The invention relates to systems and devices for measuring concentrations of nanometer or ultrafine particles, and more particularly to such systems that are adjustable in terms of their sensitivities to certain sizes or electrical mobilities of particles or sets of particles that fall within the nanometer size range.
When materials are produced or formed in the nanometer size range, i.e. from about 1 micrometer in diameter down to molecular levels, they exhibit unique properties that influence their physical, chemical and biological behavior. Nanotechnology, the field of endeavor concerned with materials in this size range, has experienced explosive growth over the last several years as new and diverse uses for nanomaterials are discovered and developed throughout a broad range of industries.
These developments have raised concerns, because the occupational health risks associated with manufacturing and using nanomaterials are not clearly understood. Many nanomaterials are formed from nanoparticles initially produced as aerosols or colloidal suspensions. Workers may be exposed to these particles through inhalation, dermal contact and ingestion, at increased levels due to working environments with nanoparticles in concentrations that far exceed ambient levels.
Traditionally, health related concerns about airborne particles have focused on particle concentrations in terms of mass per unit volume. Under this approach, permitted maximum concentration standards are determined, and mass concentrations are measured with respect to these standards. However, toxicologic studies involving ultrafine particles (0.1 micron diameter and below) suggest that particle surface area, as compared to particle mass, is the better indicator of health effects. This may follow from the fact that for any given shape (e.g. spherical), the smaller the particle, the greater is its surface area compared to its volume or mass. A proportionally larger specific surface area (i.e. surface area divided by mass) increases the tendency of a particle to react with chemicals in the body. Moreover, due to the small mass of nanoparticles, mass concentration measurements are difficult to obtain and lack the requisite sensitivity, even when based on particle accumulation such as through collection of particles on a filter. Additional studies have also suggested that health effects may also be correlated with the number of inhaled ultrafine particles that impact the lungs. Accordingly, instruments that measure particle concentrations in terms of surface area and particle number in the nanometer size range are expected to provide more useful assessments of health risks due to nanoparticle exposure.
In one example embodiment of the invention, a nanoparticle scanning and sizing system is disclosed that is compact, portable and capable of size distributions down to 10 nanometers and able to measure in both SCAN mode for real-time size distributions and in SINGLE mode for single electrical mobility concentration monitoring. One minute size distributions along with one second single size data can also be obtained from the novel and compact aerosol system. (a sizing device with a wide size and concentration range).
In a related embodiment, an improved nanoparticle sizer instrument is described herein that facilitates portability and operation with other optical sizers to increase particle size measurement range. In one example embodiment, three orders of size magnitude, such as from about 10 nanometers to about 10 microns, is measurable and facilitates real-time data collection. In related embodiments, the sizing system described herein will size particles down to the 2.3 nm and 1 nm size. Sizing below these levels may necessitate alterations in some hardware components. In addition, portability is improved with the use of long life (about 8 hours), hot swappable batteries or alternatively, fuel cells. The general concepts described herein are applicable to other aerosol instruments and are not just limited to nanoparticle sizing.
In yet another related embodiment, an RDMA (radial differential mobility analyzer) is combined with a CPC (condensation particle counter) and a power source, such as a battery or solar cell, to create a portable SMPS (scanning mobility particle sizer). In yet another embodiment, an RDMA and an electrometer is configured for another sizing system.
In one example embodiment of the invention, a filtration manifold for use in connection with a nanoparticle sizer is described that improves serviceability, air flow and filtration as well as facilitating a compact and portable design. In addition, the overall manifold construct and modular arrangement of the manifold can be used in other aerosol instruments. In this example embodiment, the manifold design is an integrated, multi-unit system that includes pressure/flow controls, a series of coaxial pressure taps and a series of interconnected filters. The manifold assembly is also a modular system that is ideal to route airflow or stream inlets and outlets wherever convenient to effectuate the desired interconnections. In related embodiments, the manifold assembly is configured for use in most particle instruments and in most miniature devices that require serviceable filtered air handling/routing such as gas instruments, small scale nanoparticle manufacturing, and semiconductor and pharmaceutical manufacturing applications.
