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US4501552A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for controlling furnace temperature

Assignee: Mitsubishi Electric Corp
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Filing: 1983-09-08
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Granted: 1985-02-26
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Expires: 2003-09-08
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Abstract

Abstract In controlling furnace temperature, a desired temperature profile of a slab in a direction along its movement through a furnace is calculated by using an expression for total fuel flow as a function of slab temperature and minimizing the total fuel flow. The present slab temperature is calculated by using the distribution of present gas temperatures in the furnace. The heating of the furnace is adjusted based on the temperature difference between the present slab temperature and a desired temperature.

Inventors

  • 👤 Yoshinori Wakamiya

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 05:46
CPC Classifications
C; C21; C21D; C21D11/00; F; F27; F27D; F27D19/00; G; G05; G05D; G05D23/00; G05D23/19; G05D23/1917

Claims Analysis

Total Claims: 3
Claim 1
Independent Claim 343 words
A method of controlling furnace temperature for use with a slab heating furnace having a zone with controllable heating means, including the steps of: (a) calculating a desired temperature profile of a slab as it progresses through a furnace divided into sub-zones along its length, said calculation minimizing total fuel flow and based on shape information of said slab, slab temperature at a prior position within said furnace, and the predetermined slab temperature at a discharge position of the furnace; (b) predicting the distribution of the gas temperature at each said subzone along the length of the furnace; (c) calculating the present slab temperature distribution by using said distribution of said gas temperature predicted in step (b); (d) comparing said slab temperature calculated in step (c) at the present time with said desired slab temperature calculated in step (a) to produce a difference between them; and (e) adjusting the output of said heating means according to said temperature deviation produced in step (d); wherein said desired temperature curve is predicted based on the T si which minimizes W T and said T si is calculated according to the equation ##EQU17## where W T is the total injected fuel flow, H g is the heat produced per unit of fuel flow, T si is the slab temperature in the ith subzone, T gi is the temperature at the center of the ith subzone, C pg is the specific heat of the exhausted gas, C is a constant relating the volume of exhausted gas to the fuel flow, A i and B i are constants depending on the structure of the furnace, T si is the slab temperature in the ith subzone, C p is the specific heat of the slab, E i is equal to (C p ·γ·H·v)/(D i ·l i ·2) where γ is the specific gravity of the slab; H is the thickness of the slab, D i is the radiative heat conversion coefficient, l i is the length of the ith subzone, and v is the velocity of the moving slab.
Claim 2
Independent Claim 343 words
A method of controlling furnace temperature for use with a slab heating furnace having a zone with controllable heating means, including the steps of: (a) calculating a desired temperature profile of a slab as it progresses through a furnace divided into sub-zones along its length, said calculation minimizing total fuel flow and based on shape information of said slab, slab temperature at a prior position within said furnace, and the predetermined slab temperature at a discharge position of the furnace; (b) predicting the distribution of the gas temperature at each said subzone along the length of the furnace; (c) calculating the present slab temperature distribution by using said distribution of said gas temperature predicted in step (b); (d) comparing said slab temperature calculated in step (c) at the present time with said desired slab temperature calculated in step (a) to produce a difference between them; and (e) adjusting the output of said heating means according to said temperature deviation produced in step (d); wherein said desired temperature curve is predicted based on the T si which minimizes W T and said T si is calculated according to the equation ##EQU17## where W T is the total injected fuel flow, H g is the heat produced per unit of fuel flow, T si is the slab temperature in the ith subzone, T gi is the temperature at the center of the ith subzone, C pg is the specific heat of the exhausted gas, C is a constant relating the volume of exhausted gas to the fuel flow, A i and B i are constants depending on the structure of the furnace, T si is the slab temperature in the ith subzone, C p is the specific heat of the slab, E i is equal to (C p ·γ·H·v)/(D i ·l i ·2) where γ is the specific gravity of the slab; H is the thickness of the slab, D i is the radiative heat conversion coefficient, l i is the length of the ith subzone, and v is the velocity of the moving slab.
Claim 3
Dependent Claim 62 words
A method of controlling a furnace temperature according to claim 1, wherein the step of calculating the desired temperature curve includes the step of calculating said total injected fuel when said predicted gas temperature is lower than an allowable temperature of said furnace, said predicted gas temperature T gi being calculated by the following equation T.sub.gi =[(T.sub.si +273).sup.4 +E.sub.i ·(T.sub.si+1 -T.sub.si-1).sup.1/4 -273.

References Cited (Backward Citations)

US4004138A Cited
US4373364A Cited
US4394121A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1988-02-26 1988-08-27 1989-02-26 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1992-02-26 1992-08-27 1993-02-26 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1996-02-26 1996-08-27 1997-02-26 $7700.00 Window Closed / Lapsed

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