초록 ▼

A fluid mover (1) includes a passage (3) of substantially constant cross section into which supersonic steam is injected through an annular nozzle (16) as a transport fluid to contact a working fluid, e.g. a liquid, to be treated, the passage further including a mixing chamber (3A) downstream of the

A fluid mover (1) includes a passage (3) of substantially constant cross section into which supersonic steam is injected through an annular nozzle (16) as a transport fluid to contact a working fluid, e.g. a liquid, to be treated, the passage further including a mixing chamber (3A) downstream of the steam injection where the mixture is accelerated upon the creation of a low pressure zone occasioned by the condensation of the steam, a dispersed droplet regime and a shock wave being generated downstream of the nozzle (16). A pseudo-convergent/divergent section is created and provides a flexible boundary in the absence of physical constraints to yield an improved performance by combining shear dispersion and/or disassociation with the effects of the shock wave. The fluid mover ( 1) may be used in a wide variety of applications for pumping, heating, mixing, disintegrating, classifying and separating among others.

대표청구항 ▼

The invention claimed is: 1. A fluid mover comprising: a hollow body provided with a straight-through passage of substantially constant cross-section, said passage having an inlet end and an outlet end for the entry and discharge respectively of a working fluid, a transport fluid nozzle substantial

The invention claimed is: 1. A fluid mover comprising: a hollow body provided with a straight-through passage of substantially constant cross-section, said passage having an inlet end and an outlet end for the entry and discharge respectively of a working fluid, a transport fluid nozzle substantially circumscribing and opening into said passage intermediate the inlet and outlet ends thereof, a transport fluid inlet communicating with the transport fluid nozzle for the introduction of a transport fluid, and a mixing chamber being formed within the passage downstream of the transport fluid nozzle, the transport fluid nozzle being of convergent-divergent geometry internally thereof such as in use to provide for the generation of supersonic flow of the transport fluid therein, and the transport fluid nozzle and mixing chamber being so disposed and configured that in use a dispersed droplet flow regime and a supersonic shockwave are created within the mixing chamber by the introduction of the transport fluid through the transport fluid nozzle and subsequent condensation thereof and whereby a pseudo convergent-divergent section is created in the working fluid flow in the mixing chamber by the introduction of the transport fluid through the transport fluid nozzle. 2. A fluid mover as in claim 1, wherein the transport fluid is steam and the transport fluid nozzle is a steam nozzle, and wherein the nozzle and mixing chamber being so disposed and configured that in use a dispersed droplet flow regime and a supersonic shockwave are created within the mixing chamber by the introduction of the transport fluid through the transport fluid nozzle and subsequent condensation thereof and whereby a pseudo convergent-divergent section is created in the working fluid flow in the mixing chamber by the introduction of the transport fluid through the transport fluid nozzle. 3. A fluid mover according to claim 1 wherein the shape of the passage may be circular, curvilinear or rectilinear. 4. A fluid mover according to claim 1 wherein the transport fluid nozzle is disposed in such manner as in use to be in close adjacency to the projected surface of the working fluid. 5. A fluid mover according to claim 4 further comprising a knife-edge separation between the transport fluid and the working fluid. 6. A fluid mover according to claim 1 wherein the transport fluid nozzle is annular. 7. A fluid mover according to claim 6 wherein the transport fluid nozzle includes a single aperture. 8. A fluid mover according to claim 1 wherein the transport fluid nozzle is configured to give the highest velocity steam jet, the lowest pressure drop and the highest enthalpy. 9. A fluid mover according to claim 1 wherein the transport fluid nozzle is angled towards the passage. 10. A fluid mover according to claim 1 which comprises a plurality of transport fluid nozzles spaced apart longitudinally of the passage, each said transport fluid nozzle being provided with a mixing chamber section downstream thereof. 11. A fluid mover according to claim 10 wherein the transport fluid nozzles are at different locations along the passage and have differing geometries. 12. A fluid mover according to claim 1 further comprising at least one secondary nozzle intermediate the inlet and the outlet ends of the passage (3). 13. A fluid mover according to claim 12 wherein said at least one secondary nozzle is located upstream and/or downstream of the transport fluid nozzle. 