Following below are more detailed descriptions of various related concepts related to, and embodiments of, methods and apparatus for an improved system and method for sizing particles in the nanometer range for various applications. It should be appreciated that various aspects of the subject matter introduced above and discussed in greater detail below may be implemented in any of numerous ways, as the subject matter is not limited to any particular manner of implementation. Examples of specific implementations and applications are provided primarily for illustrative purposes.
Referring now to
Assembly 120 is then coupled to the size selection stage which in this example embodiment is a differential mobility analyzer (DMA) device 130, such as, but not limited to, a radial DMA, used for size resolution and accuracy of the particles to be measured. The radial DMA (RDMA) unit in this example embodiment contributes to system 100's compactness and light weight. The particles exiting DMA 130 are then directed to a condensation particle counter (CPC)140. In this example embodiment, CPC 140 is an isopropyl-based CPC adapted to provide accurate measurements at high and low concentrations using a working fluid to facilitate condensation (other working fluids include but is not limited to butanol, isopropanol, other alcohols, hydrocarbons, etc.). A suitable working fluid may be chosen, such that toxicity and special handling requirements are minimized. In a related embodiment, system 100 is configurable to use a water-based CPC where toxicity is of concern (see U.S. Pat. No. 6,712,881 to Hering et al, which is incorporated herein by reference in its entirety). In this example embodiment, the instrument is operable off a rechargeable wick with an eight hour life or longer if an external liquid reservoir and power source are used.
In various related example embodiments, an optional inlet selector for eliminating particles of particular size and/or properties from the sample to be measured. The optional inlet selector includes but is not limited to a cyclone, an impactor, or a virtual impactor. The inlet selector serves to prevent interference from large particles (those outside the instrument measurement range) in less controlled aerosols. In yet another related embodiment, this component may be excluded from the device when measuring a well-controlled aerosol of a limited size range. Additionally, as the pressure drop across an inlet selector typically varies predictably as a function of inlet flow rate, it can be used as a portion of the system that measures the inlet flow rate in the device (which is useful for measuring absolute concentration of particles).
Referring again to unipolar charger 120 of
Referring again to RDMA 130 of
Referring again to CPC 140 of
Similar to systems 100 and 100A,
Referring now more specifically to example embodiments of nanoparticle sizing systems 200 and 200A, an aerosol is received at an inlet conduit 202A (with an inlet flow rate of about 0.75 lpm) and directed through a large-particle separator such as a cyclone 210A, to remove particles having aerodifferential diameters that exceed one micron. The flow of particles then flow from cyclone 210A into unipolar corona charger 220A. At corona needle sheath inlet 204A, air is pumped by a pump 205A through a charcoal filter 206A and a high efficiency particle air (HEPA) filter 207A, thereby providing a corona flow of about 0.4 lpm of ion charged air into charger 220A via a corona needle 208A (not shown but within charger 220A and which is biased to a high positive voltage e.g. 4 kilovolts and generates positive ions at its tip); which mixes with air from cyclone 210A within the charger body exiting through an orifice 209A. Meanwhile, the remaining flow from cyclone 210A is conducted into charger body or chamber 220A through another orifice, for a turbulent mixture with the positive ions to effect a diffusion charging of the particles suspended in the aerosol. A portion of positively charge air flow is channeled into a bypass tube 221A at a flow rate of about 0.9 lpm, through a filter 222A and through a valve and orifice assembly 223A with a pump 224A. The filtered air passes through another filter 225A before exiting through port 226A.
