System and method for the concentrated collection of airborne particles

Patent metadata

Field	Value
Publication number	US-9658139-B2
Application number	US-201314012818-A
Country	US
Kind code	B2
Filing date	Aug 28, 2013
Priority date	Aug 31, 2012
Publication date	May 23, 2017
Grant date	May 23, 2017

Abstract

A system and a method is described herein for the collection of small particles in a concentrated manner, whereby particles are deposited onto a solid surface or collected into a volume of liquid. The collected samples readily interface to any of a number of different elemental, chemical, or biological or other analysis techniques.

First claim

We claim:

1. A particle collection system, comprising:
a particle growth assembly having interior wetted walls and configured to receive a particle laden aerosol flow at a flow rate less than or equal to 100 L/min, the particle growth assembly including a condensing vapor having a vapor pressure at the interior walls which is near saturation, wherein the aerosol flow through the particle growth assembly is configured to be a laminar flow, the particle growth assembly including:
a conditioning portion with a wetted interior wall configured to bring the aerosol flow to near saturation at a first temperature (T 1 );
an initiator portion with a wetted interior wall operatively coupled to said conditioning portion and configured to provide supersaturation conditions at a second temperature (T 2 ) for the aerosol flow using the condensing vapor to initiate droplet growth, wherein the second temperature (T 2 ) is configured to be higher than the first temperature (T 1 ); and
a equilibrator portion with a wetted interior wall operatively coupled to said initiator portion and configured to lower a dew point for the aerosol flow and maintain supersaturation conditions for the aerosol flow at a third temperature (T 3 ), wherein the third temperature (T 3 ) is configured to be lower than the second temperature (T 2 );

a collection member for collecting by inertia the enlarged particles, the collection member positioned adjacent a nozzle member operatively coupled to an outlet of said particle growth assembly; and
a displacement assembly adapted to displace the collection member under the particle growth assembly.

2. The system of claim 1 wherein the nozzle member is heated to prevent condensation from droplets including the enlarged particles.

3. The system of claim 1 wherein the collection member includes a collection plate with one or more collection wells formed therein in an x-y grid pattern, wherein the displacement assembly includes a stepper motor that moves the collection plate in an x-y grid pattern under the nozzle member and receives enlarged particles from the nozzle member.

4. The system of claim 1 wherein the displacement assembly includes a stepper motor adapted to displace the collection member under the particle growth assembly and under the nozzle member, wherein the collection member includes a circular collection plate having one or more collection wells at a periphery of the plate and wherein the stepper motor rotationally moves the plate such that each collection well receives enlarged particles from the nozzle member.

5. The system of claim 1 wherein the particle growth assembly is substantially tubular in shape and includes a wick member extending from said conditioner through said initiator and through said equilibrator.

6. The system of claim 1 further comprising a mechanism for controlling a temperature of the collection member and wherein the temperature controlling mechanism is operatively coupled to the collection member to evaporate fluid as the enlarged particles and droplets are deposited.

7. The system of claim 1 wherein the collection member includes at least one from the group consisting of impaction assembly and a cyclone assembly.

8. The system of claim 1 further comprising an autosampler system configured to analyze the particles in the collection member.

9. The system of claim 1 wherein a shape of the particle growth assembly is substantially tubular in geometry.

10. The system of claim 1 further including an optical device for detecting particulate exiting the condenser.

11. The system of claim 1 wherein a geometric shape of the particle growth assembly includes a parallel plate configuration.

12. The system of claim 1 wherein a mass diffusivity of the condensing vapor is larger than or about equal to the thermal diffusivity of a carrier gas.

13. A method for collecting and concentrating particles for use in characterizing such particles in an aerosol flow comprising the steps of:
introducing a particle laden flow at a flow rate less than or equal to 100 L/min at a first temperature into a condenser;
passing the flow through the condenser having a second temperature greater than the first temperature flow wherein a vapor pressure of a condensing vapor at walls of the condenser is near saturation, thereby enlarging the particles to be collected;
collecting by inertia the enlarged particles unto a collection member having formed therein one or more collection wells; and
displacing with a stepper motor the collection member under a nozzle member coupled to the condenser.

14. The method of claim 13 further comprising controlling a temperature of the collection member so as to evaporate fluid as the enlarged particles and droplets are deposited.

15. The method of claim 13 wherein the step of displacing the collection member includes rotationally moving a circular collection plate having one or more collection wells at a periphery of the plate such that each collection well receives enlarged particles from the nozzle member.

16. The method of claim 13 wherein the step of displacing the collection member includes moving a collection plate, having the collection wells formed in an x-y grid pattern, in an x-y pattern such that each collection well receives enlarged particles from the nozzle member.

17. The method of claim 13 wherein the step of introducing the particle-laden flow includes conditioning a temperature and vapor pressure of the particle-laden flow.

18. The method of claim 13 further comprising the step of heating the nozzle member to reduce condensation.

19. The method of claim 18 further comprising the step of conditioning a temperature of the collected particles by impaction.

20. The method of claim 13 wherein the step of collecting the particles by inertia includes collection by impingement or impaction.

21. The method of claim 20 further comprising the step of conditioning a temperature of the collected particles by impingement.

22. The method of claim 13 wherein the step of introducing the particle-laden flow comprises actively cooling the flow such that the first temperature is at least 15° C. lower than the second temperature.

23. The method of claim 13 wherein the step of introducing the particle-laden flow comprises actively cooling the flow such that the first temperature is at least 25° C. lower than the second temperature.

24. The method of claim 13 wherein the step of introducing the particle-laden flow comprises actively cooling the flow such that the first temperature is at least 45° C. lower than the second temperature.

25. The method of claim 13 wherein a mass diffusivity of the condensing vapor is larger than or about equal to the thermal diffusivity of a carrier gas.

26. A particle collection apparatus, comprising:
an inlet receiving a particle laden aerosol flow at a flow rate less than or equal to 100 L/min;
a condenser coupled to the inlet and receiving the aerosol flow at a first temperature, the condenser having interior walls provided at a second temperature higher than the first temperature and including a condensing vapor having a vapor pressure at the interior walls which is near saturation, wherein the condenser is comprised of parallel plate configuration adapted for a laminar lateral flow of the particle laden flow; and
a collection member for collecting by inertia the enlarged particles, the collection membe

Assignees

• Tsi Inc
• Aerosol Dynamics Inc

Inventors

• Hering Susanne V
• Lewis Gregory S
• Eiguren Fernandez Arantzazu
• Quant Frederick
• Farmer Ii Kenneth R

Classifications

• G01N15/065

  using condensation nuclei counters · CPC title

• G01N2001/2217

  using a liquid · CPC title

• G01N1/2208

  with impactors · CPC title

• G01N1/2211

  with cyclones · CPC title

• G01N1/2202 Primary

  involving separation of sample components during sampling · CPC title