Patent US4391585A successfully refreshed from Google Patents.
← Back to Patent Explorer
US4391585A Expired / Lapsed US ⏱️ 0.0 years remaining

Method of operating a continuous ceramic kiln

Assignee: Air Products and Chemicals Inc
•
Filing: 1981-03-20
•
Granted: 1983-07-05
•
Expires: 2001-03-20
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract A method of operating a continuous ceramic kiln having a decarbonization zone characterized in that oxygen or oxygen enriched air is added to the decarbonization zone to maintain the average oxygen concentration in the decarbonization zone at or about a predetermined level. The predetermined level need only be adjusted for different throughputs and need not be adjusted for moderate changes in the amount of organic matter in the clay.

Inventors

  • 👤 Eric K. Riley
  • 👤 Colin D. Smith
  • 👤 Garry J. Yates
  • 👤 Norris W. Shepherd

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 23:05
CPC Classifications
F; F27; F27B; F27B9/00; F27B9/30; F27B9/36; C; C04; C04B; C04B33/00; C04B33/32

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 214 words
A method of decarbonizing shaped ceramic articles in an intermittent push continuous ceramic kiln having a heating and decarbonizing zone, a firing zone and a cooling zone fitted with means to sense the concentration of oxygen in the decarbonizing zone, said means associated with a control fitted to oxygen or oxygen enriched air injection means associated with said decarbonizing zone comprising the steps of: progressively heating said shaped ceramic articles to about 900° C. in the decarbonizing zone to oxidize organic matter contained in the articles; maintaining the oxygen concentration of the decarbonization zone at a minimum level of 7.5% by volume between pushes as determined by the equation: ##EQU3## where C is the predetermined level at a point in the decarbonization zone; R 1 is the throughput of clayware articles during satisfactory operation of the kiln without oxygen addition; A is the average oxygen concentration at said point during satisfactory operation of the kiln without oxygen addition at throughput rate R 1 ; R 2 is the new throughput of clayware articles; and X is between the limits of ≧0 and ≦0.5, by adding oxygen or oxygen enriched air to the decarbonization zone; continuing heating of said shaped ceramic articles until firing is completed; and cooling said shaped ceramic articles to ambient temperature.
Claim 2
Independent Claim 214 words
A method of decarbonizing shaped ceramic articles in an intermittent push continuous ceramic kiln having a heating and decarbonizing zone, a firing zone and a cooling zone fitted with means to sense the concentration of oxygen in the decarbonizing zone, said means associated with a control fitted to oxygen or oxygen enriched air injection means associated with said decarbonizing zone comprising the steps of: progressively heating said shaped ceramic articles to about 900° C. in the decarbonizing zone to oxidize organic matter contained in the articles; maintaining the oxygen concentration of the decarbonization zone at a minimum level of 7.5% by volume between pushes as determined by the equation: ##EQU3## where C is the predetermined level at a point in the decarbonization zone; R 1 is the throughput of clayware articles during satisfactory operation of the kiln without oxygen addition; A is the average oxygen concentration at said point during satisfactory operation of the kiln without oxygen addition at throughput rate R 1 ; R 2 is the new throughput of clayware articles; and X is between the limits of ≧0 and ≦0.5, by adding oxygen or oxygen enriched air to the decarbonization zone; continuing heating of said shaped ceramic articles until firing is completed; and cooling said shaped ceramic articles to ambient temperature.
Claim 3
Dependent Claim 36 words
A method according to claim 1, characterized in that the concentration of oxygen in the decarbonization zone is measured at a point in the decarbonization zone where the temperature is nominally between 700° and 875° C.
Claim 4
Dependent Claim 18 words
A method according to claim 2, characterized in that said temperature is nominally between 750° and 850° C.
Claim 5
Dependent Claim 45 words
A method according to claim 1, characterized in that the oxygen or oxygen enriched air is injected into the kiln at a position where the nominal kiln temperature is between 800° and 950° C. and where the injected oxygen will flow through the decarbonization zone.
Claim 6
Dependent Claim 20 words
A method according to claim 1, characterized in that said predetermined level is between 7.5 and 11% oxygen (by volume).
Claim 7
Dependent Claim 20 words
A method according to claim 5, characterized in that said predetermined level is between 8 and 8.5% oxygen (by volume).

References Cited (Backward Citations)

US2567556A Cited
US3227782A Cited
US3459412A Cited
US3542349A Cited
GB1422689A Cited
US4329142A Cited
US4223450A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-07-04 1987-01-03 1987-07-05 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-07-04 1991-01-03 1991-07-05 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-07-04 1995-01-03 1995-07-05 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag