US4852053A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Material and energy balance reconciliation
Assignee: ExxonMobil Chemical Patents Inc
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Filing: 1988-02-03
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Granted: 1989-07-25
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Expires: 2008-02-03
Abstract
Abstract A method for controlling a system parameter based on controlling a setpoint for a process control variable includes measuring the rate of input to and output from a vessel. The difference between the input and output rates is determined to provide an expected rate of accumulation in the vessel. The actual rate of accumulation in the vessel is measured. The difference between the expected rate of accumulation and the actual rate of accumulation is determined to provide a bias term. A value for the setpoint for the process control variable is calculated by solving one of a material or energy balance equation which includes the bias term and a term representative of a predetermined time period during which the controlled parameter is to reach a desired value. The setpoint for the process control variable is then controlled based on the calculated setpoint value. An apparatus is disclosed for carrying out the disclosed method.
Inventors
- 👤 Bruce D. Turrie
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 09:03
CPC Classifications
G; G05; G05D; G05D9/00; G05D9/12; Y; Y10; Y10T; Y10T137/00; Y10T137/7287; Y10T137/7303; Y10T137/7329
Claims Analysis
Total Claims: 21
Claim 1
Independent Claim
219 words
A method for controlling a parameter of a system based on controlling a setpoint for a process control variable, comprising the steps of: measuring the rate of input to and output from a vessel; measuring the actual rate of accumulation in said vessel; calculating a model bias factor by solving a first model equation by determining the difference between the input and output rates to provide a calculated expected rate of accumulation in said vessel and determining the difference between said expected rate of accumulation and said actual rate of accumulation to provide said model bias factor; calculating a value for said setpoint for said process control variable by solving a second model equation, said second model equation being representative of the balance of material or energy in said system and including a term representative of (i) a predetermined time period during which said parameter is to reach a desired value and (ii) said model bias factor, said model bias factor being a function of error in said first model equation and providing for adjustment to said second model equation based upon said error, said error corresponding to the difference between said calculated expected rate of accumulation and the measured actual rate of accumulation; and controlling said setpoint for said process control variable based on said calculated setpoint value.
Claim 2
Independent Claim
219 words
A method for controlling a parameter of a system based on controlling a setpoint for a process control variable, comprising the steps of: measuring the rate of input to and output from a vessel; measuring the actual rate of accumulation in said vessel; calculating a model bias factor by solving a first model equation by determining the difference between the input and output rates to provide a calculated expected rate of accumulation in said vessel and determining the difference between said expected rate of accumulation and said actual rate of accumulation to provide said model bias factor; calculating a value for said setpoint for said process control variable by solving a second model equation, said second model equation being representative of the balance of material or energy in said system and including a term representative of (i) a predetermined time period during which said parameter is to reach a desired value and (ii) said model bias factor, said model bias factor being a function of error in said first model equation and providing for adjustment to said second model equation based upon said error, said error corresponding to the difference between said calculated expected rate of accumulation and the measured actual rate of accumulation; and controlling said setpoint for said process control variable based on said calculated setpoint value.
Claim 3
Dependent Claim
38 words
The method of claim 1 wherein said step of measuring the rate of input to and output from a vessel includes the step of measuring the rate of flow of material input to and output from the vessel.
Claim 4
Dependent Claim
42 words
The method of claim 2 wherein determining the difference between the input and output rates includes the step of determining the difference between the input and output flow rates to provide an expected rate of accumulation of said material in said vessel.
Claim 5
Dependent Claim
30 words
The method of claim 3 wherein said step of measuring the actual rate of accumulation includes the step of measuring the actual rate of accumulation of material in said vessel.
Claim 6
Dependent Claim
66 words
The method of claim 4 wherein said step of measuring the actual rate of accumulation of material in said vessel includes the steps of periodically measuring the level of material in said vessel to provide a series of level measurements, and comparing the current level measurement to the previous level measurement to provide an indication of the actual rate of accumulation of material in said vessel.
Claim 7
Dependent Claim
30 words
The method of claim 4 wherein said second model equation is formulated such that said actual rate of accumulation equals said expected rate of accumulation plus said model bias factor.
Claim 8
Dependent Claim
22 words
The method of claim 6 wherein said calculating step includes the step of calculating a value for an input flow control setpoint.
