Patent US4177951A successfully refreshed from Google Patents.
US4177951A
Expired / Lapsed
US
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Pulverizer air flow and temperature control
Assignee: Combustion Engineering Inc
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Filing: 1978-06-28
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Granted: 1979-12-11
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Expires: 1998-06-28
Abstract
Abstract The flow of preheated and ambient air to a processor, such as a coal pulverizer, are controlled in a manner whereby the preheated air flow will be varied as a function of pulverizer discharge temperature air while "cold" ambient air flow will be varied as a function of pulverizer inlet air mass flow rate. Flow error signals are caused to vary as a function of temperature error to enhance system response to temperature errors, and flow error will be caused to take precedence over temperature error should pulverizer inlet flow fall below a predetermined minimum.
Inventors
- 👤 John A. Makuch
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 20:53
CPC Classifications
F; F23; F23K; F23K1/00; F23K1/04; F23K3/00; F23K3/02; F23N; F23N1/00; F23N1/02; F23N5/00; F23N5/18; F23N2225/00; F23N2225/08; F23N2235/00; F23N2235/02; F23N2235/06; F23N2235/10; F23N2235/12; F23N2239/00; F23N2239/02; Y; Y02; Y02E; Y02E20/00; Y02E20/34
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
281 words
A method for controlling the quantities of at least two constituents of a fluid mixture delivered to a mixing point in response to measured parameters of the mixture comprising the steps of: selecting normal values for first and second parameters of the mixture; selecting a desired minimum value for the mixture second parameter; measuring the actual value of the mixture first parameter; comparing the measured and selected normal values of the mixture first parameter; adjusting the flow of the first constituent to compensate for any difference between the measured actual and selected normal values of the mixture first parameter when the mixture second parameter is above the selected desired minimum value; modifying the selected value of the mixture second parameter as a function of any difference between the measured actual and selected normal values of the mixture first parameter; measuring the actual value of the mixture second parameter; comparing the measured and modified selected values of the mixture second parameter; adjusting the flow of the second constituent to compensate for any difference between the measured actual and modified selected values of the mixture second parameter when the second parameter is above the selected desired minimum value; adjusting the flow of the first constituent as a function of the rate of change of the second parameter when the second parameter is below the selected desired minimum value; comparing the measured and actual selected desired minimum values of the mixture second parameter when the second parameter is below the desired minimum; and adjusting the flow rate of the second constituent to compensate for any difference between the measured actual and selected minimum values when the flow rate is below the selected minimum value.
Claim 2
Independent Claim
281 words
A method for controlling the quantities of at least two constituents of a fluid mixture delivered to a mixing point in response to measured parameters of the mixture comprising the steps of: selecting normal values for first and second parameters of the mixture; selecting a desired minimum value for the mixture second parameter; measuring the actual value of the mixture first parameter; comparing the measured and selected normal values of the mixture first parameter; adjusting the flow of the first constituent to compensate for any difference between the measured actual and selected normal values of the mixture first parameter when the mixture second parameter is above the selected desired minimum value; modifying the selected value of the mixture second parameter as a function of any difference between the measured actual and selected normal values of the mixture first parameter; measuring the actual value of the mixture second parameter; comparing the measured and modified selected values of the mixture second parameter; adjusting the flow of the second constituent to compensate for any difference between the measured actual and modified selected values of the mixture second parameter when the second parameter is above the selected desired minimum value; adjusting the flow of the first constituent as a function of the rate of change of the second parameter when the second parameter is below the selected desired minimum value; comparing the measured and actual selected desired minimum values of the mixture second parameter when the second parameter is below the desired minimum; and adjusting the flow rate of the second constituent to compensate for any difference between the measured actual and selected minimum values when the flow rate is below the selected minimum value.
Claim 3
Dependent Claim
26 words
The method of claim 1 wherein the mixture first parameter is temperature and wherein said first constituent is at a higher temperature than the second constituent.
Claim 4
Dependent Claim
13 words
The method of claim 2 wherein said second parameter is mass flow rate.
Claim 5
Dependent Claim
44 words
The method of claim 3 wherein the flow of the first constituent is varied at a rate proportional to the rate of change of the mass flow rate of the mixture when the measured mass flow rate is below the selected minimum flow rate.
