Many of the particles that are suspended in air, or other gases, are too small to be easily detected or collected. For example, most particles found in ambient air are less than 100 nm in diameter. At these small sizes it is difficult to count individual particles optically, or to collect them inertially. One approach for circumventing this limitation is to enlarge these ultrafine particles through condensation to form micrometer sized droplets that are more readily detected or manipulated. Currently, particle enlargement is employed in many commercially available condensation particle counters, as well as in condensation-based particle collectors, and air-to-air particle concentrators.
Many condensation-based instruments contain a wick that holds the working fluid that vaporizes, and subsequently condenses on the particles. The performance of these instruments depends on maintaining a saturated wick, that is a wick that is filled to near, or at, capacity with the condensable working fluid. In most instruments the saturation of the wick is ensured by maintaining direct contact between the wick and a liquid reservoir. In portable condensation instruments which require tolerance to tipping and motion, or operation in microgravity environments, it is not possible to use liquid reservoirs. For such devices, all of the working fluid must be held within the wick itself. Typically, these reservoirless instruments start with a saturated wick, but subsequently fail after some hours of use as the condensing fluid is consumed.
The technology describes a wick sensor that detects the saturation level of the wick commonly used in a condensation system. Specific application is given to a water-based condensation system in which the wick saturation level can either increase, or decrease, during operation.
One general aspect includes a wick moisture sensor, including: a light source configured to illuminate a surface of the wick. The wick moisture sensor also includes a detector configured to detect reflected light from the light source that is reflected by the wick, and determine the intensity of reflected light. The wick liquid sensor also includes where the wick is formed from a porous media that is wettable by the liquid, and becomes translucent when filled with the liquid.
Another aspect includes a particle detection system, including: a wick sensor configured to determine liquid saturation of the wick, the wick is formed from multiple layers of a porous media which is wettable by the liquid and translucent when filled with the liquid, the wick sensor including, an illumination source positioned to illuminate the wick; a dark material placed under one or more layers of the wick opposite of the illumination source and a detector configured to measure the intensity of light from the illumination source scattered by wick.
One general aspect includes a particle condensation system, including: a growth chamber including a wick formed from multiple layers of a porous material which is wettable by a liquid and translucent when filled with the liquid. The particle condensation system also includes a wick sensor including a light source configured to illuminate a surface of the wick and a detector configured to detect wick reflected light from the light source and determine the intensity of reflected light.
This Summary is provided to introduce a selection of concepts in a simplified form that are further described below in the Detailed Description. This Summary is not intended to identify key features or essential features of the claimed subject matter, nor is it intended to be used as an aid in determining the scope of the claimed subject matter.
A wick sensor comprising an optical device configured to assess the extent to which the wick material is saturated with liquid is disclosed. The reflectivity of the wick, or optical appearance, changes with the saturation level of the wick. Typically, a wick material used in condensation systems is an absorbent material with a porous structure. Such materials scatter light when dry, due to their microporous structure. As these pores fill with liquid, the wick material becomes translucent. The wick sensor disclosed herein monitors this translucence. The wick sensor includes a reflectivity sensor, consisting of a small light emitting diode (in the infrared or at other wavelengths) and photo transistor. These components, and associated circuit board, are mounted in a housing placed immediately on the outside of the wick, and are positioned such that the sensor views the outer layer of the wick. A dark object is placed immediately underneath the layer of wick viewed by the reflectivity sensor. A clear window in the sensor housing allows the sensor to view the wick while protecting the sensor and its electronics from the moist wick environment.
When the wick is moist, much of the incident light from the sensor is transmitted through the wick material and absorbed, such that the reflected light signal is small. As the material dries, the reflected light signal rises, and a portion of the light scattered from the outer layer of the wick material is captured by a photo detector. This change is most apparent when a dark material is placed underneath the outer layer of the wick, as it makes the wick appear dark when saturated. The wick signal can be used to warn the operator of a drying wick, or it can be used to control the instrument operating parameters.
One application of the wick sensor is to three-stage water-based condensation systems used for measuring ambient air. With this system the water-saturation of the wick can either increase or decrease during operation, depending on ambient conditions and operating temperatures. During operation water may be taken up by the wick due to moisture present in the air that is sampled. Alternatively, the wick can lose water due to the evaporation that must occur as part of the condensation process. The net change in water held by the wick can be regulated through control of the operating temperature of the final, water recovery stage. The wick sensor of this invention indicates the saturation level of the wick, and provides feedback needed to control the wick saturation level. This feedback enables operation such that the extent of water vapor uptake and removal are balanced. If operated in an environment with sufficient moisture in the sampled airstream, the wick sensor enables operation of the system over extended periods of time, weeks to months, without need to replenish the wick.
This wick sensor assesses the moisture content of a microporous material such as is commonly used as a wick in airborne particle condensation systems. The wick sensor measures the optical reflectivity of this material. This reflectivity, or optical appearance, changes when the wick becomes saturated with a liquid, such as water or alcohol.
