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US4229226A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for the production of cement clinker low in sulphur

Assignee: KHD Humboldt Wedag GmbH
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Filing: 1978-12-29
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Granted: 1980-10-21
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Expires: 1998-12-29
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Abstract

Abstract A method and apparatus for the production of cement clinker low in sulphur from a calcium carbonate containing particulate raw material in an installation containing a multi-stage suspension gas preheater, a sintering furnace and a material cooler. A portion of the sulphur-containing exhaust gases issuing from the sintering furnace is separated, and the separated portion is preheated in the gas preheater. The material is heated in the hottest stage of the preheater to a temperature below the deacidification temperature. A reducing medium is added to the thus heated material. The remaining portion of the sulphur-containing exhaust gases is removed from the system for disposition.

Inventors

  • 👤 Andris Abelitis

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-23 10:11
CPC Classifications
F; F27; F27B; F27B7/00; F27B7/20; F27B7/2016; F27B7/2041; C; C04; C04B; C04B7/00; C04B7/36; C04B7/43

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 163 words
In a method for the production of cement clinker low in sulphur from a sulphur and calcium carbonate containing particulate raw material which involves sequentially preheating said material in a plurality of successive preheating stages of progressively increasing temperatures, sintering the preheated material in a sintering furnace to produce sulphur containing hot exhaust gases, and cooling the resulting sintered material in a cooler, the improvement which comprises: separating a portion of said sulphur containing exhaust gases issuing from said sintering furnace, passing the separated portion into the hottest zone of said preheating stages, heating the raw material in contact with said separated portion to a temperature below the deacidification temperature in said hottest stage, adding a reducing agent to the thus heated raw material, sintering the thus treated raw material and reducing agent in said sintering furnace, and removing the remaining portion of said sulphur-containing exhaust gases issuing from said sintering furnace from the system without passing the same into said preheating stages.
Claim 2
Dependent Claim 163 words
In a method for the production of cement clinker low in sulphur from a sulphur and calcium carbonate containing particulate raw material which involves sequentially preheating said material in a plurality of successive preheating stages of progressively increasing temperatures, sintering the preheated material in a sintering furnace to produce sulphur containing hot exhaust gases, and cooling the resulting sintered material in a cooler, the improvement which comprises: separating a portion of said sulphur containing exhaust gases issuing from said sintering furnace, passing the separated portion into the hottest zone of said preheating stages, heating the raw material in contact with said separated portion to a temperature below the deacidification temperature in said hottest stage, adding a reducing agent to the thus heated raw material, sintering the thus treated raw material and reducing agent in said sintering furnace, and removing the remaining portion of said sulphur-containing exhaust gases issuing from said sintering furnace from the system without passing the same into said preheating stages.
Claim 3
Dependent Claim 28 words
A method according to claim 1 which includes the step of adding a relatively coarse reducing material to the preheated raw material as it enters said sintering furnace.
Claim 4
Dependent Claim 23 words
A method according to claim 1, which includes the step of: introducing cooler air into the hottest stage of the suspension gas preheater.
Claim 5
Dependent Claim 25 words
A method according to claim 1, in which: said remaining portion of sulphur-containing exhaust gases is cooled and purified before being released into the atmosphere.

References Cited (Backward Citations)

US3212764A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-10-21 1984-04-21 1984-10-21 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-10-21 1988-04-21 1988-10-21 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-10-21 1992-04-21 1992-10-21 $7700.00 Window Closed / Lapsed

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