The aerosol leaving mixing chamber 220A includes a suspension of positively charged particles and positive ions that is then channeled into a radial differential mobility analyzer (RDMA) 230A with the help of a sheath flow of clean air. The sheath flow is formed from part of the particle laden air flowing into tube 232A which is filtered through a filter 233A and is drawn by a pump 234A. The pumped air flows through a filter 236A and through an orifice 237A (about 0.020 inch in size) and eventually is redirected into RDMA 230A as the clean air sheath flow at a flow rate of about 0.75 lpm. In related embodiments, the sheath flow rate is as high as 4 lpm and charger flow rate as high as 2.5 lpm; with either flow rate being as low as 0.05 lpm as well.
Particle laden air of a predefined size particle size exits RDMA 230A as CPC/aerosol flow via a tube 239A at a flow rate of about 0.25 lpm and is fed into a CPC 240A. CPC 240A uses condensation particle counting technology as described in U.S. Pat. No. 4,790,650 to Keady and U.S. Pat. No. 5,118,959 to Caldow et al and an optical detection system as described in U.S. Pat. No. 6,831,279 to Ho et al, all of which are incorporated by reference in their entireties. Coupled to CPC 240A is a reservoir/fill valve assembly 250A adapted to continuously saturate a removable wick within CPC 240A. Assembly includes a fill bottle adapted for a user selected working fluid to be used by system 200A in CPC 230A. Once the particle laden air sample exits CPC 240A (after being counted and analyzed) it passes through a filter 242A and through an orifice 244A (about 0.012 inch in size) and exits into bypass tube 221A after which it exits the system through exit port 226A.
Although not specifically shown in the figures of systems 100, 100A, 200 and 200A, a novel pump and manifold assembly (as shown and discussed in more detail in
Referring now to
Referring now to
Referring now to
A pump and manifold assembly 350 is also included in system 300 (see
Referring now to
In general, flow systems are created to be driven by pumps, vacuum sources or pressure sources. Supply (positive flow) flows are distributed to external hardware, and are typically filtered and simultaneously measured. The flow measurement should be unobtrusive (i.e. does not affect flow being measured) and when made by measuring pressure drop across an orifice, should not be measured across the filter, as the pressure drop across a filter changes as the filter loads become clogged. This typically requires that the orifice be located away from the filter and generally requires additional tubing and fittings that are external to the filter. In the manifold blocks of the invention (effectively the repeatable block/units referred to above) the filter, orifice, and pressure taps are located near one another, generally along a single axis, with access to the filter media from one convenient direction. The geometry and structure of these units is such that interconnections between units can be made from many directions. For both the inlet and outlets to the filter, connections can be made from any path not parallel to the central axis. In the case of the outlet, small diameter connections (smaller than the central diameter of the filter media, not intersecting pressure taps) can be arranged along this path (see
Similar to this repeatable unit, return flows from an external device are also filtered. These units can also be combined or integrated into the manifold unit 850 thereby omitting the central orifice and pressure tap. The outlet of such a filter would be connected to a negative pressure source (e.g. the inlet to a pump for its protection). This repeatable manifold unit 850A is shown in
Referring now to
A typical flow system will also contain multiple branches, for instance where one pump supplies filtered air through two or more different filters or where two or more flows are filtered before exiting the system through a pump (the system exhaust). Such an arrangement is shown in
For a large flow system, these repeating filtering blocks/units and features may be combined into a single manifold with mostly repeating units. The complexity of interconnects and the size of externally connected components is all that controls the size of the resulting manifold, above and beyond the size of the repeating units. Manifold 850 shown in
The design of the present manifold assembly solves the problem of serviceability and manufacturability of most filter manifolds by allowing assembly and replacement of filters from a single direction through a single unobstructed access panel, such as cover 866. The method of arranging filter units allows for ease of assembly of external tubing and vacuum/pressure sources and allow the designer to route connection so as to minimize tube length. The modularity and the design of the modular units allows for co-location of functions (filtration, flow measurement, and flow restriction/control), simplifying the construction of an aerosol instrument system. The filter units are small and internal connections allow for miniaturization, especially when compared to non-integrated solutions. Moreover, since it is a modular design as much as a fixed design, the basic units can be customized and combined for use in many different aerosol instrument applications.
