System and process for treating sulfur
An apparatus configured for treating sulfur at an elevated pressure. Embodiments of the apparatus comprises a vessel into which the sulfur is injected and a device for alleviating the pressure of the sulfur.
1. An apparatus for handling molten sulfur at elevated pressure, comprising:
a first tank having an inlet and an outlet,
a fluid channel traversing a vertical distance from the first tank outlet, said fluid channel having first and second ends, said first fluid channel end in fluid communication with said first tank outlet;
a second tank having a fluid inlet and a fluid outlet, said fluid inlet being in fluid communication with said first channel second end and disposed at a vertical distance above the fluid channel first end.
2. The apparatus according to claim 1 , further including a third tank having a fluid inlet in fluid communication with said second tank fluid outlet and having a fluid outlet in fluid communication with the first tank.
3. The apparatus according to claim 1 , wherein the level of molten sulfur in said second tank is maintained below said second tank fluid inlet by a first gas line.
4. The apparatus according to claim 1 , wherein said first and second tanks comprise first and second overhead spaces, respectively, and wherein said first and second overhead spaces are in fluid communication via a first gas line.
5. The apparatus according to claim 1 , wherein the rate of flow through said first gas line is controlled in response to a measurement of gas pressure within said second tank.
6. The apparatus according to claim 1 , wherein the rate of flow through said fluid channel is controlled by controlling the gas pressure in said second tank.
7. The apparatus according to claim 1 , wherein the rate of flow through said fluid channel is controlled by controlling the gas pressure differential between said first tank and said second tank.
8. The apparatus according to claim 2 , wherein the level of molten sulfur in said third tank is maintained below said third tank fluid inlet.
9. The apparatus according to claim 2 , wherein said second and third tanks comprise second and third overhead spaces, respectively, and wherein said second and third overhead spaces are in fluid communication via a second gas line.
10. The apparatus according to claim 2 , wherein the the second gas line comprises a molten sulfur flow control in response to a measurement of gas pressure within said third tank.
11. The apparatus according to claim 10 , wherein the rate of flow through said second gas line is controlled by controlling the gas pressure in said third tank.
12. The apparatus according to claim 10 , wherein the rate of flow through said second gas is controlled by controlling the gas pressure differential between said second tank and said third tank.
13. An apparatus for handling molten sulfur at elevated pressure, comprising:
a first tank having an inlet and at least one outlet,
a fluid channel traversing a vertical distance, said fluid channel having first and second ends, said first fluid channel end in fluid communication with said first tank at least one outlet;
at least one second tank having a fluid inlet and a fluid outlet, said fluid inlet being in fluid communication with said first channel second end.
14. The apparatus according to claim 13 , wherein the level of molten sulfur in said at least one second tank is maintained below said second tank fluid inlet.
15. The apparatus according to claim 13 , wherein said first and second tanks have first and second overhead spaces, respectively, and wherein said first and second overhead spaces are in fluid communication via a first gas line.
16. The apparatus according to claim 13 , wherein the rate of flow through said first gas line is controlled in response to a measurement of gas pressure within said at least one second tank.
17. The apparatus according to claim 13 , wherein the rate of flow through said fluid channel is controlled by controlling the gas pressure in said at least one second tank.
18. The apparatus according to claim 13 , wherein the rate of flow through said fluid channel is controlled by controlling the gas pressure differential between said first tank and said at least one second tank.