Method for detecting heat exchanger tube failures when using input/loss performance monitoring of a power plant

• US 6,745,152 B1
• Filed: 04/24/2002
• Issued: 06/01/2004
• Est. Priority Date: 03/24/1998
• Status: Expired due to Fees

• Current Assignee: Exergetic Systems LLC
• Original Assignee: Exergetic Systems LLC
• Inventors: Lang, Fred D
• Primary Examiner(s): Hoff, Marc S.
• Assistant Examiner(s): Barbee, Manuel L
• Application Number:
  US10/131,932
• Time in Patent Office: 769 Days
• Field of Search: 702/22-25, 702/30-32, 702/45, 702/50, 702/51, 702/55, 702/114, 702/181-185, 60/392.4, 60/395.11, 606/61, 607/93, 700/274, 700/286, 703/2, 706/907, 706/915, 165/11.1, 165/70, 431/16, 431/22
• US Class Current: 702/183
• CPC Class Codes: F22B 35/18 Applications of computers to steam boiler control
• CPC Class Codes: F23N 1/002 using electronic means F23N1/04 - F23N1/10 take precedence
• CPC Class Codes: F23N 2221/08 Preheating the air
• CPC Class Codes: F23N 2221/10 Analysing fuel properties, e.g. density, calorific
• CPC Class Codes: F23N 2223/40 Simulation
• CPC Class Codes: F23N 2225/22 heat losses
• CPC Class Codes: F23N 5/003 using detectors sensitive to combustion gas properties F23N5/02, F23N5/18 - F23N5/26 take precedence
• CPC Class Codes: Y02E 20/32 Direct CO2 mitigation

Abstract

This invention relates to a fossil-fired thermal system such as a power plant or steam generator, and, more particularly, to a method for rapid detection of tube failures without direct instrumentation, thereby preventing serious damage to heat exchangers. This method is applicable to Input/Loss methods of monitoring fossil-fired thermal systems.

Claims

1. A method for quantifying the operation of a fossil-fired thermal system when a fuel chemistry is determined from Input/Loss methods through knowledge of when its heat exchanger leaks at a tube leakage flow rate into the combustion gases, the method for quantifying the operation comprising the steps of:

selecting a set of minimization techniques applicable to the thermal system and its fuel, and a set of routine inputs and convergence criteria to the minimization techniques, and a Choice Operating Parameter of tube leakage flow rate, and an initial value of tube leakage flow rate,

selecting a set of routine Choice Operating Parameters and their initial values,

determining a set of System Effect Parameters applicable to the thermal system and its fuel whose functionalities effect the determination of system heat rate rate and tube leakage flow rate,

determining a set of Reference System Effect Parameters applicable to the set of System Effect Parameters,

determining an objective function applicable to the thermal system'"'"'s stoichiometric situation which uses the Choice Operating Parameters of tube leakage flow rate, the set of routine Choice Operating Parameters, the set of System Effect Parameters, and the set of Reference System Effect Parameters,

optimizing the Choice Operating Parameters of tube leakage flow rate and the set of routine Choice Operating Parameters by employing the set of minimization techniques and the objective function such that convergence criteria is met resulting in a set of converged Choice Operating Parameters including a final tube leakage flow rate, and

reporting the final tube leakage flow rate such that corrective action may take place.

2. The method according to claim 1 further comprising the steps of:

determining the fuel chemistry of the fuel being combusted by the thermal system using Input/Loss methods, the set of converged Choice Operating Parameters and Operating Parameters as influenced by tube leakage flow rate,

determining a set of Reference Fuel Chemistry data,

determining a fuel heating value of the system using the fuel chemistry and the set of Reference Fuel Chemistry data,

determining a Firing Correction base on Operating Parameters,

determining a boiler efficiency of the thermal system independent of fuel flow using the set of converged Choice Operating Parameters including the tube leakage flow rate, the fuel chemistry, the fuel heating value, the Firing Correction and Operating Parameters,

determining an energy flow to the working fluid of the thermal system based on the Operating Parameters as influenced by the tube leakage flow rate,

determining a fuel flow of the fuel being combusted using the energy flow to the working fluid, the fuel heating value, the Firing Correction and the boiler efficiency, and

reporting the fuel flow as influenced by the tube leakage flow rate.

