Spinning fluids reactor
A spinning fluids reactor, includes a reactor body ( 24 ) having a circular cross-section and a fluid contactor screen ( 26 ) within the reactor body ( 24 ). The fluid contactor screen ( 26 ) having a plurality of apertures and a circular cross-section concentric with the reactor body ( 24 ) for a length thus forming an inner volume ( 28 ) bound by the fluid contactor screen ( 26 ) and an outer volume ( 30 ) bound by the reactor body ( 24 ) and the fluid contactor screen ( 26 ). A primary inlet ( 20 ) can be operatively connected to the reactor body ( 24 ) and can be configured to produce flow-through first spinning flow of a first fluid within the inner volume ( 28 ). A secondary inlet ( 22 ) can similarly be operatively connected to the reactor body ( 24 ) and can be configured to produce a second flow of a second fluid within the outer volume ( 30 ) which is optionally spinning.
1. A spinning fluids reactor, comprising:
a) an elongate reactor body having a circular cross-section;
b) a fluid contactor screen within the reactor body, said fluid contactor screen having a plurality of apertures and a circular cross-section concentric with the reactor body for a length thus forming an inner volume bound by the fluid contactor screen and an outer volume bound by the reactor body and the fluid contactor screen;
c) a primary inlet operatively connected to the reactor body and configured to produce a first spinning flow of a first fluid within the inner volume which is a flow-through flow;
d) a secondary inlet operatively connected to the reactor body and configured to produce a second flow of a second fluid within the outer volume; and
e) an outlet operatively connected to the reactor body and in fluid communication with the inner and the outer volumes.
2. A reactor as in claim 1 , wherein a ratio of the inner volume to the outer volume is about 1:1 to about 1:5.
3. A reactor as in claim 1 , wherein openings in the fluid contactor screen are about 0.02 mm to about 2 mm.
4. A reactor as in claim 1 , wherein the fluid contactor screen is a wire mesh screen.
5. A reactor as in claim 1 , wherein the fluid contactor screen is a perforated sheet.
6. A reactor as in claim 1 , wherein the first spinning flow and the second flow are substantially concentric.
7. A reactor as in claim 1 , wherein the secondary inlet is configured to produce tangential injection such that the second flow is a spinning flow.
8. A reactor as in claim 1 , wherein the elongate reactor body comprises a conical shape portion having a decreasing diameter from an upper end to a lower end of the elongate reactor body.
9. A reactor as in claim 8 , wherein the conical shape portion has an incline angle from about 1° to about 3°.
10. A reactor as in claim 8 , wherein the elongate reactor body further comprises an upper cylindrical portion and wherein the upper end of the conical shape portion is oriented adjacent the upper cylindrical portion.
11. A reactor as in claim 1 , wherein the elongate reactor body comprises a cylindrical shape having a substantially uniform diameter.
12. A reactor as in claim 1 , wherein the elongate reactor body includes a conical shaped section and a cylindrical shaped section.
13. A reactor as in claim 1 , wherein the fluid contactor screen is conically shaped and has a length that is from about 2 to about 8 times a diameter of the fluid contactor screen.
14. A reactor as in claim 1 , wherein the fluid contactor screen is cylindrically shaped and has a length that is from about 2 to about 5 times a diameter of the fluid contactor screen.
15. A reactor as in claim 1 , further comprising a UV light source oriented to direct UV light into at least a portion of at least one of the inner volume and the outer volume.
16. A method of reacting compounds, comprising:
a) forming a continuous first spinning flow with a first fluid having a first momentum; and
b) forming a second flow with a second fluid circumscribing the first spinning flow, said second flow having a second momentum, wherein a ratio of the first momentum to the second momentum is about 0.7 to about 1.3, wherein a cylindrical barrier between the first spinning flow and the second flow permits contact through the barrier of the second fluid to the first fluid sufficient to form a reaction product.
17. A method as in claim 16 , wherein the first spinning flow is an annular flow along an internal surface of the barrier.
18. A method as in claim 16 , wherein the annular flow has an average thickness from about 10% to about 30% of a diameter of the cylindrical barrier.
19. A method as in claim 16 , wherein a volumetric flow rate of the second fluid over the volumetric flow rate of the first fluid is less than about 12.
20. A method as in claim 16 , wherein a ratio of an inner volume of the first spinning flow to an outer volume of the second flow is about 1:1 to about 1:5.
21. A method as in claim 16 , wherein the first spinning flow and the second flow are directionally coincident.