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US4387654A Expired / Lapsed US ⏱️ 0.0 years remaining

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
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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.

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

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