3. The method according to claim 2 further comprising the steps of:

determining a power output from the thermal system,

determining a system heat rate using the fuel flow, the fuel heating value, the Firing Correction and the power output from the thermal system, and

reporting the system heat rate as influenced by the tube leakage flow rate.

4. The method according to claim 2 further comprising the steps of:

determining a power output from the thermal system,

determining a system heat rate using the energy flow to the working fluid, the boiler efficiency and the power output from the thermal system, and

reporting the system heat rate as influenced by the tube leakage flow rate.

5. The method of claim 1, wherein the step of selecting the set of minimization techniques applicable to the thermal system and its fuel comprises a step of:

including a BFGS technique.

6. The method of claim 1, wherein the step of selecting the set of minimization techniques applicable to the thermal system and its fuel comprises a step of:

including a Simulated Annealing technique.

7. The method of claim 1, wherein the step of selecting the set of minimization techniques applicable to the thermal system and its fuel comprises a step of:

including a neural network technique.

8. The method of claim 1, wherein the step of selecting the set of minimization techniques applicable to the thermal system and its fuel comprises a step of:

including a Neugents technology.

9. The method of claim 1, wherein the step of selecting the set of routine Choice Operating Parameters and their initial values, comprises a step of:

determining a set of scaling factors for the set of routine Choice Operating Parameters resulting in the set of routine Choice Operating Parameters whose values are scaled.

10. The method of claim 1, wherein the step of optimizing the Choice Operating Parameter of tube leakage flow rate and the set of routine Choice Operating Parameters, comprises a step of:

determining a set of correction factors to the set of Choice Operating Parameters using their initial and converged values.

11. The method of claim 1, wherein the step of selecting the set of minimization techniques applicable to the thermal system and its fuel, and the set of routine inputs and convergence criteria to the minimization techniques, and the Choice Operating Parameters of tube leakage flow rate, and the initial value of tube leakage flow rate, comprises the steps of:

selecting a Simulated Annealing technique,

processing a set of routine inputs and convergence criteria to the Simulated Annealing technique,

equating a set of routine Choice Operating Parameters excluding a Choice Operating Parameter for effluent water to their last converged values,

multiplying a value of uncorrected effluent water concentration by a reference correction factor resulting in a constant effluent water concentration,

determining a set of System Effect Parameters applicable to the thermal system and its fuel whose functionalities effect the determination of system heat rate rate and tube leakage flow rate,

determining a set of Reference System Effect Parameters applicable to the set of System Effect Parameters,

determining an objective function applicable to the thermal system'"'"'s stoichiometric situation and possible tube leakage which employs System Effect Parameters, and Reference System Effect Parameters,

optimizing the Choice Operating Parameters of tube leakage flow rate and the set of routine Choice Operating Parameters excluding the Choice Operating Parameter for effluent water, using the initial estimate of tube leakage flow rate and the constant effluent water concentration by employing the Simulated Annealing technique used to minimize the objective function such that convergence criteria is met resulting in an initial computed tube leakage flow rate, and

determining the initial value of tube leakage flow rate by equating it to the initial computed tube leakage flow rate.

12. A method for quantifying the operation of a fossil-fired thermal system, when a fuel chemistry is determined from Input/Loss methods through knowledge of a stoichiometric mechanism of how a heat exchanger could be leaking at a tube leakage flow rate into the combustion gases, the method for quantifying the operation comprising the steps of:

determining a fuel chemistry of the fuel being combusted by the thermal system using Input/Loss methods, Choice Operating Parameters, Operating Parameters and Reference Fuel Characteristics resulting in a fuel elementary composition, a fuel ash fraction and a fuel water fraction said composition and fractions resulting in a set of fuel concentrations,

establishing a set of concentration limits for each fuel constituent based on Reference Fuel Characteristics,

testing the set of fuel concentrations against the set of concentration limits resulting in a trip mechanism indicating stoichiometric reason how a heat exchanger leaks at a tube leakage flow rate into the combustion gases,

reporting the trip mechanism to the operator of the thermal system.