Typically, particle condensation systems require that the wick that holds the condensing fluid be continually replenished via liquid injection, or physical contact with a liquid reservoir. Using the wick sensor, a particle condensation system capable of maintaining a properly wetted wick through recovery of water vapor from the sampled air stream is provided. This is done by using the wick sensor as a feedback signal to set the temperature of the third, moderator stage. It is the temperature of this stage that determines the amount of water vapor in the flow that exits the instrument. Importantly, model calculations presented in U.S. Pat. No. 8,801,838 (Hering et al.), and laboratory data show that the particle activation and condensational growth is independent of operating temperature of the third and final moderator stage. Thus the moderator stage operating temperature can be adjusted to control the amount of water recaptured by the wick, without affecting instrument performance. The wick sensor reading can be used to adjust the moderator temperature to add or remove water from the wick, as needed. If the wick is dryer than desired, the moderator temperature is lowered, and if it is wetter than desired, the moderator temperature is raised. A PID control algorithm can be used to adjust the moderator temperature to add or remove water from the wick, as needed.
In instances in which the instrument 30 is configured to measure the relative humidity and temperature of the sampled air stream, the corresponding dew point value can be used as a first estimate of the temperature set point of the moderator stage 34. In this instance, the control algorithm operable by the processor to control the temperature of the moderator stage 34 reduces to a function of this input dew point, and a simple proportional gain, as follows:
Tmod,new=f(DPin)+g*(wtarg−w)
where:
The reflectivity, and hence the raw wick sensor output, increases as the wick dries. Hence (wtarg−w) is a positive value when the wick is wetter than the target value, and the algorithm will increase the set point for the moderator temperature. Similarly, if (wtarg−w) is a negative, the wick is drier than the target value, and the algorithm will decrease the set point for the moderator temperature. In other words, g is positive. The function f(DPin) returns a first estimate the moderator temperature needed to make the water vapor content of the flow exiting the instrument equal that which enters. This function is determined experimentally, and is dependent on the specific system design, but is generally, it is independent of the input relative humidity.
In situations where the prevailing ambient air contains very little water vapor, i.e. when the prevailing dew point is low, the sustained operation requires some humidification of the sampled air stream. This can be accomplished by passing the sample air flow through a short piece of Nafion (R) tubing (available from Permapure, Lakewood, N.J.) that is surrounded by liquid water, or by high humidity air such as can be obtained using a hygroscopic salt such as sodium polyacrylate.
The implementation of the wick sensor presented here is for a water-based condensation system adapted to particle counting. This same approach could be used for a condensation system for particle collection, or aerodynamic particle focusing. The wick sensor is applicable to alcohol-based condensation system using a microporous wick, or to any working fluid with a similar refractive index such that the light scattering from the wick decreases as the pores are filled with the liquid. Although the implementation here is presented with a condensation system without a liquid reservoir, it could also be used in a system where the working fluid is injected into the wick. In this instance the sensor would minimize the amount of working fluid consumed.
Although the subject matter has been described in language specific to structural features and/or methodological acts, it is to be understood that the subject matter defined in the appended claims is not necessarily limited to the specific features or acts described above. Rather, the specific features and acts described above are disclosed as example forms of implementing the claims.
This application claims the benefit of priority to U.S. Provisional Application No. 62/572,394, filed Oct. 13, 2017, entitled “Wick Moisture Sensor for Airborne Particle Condensational Growth Systems”, which is incorporated herein by reference in its entirety. This invention was made with government support under contracts #NNX15CC78P #NNX16CC22C from NASA. The government has certain rights in this invention.
Number | Name | Date | Kind |
---|---|---|---|
2042095 | Grant | May 1936 | A |
2684008 | Vonnegut | Jul 1954 | A |
2721495 | Schaefer | Oct 1955 | A |
