Desuperheater system

1. A desuperheater system for cooling a process fluid comprising:

a pipe through which the process fluid flows defining an axis;

a plurality of injector housings attached to and arranged radially around the pipe, the plurality of injector housings each defining an injector cavity in fluid communication with an injector housing inlet port, the injector housing inlet port being in fluid communication with a cooling fluid;

a plurality of injectors each including an inlet portion at a first end and defining an injector inlet port and a probe portion extending from the inlet portion and including an injector nozzle defining an injection angle, the injector nozzle being at a second end opposite the first end, one of the plurality of injectors being received in each injector cavity with the injector inlet port aligned and in fluid communication with the injector housing inlet port, the injector nozzles being in fluid communication with the process fluid, the injection angle of each injection nozzle being selected individually;

a control valve including a valve inlet port configured to receive a cooling fluid, the control valve configured to selectively provide fluid communication between the valve inlet port and at least one of the plurality of injectors to inject the cooling fluid into the process fluid;

wherein the plurality of injector housings comprises six injector housings;

a first group of the six injector housings includes three injector housings arranged radially in one hundred and twenty degree increments around the pipe at a first axial location on the pipe; and

a second group of the six injector housings includes three injector housings arranged radially in one hundred and twenty degree increments around the pipe, offset sixty degrees from the first group at a second axial location on the pipe.

2. The desuperheater system of claim 1 , wherein the control valve further includes a piston housing, a piston mechanism arranged within the piston housing, and a plurality of injection tubes each providing fluid communication between the piston housing and one of the plurality of injectors.

3. The desuperheater system of claim 2 , wherein the piston mechanism moves to selectively provide fluid communication between the valve inlet port and at least one of the plurality of injectors.

4. The desuperheater system of claim 1 , wherein the first axial location is upstream of the second axial location.

5. The desuperheater system of claim 1 , wherein the pipe further comprises a pipe liner arranged concentrically within the pipe and including a plurality of liner apertures.

6. The desuperheater system of claim 5 , wherein the plurality of liner apertures are each arranged to substantially align with one of the plurality of injector housings.

7. The desuperheater system of claim 1 , wherein each of the injector cavities receive the one of the plurality of injectors so that cooling flow from the control valve to the one of the plurality of injectors flows from the injector housing inlet port through the injector cavity before entering an injector inlet port of the one of the plurality of injectors.

8. The desuperheater system of claim 1 , wherein the injector nozzles are swirl nozzles.

9. The desuperheater system of claim 1 , wherein at least one of the injector nozzles is a first nozzle and at least one of the injector nozzles is a second nozzle, the first nozzle having a larger coefficient of velocity than the second nozzle.

10. The desuperheater system of claim 1 , wherein the plurality of injectors are arranged radially around the pipe and spaced axially relative to one another.

11. The desuperheater system of claim 5 , further including a spacer at an end of the liner, the spacer providing a radial gap between the liner and the pipe and inhibiting heat transfer between the fluid and the pipe.

12. A method of operating a desuperheater system for cooling a process fluid, the method comprising:

selecting a first injector group that includes a first plurality of injectors arranged circumferentially around a pipe at a first longitudinal location along the pipe and having one of a first injection angle and a second injection angle;

selecting a second injector group that includes a second plurality of injectors arranged circumferentially around the pipe at a second longitudinal location along the pipe that is different from the first longitudinal location, the second injector group being angularly offset from the first group by 60 degrees and having one of the first injection angle and the second injection angle;

passing a flow of steam through the pipe;

moving a control valve piston mechanism to a first position where cooling fluid is inhibited from flowing to the first injector group and the second injector group;

moving the control valve piston mechanism to a second position where cooling fluid is provided to the first injector group;

atomizing the cooling fluid through swirl nozzles of the first injector group;

moving the control valve piston mechanism to a third position where cooling fluid is provided to the first injector group and the second injector group; and

atomizing cooling fluid through swirl nozzles of the second injector group that are arranged downstream of the first injector group.

13. The method of claim 12 , wherein selecting a first injector group includes choosing from one of a first coefficient of velocity and a second coefficient of velocity.

14. The method of claim 12 , wherein selecting the second injector group includes selecting an injection angle that is different than the injection angle selected for the first injector group.

15. The method of claim 12 , further comprising moving the control valve piston mechanism linearly between the first position, the second position, and the third position.

16. The method of claim 12 , wherein selecting the first injector group includes inserting the swirl nozzles of the first injector group into first injector housings coupled to the pipe.

17. The method of claim 12 , wherein atomizing the cooling fluid through swirl nozzles of the first injector group includes atomizing the cooling fluid through three swirl nozzles arranged radially around the pipe.

18. A desuperheater system for cooling a process fluid comprising:

a pipe through which the process fluid flows, the pipe defining an axis;

a first group of three injector housings arranged radially in one hundred and twenty degree increments around the pipe;

a second group of three injector housings arranged radially in one hundred and twenty degree increments around the pipe, the second group of three injector housings being offset from the first set of three injector housings by sixty degrees and the second group of three injector housings being spaced along the axis from the first group of three injector housings, each of injector housings of the first and second groups of three injectors housings including an injector cavity;

a plurality of injectors each including an injector nozzle defining an injection angle, a respective one of the plurality of injectors being received in each injector cavity, the injector nozzles being in fluid communication with the process fluid, the injection angle of each injection nozzle being selected individually, each injection nozzle being selected from one of a first nozzle and a second nozzle, the first nozzle having a larger coefficient of velocity that the second nozzle; and

a control valve including a valve inlet port configured to receive a cooling fluid, the control valve configured to selectively provide fluid communication between the valve inlet port and at least one of the plurality of injectors to inject the cooling fluid into the process fluid.