Trapped vortex particle-to-vapor converter

• US 9,744,490 B1
• Filed: 04/05/2013
• Issued: 08/29/2017
• Est. Priority Date: 04/06/2012
• Status: Expired due to Fees

• Current Assignee: Enertechnix, Inc.
• Original Assignee: Enertechnix, Inc.
• Inventors: Novosselov, Igor, Ariessohn, Peter
• Primary Examiner(s): Bui, Dung H
• Application Number:
  US13/986,145
• Time in Patent Office: 1,607 Days
• CPC Class Codes: B01D 45/08 by impingement against baffle separators
• CPC Class Codes: B01D 45/12 by centrifugal forces centrifuges B04B; cyclones B04C
• CPC Class Codes: B01D 45/16 generated by the winding course of the gas stream , the centrifugal forces being generated solely or partly by mechanical means, e.g. fixed swirl vanes
• CPC Class Codes: B01D 50/20 Combinations of devices covered by groups B01D45/00 and B01D46/00

Abstract

Apparatus and methods for selectively separating a volatile constituent of a particle from a gas stream for analysis. Particles are separated from bulk flow by inertia and impacted in a cavity containing a small but stable vortex or eddy. Heat is applied to volatilize constituents of the particles. The gas entrained within the vortex, which exchanges only slowly with the bulk flow, is withdrawn for analysis. In this way, a high volume flow containing particles of interest is reduced to a low volume flow containing a vapor concentrate. Advantageously, the apparatus may be operated at very low pressure drops in fully continuous, semi-continuous or batch mode according to the requirements of the downstream analytical unit. The apparatus finds use in active surveillance, such as in use of aerosols to detect explosives or chemical residues on persons, vehicles or luggage in real time.

Claims

1. An apparatus for selectively separating a volatile constituent of particles from a flowing gas stream for analysis, which comprises

a housing with an inlet flow duct opening from an intake port that receives the gas stream at an upstream end at a first flow rate as driven by a pressure differential applied to said gas stream, said inlet flow duct with an enclosing wall therearound, and an outlet flow duct having an exhaust port at a downstream end for exhausting said gas stream therefrom;

a trapped vortex cavity communicating with and adjoining said inlet flow duct, wherein said trapped vortex cavity is bounded by superior, lateral, inferior, and posterior, surfaces, and an anterior opening to said inlet flow duct, said inferior surface extending longer toward said inlet flow duct than said superior surface;

said inferior surface of said cavity defines an upstream-facing step with diverter lip that extends toward flow lines of said gas stream when said gas stream flows through said inlet flow duct, partially constricting the flowing gas stream, and defining an inertial particle impactor face, such that said particles in said flowing gas stream impact against said upstream-facing step, and wherein said superior surface of said cavity defines a downstream-facing step that terminates at a junction flush with said inlet flow duct;

said diverter lip extending beyond said downstream facing step toward said gas stream flow lines, whereby a trapped vortex of said gas is created in said vortex cavity when said gas is flowing through said inlet flow duct and said outlet flow duct;

a sampling outlet defined through an internal surface of said trapped vortex cavity, wherein said outlet is enabled for aspirating and collecting a gas sample volume from said cavity at a second flow rate, said second flow rate having fractional value of said first flow rate.

2. The apparatus of claim 1, wherein said enclosing wall of said inlet flow duct is contoured to direct particles against said inertial particle impactor face.

3. The apparatus of claim 1, further comprising a heater for heating a portion of the trapped vortex cavity surfaces to a higher temperature to promote vaporization or sublimation of the collected sample, whereby said-volatile constituents is trapped as a vapor concentrate in said trapped vortex cavity until aspirated through said sampling outlet.

4. The apparatus of claim 3, wherein said heater comprises a resistive heating element that is thermally coupled to said portion of said trapped vortex cavity surfaces.

5. The apparatus of claim 3, wherein an infrared diode is mounted in said cavity.

6. The apparatus of claim 3, wherein one of said surfaces of said cavity is lined with a magnetically susceptible layer that is configured to be inductively heated.

7. The apparatus of claim 3, wherein said heater is a flash heater that is thermally coupled to one of said surfaces of said cavity.

8. The apparatus of claim 3, wherein said heater is used to continuously heat one of said surfaces of said cavity.

9. The apparatus of claim 1, further comprising a first pump or blower for applying said pressure differential to said gas.

10. The apparatus of claim 3, further comprising a second pump or blower for aspirating said gas sample volume from said cavity at a low volume flow rate.

11. The apparatus of claim 10, wherein said second pump or blower is operated continuously for continuous aspiration of said vapor concentrate.

12. The apparatus of claim 1, wherein said cavity and said inertial surface thereof are comprised of a thermally conductive material and said enclosing wall of said inlet flow duct are composed of a thermally insulative material.

13. The apparatus of claim 12, wherein said thermally insulative material is a ceramic or a glass and said thermally conductive material is a metal.

14. The apparatus of claim 1, further comprising a low volume flow source for supplying a make-up gas volume to said trapped vortex cavity, wherein said make-up gas volumetric flow rate is equal to or less than the gas sample volumetric flow rate aspirated from the cavity.

15. The apparatus of claim 14, wherein the low volume flow source is comprised of a dry gas.

16. The apparatus of claim 15, wherein the dry gas is argon.

17. The apparatus of claim 1, further comprising an air-to-air aerosol concentrator operatively joined to said inlet flow duct upstream of said trapped vortex cavity.

18. The apparatus of claim 1, further comprising a directional nose having at least one pulsed jet disposed thereon, said pulsed jet for dislodging a particle from a surface into the flowing gas stream.

19. The apparatus of claim 1, wherein said upstream-facing step is contoured for non-turbulently separating a critical streamline layer of the gas flow from a boundary streamline layer of heated trapped vortex flow such that said particles cross the boundary streamline layer, but a resident gas volume and heat of gas flowing in a vortex within said cavity is essentially isolated from the flowing gas stream.

20. The apparatus of claim 19, wherein said upstream-facing step is contoured at said diverter lip for non-turbulently separating a critical streamline layer of the gas flow from a boundary streamline layer of said heated trapped vortex flow such that said particles cross the boundary streamline layer, but said resident gas volume and heat of gas flowing in said vortex within said cavity is essentially isolated from the flowing gas stream.