Claim 6
Dependent Claim
26 words
The method of claim 4 wherein the mixture is a particle laden air stream and said first and second constituents respectively comprise preheated and ambient air.
Claim 7
Dependent Claim
61 words
The method of claim 1 wherein the mixture consists of a fuel stream comprising dry pulverized coal entrained in air, the first and second constituents respectively comprise preheated and ambient air and the mass flow rates of the preheated and ambient are adjusted in opposite directions when the actual value of the mass flow rate is above the minimum selected value.
Claim 8
Dependent Claim
236 words
Apparatus for controlling the delivery of air to a coal pulverizer, the pulverizer including supplies of pressurized, preheated and unheated transport air and providing a mixture including dry pulverized coal entrained in air, said control apparatus comprising: means for generating a signal commensurate with a desired temperature of the coal-air mixture provided by the pulverizer; means for providing a signal commensurate with the actual temperature of the coal-air mixture provided by the pulverizer; means for generating a signal commensurate with a desired normal rate of flow of air to the pulverizer; means for providing a signal commensurate with the actual rate of flow of air to the pulverizer; means responsive to the signals commensurate with actual and desired mixture temperature for generating a first flow error signal; means responsive to said first flow error signal for adjusting the flow of the preheated air as a direct function of temperature error; means responsive to said first error signal and said signal commensurate with desired flow rate for generating a desired flow rate signal which varies inversely with temperature error; means for comparing said signals commensurate with inversely variable desired flow rate and actual flow rate for generating a second error signal, said second error signal varying directly with flow error and inversely with temperature error; and means responsive to said second error signal for causing a variation in the flow of said unheated air to the pulverizer.
Claim 9
Dependent Claim
236 words
Apparatus for controlling the delivery of air to a coal pulverizer, the pulverizer including supplies of pressurized, preheated and unheated transport air and providing a mixture including dry pulverized coal entrained in air, said control apparatus comprising: means for generating a signal commensurate with a desired temperature of the coal-air mixture provided by the pulverizer; means for providing a signal commensurate with the actual temperature of the coal-air mixture provided by the pulverizer; means for generating a signal commensurate with a desired normal rate of flow of air to the pulverizer; means for providing a signal commensurate with the actual rate of flow of air to the pulverizer; means responsive to the signals commensurate with actual and desired mixture temperature for generating a first flow error signal; means responsive to said first flow error signal for adjusting the flow of the preheated air as a direct function of temperature error; means responsive to said first error signal and said signal commensurate with desired flow rate for generating a desired flow rate signal which varies inversely with temperature error; means for comparing said signals commensurate with inversely variable desired flow rate and actual flow rate for generating a second error signal, said second error signal varying directly with flow error and inversely with temperature error; and means responsive to said second error signal for causing a variation in the flow of said unheated air to the pulverizer.
Claim 10
Dependent Claim
100 words
The apparatus of claim 7 further comprising: means for generating a signal commensurate with a minimum desired rate of flow of air to the pulverizer; means for comparing the signals commensurate with minimum desired and actual flow rates for generating a flow error signal which is proportional to rate of change of flow when actual air flow to the pulverizer is below the preselected minimum; and means for applying said proportional flow error signal to said means for adjusting the flow of preheated air whereby the preheated air flow will be increased when actual flow is below the desired minimum.
Claim 11
Dependent Claim
60 words
The apparatus of claim 7 further comprising: means for selecting the one of the minimum desired and inversely variable flow rate signals corresponding to the greater pulverizer input mass flow rate; and means for delivering the selected flow rate signal passed by said selecting means to said second error signal generating means for comparison with the actual flow rate signal.
Claim 12
Dependent Claim
60 words
The apparatus of claim 8 further comprising: means for selecting the one of the minimum desired and inversely variable flow rate signals corresponding to the greater pulverizer input mass flow rate; and means for delivering the selected flow rate signal passed by said selecting means to said second error signal generating means for comparison with the actual flow rate signal.
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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) | 1982-12-10 | 1983-06-11 | 1983-12-11 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-12-10 | 1987-06-11 | 1987-12-11 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-12-10 | 1991-06-11 | 1991-12-11 | $7700.00 | Window Closed / Lapsed |