COPYRIGHT NOTICE
[0001] A portion of the disclosure of this patent document contains material that is subject
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by anyone of the patent document or the patent disclosure, as it appears in the Patent
and Trademark Office patent files or records, but otherwise reserves all copyright
rights whatsoever.
TECHNICAL FIELD
[0002] This description relates to systems and methods that employ high voltage, high power
nanosecond pulses in treating emission, for example emissions from cooking, or from
combustion engines (
e.g., diesel, natural gas, gasoline engines).
BACKGROUND
[0003] Smoke emissions from chain-driven (
i.e., conveyor-belt) charbroilers has been regulated by the air quality management district
(SC-AQMD) in southern California since 1997 (see RULE 1138). This "smoke" consists
of oil particles (particulate matter) typically around 150nm in diameter. This problem
has been "solved" using high temperature catalysts that cost $1500-$2000, are stable
for more than 10 years, and are nearly maintenance-free. These catalyst-based systems
make use of the high temperatures within a few inches of the cooking surface. However,
these relatively large chain-driven charbroilers are only found in large fast food
restaurants and comprise a relatively small fraction of total restaurant smoke emissions.
[0004] Open-underfire broilers (the kind most people are familiar with) are found in thousands
of restaurants in the southern California area alone. These emissions are currently
not regulated but account for 85% of all restaurant emissions in the South Coast region
of California. Typical mass flow rates for these charbroilers are around 10 lbs/day
or volumetric flow rates of 1600 ft
3/min and higher. This corresponds to approximately 5 grams of particulate matter (PM)
per hamburger. The same high temperature catalysts used for the chain-driven broilers
are not applicable here, because the exhaust is cold by the time it reaches the hood
approximately 1m away.
SUMMARY
[0005] The present disclosure is directed toward a system and method to remove and/or reduce
smoke, particulate, odor, and/or grease from emissions streams, for example emission
streams resulting from commercial or even residential cooking, for instance commercial
charbroiling processes, or for example from internal combustion engines (
e.g., diesel, natural gas, gasoline engines). This is achieved by means of treating the
emissions stream as it flows through an exhaust system and into a Transient Plasma
Emission Remediation (TPER) Reactor, where it is treated with a non-equilibrated transient
plasma that is generated by high voltage electrical pulses, each with a duration of
nanoseconds, and to which a bias voltage is applied (
e.g., negative DC bias voltage, positive DC bias voltage, sinusoidal or AC bias voltage)
preferably has a least a negative voltage component.
[0006] In particular, a method and system for treating emissions streams, for example emissions
from cooking appliances (e.g., charbroilers, broilers, grills, stove, ovens and other
kitchen or restaurant equipment), includes an exhaust pathway (
e.g., vent, duct), a TPER reactor positioned to treat an exhaust stream vented via the
exhaust pathway, a nanosecond high voltage pulse generator coupled to drive the transient
pulsed plasma reactor, and a voltage source (
e.g., DC voltage source, sinusoidal voltage source) to supplement the TPER reactor with
a bias voltage. The system substantially reduces one or more of smoke, particulate
matter, odor and/or grease in the emission stream, produced, for example, in cooking,
for instance in commercial charbroiling processes (
e.g., cooking / grilling of hamburger meat), or produced in operation of, for example,
internal combustion engines (
e.g., diesel, natural gas, gasoline engines). Both a reduction in the size distribution
and total particulate mass is advantageously achieved using the methods and systems
described herein. Reduction in or treatment of smoke, odor and/or grease may also
result.
[0007] A voltage source (
e.g., DC voltage source, sinusoidal voltage source) may be connected to apply a bias voltage
(
e.g., negative DC bias voltage, positive DC bias voltage, sinusoidal or AC bias voltage)
via a center conductor of a TPER reactor. In this configuration, the high voltage
nanosecond pulses are coupled onto the center conductor of the TPER reactor and are
superimposed on top of the bias voltage, which preferably has a least a negative component
(
e.g., sinusoidal, or negative DC bias voltage). This may be done either to produce a
static electric field that lowers the electric field. The bias voltage may also be
used to produce a static electric field that behaves like an electrostatic precipitator
(ESP) and serves to precipitate particulate matter out of the gas flow.
[0008] The foregoing summary does not encompass the claimed subject matter in its entirety,
nor are the embodiments intended to be limiting. Rather, the embodiments are provided
as mere examples.
