Methods of separating mixtures of miscible fluids
View Patent ↗Disclosed herein are systems and methods for vortex tube desulfurization of jet fuels. Also disclosed are processes for separation of closely boiling species in a mixture of miscible fluids.
1. A method for separating at least one sulfur-containing compound from a hydrocarbon-based fuel, the method comprising:
introducing a pressurized and heated parent stream comprising a mixture of the at least one sulfur-containing compound and the hydrocarbon-based fuel into a first vortex tube at a tangential inlet, the first vortex tube comprising an axial primary outlet at an inlet end and a secondary outlet at an opposing end;
withdrawing a predominantly vapor primary stream from the primary outlet, the primary stream comprising a lower concentration of the at least one sulfur-containing compound than the parent stream; and
removing a predominantly liquid secondary stream from the secondary outlet, the secondary stream comprising a higher concentration of the at least one sulfur-containing compound than the parent stream.
2. The method of claim 1 , wherein the pressurized and heated parent stream is in a two-phase state that is at least predominantly gaseous.
3. The method of claim 2 , wherein at least 80 wt % of the pressurized and heated parent stream is gaseous.
4. The method of claim 1 , wherein the pressurized and heated parent stream enters the first vortex tube at a first temperature within or above a boiling point range of the mixture.
5. The method of claim 1 , wherein the secondary outlet is radial, tangential or axial.
6. The method of claim 1 , wherein the hydrocarbon-based fuel comprises jet fuel.
7. The method of claim 6 , wherein the jet fuel is selected from the group consisting of Jet A, Jet A-1, Jet B, kerosene no. 1-K, JP-4, JP-5, JP-8, and JP-8+100.
8. The method of claim 1 , wherein an inlet pressure is at least 2 bars.
9. The method of claim 1 , wherein an inlet pressure is less than 2 bars and pressures downstream of each of the primary outlet and the secondary outlet are sub-atmospheric.
10. The method of claim 1 , wherein the secondary stream removed from the secondary outlet comprises from about 1 wt % to about 20 wt % of the parent stream.
11. The method of claim 1 , wherein the pressurized and heated parent stream enters the first vortex tube at a temperature in a range from about 200° C. to about 400° C.
12. The method of claim 1 , wherein a concentration of the at least one sulfur-containing compound in the primary stream is reduced by at least 20% compared to a concentration of the at least one sulfur-containing compound in the parent stream.
13. The method of claim 12 , wherein the concentration of the at least one sulfur-containing compound in the primary stream is reduced by at least 40% compared to the concentration of the at least one sulfur-containing compound in the parent stream.
14. The method of claim 1 , wherein the at least one sulfur-containing compound is selected from the group consisting of benzothiophene, alkyl benzothiophenes, dibenzothiophene, and alkyl dibenzylthiophenes.
15. The method of claim 14 , wherein the at least one sulfur-containing compound is selected from the group consisting of 2-methylbenzothiophene, 3-methylbenzothiophene, 5-methylbenzothiophene, 2,3-dimethylbenzothiophene, 2,3,7-trimethyl benzothiophene, 2,3,5-trimethyl benzothiophene, and 2,3,6-trimethyl benzothiophene.
16. The method of claim 1 , further comprising:
directing the primary stream into a second stage A vortex tube at a tangential inlet proximal to a first end thereof, the second stage A vortex tube comprising an axial primary outlet at the first end and a secondary outlet at a second end distal to the first end;
removing a product stream from the second stage A vortex tube through the primary outlet thereof; and
removing a first recycling stream from the second stage A vortex tube through the secondary outlet thereof;
wherein the product stream comprises a lower concentration of the at least one sulfur-containing compound than the primary stream and the first recycling stream comprises a higher concentration of the at least one sulfur-containing compound than the primary stream.
17. The method of claim 16 , further comprising heating at least a portion of the primary stream to a second temperature prior to directing the primary stream into the second stage A vortex tube.
18. The method of claim 16 , further comprising reintroducing the first recycling stream to the first vortex tube.
19. The method of claim 18 , wherein reintroducing the first recycling stream to the first vortex tube comprises passing the first recycling stream through an axial inlet extending into the first vortex tube at the second end thereof.
20. The method of claim 16 , further comprising:
directing the secondary stream into a second stage B vortex tube at a tangential inlet proximal to a first end thereof, the second stage B vortex tube comprising an axial primary outlet at the first end and a secondary outlet at a second end distal to the first end;
removing a second recycling stream from the second stage B vortex tube through the primary outlet thereof; and
removing a waste stream from the second stage B vortex tube through the secondary outlet thereof;
wherein the second recycling stream comprises a lower concentration of the at least one sulfur-containing compound than the secondary stream and the waste stream comprises a higher concentration of the at least one sulfur-containing compound than the secondary stream.
21. The method of claim 20 , further comprising:
blending the second recycling stream with the first recycling stream to create a blended stream;
directing the blended stream into a third stage vortex tube via an inlet proximal to a first end thereof, the third stage vortex tube comprising an axial primary outlet at the first end and a secondary outlet at a second end distal to the first end;
removing a recovery stream from the third stage vortex tube through the primary outlet thereof; and
removing a waste stream from the third stage vortex tube through the secondary outlet thereof;
wherein the recovery stream comprises a lower concentration of the at least one sulfur-containing compound than the blended stream and the waste stream comprises a higher concentration of the at least one sulfur-containing compound than the blended stream.
22. The method of claim 21 , further comprising mixing the recovery stream with the product stream to provide a recovered product stream, wherein the recovered product stream comprises a lower concentration of the at least one sulfur-containing compound than the primary stream.