Methods and systems for controlling gas temperatures
View Patent ↗Methods and systems for controlling the temperature of a heated flue gas stream downstream of a multi-part heat exchanger within a desired operating range through the use of a fluid bypass line which bypasses one or more sections, but not all sections, of the multi-part heat exchanger. In some but not necessarily all embodiments some fluid flow is maintained through the heat exchanger at all times. In one embodiment, the method includes sensing a temperature in said flue gas stream in proximity to an intermediate header of said multi-part heat exchanger and controlling a position of a bypass line control valve to control an amount of fluid passing through a fluid bypass line that bypasses the section of the multi-part heat exchanger between an inlet header and the intermediate header based on said temperature in said flue gas stream in proximity to the intermediate header of said multi-part heat exchanger.
1. A method for controlling the temperature of a heated flue gas stream at a location downstream of a multi-part heat exchanger within a desired operating temperature range, the method comprising:
sensing, using a first temperature sensor, a temperature in said flue gas stream in proximity to an intermediate header of said multipart heat exchanger, said multi-part heat exchanger including:
a first heat exchanger section located in said flue gas stream said first heat exchanger section having a fluid inlet coupled to a fluid feed line;
a second heat exchanger section located in series with said first heat exchanger section in said flue gas stream, said second heat exchanger section being located upstream of said first heat exchanger section in said flue gas stream; and
said intermediate header having a first mixer fluid input, a second mixer fluid input, and a fluid outlet, said first mixer fluid input being coupled to a fluid output of said first heat exchanger section, and said fluid outlet being coupled to a fluid inlet of said second heat exchanger section; and
a fluid bypass line coupling said fluid feed line to said second mixer fluid input of said intermediate header, said fluid bypass line extending outside of said flue gas stream and providing a fluid bypass allowing at least some fluid supplied by said fluid feed line to fully bypass said first heat exchanger section; and
controlling a position of a bypass line control valve to control an amount of fluid passing through said fluid bypass line to the second mixer fluid input based on said temperature in said flue gas stream in proximity to the intermediate header of said multipart heat exchanger.
2. The method of claim 1 ,
wherein said bypass line control valve is a multi-position valve supporting multiple positions between a full open and a full closed position; and
wherein said controlling the position of said bypass line control valve includes maintaining said bypass line in a full open state when said temperature measured by said first temperature sensor in said flue gas stream is below a first temperature and closing said valve as said temperature measured by said first temperature sensor increases beyond said first temperature.
3. The method of claim 2 further comprising:
sensing, using a second temperature sensor located in said flue gas stream in proximity to a flue gas outlet, a flue gas output temperature; and
wherein controlling the amount of fluid allowed to pass through said fluid bypass line to the second mixer fluid input is also based on the flue gas output temperature sensed by said second temperature sensor.
4. The method of claim 3 , wherein controlling the position of said bypass line control valve includes:
maintaining said bypass line control valve in a fully closed state when said second temperature sensor indicates the flue gas output temperature is in a desired operating range.
5. The method of claim 2 further comprising:
controlling a position of an economizer flow control valve, from a minimally open position to a fully open position, to control an amount of fluid passing through said first heat exchanger section as a function of at least one of the temperature measured by said first temperature sensor or the temperature measured by said second temperature sensor.
6. The method of claim 5 , wherein controlling a position of an economizer flow control valve includes opening the economizer flow control valve when said first temperature sensor indicates a temperature which increases over said first temperature.
7. The method of claim 6 , wherein controlling the position of said economizer flow control valve is further based on the flue gas output temperature sensed by said second temperature sensor in addition to the temperature sensed by said first temperature sensor.
8. The method of claim 7 , wherein controlling the position of the economizer flow control valve includes:
controlling the economizer flow control valve to operate in a fully open state after: (i) said second temperature sensor senses a flue gas output temperature that is in a desired operating range, (ii) said bypass line control valve has been put in a fully closed state, and (iii) said economizer flow control valve has been opened to the fully open state.
9. The method of claim 8 , wherein controlling the economizer flow control valve includes maintaining at least some flow through the economizer flow control valve during all times of operation.
10. The method of claim 9 , wherein said at least some flow is not less than 10% of the maximum fluid flow through said economizer flow control valve.