13. A method for quantifying the operation of a fossil-fired thermal system, when a fuel chemistry is determined from Input/Loss methods, through knowledge of a stoichiometric mechanism of how a heat exchanger could be leaking at a tube leakage flow rate into the combustion gases, the method for quantifying the operation comprising the steps of:

selecting a set of minimization techniques applicable to the thermal system and its fuel,

processing a set of routine inputs and convergence criteria to the minimization techniques,

assuming a tube leakage flow rate is zero,

selecting a set of routine Choice Operating Parameters and their initial values,

determining a set of System Effect Parameters applicable to the thermal system and its fuel whose functionalities effect the determination of system heat rate,

determining a set of Reference System Effect Parameters applicable to the set of System Effect Parameters,

determining an objective function applicable to the thermal system'"'"'s stoichiometric situation, the set of routine Choice Operating Parameters, the set of System Effect Parameters and the set of Reference System Effect Parameters,

optimizing the set of routine Choice Operating Parameters by employing the set of minimization techniques and the objective function such that convergence criteria is met resulting in a set of converged Choice Operating Parameters,

determining a set of correction factors to Choice Operating Parameters using their initial and converged values,

determining a fuel chemistry of the fuel being combusted by the thermal system using Input/Loss methods, the set of converged Choice Operating Parameters, Operating Parameters and Reference Fuel Characteristics resulting in a fuel elementary composition, a fuel ash fraction and a fuel water fraction said composition and fractions resulting in a set of fuel concentrations,

establishing a set of concentration limits for each fuel constituent based on Reference Fuel Characteristics and then testing the set of fuel concentrations against the set of concentration limits resulting in a trip mechanism indicating the stoichiometric reason how a heat exchanger leaks at a tube leakage flow rate into the combustion gases, and

reporting the trip mechanism to the operator of the thermal system.

14. The method of claim 13, wherein the step of establishing a set of concentration limits for the set of fuel concentration based on Reference Fuel Characteristics and then testing the set of fuel concentrations against the concentration limits comprises a step of:

establishing a set of correction factor limits for the selected Choice Operating Parameters, and testing the set of correction factors against the set of correction factor limits resulting in a trip mechanism indicating the stoichiometric reason how a heat exchanger leaks a tube leakage flow rate into the combustion gases.

15. A method for quantifying the operation of a fossil-fired thermal system when a fuel chemistry is determined from Input/Loss methods through knowledge of when its heat exchanger leaks at a tube leakage flow rate into the combustion gases, the method for quantifying the operation comprising the steps of:

selecting a neural network technology applicable to the thermal system and its fuel,

selecting a set of routine inputs and database for the neural network technology,

selecting a Choice Operating Parameters of tube leakage flow rate and an initial value of tube leakage flow rate,

selecting a set of routine Choice Operating Parameters and their initial values,

determining a set of System Effect Parameters applicable to the thermal system and its fuel whose functionalities effect the determination of system heat rate and tube leakage flow rate,

determining a set of Reference System Effect Parameters applicable to the set of System Effect Parameters,

optimizing the Choice Operating Parameters of tube leakage flow rate and the set of routine Choice Operating Parameters using the neural network technology, the set of routine inputs and database, the set of System Effects Parameters and the set of Reference Systems Effect Parameters such that convergence criteria is met resulting in a set of converged Choice Operating Parameters including a final tube leakage flow rate, and

reporting the final tube leakage flow rate such that corrective action may take place.

16. The method of claim 15, wherein the step of selecting the neural network technology applicable to the thermal system and its fuel, comprises a step of:

selecting a Neugents technology.

17. A method for quantifying the operation of a fossil-fired thermal system when a fuel chemistry is determined from Input/Loss methods in through knowledge of when its heat exchanger leaks at a tube leakage flow rate into the combustion gases, the method for quantifying the operation comprising the steps of:

establishing a combustion equation,

determine a molar equivalent to tube leakage,

forming a hydrogen stoichiometric balance based on the combustion equation which balance includes the molar equivalent to tube leakage,

solving the hydrogen stoichiometric balance for the molar equivalent to the leakage,

determining the tube leakage flow rate from the molar equivalent to tube leakage, and reporting the final tube leakage flow rate such that corrective action may take place.

18. A method for quantifying the operation of a fossil-fired thermal system when a fuel chemistry is determined from Input/Loss methods through knowledge of when its heat exchanger leaks at a tube leakage flow rate into the combustion gases, the method for quantifying the operation comprising the steps of:

establishing a combustion equation,

forming a hydrogen balance based on the combustion equation which balance includes a term descriptive of tube leakage,

solving the hydrogen balance for the term descriptive of tube leakage,

converting the term descriptive of tube leakage to the tube leakage flow rate, and

reporting the tube leakage flow rate such that corrective action may take place.