Continuous Flow Condensation Nuclei Counter

Sinclair April 23, 1

Patent Grant 3806248

U.S. patent number 3,806,248 [Application Number 05/334,497] was granted by the patent office on 1974-04-23 for continuous flow condensation nuclei counter. This patent grant is currently assigned to The United States of America as represented by the United States Atomic. Invention is credited to David Sinclair.


United States Patent 3,806,248
Sinclair April 23, 1974

CONTINUOUS FLOW CONDENSATION NUCLEI COUNTER

Abstract

A condensation nuclei particle counter for continuous operation capable of condensing out nuclei within the range of 0.002-0.1 micrometers. The aerosol is humidified by a pool of an alcohol or other volatile liquid of low freezing point and then condensed in a chamber whose walls are maintained at a temperature of -10.degree. to -20.degree. C. A light beam is passed through the resultant fog and the attenuation is measured as an indication of the particle density.


Inventors: Sinclair; David (Martinsville, NJ)
Assignee: The United States of America as represented by the United States Atomic (Washington, DC)
Family ID: 23307485
Appl. No.: 05/334,497
Filed: February 21, 1973

Current U.S. Class: 356/37
Current CPC Class: G01N 15/065 (20130101)
Current International Class: G01N 15/06 (20060101); G01n 001/00 ()
Field of Search: ;356/37,102,103 ;340/236

References Cited [Referenced By]

U.S. Patent Documents
3592546 July 1971 Gussman
3694085 September 1972 Rich
Primary Examiner: Wibert; Ronald L.
Assistant Examiner: McGraw; V. P.
Attorney, Agent or Firm: Horan; John A. Belkin; Leonard

Claims



What is claimed is:

1. A continuous flow particle counter for determining the nuclei concentration of an aerosol comprising:

a. means forming a first chamber for mixing therein said aerosol with a condensable vapor, said chamber containing a pool of the aforesaid condensed vapor, said mixing taking place above said pool;

b. means forming a second chamber whose walls are maintained at a temperature substantially lower than the temperature within said first chamber;

c. means for continuously delivering a mixture of said aerosol and vapor from said first chamber into said second chamber where a visible fog is formed from said mixture due to the cooling effect on the walls of said second chamber;

d. means for continuously withdrawing mixture from said second chamber; and

e. means for continuously detecting the visible nuclei concentration of said fog.

2. The counter of claim 1 having means for maintaining turbulent flow conditions within said chambers.

3. The counter of claim 2 in which said condensable vapor is an alcohol.

4. The counter of claim 3 in which the walls of said second chamber are maintained at a temperature of -10.degree. to -20.degree.C.

5. The counter of claim 2 in which said detecting means comprises a light source and means for measuring light from said light source after passing through said second chamber, whereby the fog within said second chamber attenuates the light passing through.
Description



BACKGROUND OF THE INVENTION

The invention described herein was made in the course of employment with the U.S. Atomic Energy Commission.

During recent years there has been increased interest in the analysis and measurement of sub-micron aerosols. Those aerosols, generally referred to as condensation nuclei, are of particular concern because they are believed to be the progenitors of a variety of larger aerosols such as cloud, fog, smog, dust, and haze in which there is a great deal of concern. The size range of particular interest for the condensation nuclei is 0.002 to 0.1 micrometers.

Conventional apparatus such as light-scattering photometers and light microscopes are not capable of measuring particulates of such small size. Furthermore, techniques which can be employed in the measurement of such small particles do not conveniently lend themselves to continuous on-line operation and are generally too inconvenient and too complicated to employ on a regular basis for monitoring atmospheric conditions. Continuously operating devices which have been developed lack sufficient portability which would permit on short notice the measurement of aerosol conditions at different locations. Furthermore, a continuous operating device which has been developed requires the use of a secondary flow of cold air to bring the temperature of the aerosol down to proper supersaturating conditions and it has been found that such an arrangement will not measure particles present down to 0.002 micrometers diameter.

SUMMARY OF THE PRESENT INVENTION

Many of the aforementioned problems are overcome by the present invention in which it is possible to measure aerosols in the sub-micron range of 0.002 to 0.1 micrometers on a continuous basis, with little difficulty and inconvenience, and with great accuracy. An additional feature of this invention is that the apparatus is such that it can be moved to different locations quickly and with a minimum of inconvenience.

Briefly described, a preferred embodiment of this invention consists of a chamber wherein the aerosol of interest is mixed with a suitable condensable vapor such as an alcohol, and another chamber maintained at a substantially lower temperature into which the mixture passes for cooling to supersaturation and formation of a fog. By substantially lower temperature is meant a temperature low enough to cause the fog to form about the nuclei. The chambers are provided with turbulence producing baffles and a detection system for measuring the visible concentration of the fog. The detection system may consist of a light source at an end of the cold chamber and a light detection and measuring device such as a photo cell at the other end to sense the light attenuation caused by the fog. The apparatus is continuously operating, that is, fresh aerosol is continuously drawn in and exhausted. Typically, the nuclei counter would be used in conjunction with an aerosol measuring system such as a diffusion battery to measure particle size and size distribution.