BRIEF DESCRIPTION OF THE DRAWINGS
[0009] In the drawings, identical reference numbers identify similar elements or acts. The
sizes and relative positions of elements in the drawings are not necessarily drawn
to scale. For example, the shapes of various elements and angles are not drawn to
scale, and some of these elements are arbitrarily enlarged and positioned to improve
drawing legibility. Further, the particular shapes of the elements as drawn, are not
intended to convey any information regarding the actual shape of the particular elements,
and have been solely selected for ease of recognition in the drawings.
Figure 1 is a schematic diagram showing a system to treat emissions, for example cooking
emissions, according to at least one illustrated implementation, the system including
a kitchen ventilation system including a charbroiler, hood, duct, and blower, and
the system also including a Transient Plasma Emission Remediation (TPER) reactor installed
in a flow path of the kitchen ventilation system, and a nanosecond pulse generator
coupled to drive the TPER reactor.
Figure 2 is a circuit diagram showing a circuit suitable for inclusion in the a nanosecond
pulse generator of Figure 1, according to at least one illustrated implementation,
the illustrated circuit operable to generate the high voltage, nanosecond duration
electrical pulses to generate plasma in the TPER reactor.
Figure 3 is a schematic diagram showing a system to treat emissions, for example cooking
emissions, according to at least another illustrated implementation, the system including
a kitchen ventilation system including a charbroiler, hood, duct, and blower, and
the system also including a Transient Plasma Emission Remediation (TPER) reactor installed
in a flow path of the kitchen ventilation system, and a DC bias voltage in addition
to a nanosecond pulse generator coupled to drive the TPER reactor.
Figure 4 is a circuit diagram showing both a voltage supply that supplies a bias voltage
(e.g., negative DC bias voltage, positive DC bias voltage, sinusoidal or AC bias voltage)
and the high voltage nanosecond supply coupled to drive the TPER reactor of Figure
3.
Figure 5 is a schematic diagram of an experimental setup used to test a TPER reactor
and nanosecond pulse generator.
Figure 6A is a graph that shows plots of a set of particle number densities versus
particle size measured (using an SMPS) with and without the plasma treatment for a
flow conditions of 2.5m/s.
Figure 6B is a graph that shows plots of a set of particle number densities versus
particle size measured (using an SMPS) with and without the plasma treatment for a
flow conditions of 0.25m/s.
Figure 7A is a graph that shows plots of a relative particle mass measured versus
particle size with and without the plasma treatment for a flow condition of 2.5m/s.
Figure 7B is a graph that shows plots of a relative particle mass versus particle
size measured with and without the plasma treatment for a flow condition of 0.25m/s.
Figure 8 is a graph that shows an integrated particle numbers (i.e., total particle number) plotted as a function of pulse repetition rate.
Figure 9A is a graph that shows a set of plots of a set of particle number densities
for various sized particles measured for various respective pulser input voltages.
Figure 9B is a graph that shows a plot of integrated peak areas (i.e., total particle mass) plotted as a function of pulser input voltage.
Figure 10A is an isometric view of a plasma-based reactor for treating restaurant
particulate emissions remediation, according to at least one illustrated implementation.
Figure 10B is a photograph of a plasma discharge at the output port of the reactor
system of Figure 10A.
Figure 11 is a graph showing plots of a particle size distributions produced using
POA-4 oil in an aerosol particle generator, with spectra captured 30 minutes apart
using a scanning mobility particle sizer (SMPS).
Figure 12A is a graph showing a plot of a particle size distribution obtained with
PAO-4 under an applied DC voltage of 5kV, both with and without a 30kV nanosecond
pulsed plasma (pulse repetition rate of 200Hz and electrically continuous power of
30W).
Figure 12B is a graph showing a plot of a particle size distribution obtained with
PAO-4 under an applied DC voltage 10kV, both with and without a 30kV nanosecond pulsed
plasma (pulse repetition rate of 200Hz and electrically continuous power of 30W).
Figure 13A is a graph showing a particle size distribution obtained with soybean oil
under an applied DC voltage of 2.5kV, both with and without the nanosecond pulsed
plasma running at a peak voltage of 30kV, pulse repetition rate of 200Hz, and continuous
power of 30W.
Figure 13B is a graph showing a particle size distribution obtained with soybean oil
under an applied DC voltage of 5kV, both with and without the nanosecond pulsed plasma
running at a peak voltage of 30kV, pulse repetition rate of 200Hz, and continuous
power of 30W.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0010] In the following description, certain specific details are set forth in order to
provide a thorough understanding of various disclosed embodiments. However, one skilled
in the relevant art will recognize that embodiments may be practiced without one or
more of these specific details, or with other methods, components, materials, etc.
In other instances, certain structures associated with food preparation devices such
as ovens, skillets, and other similar devices, closed-loop controllers used to control
cooking conditions, food preparation techniques, wired and wireless communications
protocols, geolocation, and optimized route mapping algorithms have not been shown
or described in detail to avoid unnecessarily obscuring descriptions of the embodiments.
