System and method for gasification

1. A system, comprising:

a gasification vessel configured to receive a fuel and an oxidizer;

a gasifier disposed in the gasification vessel and configured to partially oxidize the fuel and the oxidizer to generate a syngas; and

a convective syngas cooler configured to cool the syngas via heat exchange with a coolant, wherein the convective syngas cooler is disposed in an interior of the gasification vessel, wherein the convective syngas cooler comprises a plurality of tubes surrounded by a shell, and wherein the convective syngas cooler is configured to flow the syngas through the plurality of tubes and the coolant through the shell.

2. The system of claim 1 , wherein the gasifier comprises a reaction chamber disposed in the interior of the gasification vessel, and the reaction chamber is configured to contain the partial oxidation of the fuel and the oxidizer, and wherein the convective syngas cooler surrounds the reaction chamber in a coaxial arrangement.

3. The system of claim 1 , wherein the coolant comprises a boiler feedwater.

4. The system of claim 1 , wherein each of the plurality of tubes comprises:

a tubular body configured to route the syngas through the convective syngas cooler; and

an inlet ferrule coupled to the tubular body and configured to route the syngas to the tubular body of each of the plurality of tubes.

5. The system of claim 4 , wherein each inlet ferrule comprises a conical-shaped structure with an opening and a throat, an opening diameter is greater than a throat diameter, and the throat is coupled to the tubular body of the respective tube.

6. The system of claim 5 , wherein the openings of the inlet ferrules laterally abut one another.

7. The system of claim 5 , wherein the opening of the inlet ferrule comprises a pentagonal or hexagonal shape.

8. The system of claim 5 , wherein an inner surface of the inlet ferrule is configured to be exposed to the syngas, and the inner surface is coated with a coating configured to resist adhesion of particles contained in the syngas.

9. The system of claim 1 , wherein the convective syngas cooler is configured such that the syngas is routed through an upper portion of the gasification vessel.

10. The system of claim 1 , wherein each of the plurality of tubes comprises an inlet diameter and an outlet diameter, and the inlet diameter is greater than the outlet diameter.

11. A method, comprising:

partially oxidizing a fuel and an oxidizer in a gasifier to generate a syngas, wherein the gasifier is disposed in a gasification vessel;

cooling the syngas using a convective syngas cooler disposed in an interior of the gasification vessel;

containing the partial oxidation of the fuel and the oxidizer in a reaction chamber disposed in the interior of the gasification vessel; and

routing the syngas through a plurality of tubes of the convective syngas cooler annularly disposed about the reaction chamber.

12. The method of claim 11 , comprising converging the syngas via a plurality of inlet ferrules coupled to the plurality of tubes, wherein the inlet ferrule comprises a conical-shaped structure with an opening and a throat, wherein an opening diameter is greater than a throat diameter.

13. The method of claim 12 , wherein each of the openings of the inlet ferrules comprises a polygonal shape, and the openings are configured to laterally abut one another.

14. A system, comprising:

a partial oxidation vessel configured to receive a fuel and an oxidizer;

a combustor disposed in the partial oxidation vessel configured to partially oxidize the fuel and the oxidizer to generate a syngas;

a partial oxidation chamber disposed in the partial oxidation vessel and configured to route the syngas to a quench chamber disposed at a lower portion of the partial oxidation vessel; and

a convective syngas cooler configured to cool the syngas via heat exchange with a coolant, wherein the convective syngas cooler is disposed in an interior of the partial oxidation vessel annularly surrounding the partial oxidation chamber and above the quench chamber, and the convective syngas cooler is configured to route the syngas through an upper portion of the partial oxidation vessel, and wherein the convective syngas cooler comprises a plurality of tubes configured to flow the syngas, each of the plurality of tubes comprises an inlet diameter and an outlet diameter, and the inlet diameter is greater than the outlet diameter.

15. The system of claim 14 , wherein each of the plurality of tubes comprises:

a tubular body configured to route the syngas through the convective syngas cooler; and

an inlet ferrule configured to route the syngas to the tubular body and comprising a conical-shaped structure with an opening and a throat, wherein an opening diameter is greater than a throat diameter, and wherein the throat is coupled to the tubular body.