System and method for slurry handling

1. A system, comprising:

a slurry source configured to output a slurry having a suspension of solids in a liquid; and

a slurry depressurizing system comprising a turbomachine configured to continuously receive the slurry from the slurry source at a first pressure and continuously discharge the slurry at a second pressure, and the turbomachine is configured to reduce the pressure of the slurry from the first pressure to the second pressure while recovering energy from the slurry.

2. The system of claim 1 , wherein the turbomachine comprises an expansion turbine.

3. The system of claim 1 , wherein the turbomachine comprises a centrifugal pump configured to operate in a reverse flow mode.

4. The system of claim 1 , wherein the turbomachine comprises a rotating element configured to rotate in response to a flow of the slurry through the turbomachine, and a load coupled to the rotating element is configured to receive a rotational output in response to rotation of the rotating element.

5. The system of claim 4 , wherein the load comprises a friction brake configured to convert the rotational output into heat energy, a generator configured to convert the rotational output into electrical power, or machinery configured to operate using the rotational output, or a combination thereof.

6. The system of claim 1 , comprising a cooler disposed upstream of the turbomachine, wherein the cooler is configured to cool the slurry prior to flowing the slurry to the turbomachine.

7. The system of claim 1 , comprising a driver coupled to the turbomachine, wherein the driver is configured to provide power to the turbomachine during startup, shutdown, a low flow condition, or any combination thereof.

8. The system of claim 1 , wherein the turbomachine is driven in response to a flow of the slurry through the turbomachine, and the turbomachine comprises an electrical generator.

9. The system of claim 1 , wherein the slurry source comprises a gasifier having a reaction chamber, wherein the slurry depressurizing system is disposed along a flow path downstream from the gasifier.

10. The system of claim 1 , wherein the slurry depressurizing system is a slag slurry depressurizing system, the turbomachine is a slag slurry expansion turbomachine, and the slurry is a slag slurry comprising slag solids in the liquid.

11. The system of claim 10 , comprising a slag crusher disposed along a flow path upstream of the slag slurry expansion turbomachine, wherein the slag crusher is configured to crush the slag solids to generate crushed slag solids, and a first average particle size of the crushed slag solids is less than a second average particle size of the slag solids.

12. The system of claim 1 , comprising a controller configured to control continuous flow of the slurry downstream from the slurry source and continuous depressurization of the slurry via the turbomachine.

13. A system, comprising:

a slurry source comprising a gasifier configured to gasify a feedstock to generate a syngas and gasification solids that mix with a liquid to form a slurry; and

a turbomachine disposed along a flow path downstream from the slurry source, wherein the turbomachine is configured to continuously receive the slurry downstream from the slurry source at a first pressure, the turbomachine is configured to continuously discharge the slurry at a second pressure, and the first pressure is greater than the second pressure.

14. The system of claim 13 , comprising a crusher disposed along the flow path between the slurry source and the turbomachine, wherein the crusher is configured to crush the gasification solids to generate crushed gasification solids, wherein a first average particle size of the crushed gasification solids is less than a second average particle size of the gasification solids.

15. The system of claim 14 , wherein the first particle size is less than approximately 6 mm.

16. The system of claim 13 , wherein a pressure difference between the first pressure and the second pressure is greater than approximately 1000 kPa.

17. The system of claim 13 , comprising a flow control valve configured to adjust a flow rate of the slurry flowing to the turbomachine.

18. The system of claim 13 , wherein the turbomachine is configured to generate electrical power, mechanical power, or heat via a friction brake in response to a flow of the slurry through the turbomachine.

19. The system of claim 13 , wherein the turbomachine comprises a centrifugal pump configured to operate in a reverse flow mode, and the centrifugal pump comprises bearings configured to operate in the reverse flow mode.

20. The system of claim 13 , comprising a controller configured to control continuous removal of the gasification solids from the slurry source and continuous depressurization of the slurry via the turbomachine.

21. The system of claim 20 , comprising a plurality of sensors configured to provide feedback to the controller, wherein the feedback comprises temperature data, pressure data, flow data, or viscosity data, or a combination thereof.

22. A method, comprising:

receiving a continuous flow of a slurry from a slurry source at a first pressure into a turbomachine along a flow path downstream from the slurry source, wherein the slurry comprises a suspension of solids in a liquid;

feeding the continuous flow of the slurry from the slurry source through the turbomachine; and

discharging the continuous flow of the slurry from the turbomachine at a second pressure, wherein the first pressure is greater than the second pressure.

23. The method of claim 22 , comprising generating electric power or mechanical power in response to the continuous flow of the slurry through the turbomachine.

24. The method of claim 22 , wherein the slurry source comprises a gasifier having a reaction chamber.