Patent US3734894A successfully refreshed from Google Patents.
US4387654A
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Method for firing a rotary kiln with pulverized solid fuel
Assignee: John Zink Co LLC
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Filing: 1981-09-02
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Granted: 1983-06-14
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Expires: 2001-09-02
Abstract
Abstract Disclosed is a method for firing a kiln as well as a method for producing cement clinker in which pulverized coal is initially entrained in an airflow of about 2% of the theoretical amount of air needed to combust the coal and transport it to a burner. Supplemental primary air heated sufficiently to vaporize volatiles in the coal is mixed with the coal flow in a burner, discharged into the kiln and hence ignited. Secondary combustion air heated to between 800° F. to 1650° F. and more is added in the kiln to effect the substantially complete combustion of the pulverized coal in the kiln.
Inventors
- 👤 Chester S. Binasik
- 👤 Louis D. Siegert
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-24 18:13
CPC Classifications
C; C21; C21B; C21B13/00; C21B13/08; F; F23; F23C; F23C6/00; F23C6/04; F23D; F23D1/00; F23K; F23K3/00; F23K3/02; F27; F27B; F27B7/00; F27B7/20; F27B7/34; F23D2900/00; F23D2900/00018
Claims Analysis
Total Claims: 17
Claim 1
Independent Claim
238 words
A method for firing a coal burner for a kiln comprising the steps of: providing pulverized coal at a predetermined rate which corresponds to the desired rate with which pulverized coal is combusted in the kiln; pneumatically transporting the pulverized coal to the burner with an amount of primary combustion air of at most about 5% of the theoretical amount of air needed to combust the pulverized coal; forming a supplemental primary combustion airflow measured so that the primary combustion airflow and the supplemental primary combustion airflow comprise at most about 20% of the theoretical amount of air needed to combust the pulverized coal; heating the supplemental primary air to a temperature of at least about 600° F.; combining the primary combustion airflow and the pulverized coal entrained therein with the supplemental primary combustion airflow to form a coal-airstream at the burner; flowing the coal-airstream over a sufficient distance so that volatiles in the pulverized coal in the stream are driven off; thereafter igniting the coal-airstream to form a flame directed into the kiln; generating a secondary combustion airstream for providing the balance of combustion air required for fully combusting the pulverized coal in the stream; heating the secondary combustion air with product discharged from the kiln to a temperature of at least about 800° F.; and mixing the secondary combustion air with pulverized coal discharged into the kiln to effect the full combustion of the pulverized coal.
Claim 2
Independent Claim
238 words
A method for firing a coal burner for a kiln comprising the steps of: providing pulverized coal at a predetermined rate which corresponds to the desired rate with which pulverized coal is combusted in the kiln; pneumatically transporting the pulverized coal to the burner with an amount of primary combustion air of at most about 5% of the theoretical amount of air needed to combust the pulverized coal; forming a supplemental primary combustion airflow measured so that the primary combustion airflow and the supplemental primary combustion airflow comprise at most about 20% of the theoretical amount of air needed to combust the pulverized coal; heating the supplemental primary air to a temperature of at least about 600° F.; combining the primary combustion airflow and the pulverized coal entrained therein with the supplemental primary combustion airflow to form a coal-airstream at the burner; flowing the coal-airstream over a sufficient distance so that volatiles in the pulverized coal in the stream are driven off; thereafter igniting the coal-airstream to form a flame directed into the kiln; generating a secondary combustion airstream for providing the balance of combustion air required for fully combusting the pulverized coal in the stream; heating the secondary combustion air with product discharged from the kiln to a temperature of at least about 800° F.; and mixing the secondary combustion air with pulverized coal discharged into the kiln to effect the full combustion of the pulverized coal.