14. A fluid mover according to claim 1 wherein the cross sectional dimension of the passage at the location of the transport fluid nozzle is greater than that either upstream or downstream thereof. 15. A fluid mover according to claim 1 wherein the cross-sectional area of the mixing chamber is equal to or greater than that of the passage. 16. A fluid mover according to claim 15 wherein the cross-sectional area of the mixing chamber varies with its length. 17. A fluid mover according to claim 16 wherein the degree of variation differs along the length of the mixing chamber. 18. A fluid mover according to claim 1 further comprising a cowl downstream of the outlet from the passage. 19. A method of moving a working fluid comprising the steps of: (a) presenting a fluid mover to the fluid, the mover having a straight-through passage of substantially constant cross section, (b) applying a substantially circumscribing stream of a transport fluid to the passage through an annular transport fluid nozzle thereby creating a pseudo-convergent/divergent section in the working fluid flow, (c) causing the collapse of the transport fluid thereby to create a region of low pressure to induce flow of the working fluid through the passage, (d) generating a dispersed droplet flow regime and a supersonic shock wave within a mixing chamber downstream of the transport fluid nozzle, (e) inducing flow of the working fluid through the passage from an inlet end to an outlet end thereof, and (f) modulating the shock wave to vary the working fluid discharge from the outlet end. 20. A method as in claim 19, wherein steam is the transport fluid. 21. A method according to claim 20 which comprises varying the steam characteristics of pressure, flow rate, dryness and/or temperature to provide the required performance of the steam nozzle. 22. A method according to claim 20 comprising the step of introducing additional fluid into the passage downstream of the transport fluid nozzle to enhance the condensation of the steam. 23. A method according to claim 22 wherein the additional fluid is working fluid. 24. A method according to claim 22 wherein the additional fluid is water. 25. A method of moving a working fluid according to claim 20 comprising the step of introducing at least one additional liquid into the passage upstream or downstream of the nozzle, and wherein the working fluid is air, and the additional liquid is water whereby the water is atomised upon encountering the shearing effect of the steam and the supersonic shock wave thereby to generate a mist. 26. A method according to claim 19 wherein the pseudo-convergent/divergent section in the fluid flow presents a flexible boundary lying between the working fluid and the wall of the passage. 27. A method according to claim 19 further comprising the step of introducing at least one additional fluid and/or solid into the passage upstream or downstream of the transport fluid nozzle. 28. A method according to claim 27 wherein at least one additional fluid in the form of one or more liquids is introduced into the passage. 29. A method according to claim 27 wherein at least one additional solid in particulate form is introduced into the passage. 30. A method according to claim 27 wherein at least one additional solid in pulverulent form is introduced into the passage. 31. A method according to claim 27 wherein at least one additional solid in gelatinous and/or glutinous form is introduced into the passage. 32. A method according to claim 19 wherein the working fluid is a liquid. 33. A method according to claim 32 wherein the working fluid includes a foaming agent. 34. A method according to claim 19 wherein the working fluid is a mixture of a fluid and solids material. 35. A method according to claim 34 wherein the mixture is a sludge or slurry. 36. A method according to claim 34 wherein the solids material is particulate in form. 37. A method according to claim 34 wherein the solids material is in pulverulent form. 38. A method according to claim 34 wherein the solids material is a fatty substance, oil or grease. 39. A method of moving a working fluid according to claim 38 wherein the fatty substance, oil or grease of the working fluid is emulsified thereby. 40. A method of moving a working fluid according to claim 34 which comprises the step of allowing the solids material to disintegrate and/or mix within the fluid. 41. A method of moving a working fluid according to claim 40, which comprises the step of introducing the solids material into the fluid through at least one secondary nozzle. 42. A method according to claim 19 wherein the working fluid is gaseous. 43. A method according to claim 42 wherein the gaseous working fluid is air. 44. A method according to claim 42 wherein the gaseous working fluid is smoke. 45. A method moving a working fluid according to claim 19 wherein the working fluid is heated thereby.