In a related embodiment, the manifold system is configurable to join neighboring filters, to internally connect them to external pressure or vacuum sources, to connect filter cavities to additional external filters or flow treatment devices, or to incorporate valves or other devices to restrict, set, or control the various flows.
In other various embodiments, the nanoparticle scanning system and apparatus described herein include a novel manifold device having an orifice and pressure taps for measuring pressure drop are included in the same filter cavity unit, that the units are arranged such that interconnections are internal to a manifold, and that the units are designed to be modular so that they can be arranged for most aerosol flow applications. The invention is also unique in that all filter media can be installed from a single direction (for serviceability), can be changed depending on the desired level of filtration (more or less efficient), and that inlets and outlets to external devices (sources or sinks for the flow) can be arranged to minimize the length of tubing needed for these external interconnections.
As maintaining proper flows is critical to accurate measurements, such devices use one or various devices for measuring flows, such as thermal mass flow meters, or as in our current prototype, the pressure drop across a known geometry (a fixed orifice). Other methods may be used as well including the use of pressure drop for flow measurement which is especially useful because it is small in size and of limited power consumption.
In various embodiments of the inventions, there are included various (controlled or limited) pumps (internal or replaced by a means of connecting to external sources for moving gas flows), filters, tubes and other flow passages. These items may or may not be combined into manifolds, to reduce size and improve serviceability and manufacturability. For portability, any of the pumps should be internal, small, and of low power consumption. Such pumps require low flow size devices (like the RDMA) and low flow detectors (like a CPC), as large flows would require pumps with much larger power requirements (limiting or eliminating portability).
Various embodiments include circuitry for user interface, feedback, and reporting of measurements, as well as circuitry necessary for controlling flows, applying constant or time-varying voltages to the RDMA, for interpreting measurements/signals received from the CPC, and for other tasks. Finally, batteries are used for true portability. Such batteries may be internal, or removable. If removable, it would be ideal that they were also hot-swappable, as they are in this device. When used in a stationary mode, the device should also be usable with an external DC or AC power source.
The following U.S. patents and publications are herein incorporated by reference in their entirety: U.S. Pat. Nos. 5,117,190; 5,118,959; 5,596,136; 5,606,112; 5,620,100; 6,003,389; 6,012,343; 6,230,572; 6,568,245; 7,230,431 and 2011/0056273.
While the invention has been described in connection with certain preferred embodiments, there is no intent to limit it to those embodiments. On the contrary, it is recognized that various changes and modifications to the exemplary embodiments described herein will be apparent to those skilled in the art, and that such changes and modifications may be made without departing from the spirit and scope of the present invention. Therefore, the intent is to cover all alternatives, modifications and equivalents included within the spirit and scope of the invention as defined by the appended claims.
The present application claims priority to International Application No. PCT/US2013/022224, filed on Jan. 18, 2013, which in turn claims priority to and the benefit of U.S. Provisional Application No. 61/589,098, filed Jan. 20, 2012, the disclosures of which are hereby incorporated by reference in their entireties.
Filing Document | Filing Date | Country | Kind |
---|---|---|---|
PCT/US2013/022224 | 1/18/2013 | WO | 00 |
Publishing Document | Publishing Date | Country | Kind |
---|---|---|---|
WO2013/109942 | 7/25/2013 | WO | A |
Number | Name | Date | Kind |
---|---|---|---|
5072626 | Ensor et al. | Dec 1991 | A |
5922976 | Russell et al. | Jul 1999 | A |
20050162173 | Mirme | Jul 2005 | A1 |
20050173629 | Miller et al. | Aug 2005 | A1 |
20060284077 | Fissan et al. | Dec 2006 | A1 |
20080264491 | Klee et al. | Oct 2008 | A1 |
20100001184 | Chen et al. | Jan 2010 | A1 |
Number | Date | Country | |
---|---|---|---|
20140339415 A1 | Nov 2014 | US |
Number | Date | Country | |
---|---|---|---|
61589098 | Jan 2012 | US |