Claim 3
Independent Claim
204 words
A method for firing a coal burner for a kiln comprising the steps of: providing pulverized coal; establishing an airflow of not substantially more than 5% of the theoretical amount of air needed to combust the pulverized coal in the kiln; entraining pulverized coal in the airflow at a predetermined rate which corresponds to the desired rate with which pulverized coal is combusted in the kiln to thereby form a pulverized coal flow; mixing the coal flow with an amount of supplemental, primary air to establish a coal-airstream having no more than about 20% of the theoretical amount of air needed to combust the pulverized coal in the kiln; directing the coal-airstream through a burner tube; heating the supplemental primary air to a sufficient temperature and retaining the coal-airstream in the burner tube for a sufficient length of time to vaporize in the coal-airstream volatiles present in the coal; thereafter discharging the stream from the burner tube into the kiln; igniting the stream; and introducing sufficient secondary air having a temperature of at least about 800° F. into the kiln and in substantially surrounding relationship to the stream discharged into the kiln so as to substantially completely combust the pulverized coal in the kiln.
Claim 4
Independent Claim
204 words
A method for firing a coal burner for a kiln comprising the steps of: providing pulverized coal; establishing an airflow of not substantially more than 5% of the theoretical amount of air needed to combust the pulverized coal in the kiln; entraining pulverized coal in the airflow at a predetermined rate which corresponds to the desired rate with which pulverized coal is combusted in the kiln to thereby form a pulverized coal flow; mixing the coal flow with an amount of supplemental, primary air to establish a coal-airstream having no more than about 20% of the theoretical amount of air needed to combust the pulverized coal in the kiln; directing the coal-airstream through a burner tube; heating the supplemental primary air to a sufficient temperature and retaining the coal-airstream in the burner tube for a sufficient length of time to vaporize in the coal-airstream volatiles present in the coal; thereafter discharging the stream from the burner tube into the kiln; igniting the stream; and introducing sufficient secondary air having a temperature of at least about 800° F. into the kiln and in substantially surrounding relationship to the stream discharged into the kiln so as to substantially completely combust the pulverized coal in the kiln.
Claim 5
Dependent Claim
40 words
A method according to claim 2 including the step of controlling the amount of air in the coal-airstream so that the stream comprises no more than about 10% of the theoretical amount of air needed to combust the pulverized coal.
Claim 6
Dependent Claim
28 words
A method according to claim 2 wherein the heating step comprises the step of heating the supplemental primary air to a temperature range of between about 600°-1500° F.
Claim 7
Dependent Claim
26 words
A method according to claim 2 wherein the secondary combustion air has a temperature in the range of between about 800° F. to about 1650° F.
Claim 8
Dependent Claim
21 words
A method according to claim 5 including the step of heating the secondary combustion air with product fired in the kiln.
Claim 9
Dependent Claim
23 words
A method according to claim 2 wherein the step of entraining includes the step of gravitationally moving the pulverized coal to the airflow.
Claim 10
Dependent Claim
34 words
A method according to claim 2 wherein the supplemental primary air mixed with the coal flow comprises no more than about 8% of the theoretical amount of air needed to combust the pulverized coal.
Claim 11
Dependent Claim
31 words
A method according to claim 2 wherein the step of establishing includes the step of pressurizing the air to at least about 2 psi above the pressure prevailing in the kiln.
Claim 12
Dependent Claim
36 words
A method according to claim 8 wherein the step of pressurizing comprises the step of pressurizing the air to a range of between about 2 to about 15 psi above the pressure prevailing in the kiln.
Claim 13
Dependent Claim
37 words
A method according to claim 2 wherein the step of establishing includes the step of pressurizing the air sufficiently so that the pulverized coal flow travels at a speed of at least about 4000 ft. per minute.
Claim 14
Dependent Claim
26 words
A method according to claim 2 including the step of including in the pulverized coal flow up to about 100% of a material comprising essentially carbon.
Claim 15
Dependent Claim
12 words
A method according to claim 12 wherein the material comprises petroleum coke.
Claim 16
Dependent Claim
27 words
A method according to claim 13 wherein petroleum coke is included in the pulverized coal flow in an amount of no more than about 25% by weight.
Claim 17
Dependent Claim
36 words
A method according to claim 2 wherein the step of establishing comprises the step of establishing an airflow of not substantially more than about 2% of the theoretical amount of air needed to combust the coal.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1986-06-13 | 1986-12-13 | 1987-06-14 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-06-13 | 1990-12-13 | 1991-06-14 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-06-13 | 1994-12-13 | 1995-06-14 | $7700.00 | Window Closed / Lapsed |