In other instances, certain structures associated with conveyors and/or robots are
have not been shown or described in detail to avoid unnecessarily obscuring descriptions
of the embodiments.
[0011] Unless the context requires otherwise, throughout the specification and claims which
follow, the word "comprise" and variations thereof, such as, "comprises" and "comprising"
are to be construed in an open, inclusive sense, that is as "including, but not limited
to."
[0012] Reference throughout this specification to "one embodiment" or "an embodiment" means
that a particular feature, structure or characteristic described in connection with
the embodiment is included in at least one embodiment. Thus, the appearances of the
phrases "in one embodiment" or "in an embodiment" in various places throughout this
specification are not necessarily all referring to the same embodiment. Furthermore,
the particular features, structures, or characteristics may be combined in any suitable
manner in one or more embodiments.
[0013] As used in this specification and the appended claims, the singular forms "a," "an,"
and "the" include plural referents unless the content clearly dictates otherwise.
It should also be noted that the term "or" is generally employed in its sense including
"and/or" unless the content clearly dictates otherwise.
[0014] The headings and Abstract of the Disclosure provided herein are for convenience only
and do not interpret the scope or meaning of the embodiments.
[0015] Figure 1 shows a system 100 to treat emissions, for example cooking smoke emissions,
using a transient pulsed plasma, according to one illustrated implementation.
[0016] The system 100 includes a Transient Plasma Emission Remediation (TPER) reactor 102
and a nanosecond pulse generator 104 coupled to drive that TPER reactor 102. The TPER
reactor 102 is designed to connect to an exhaust system 106, for example in series
with one or more ducts 108a, 108b, 108c (three shown, collectively 108) that are part
of the exhaust system 106 that vents the emissions (
e.g., smoke, particulate, odor, grease) 109 generated, for example, by a cooking appliance
110 (
e.g., charbroiler) out of a building and into the atmosphere. The exhaust system 106
may include one or more hoods 112 positioned relatively above the cooking appliance
110 to capture the cooking emissions (
e.g., smoke, particulate, odor, grease) 109 produced by a combustion processor, for instance
the cooking process. The hood 112 can take a variety of forms. The hood 112 will typically
comprise a stainless steel sheet metal enclosure with a relative large hood input
vent at one end, and a relatively smaller hood output vent at another end. The exhaust
system 106 may include one or more blowers (
e.g., fans) 114 positioned to draw and, or push the cooking emissions (
e.g., smoke, particulate, odor, grease) 109 through the duct(s) 108 from the hood 112 to
an exhaust outlet vent 116. The hood 112 and the ducts 108 define a fluid flow path
(represented by arrows) 113 to constrain and guide passage of the capture the emissions
(
e.g., smoke, particulate, odor, grease) 109. While illustrated in the context of a kitchen
and cooking, the apparatus, methods and techniques described herein may be employed
to treat other streams of emissions generated in other contexts. For example, the
apparatus, methods and techniques described herein may be employed to treat other
streams of emissions generated from operation of internal combustion engines (
e.g., diesel, natural gas, gasoline engines).
[0017] In one embodiment, the TPER reactor 102 is comprised of a stainless steel cylindrical
reactor anode 102a with a coaxial electrode 102b. This coaxial TPER reactor 102 comprises
a thin wire, between 0.001 inch and 1 inch in diameter that is centered inside of
an electrically conductive tube with an inner diameter between 1 inch and 24 inches,
where the inner diameter is determined by the maximum voltage of the nanosecond pulse
generator 104 that is driving the plasma generating reactor 102. An impedance of TPER
reactor 102 is matched with a source cable 126 in order to reduce voltage reflections.
The TPER reactor 102 provides a corona discharge in a coaxial cell geometry.
[0018] Figure 1 also shows the resulting transient plasma (
i.e., high electron energy, low-temperature plasma) 118, as well as the shape of a typical
high voltage pulse 120 produced by the nanosecond pulse generator and supplied to
the TPER reactor 102. The plasma 118 is generated inside the TPER reactor 102 by driving
a high voltage, nanosecond duration electrical pulse 120 onto the center conductor
102a or conductors of the TPER reactor(s) 102. In some implementations, the nanosecond
duration electrical pulse 120 may have a duration of approximately equal to or less
than 100 ns and may have a magnitude of approximately equal to or greater than >1
kV. For instance, suitable values for the nanosecond duration electrical pulse 120
may be a duration in a range of 0.1 ns to 100 ns, inclusive, and a magnitude in a
range of 1 kV to 100 kV, inclusive.