It is thus a principal object of this invention to provide a continuous flow particle counter for determining nuclei concentration and size in the sub-microscopic particle size range.

Other objects and advantages of this invention will hereinafter become evident from the following description of a preferred embodiment of this invention.

BRIEF DESCRIPTION OF THE DRAWING

The FIGURE illustrates an elevation view in section of a preferred embodiment of this invention.

DESCRIPTION OF THE PREFERRED EMBODIMENT

Referring to the FIGURE, counter 10 consists of an elongated housing 12 which may be rectangular or circular in cross section surrounded by a layer of thermal insulation 14. A cylindrical container 16 is mounted above housing 12 with an access tube 18 providing communication as illustrated between end chambers within these two members.

Container 16 is divided into several chambers by baffles 22a, 22b and 22c each of which is provided with an axial opening 24a, 24b and 24c, respectively. For reasons which will be apparent later, a liquid pool 25 is provided in all of the chambers, except, of course, the end chamber having access tube 18. The liquid making up pool 25 is any liquid which will evaporate under the conditions described and condense when cooled to form a fog. The bottoms of baffles 22a and 22b are provided with small openings 27a and 27b, respectively, to provide a uniform level of said pool. Liquid is inserted through a small opening 25a which may be closed with a stopper 25b. There is provided an aerosol inlet tube 26 to a chamber of container 16 at the upstream or opposite end of the latter from access tube 18.

Container 12 is divided into chambers by baffles 28a-28e having openings as illustrated. The bottoms of baffles 28a-28e are provided with small openings 29a-29e, respectively, to permit drainage of condensed vapor. An exhaust tube 32, to carry away the mixture, is connected to a liquid trap T, a flow meter M, and the suction side of an air pump P to draw the aerosol through inlet tube 26 and chambers 16 and 12 as already described. Flow of the aerosol is indicated by arrows.

Extending from the downstream end of housing 12 is an assembly 34 containing an electric lamp 36 and a lens 38 mounted on a sleeve 39 with O-rings 40 and 41. When lamp 36 is energized, light is directed by lens 38 down through the length of housing 12, passing through the central openings in baffles 28a-28e.

At the upstream end of container 12 is a photocell and window assembly 42 which comprises a sleeve 44 with O-rings 46 and 48, baffle 28e, and photocell unit 52. The latter measures the light received from lamp 36, and as is understood in the art, suitable apparatus (not shown) is provided to record and/or indicate the intensity of the light received by photocell unit 52.

In order to maintain housing 12 at the proper operating temperature, wrapped around the walls of housing 12 may be refrigeration coils or thermo-electric cooling modules 54a, 54b, etc., disposed at suitable locations on the outside of the walls of housing 12, as shown.

In the operation of the apparatus described, the aerosol, the extent of whose condensation nuclei is to be measured, enters counter 10 by way of inlet tube 26 and passes down through the length of container 16. The aerosol mixes with the vapors of the liquid making up pool 25, baffles 24a-24c acting to promote turbulence thereby increasing the extent to which the mixing takes place and forming a near saturated mixture. At the downstream end of container 16 the gaseous mixture passes into housing 12 by way of access tube 18 and flows the length of housing 12 at the downstream end of which the mixture leaves by way of exhaust tube 32. Baffles 28a-28e similarly promote turbulence and thorough mixing within the chambers. The walls of housing 12 are maintained at a suitable lower temperature such that the gaseous mixture is cooled sufficiently to become super-saturated, a fog being formed due to the presence of the nuclei in the aerosol. The turbulence caused by baffles 28a-28e enhances heat transfer between the walls of housing 12 and the gaseous mixture, insuring an adequate low temperature throughout the gaseous fluid.

The resulting fog attenuates the light passing from lamp 36 to photocell unit 52 and the observed or recorded intensity of the light is a direct indication of the number of particles within the aerosol.

Counter 10 is calibrated by running aerosols of known particulate content through the apparatus.

An important aspect of this invention involves the maintenance of sufficiently high saturation under dynamic conditions in contrast to the static conditions found in other such devices during humidification and temperature equalization of the sample. This effect is enhanced in the present invention by utilizing as the liquid in pool 25 an alcohol, preferably ethanol, and maintaining the temperature of the walls of housing 12 in the range of about -10.degree. C. to -20.degree.C.

EXAMPLE

A counter was constructed with container 16 made from a copper tube 30.5 cm long and 5.1 cm diameter containing a 1 cm deep pool of ethyl alcohol. Housing 12 was made from copper, with a length of 30.5 cm and an inside diameter of 3.8 cm with 1.3 cm walls. Aerosol flow rate was 4 liters/min. with the time of exposure about nine seconds in container 16 and five seconds in housing 12. The wall of the latter was maintained in the -10.degree.C. to -20.degree.C. temperature range. This counter was able to produce a fog out of nuclei down to about 0.002 micrometers diameter.

An important feature of this invention is that it provides continuous flow counting, in contrast to conventional nuclei counters which operate by intermittent sampling and adiabatic expansion. Diffusion batteries, which are essential for rapid measurement of these sizes, require constant flow of aerosol.

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