to the batch flow therethrough, the media being introduced into the drum (1) at the preheat temperature, the media issuing from the drum (1) being introduced into the drum (4) to be heated by the hot clinkers introduced therein from the clinker kiln, the media issuing from the drum (4) is introduced into the calcining drum (2) and the media issuing from the calcining drum (2) is returned to the preheating apparatus for preheating in accordance with step (b) above.
Claim 3
Dependent Claim
26 words
The process of claim 1, further comprising: (d) conducting waste heat from the clinker kiln to the preheating apparatus to preheat the media in step (b).
Claim 4
Independent Claim
192 words
A method of manufacturing cement comprising the steps of: (a) flowing raw cement batch, in series, through (1) a dehydration drum, (2) a calcining drum, (3) a clinker kiln in which the batch from the calcining drum is heated from about 2600° F. to 2800° F., and (4) a cooling drum, each of said drums being rotatable about an inclined longitudinal axis and the batch flowing downwardly through each of the drums; (b) preheating a body of particulate heat transfer media in a preheat hopper to a temperature in excess of about 300° F.; (c) flowing particulate heat transfer media upwardly through each of the drums (1), (2) and (4) in a direction countercurrent to the batch flow therethrough, the media being introduced into the drum (1) at the preheat temperature, the media issuing from the drum (1) being introduced into the drum (4) to be heated by the hot clinkers introduced therein from the clinker kiln, the hot media issuing from the drum (4) is introduced into the calcining drum (2) and the media issuing from the calcining drum (2) is returned to the body of media in the preheat hopper.
Claim 5
Independent Claim
192 words
A method of manufacturing cement comprising the steps of: (a) flowing raw cement batch, in series, through (1) a dehydration drum, (2) a calcining drum, (3) a clinker kiln in which the batch from the calcining drum is heated from about 2600° F. to 2800° F., and (4) a cooling drum, each of said drums being rotatable about an inclined longitudinal axis and the batch flowing downwardly through each of the drums; (b) preheating a body of particulate heat transfer media in a preheat hopper to a temperature in excess of about 300° F.; (c) flowing particulate heat transfer media upwardly through each of the drums (1), (2) and (4) in a direction countercurrent to the batch flow therethrough, the media being introduced into the drum (1) at the preheat temperature, the media issuing from the drum (1) being introduced into the drum (4) to be heated by the hot clinkers introduced therein from the clinker kiln, the hot media issuing from the drum (4) is introduced into the calcining drum (2) and the media issuing from the calcining drum (2) is returned to the body of media in the preheat hopper.
Claim 6
Dependent Claim
173 words
In the manufacture of cement wherein a cement batch is dehydrated, calcined, clinkerized and cooled in successive steps, the improvements of: (a) flowing raw cement batch, in series, through (1) a dehydration drum in which the batch is heated to a dehydration temperature, (2) a calcining drum in which the dehydrated batch is calcined, (3) a clinker kiln in which the calcined batch is heated to a clinkerization temperature, and (4) a cooling drum in which the clinkers are cooled, each of said drums being rotatable about an inclined longitudinal axis and the batch flowing downwardly through each of the drums; (b) preheating a body of particulate heat transfer media at a preheat location to a temperature in excess of 300° F.; (c) flowing particulate heat transfer media upwardly through each of the drums (1), (4) and (2) in that order and in a direction countercurrent to the batch flow therethrough; and (d) returning the relatively cool media from the drum (2) to the body of heat transfer media at the preheat location.
Claim 7
Dependent Claim
173 words
In the manufacture of cement wherein a cement batch is dehydrated, calcined, clinkerized and cooled in successive steps, the improvements of: (a) flowing raw cement batch, in series, through (1) a dehydration drum in which the batch is heated to a dehydration temperature, (2) a calcining drum in which the dehydrated batch is calcined, (3) a clinker kiln in which the calcined batch is heated to a clinkerization temperature, and (4) a cooling drum in which the clinkers are cooled, each of said drums being rotatable about an inclined longitudinal axis and the batch flowing downwardly through each of the drums; (b) preheating a body of particulate heat transfer media at a preheat location to a temperature in excess of 300° F.; (c) flowing particulate heat transfer media upwardly through each of the drums (1), (4) and (2) in that order and in a direction countercurrent to the batch flow therethrough; and (d) returning the relatively cool media from the drum (2) to the body of heat transfer media at the preheat location.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1990-06-01 | 1990-12-01 | 1991-06-02 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-06-01 | 1994-12-01 | 1995-06-02 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-06-01 | 1998-12-01 | 1999-06-02 | $7700.00 | Window Closed / Lapsed |