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
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.
* * * * *