[0019] In another implementation, a 4-electrode geometry is utilized for the plasma generating
reactor 102, where the diameter of the wire generating the plasma and the outer tube
are sized similarly to the ones described for the single wire geometry.
[0020] The system 100 may take the form of a retro-fit system, for example sized and dimensioned
or shaped to be installed as part of a previously installed exhaust system, for example
an exhaust system that draws emissions (smoke, particulate, odor, grease) from a vicinity
of a cooking appliance and venting such into the atmosphere, typically with one or
more filters. The retro-fit system may allow for the removal of one or more filters,
for example including a replacement section or piece of duct to replace a section
in which filters are mounted, or to provide a bypass fluid path around pre-existing
filters or pre-existing filter section. In some implementations, one or more TPER
reactors 102 could be installed on a roof of a building, for example connected in
series with existing exhaust ducts.
[0021] Figure 2 shows a circuit 200 that is operable to generate a high voltage pulse to
drive a TPER reactor 102, for example the TPER reactor 102 illustrated in Figure 1.
A series of inductively coupled switching stages 202a, 202b, 202c, 202d (only four
shown, collectively 202) discharge capacitors C1, C2, C3, C4 in series to achieve
voltage multiplication. Operating switches M1, M2, M3, M4 causes energy to flow from
these capacitors C1, C2, C3, C4 to energize a drift step recovery diode D9, which
rapidly interrupts energy stored by a charge circuit inductor L5 to produce a high
power, high voltage electrical pulse, which is transmitted to the anode or anodes
of the TPER reactor 102.
[0022] Figure 3 shows a system 300 to treat emissions, for example cooking emissions (
e.g., smoke, particulate, odor, grease) using a transient pulsed plasma, according to
another illustrated implementation. The system 300 is similar to the system 100 (Figure
1), and similar or even identical structures are identified in Figure 3 with the same
reference numbers as employed in Figure 1. In the interest of conciseness, only significant
differences are discussed below.
[0023] In the system 300, a DC voltage source 302 may also be connected to the TPER reactor
102, in addition to the high voltage nanosecond pulse generator (
e.g., power supply) 104. In this implementation, the nanosecond duration pulses 120 are
coupled onto the anode or anodes of the TPER reactor 102, which is biased to a set
DC voltage via the DC voltage source 302. The voltage of the nanosecond duration pulses
120 adds to the DC voltage.
[0024] Figure 4 shows a portion of a system 400 to treat emissions, for example cooking
emissions (
e.g., smoke, particulate, odor, grease) using a transient pulsed plasma, according to
one illustrated implementation. In this implementation, the nanosecond pulses 120
(Figs. 1 and 3) are capacitively coupled onto the anode or anodes 102a (Figs. 1 and
3) of the TPER reactor 102 through a DC coupling capacitor C
1. A low pass filter (illustrated enclosed in broken-line box) 402 is used to isolate
the DC supply (
e.g., DC voltage source 302) from the high voltage, nanosecond duration pulse generator
104.
[0025] In particular, the system shows one implementation of how a DC voltage source 302
and a high voltage, nanosecond duration pulse generator (
e.g., power supply) 104 may be connected to a TPER reactor 102. Both the DC voltage source
302 and the high voltage, nanosecond duration pulse generator 104 are electrically
coupled to the anode or anodes of the TPER reactor 102. The DC voltage source 302
is electrically isolated from the high voltage, nanosecond pulse generator 104 by
a low pass filter, comprised of inductor Li, resistor R
2, and capacitor C
2. The high voltage, nanosecond pulse generator 104 is electrically isolated from the
DC voltage source 302 by a coupling capacitor C
1. A resistor R
1 provides a DC path to allow the DC voltage source 302 to fully charge the coupling
capacitor C
1. The values of coupling capacitor C
1, inductor L
1, and capacitor C
2 are determined by the desired or defined pulse parameters of the high voltage, nanosecond
pulse generator 104. Capacitor C
1 and capacitor C
2 are chosen to provide low impedance to the nanosecond duration pulse; whereas, inductor
L
1 is chosen to appear as a high impedance. The value of resistor R
1 is chosen to be sufficiently large so as to avoid excessive heating when the high
voltage nanosecond pulse generator 104 is running at maximum or rated power. Resistor
R
2 is chosen to sufficiently damp the resonance of inductor Li, coupling capacitor C
1, and capacitor C
2. Applicants have determined that while a positive DC bias voltage produces favorable
results for treating at least one of smoke, particulate, odor, and/or grease, a negative
DC bias voltage produces particularly surprisingly even more favorable results. Applicants
also note that a sinusoidal or AC bias voltage may produce favorable results for at
least one of smoke, particulate, odor, and/or grease. In some implementations, DC
voltage source may supply a negative or a positive bias voltage. In some implementations,
a sinusoidal or AC may supply a sinusoidal or AC bias voltage which may be applied,
or one portion (
e.g., negative voltage portion, positive voltage portion) may be applied to the conductor.