Claim 9
Dependent Claim
22 words
The method of claim 6 wherein said calculating step includes the step of calculating a value for an output flow control setpoint.
Claim 10
Dependent Claim
22 words
The method of claim 6 wherein said second model equation further includes a term representative of a substance generated within said vessel.
Claim 11
Dependent Claim
15 words
The method of claim 1 comprising the further step of filtering said model bias factor.
Claim 12
Dependent Claim
37 words
The method of claim 1 wherein said step of measuring the rate of input to and output from a vessel includes the step of measuring the rate of energy added to and energy removed from said vessel.
Claim 13
Dependent Claim
42 words
The method of claim 11 wherein determining the difference between the input and output rates includes the step of determining the difference between the energy input and energy output rates to provide an expected rate of accumulation of energy in said vessel.
Claim 14
Dependent Claim
30 words
The method of claim 12 wherein said step of measuring the actual rate of accumulation includes the step of measuring the actual rate of accumulation of energy in said vessel.
Claim 15
Dependent Claim
60 words
The method of claim 13 wherein said step of measuring the actual energy in said vessel includes the steps of periodically measuring the energy in said vessel to provide a series of energy measurements, and comparing the current energy measurement to the previous energy measurement to provide an indication of the actual rate of accumulation of energy in said vessel.
Claim 16
Dependent Claim
30 words
The method of claim 13 wherein said second model equation is formulated such that said actual rate of accumulation equals said expected rate of accumulation plus said model bias factor.
Claim 17
Dependent Claim
22 words
The method of claim 15 wherein said calculating step includes the step of calculating a value for an input fuel control setpoint.
Claim 18
Dependent Claim
23 words
The method of claim 15 wherein said calculating step includes the step of calculating a value for an input coolant flow control setpoint.
Claim 19
Dependent Claim
21 words
The method of claim 15 wherein said second model equation further includes a term representative of heat generated within said vessel.
Claim 20
Independent Claim
240 words
An apparatus for controlling a parameter of a system based on controlling a setpoint for a process control variable of a process carried out in a vessel, comprising: means for measuring the rate of input to and output from said vessel; sensing means for sensing the actual rate of accumulation in said vessel; means for calculating a model bias factor by solving a first model equation including means for determining the difference between the input and output rates to provide a calculated expected rate of accumulation in said vessel and means for determining the difference between said expected rate of accumulation and said actual rate of accumulation to provide said model bias factor; means for calculating a value for said setpoint for said process control variable by solving a second model equation, said second model equation being representative of the balance of material or energy in said system and including a term representative of (i) a predetermined time period during which said parameter is to reach a desired value and (ii) said model bias factor, said model bias factor being a function of error in said first model equation and providing for adjustment to said second model equation based upon said error, said error corresponding to the difference between said calculated expected rate of accumulation and the measured actual rate of accumulation; and output means for controlling said setpoint for said process control variable based on said calculated setpoint value.
Claim 21
Independent Claim
240 words
An apparatus for controlling a parameter of a system based on controlling a setpoint for a process control variable of a process carried out in a vessel, comprising: means for measuring the rate of input to and output from said vessel; sensing means for sensing the actual rate of accumulation in said vessel; means for calculating a model bias factor by solving a first model equation including means for determining the difference between the input and output rates to provide a calculated expected rate of accumulation in said vessel and means for determining the difference between said expected rate of accumulation and said actual rate of accumulation to provide said model bias factor; means for calculating a value for said setpoint for said process control variable by solving a second model equation, said second model equation being representative of the balance of material or energy in said system and including a term representative of (i) a predetermined time period during which said parameter is to reach a desired value and (ii) said model bias factor, said model bias factor being a function of error in said first model equation and providing for adjustment to said second model equation based upon said error, said error corresponding to the difference between said calculated expected rate of accumulation and the measured actual rate of accumulation; and output means for controlling said setpoint for said process control variable based on said calculated setpoint value.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
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| 3.5 Years (Year 4) | 1992-07-24 | 1993-01-23 | 1993-07-25 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1996-07-24 | 1997-01-23 | 1997-07-25 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2000-07-24 | 2001-01-23 | 2001-07-25 | $7700.00 | Window Closed / Lapsed |