Controlled dispersion multi-phase nozzle and method of making the same

• US 7,237,574 B2
• Filed: 05/12/2005
• Issued: 07/03/2007
• Est. Priority Date: 05/13/2004
• Status: Active Grant

• Current Assignee: Caldera Engineering, LC
• Original Assignee: Caldera Engineering, LC
• Inventors: Chipman, Stephen R., Robison, Jeffrey C., Luque, Michael R., Smith, Craig C., Pieterse, Herman
• Primary Examiner(s): Bastianelli; John
• Application Number:
  US11/127,918
• Publication Number:
  US 20060065869A1
• Time in Patent Office: 782 Days
• Field of Search: 251120-124, 138/44
• US Class Current: 138/44
• CPC Class Codes: F16K 47/16 the throttling member being a cone

Abstract

A nozzle design and method for designing such a nozzle being adapted for three phase slurry flow from the choke into the flash tank during pressure let-down in autoclave mining operations that uses a selection of the expansion ratio in the choke to select a nozzle dispersion angle to select a spread of the flow over the slurry pool in the flash tank, to generally maximize the use of the pool for energy dissipation without causing undo wear and tear on the tank walls.

Claims

1. A method of designing a flash nozzle, wherein said flash nozzle comprises a choke inlet, a throat, and an expanding choke outlet, wherein the choke inlet is upstream from the throat, which is upstream from the expanding choke outlet, wherein the flash nozzle is used to introduce slurry at supersonic flow rates into a flash vessel at a given operating pressure downstream from said nozzle, and wherein the flash vessel is configured to accumulate slurry in a slurry pool contained therein, wherein the method comprises:

specifying a choke angle, X, representing the angle from an axis of the flash nozzle at which said expanding choke outlet expands;

defining slurry flow properties at a point located before the slurry enters said flash nozzle, wherein said slurry flow properties comprise at least one of density, flow rate, pressure, temperature, solid fraction, and vapor fraction;

modeling the slurry expansion in the flash vessel starting at the point where the slurry exits the expanding choke outlet, wherein said modeling is based on said flash vessel operating pressure, said choke angle, X, and thermodynamic characteristics of said slurry, wherein said expansion of the slurry past the end of said expanding choke outlet is defined by a slurry expansion angle, Y;

repeating the above steps with a new choke angle, X, until a total dispersion angle, X plus Y, is achieved, wherein said total dispersion angle, X plus Y, is greater than said choke outlet angle, X; and

producing a flash nozzle from said model having a choke outlet angle of X, wherein said total dispersion angle, X plus Y, is greater than said choke outlet angle, X, for said defined slurry flow properties and said flash vessel operating pressure.

2. The method of claim 1, further comprising calculating an expanding choke outlet area based on said specified choke outlet angle, X.

3. The method of claim 1, further comprising calculating a throat area based on said specified choke outlet angle, X, and said expanding choke outlet area, such that said total dispersion angle, X plus Y, is greater than said choke outlet angle, X.

4. The method of claim 3, further comprising setting a expanding choke outlet area to throat area ratio, such that said total dispersion angle, X plus Y, is greater than said choke outlet angle, X.

5. The method of claim 4, wherein said expanding choke outlet area to throat area ratio is greater than about 1.

6. The method of claim 4, wherein said choke outlet angle, X, is specified by specifying said expanding choke outlet area.

7. The method of claim 1, wherein said thermodynamic characteristics comprise at least one of enthalpy, entropy, and mach number.

8. The method of claim 1, wherein said total dispersion angle, X plus Y, meets the objective of spreading the expanding slurry over a significant area of the slurry pool, thereby minimizing the wear and tear to said flash vessel.

9. A method of designing a flash nozzle, wherein said flash nozzle comprises a choke inlet, a throat, and an expanding choke outlet, wherein the choke inlet is upstream from the throat, which is upstream from the expanding choke outlet, wherein the flash nozzle is used to introduce slurry at supersonic flow rates into a flash vessel at a given operating pressure downstream from said nozzle, and wherein the flash vessel is configured to accumulate slurry in a slurry pool contained therein, wherein the method comprises the steps of:

specifying a choke angle, X, representing the angle from an axis of the flash nozzle at which said expanding choke outlet expands;

defining slurry flow properties at a point located before the slurry enters said flash nozzle, wherein said slurry flow properties comprise at least one of density, flow rate, pressure, temperature, and steam fraction;

calculating an expanding choke outlet area, wherein said expanding choke outlet area varies based on said specified choke angle, X;

specifying a throat area, wherein said throat area is independent of said specified choke outlet angle, X; and

modeling the slurry expansion in the flash vessel starting at the point where the slurry exits the expanding choke outlet, wherein said modeling is based on the pressure vessel operating pressure, the ratio between said expanding choke outlet area and said throat area, and thermodynamic characteristics, wherein said thermodynamic characteristics comprise at least one of enthalpy, entropy, and mach number, and wherein said modeling calculates an angle of slurry expansion from the expanding choke outlet slurry defined as expansion angle, Y, and wherein the sum of said choke outlet angle, X, and said slurry expansion angle, Y, creates a total dispersion angle, X plus Y, which is greater than said choke outlet angle, X;

producing a flash nozzle from said model having a choke outlet angle of X, wherein said total dispersion angle, X plus Y, is greater than said choke outlet angle, X, for said selected slurry flow properties and the pressure vessel operating pressure.

10. The method of claim 9, further comprising the step of requiring that said total dispersion angle, X plus Y, meets the objective of spreading the expanding slurry over a significant area of said slurry pool.

11. The method of claim 9, wherein said modeling step assumes that said slurry is a homogeneous equilibrium, three-phase fluid.

12. The method of claim 9, wherein said modeling step assumes an isentropic expansion.

13. The method of claim 9, wherein said flash nozzle further comprises a plug head for opening and closing said throat.

14. The method of claim 10, wherein said objective of spreading the expanding slurry over a significant area of the slurry pool requires that substantially all of the expanded slurry contacts the slurry pool in said flash vessel, thereby minimizing the slurry contacting the walls of said flash vessel and thereby reducing the velocity with which the expanded slurry contacts the bottom of the vessel.