[0026] A proof-of-principle experiment of this method and system has been performed in which
a TPER reactor based system was tested in a test kitchen facility. Two TREP reactors
were installed in parallel to a kitchen ventilation system including a charbroiler,
hood, duct, and blower. Only a fraction of the full flow was passed through the TPER
reactors.
[0027] Figure 5 shows a system 500 used to perform the experiment referred to immediately
above. The system 500 is similar to the system 100 (Figure 1), and similar or even
identical structures are identified in Figure 5 with the same reference numbers as
employed in Figure 1. In the interest of conciseness, only significant differences
are discussed below.
[0028] In contrast to the system 100 (Figure 1), the system 500 includes a main duct 502
and a tap duct 504. The tap duct 504 is used to tap or exhaust a slip stream of the
smoke exhaust 506 from the main duct 502 and treated the slip stream of the smoke
exhaust 506 by a pair of TPER reactors 508. The TPER reactors 508 comprise two 3"
diameter TPER reactors, each 3 feet in length, and arranged in parallel with one another.
Each TPER reactor 508 was powered by a nanosecond pulse generator 104, in particular
a TPS Model 20X nanosecond pulse generator. The system 500 includes a spectrometer
510. The treated smoke exhaust 512 returns to the main duct 502 after being subjected
to the non-equilibrated transient plasma.
[0029] In particular, particle distributions were collected using a Scanning Mobility Particle
Sizer (SMPS) spectrometer (TSI Model 3776) over the range from 14-650nm. Hamburgers
(75% lean, 25% fat) were cooked for 4.5 minutes per side continuously for 3 hours
during this study, as shown in Figure 3. 15 patties were cooked at a time on a grill
that was 25×30" in area. A total of 375 patties were cooked during this study. The
cooking emissions (
e.g., smoke) 109 collected by the hood 112 was then treated with the TPER reactors.
[0030] Figure 6A is a graph 600a that shows the particle number densities measured with
and without the plasma treatment via the experimental system 500 (Figure 5) described
above at a reactor flow condition of 2.5m/s. Figure 6B is a graph 600b that shows
the particle number densities measured with and without the plasma treatment via the
experimental system 500 (Figure 5) described above for a reactor flow condition of
0.25m/s. The integrated peak areas are indicated in Figures 6A and 6B. For these datasets,
the original untreated particle distributions are peaked around 125-150nm diameter.
With plasma treatment, a significant drop in the particle number was observed along
with the emergence of a narrow distribution centered around 30-40nm. The integrated
area of the dominant peak shows a factor of 1.7X reduction in PM number density (
i.e., 4.62/2.71=1.7X) at high flow rates (2.5m/s) and a 10-fold reduction in PM at low
flow rates (0.25m/s).
[0031] Since smaller diameter nanoparticles have substantially lower mass than larger diameter
nanoparticles, it may be more appropriate to plot the particle mass instead of number
density. Figures 7A and 7B are graphs 700a, 700b, respectively, that show the "Relative
Particle Mass" in arbitrary units obtained by multiplying the number densities in
Figures 3 and 4, respectively, by the diameter cubed. The integrated peak areas are
indicated in Figures 7A and 7B. Here, 2.4X and 55X-fold reductions in total PM mass
were observed for flow rates of 2.5 and 0.25 m/s, respectively.
[0032] The particle distributions were also measured as a function of the pulse repetition
rate. Figure 8 is a graph 800 that shows the integrated particle number plotted as
a function of pulse repetition rate, which decreases linearly with increasing repetition
rate. Here, the total particle number decreases linearly with increasing repetition
rate. These results demonstrate the scalability of this approach for treating higher
flow rates and larger systems at higher repetition rates.
[0033] Figure 9A is a graph 900a that shows the particle distributions as a function of
voltage dependence. Figure 9B is a graph 900b that shows a plot of integrated peak
areas (
i.e., total particle mass) plotted as a function of pulser input voltage for the particle
distributions of Figure 9A. Here, again, a monotonic decrease is observed in the integrated
area of the PM peak distribution (
i.e., total PM mass), with an overall reduction of 40X observed at a pulser input voltage
of 400 VDC. These input voltages correspond to pulse energies of approximately 10,
20, 40, and 50mJ. These results demonstrate the scalability of this approach for treating
higher flow rates and larger systems with higher pulse powers.
