Once-through evaporator systems

Patent metadata

Field	Value
Publication number	US-11506378-B2
Application number	US-201816194455-A
Country	US
Kind code	B2
Filing date	Nov 19, 2018
Priority date	Dec 8, 2017
Publication date	Nov 22, 2022
Grant date	Nov 22, 2022

Abstract

The present application provides a once-through evaporator system. The once-through evaporator system may include a number of once-through evaporator sections having an upstream distribution valve and a downstream temperature sensor and a position controller in communication with each distribution valve.

First claim

We claim:

1. A once-through evaporator system, comprising:
a plurality of once-through evaporator sections;
each of the plurality of once-through evaporator sections comprising an upstream distribution valve and a downstream temperature sensor; and
a position controller in communication with each upstream distribution valve,
wherein each downstream temperature sensor and a temperature controller are disposed in communication with each position controller, wherein each position controller is configured to determine a static head prediction and a required pressure drop over each upstream distribution valve to determine a valve stroke of the respective upstream distribution valve, wherein each temperature controller is configured to provide a flow target to each position controller as a set point, wherein the set point is based on an average of once-through evaporator section temperatures, wherein the set point is biased by a dead band based on the average of once-through evaporator section temperatures with respect to an average saturation temperature.

2. The once-through evaporator system of claim 1 , wherein each temperature controller biases the respective set point based on a feedforward signal.

3. The once-through evaporator system of claim 2 , wherein each positon controller and each temperature controller comprise a proportional-integral-derivative controller.

4. The once-through evaporator system of claim 1 , wherein each of the plurality of once-through evaporator sections comprises an upstream flow meter to determine a flow rate therethrough.

5. The once-through evaporator system of claim 4 , wherein each of the plurality of once-through evaporator sections comprises a sectional flow controller in communication with the upstream flow meter.

6. The once-through evaporator system of claim 1 , further comprising a main control valve supplying each of the plurality of once-through evaporator sections and a feedwater controller in communication with the main control valve.

7. The once-through evaporator system of claim 1 , further comprising a water separator downstream of the plurality of once-through evaporator sections.

8. The once-through evaporator system of claim 7 , further comprising a plurality of superheaters downstream of the water separator.

9. The once-through evaporator system of claim 1 , comprising a water separator with a water separator temperature sensor downstream of the plurality of once-through evaporator sections, wherein each upstream distribution valve is in communication with a deadband flow control system having at least one controller.

10. The once-through evaporator system of claim 1 , wherein each position controller is configured to determine the static head prediction and the required pressure drop over each upstream distribution valve at a measured or commanded flow rate.

11. The once-through evaporator system of claim 10 , wherein the required pressure drop over each upstream distribution valve at the measured or commanded flow rate is used to maintain a minimum pressure drop over the upstream distribution valves to maintain controllability of each upstream distribution valve.

12. The once-through evaporator system of claim 1 , wherein the valve stroke is used to position the upstream distribution valves via open loop control.

13. The once-through evaporator system of claim 1 , wherein the valve stroke is used as a feedforward input into each temperature controller.

14. A method to control a once-through evaporator system with a plurality of once-through evaporator sections, comprising:
receiving section temperatures of the plurality of once-through evaporator sections, wherein each of the plurality of once-through evaporator sections comprises an upstream distribution valve, a downstream temperature sensor, and a position controller in communication with each upstream distribution valve, wherein each downstream temperature sensor and a temperature controller are in communication with each position controller;
determining, via each position controller, a static head prediction and a required pressure drop over each upstream distribution valve to determine a valve stroke of the respective upstream distribution valve;
providing, via each temperature controller, a flow target to each position controller as a set point, wherein the set point is based on an average of the section temperatures of the plurality of once-through evaporator sections; and
biasing the set point by a dead band based on the average of the section temperatures with respect to an average saturation temperature.

15. A once-through evaporator system, comprising:
a plurality of once-through evaporator sections, wherein each of the plurality of once-through evaporator sections comprises an upstream distribution valve and a downstream temperature sensor;
a water separator with a water separator temperature sensor downstream of the plurality of once-through evaporator sections;
a position controller in communication with each upstream distribution valve; and
a deadband flow control system comprising a temperature control loop with a temperature controller, wherein each upstream distribution valve is in communication with the deadband flow control system, wherein each downstream temperature sensor of the plurality of once-through evaporator sections is in communication with the temperature controller, wherein the deadband flow control system is configured to sum the output of each downstream temperature sensor of the plurality of once-through evaporator sections and the water separator temperature sensor and compare the sum to a deadband signal to determine a set point for the temperature controller, wherein the deadband flow control system comprises a flow control loop with a flow controller, wherein the deadband flow control system is configured to combine the set point for the temperature controller with a feedforward signal for a flow controller set point.

Assignees

• General Electric Technology Gmbh

Inventors

• Koller Petrus Johannes
• Lenherr Hans Ulrich
• Taylor Alexander
• Gysel Stefan Lukas

Classifications

• Y02E20/16

  Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT] · CPC title

• F22B35/10 Primary

  of once-through type · CPC title

• F22B1/1815

  using the exhaust gases of gas-turbines · CPC title

• F22B29/06 Primary

  of once-through type, i.e. built-up from tubes receiving water at one end and delivering superheated steam at the other end of the tubes (combined low- and high-pressure boilers of forced-flow type F22B33/16) · CPC title

• F22B35/108

  Control systems for steam generators having multiple flow paths · CPC title