3011387 | Johnson | Dec 1961 | A |
3011390 | Van Luik | Dec 1961 | A |
3037421 | Bigelow | Jun 1962 | A |
3592546 | Gussman | Jul 1971 | A |
3632210 | Rich | Jan 1972 | A |
3694085 | Rich | Sep 1972 | A |
3738751 | Rich | Jun 1973 | A |
3806248 | Sinclair | Apr 1974 | A |
3890046 | Hart | Jun 1975 | A |
4293217 | Bird | Oct 1981 | A |
4449816 | Kohsaka | May 1984 | A |
4761074 | Kohsaka | Aug 1988 | A |
4790650 | Keady | Dec 1988 | A |
4792199 | Borden | Dec 1988 | A |
4868398 | Mulcey | Sep 1989 | A |
4950073 | Sommer | Aug 1990 | A |
4967187 | Dumas | Oct 1990 | A |
5011281 | Harris | Apr 1991 | A |
5026155 | Ockovic | Jun 1991 | A |
5045693 | McKeon | Sep 1991 | A |
5098657 | Blackford | Mar 1992 | A |
5118959 | Caldow | Jun 1992 | A |
5176723 | Liu | Jan 1993 | A |
5239356 | Hollander | Aug 1993 | A |
5278626 | Poole | Jan 1994 | A |
5519490 | Nakata | May 1996 | A |
5525514 | Jacobs | Jun 1996 | A |
5659388 | Scheer | Aug 1997 | A |
5675405 | Schildmeyer | Oct 1997 | A |
5872622 | Schildmeyer | Feb 1999 | A |
5903338 | Mavliev | May 1999 | A |
5964181 | Pereyra | Oct 1999 | A |
6330060 | Flagan | Dec 2001 | B1 |
6469780 | McDermott | Oct 2002 | B1 |
6498641 | Schildmeyer | Dec 2002 | B1 |
6529272 | Flagan | Mar 2003 | B2 |
6567157 | Flagan | May 2003 | B1 |
6829044 | Liu | Dec 2004 | B2 |
6980284 | Ahn | Dec 2005 | B2 |
7494567 | Haran | Feb 2009 | B2 |
7656510 | Roberts | Feb 2010 | B2 |
7719683 | Ahn | May 2010 | B2 |
7724368 | Ahn | May 2010 | B2 |
7828273 | Molter | Nov 2010 | B2 |
7988135 | Molter | Aug 2011 | B2 |
8072598 | Ahn | Dec 2011 | B2 |
8459572 | Hering | Jun 2013 | B2 |
8465791 | Liu | Jun 2013 | B2 |
8576400 | Hulteen | Nov 2013 | B2 |
8603247 | Liu | Dec 2013 | B2 |
9535022 | Meredith | Jan 2017 | B1 |
9579662 | Hering | Feb 2017 | B2 |
9610531 | Hering | Apr 2017 | B2 |
20030020910 | Peterson | Jan 2003 | A1 |
20040051817 | Takahashi | Mar 2004 | A1 |
20050134580 | Sonoda | Jun 2005 | A1 |
20060001866 | Clarke | Jan 2006 | A1 |
20090252870 | Munneke | Oct 2009 | A1 |
20150112165 | Heikenfeld | Apr 2015 | A1 |
20150293016 | Perkins | Oct 2015 | A1 |
20160054589 | Otts | Feb 2016 | A1 |
Number | Date | Country |
---|---|---|
102005001992 | Jul 2006 | DE |
0658461 | Nov 1993 | EP |
4108034 | Jun 2008 | JP |
Entry |
---|
PCT International Search Report, PCT Patent Application No. PCT/US2018/055911. |
PCT Written Opinion of the International Searching Authority, PCT Patent Application No. PCT/US2018/055911. |
Hoppel, W. A., Twomey, S., & Wojciechowski, T. A. (1979). A segmented thermal diffusion chamber for continuous measurements of CN. Journal of Aerosol Science, 10(4), 369-373. |
Leaitch, R., & Megaw, W. J. (1982). The diffusion tube; a cloud condensation nucleus counter for use below 0.3% supersaturation. Journal of Aerosol Science, 13(4), 297-319. |
Bricard, J., Delattre, P., Madelaine, G. and Pourprix, M., 1976, in Fine Particles (Edited by Liu, B. Y. H.) Academic Press, New York. pp. 565-580. |
“Argawal and Sem J. , 1980, Continuous flow, single-particle-counting condensation nucleus counter, Journal of Aerosol Science, vol. I I, pp. 343-357. Cite with reference to Bricard”. |
Hering, S. V., & Stolzenburg, M. R. (2005). A method for particle size amplification by water condensation in a laminar, thermally diffusive flow. Aerosol Science and Technology, 39(5), 428-436. |
Hering, S. V., Stolzenburg, M. R., Quant, F. R., Oberreit, D. R., & Keady, P. B. (2005). A laminar-flow, water-based condensation particle counter (WCPC). Aerosol Science and Technology, 39(7), 659-672. |
Weber, R. J., Orsini, D., Daun, Y., Lee, Y. N., Klotz, P. J., & Brechtel, F. (2001). A particle-into-liquid collector for rapid measurement of aerosol bulk chemical composition. Aerosol Science & Technology, 35(3), 718-727. |
Eiguren Fernandez, A., Lewis, G. S., & Hering, S. V. (2014). Design and laboratory evaluation of a sequential spot sampler for time-resolved measurement of airborne particle composition. Aerosol Science and Technology, 48(6), 655-663. |
Hering, S. V., Lewis, G. S., Spielman, S. R., & Eiguren-Fernandez, A. (2019). A MAGIC concept for self-sustained, water-based, ultrafine particle counting. Aerosol Science and Technology, 53(1), 63-72. |
Skala, G. F. (1963). A New Instrument for the Continuous Measurement of Condensation Nuclei. Analytical Chemistry, 35(6), 702-706. |
Roberts, G.C., & Nenes, A. (2005). A continuous-flow streamwise thermal-gradient CCN chamber for atmospheric measurements. Aerosl Science and Technology, 39(3), 206-221. |
Hering, et al., U.S. Appl. No. 16/671,594 Humidity Conditioning for Water-Based Condensational Growth of Ulrtafine Particles, filed Nov. 1, 2019. |
International Preliminary Report on Patentability, dated Apr. 23, 2020, PCT Application No. PCT/US2018/055911. |
Number | Date | Country | |
---|---|---|---|
20200116619 A1 | Apr 2020 | US |