[0034] These measurements demonstrate the effectiveness of transient pulsed plasmas to provide
substantial remediation of particulate matter (PM) produced by commercial charbroiling
processes (
e.g., cooking of hamburger meat). The scalability of this approach for treating higher
flow rates and larger systems is also demonstrated as a function of both pulse repetition
rate and pulse energy.
[0035] This plasma-based approach provides a fundamentally different mechanism for breaking
down oil-based particulate matter that cannot be achieved with conventional UV and/or
ozone approaches, both of which are present in the plasma. Here, highly reactive chemical
radical species, including atomic oxygen, are largely responsible for the effective
breakdown of these oil aerosol particles.
[0036] One possible advantage of this plasma-based approach lies in the substantially improved
flow through the system, which reduces the power requirements associated with the
fan or blower. Typically, with filter-based approaches, 2-3 filters are configured
in series, resulting in a considerable pressure drop which, in turn, requires high
power blowers to be utilized in order to achieve the necessary flow rates for kitchen
ventilation compliance. Since there is essential no pressure drop across the plasma-based
reactor, significantly lower blower powers can be used to achieve the same flow rates,
enabling the overall system (including the nanosecond pulse generator) to consume
less power than current filter-based systems.
[0037] Other features of the disclosed embodiments will become apparent from the following
detailed description, taken in conjunction with the accompanying drawings, which illustrate,
by way of example, the principles of the disclosed embodiments.
[0038] Another proof-of-principle experiment of the method by which a DC bias is applied
together with the nanosecond pulse is shown in Figures 10A, 10B, 11, 12A, 12B, 13A
and 13B. Here, both polyaromatic olefin PAO-4 and soybean oil particulates created
by an oil aerosol generator are treated. As illustrated by the data, a more than three-order-of-magnitude
reduction in particulates (
i.e., 99.9% remediation) can be achieved with the treatment system described herein. In
these tests, the plasma discharge is produced in a 4" diameter cylindrical reactor
(illustrated in Figures 10A and 10B) with a 5-10 nanosecond high voltage (30 kV) pulse
generator together with applied DC bias voltages up to 20 kV. The distribution of
nanoparticle sizes is centered around 225 nm in diameter, as measured using a scanning
mobility particle sizer (SMPS) spectrometer and follows a log-normal distribution.
[0039] In this experiment, an oil aerosol generator from Aerosol Technologies International
(ATI, Inc.) was employed, which creates an oil aerosol by forcing compressed air through
a Laskin nozzle. The plasma-based flow reactor used comprises a 4 foot-long, 4 inch-diameter
stainless steel cylindrical anode with a 25mil single-wire cathode arranged in a coaxial
geometry, as illustrated in Figures 10A and 10B. This plasma-based flow system has
electrical feedthroughs on either end of the reactor, one for supplying high DC voltages
and the other for high voltage nanosecond pulses, as indicated in Figure 10A. AC and
DC filters have been built into these feedthroughs in order to protect the nanosecond
pulse generator from the high voltage DC bias and vice versa. The plasma is produced
using a TPS Model 30X pulse generator operating at a peak voltage of 30kV, a pulse
repetition rate of 200Hz, and a continuous power of 30W. Here, the generation of plasma
is assisted by 20kV DC power supply capable of supplying up to 30W of continuous power.
Baseline particle distributions (
i.e., histograms) were measured using a scanning mobility particle sizer (SMPS) without
a plasma or DC bias and exhibit highly stable distributions, as show in Figure 11.
[0040] Figure 12A shows particle size distributions taken under an applied DC voltage of
5kV both with and without the nanosecond pulse generator running at a peak voltage
of 30kV, pulse repetition rate of 200Hz, and continuous electrical power of 30W. A
comparison of these two distributions shows a more than 12-fold reduction of total
PM concentration (
i.e., 92% remediation). Here, the integrated areas are indicated in the plot corresponding
to the total particle concentrations both with and without the transient pulsed plasma.
Similarly, Figure 12B shows particle size distributions taken with an applied DC voltage
of 10kV both with and without a nanosecond pulse generator, exhibiting a more than
1500-fold reduction in PM concentration (
i.e., 99.9% remediation). It should be noted that the particle distributions taken with
5kVDC and lOkVDC only, without the nanosecond pulse generator, are nearly identical
to the untreated baseline data (i.e., no remediation) plotted in Figure 11.
[0041] A separate set of measurements was taken using soybean oil rather than PAO-4. The
soybean oil more closely resembles the oil-based nanoparticles that are generated
by the charbroiling of hamburger meat and is often used as a surrogate grease generator
following the UL 1046 standard method. However, it is also worth noting that these
soybean oil grease aerosol particles are generated at room temperature and do not
contain any carbonaceous particles, such as those produced in the combustion of natural
gas. Figure 13A shows particle size distributions taken with an applied DC voltage
of 2.5kV both with and without the nanosecond pulsed plasma. Figure 13B shows particle
size distributions taken with an applied DC voltage of 5kV both with and without the
nanosecond pulsed plasma. For a DC bias of 2.5kV, a 21-fold reduction in PM concentration
(
i.e., 96% remediation) was observed. For a DC bias of 5kVDC, a more than 1260-fold reduction
in PM concentration (
i.e., 99.9% remediation) was observed. Without being bound by theory, the improved remediation
obtained with a DC bias of 5kV compared to that of 2.5kVDC can be attributed to the
increased electric fields that are achieved when adding the 30kV peak pulse voltage.
At higher DC biases, the plasma density is higher and fills a more substantial volume
of the reactor. It should, again, be noted that the distributions observed with 2.5
and 5kVDC bias only (
i.e., without the nanosecond pulse generator) are nearly identical to the untreated data
(
i.e., no remediation).
[0042] Various embodiments of the devices and/or processes via the use of block diagrams,
schematics, and examples have been set forth herein. Insofar as such block diagrams,
schematics, and examples contain one or more functions and/or operations, it will
be understood by those skilled in the art that each function and/or operation within
such block diagrams, flowcharts, or examples can be implemented, individually and/or
collectively, by a wide range of hardware, software, firmware, or virtually any combination
thereof. In one implementation, the present subject matter may be implemented via
Application Specific Integrated Circuits (ASICs). However, those skilled in the art
will recognize that the embodiments disclosed herein, in whole or in part, can be
equivalently implemented in standard integrated circuits, as one or more computer
programs running on one or more computers (
e.g., as one or more programs running on one or more computer systems), as one or more
programs running on one or more controllers (
e.g., microcontrollers) as one or more programs running on one or more processors (
e.g., microprocessors), as firmware, or as virtually any combination thereof, and that
designing the circuitry and/or writing the code for the software and or firmware would
be well within the skill of one of ordinary skill in the art in light of this disclosure.
[0043] When logic is implemented as software and stored in memory, one skilled in the art
will appreciate that logic or information, can be stored on any nontransitory computer-readable
medium for use by or in connection with any computer and/or processor related system
or method. In the context of this document, a memory is a computer-readable medium
that is an electronic, magnetic, optical, or other another physical device or means
that contains or stores a computer and/or processor program. Logic and/or the information
can be embodied in any computer-readable medium for use by or in connection with an
instruction execution system, apparatus, or device, such as a computer-based system,
processor-containing system, or other system that can fetch the instructions from
the instruction execution system, apparatus, or device and execute the instructions
associated with logic and/or information. In the context of this specification, a
"computer-readable medium" can be any means that can store, communicate, propagate,
or transport the program associated with logic and/or information for use by or in
connection with the instruction execution system, apparatus, and/or device. The computer-readable
medium can be, for example, but not limited to, an electronic, magnetic, optical,
electromagnetic, infrared, or semiconductor system, apparatus, device, or propagation
medium. More specific examples (a non-exhaustive list) of the computer-readable medium
would include the following: an electrical connection having one or more wires, a
portable computer diskette (magnetic, compact flash card, secure digital, or the like),
a random access memory (RAM), a read-only memory (ROM), an erasable programmable read-only
memory (EPROM, EEPROM, or Flash memory), an optical fiber, and a portable compact
disc read-only memory (CDROM). Note that the computer-readable medium, could even
be paper or another suitable medium upon which the program associated with logic and/or
information is printed, as the program can be electronically captured, via for instance
optical scanning of the paper or other medium, then compiled, interpreted or otherwise
processed in a suitable manner if necessary, and then stored in memory.
[0044] In addition, those skilled in the art will appreciate that certain mechanisms of
taught herein are capable of being distributed as a program product in a variety of
forms, and that an illustrative embodiment applies equally regardless of the particular
type of nontransitory signal bearing media used to actually carry out the distribution.
Examples of nontransitory signal bearing media include, but are not limited to, the
following: recordable type media such as floppy disks, hard disk drives, CD ROMs,
digital tape, and computer memory.
[0046] From the foregoing it will be appreciated that, although specific embodiments have
been described herein for purposes of illustration, various modifications may be made
without deviating from the spirit and scope of the teachings. Accordingly, the claims
are not limited by the disclosed embodiments.
1. A method to treat exhaust streams, the method comprising:
capturing an exhaust stream;
driving a transient plasma emission remediation (TPER) reactor with a high voltage
pulse with a duration of nanoseconds to generate a non-equilibrated transient plasma
in a portion of the TPER reactor through which the captured exhaust stream passes;
applying a negative bias voltage or a sinusoidal bias voltage by a voltage source
to an energized conductor of the TPER reactor; and
passing the captured exhaust stream through the TPER reactor drive with the high voltage,
nanosecond duration pulse and the applied negative bias voltage or sinusoidal bias
voltage.
2. The method of claim 1 wherein the voltage source is a DC voltage source and applying
a negative bias voltage or a sinusoidal bias voltage by a voltage source to an energized
conductor of the TPER reactor includes applying a negative DC bias to an energized
conductor of the TPER reactor.
3. The method of claim 1 wherein the voltage source is a sinusoidal voltage source and
applying a negative bias voltage or a sinusoidal bias voltage by a voltage source
to an energized conductor of the TPER reactor includes applying a sinusoidal bias
to an energized conductor of the TPER reactor.
4. The method of any of claims 2 or 3 wherein applying a negative bias voltage or a sinusoidal
bias voltage by a voltage source to an energized conductor of the TPER reactor includes
applying a negative bias voltage or a sinusoidal bias voltage that produces a static
electric field that does not produce an electrical discharge.
5. The method of claim any of claims 2 or 3 wherein applying a negative bias voltage
or a sinusoidal bias voltage by a voltage source to an energized conductor of the
TPER reactor includes applying a negative bias voltage or a sinusoidal bias voltage
that lowers a field needed to be generated by the high voltage, nanosecond duration
pulse.
6. The method of any of claims 2 or 3 wherein applying a negative bias voltage or a sinusoidal
bias voltage by a voltage source to an energized conductor of the TPER reactor includes
applying a negative DC bias voltage that produces a static electric field that precipitates
particulate matter out of the gas flow.
7. The method of any of claims 1 through 3, further comprising:
coupling the high voltage, nanosecond duration pulse onto a negative bias voltage
or a sinusoidal bias voltage biased conductor of the TPER reactor through a coupling
capacitor, and isolating the voltage source from a source of the high voltage, nanosecond
duration pulse by a low pass filter.
8. The method of any of claims 1 through 3 wherein driving the TPER reactor with a high
voltage pulse with a duration of nanoseconds includes applying an electric field of
the high voltage, pulse with a nanosecond duration pulse on top of a static electric
field produced by the negative bias voltage or the sinusoidal bias voltage.
9. The method of any of claims 1 through 3 wherein driving the TPER reactor with a high
voltage pulse with a duration of nanoseconds includes applying a fast rising, high
voltage pulse with a duration of nanoseconds to at least one electrode of the TPER
reactor.
10. The method of any of claims 1 through 3 wherein capturing an exhaust stream includes
capturing the exhaust stream via a hood positioned over a cooking appliance.
11. The method of claim 10 wherein capturing the exhaust stream via a hood positioned
over a cooking appliance includes capturing at least two of: smoke, particulate, grease
and odor generated by charbroiling of meat by a charbroiler.
12. The method of any of claims 1 through 3 wherein capturing an exhaust stream includes
capturing the exhaust stream from an internal combustion engine.
13. A system to treat exhaust streams, the system comprising:
at least one a transient plasma emission remediation (TPER) reactor, the at least
one a TPER reactor including an electrically conductive tube that forms a first electrode
and at least a second electrode positioned in an interior of the electrically conductive
tube, the electrically conductive tube sized to be serially coupled in a flow path
formed by one or more ducts;
at least one nanosecond pulse generator coupled to drive the at least one TPER reactor;
and
a high voltage source electrically coupled to apply a negative bias voltage or a sinusoidal
bias voltage to at least one conductor of the at least one TPER reactor.
14. The system of claim 13 wherein the voltage source is a DC voltage source and applies
a negative DC bias to an energized conductor of the TPER reactor.
15. The system of any of claims 13 or 14, further comprising:
a coupling capacitor through which a high voltage, nanosecond duration pulse is coupled
onto the at least one conductor to which the negative DC bias voltage is applied;
and
a low pass filter that isolates the DC high voltage source from the at least one nanosecond
pulse generator that generates high voltage, nanosecond duration, and wherein:
the at least one nanosecond pulse generator coupled to drive the at least one TPER
reactor is operable to supply a fast rising, high voltage pulse with a duration of
nanoseconds to produce a non-equilibrated transient plasma inside at least a portion
of the at least one TPER reactor.