US20080049545A1 - Acoustic acceleration of fluid mixing in porous materials - Google Patents
Acoustic acceleration of fluid mixing in porous materials Download PDFInfo
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- US20080049545A1 US20080049545A1 US11/507,691 US50769106A US2008049545A1 US 20080049545 A1 US20080049545 A1 US 20080049545A1 US 50769106 A US50769106 A US 50769106A US 2008049545 A1 US2008049545 A1 US 2008049545A1
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- 238000002156 mixing Methods 0.000 title claims abstract description 33
- 239000012530 fluid Substances 0.000 title claims abstract description 29
- 239000011148 porous material Substances 0.000 title claims abstract description 18
- 230000001133 acceleration Effects 0.000 title description 3
- 238000000034 method Methods 0.000 claims abstract description 9
- 230000006835 compression Effects 0.000 claims description 13
- 238000007906 compression Methods 0.000 claims description 13
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- 238000010168 coupling process Methods 0.000 claims description 9
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- 230000000694 effects Effects 0.000 claims description 4
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- 230000010363 phase shift Effects 0.000 claims description 2
- 239000002356 single layer Substances 0.000 claims description 2
- 230000001360 synchronised effect Effects 0.000 claims description 2
- 239000000376 reactant Substances 0.000 description 10
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 9
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- 238000009792 diffusion process Methods 0.000 description 6
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- 239000000446 fuel Substances 0.000 description 5
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- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
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Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F31/00—Mixers with shaking, oscillating, or vibrating mechanisms
- B01F31/80—Mixing by means of high-frequency vibrations above one kHz, e.g. ultrasonic vibrations
- B01F31/86—Mixing by means of high-frequency vibrations above one kHz, e.g. ultrasonic vibrations with vibration of the receptacle or part of it
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J4/00—Feed or outlet devices; Feed or outlet control devices
- B01J4/04—Feed or outlet devices; Feed or outlet control devices using osmotic pressure using membranes, porous plates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/45—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads
- B01F25/452—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads characterised by elements provided with orifices or interstitial spaces
- B01F25/4524—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads characterised by elements provided with orifices or interstitial spaces the components being pressed through foam-like inserts or through a bed of loose bodies, e.g. balls
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J19/10—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing sonic or ultrasonic vibrations
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
- B01F2101/59—Mixing reaction ingredients for fuel cells
Definitions
- the invention relates generally to the field of combining fluids. More specifically, the invention relates to apparatus and methods for uniformly mixing fluid phases entrained in a porous medium.
- a conventional means of mixing two or more miscible liquids is mechanical manipulation to stir and exploit fluidic forces to produce localized regions corresponding to relatively high fluid flow rates.
- the flow rates operate to produce localized turbulent forces within the fluid field.
- the turbulence provides a contact surface between the liquids such that diffusion of the fluid components into each other produces a homogeneous mixture.
- Mixing also includes homogeneous compositions of immiscible fluids such as oil and air, typically used in oil jet pumps for gear lubrication. Oil and air are not miscible in a chemical sense, but may be combined in a mechanical sense. The term frequently used for mixing immiscible substances is homogenization.
- Ultrasonic mixers use piezoelectric transducers to generate vibrations.
- High power output may be required to maintain the desired amplitude and intensity under conditions of increased load such as high viscosity or immiscibility.
- One aspect of the invention provides a porous material mixer.
- Mixers according to this aspect of the invention comprise a vessel for holding at least one porous medium, at least one actuator acoustically coupled with at least one wall of the vessel for generating a wave, and at least one inlet in the vessel for admitting at least two fluids for combining, wherein the wave effects mixing of the at least two fluids.
- Another aspect of the invention is a method for mixing at least two fluids in a porous material.
- Methods according to this aspect begin with introducing the fluids into a mixing vessel, the mixing vessel comprising at least one inlet, at least one linear motor coupled to at least one actuator wherein the actuator is acoustically coupled to a wall of the vessel, exciting the at least one linear motor with a control signal of predetermined frequency, and forming a compression/expansion wave determined by the actuator acoustic coupling and the predetermined frequency wherein fluid motion within the vessel is effected.
- FIG. 1 is a perspective view of an exemplary ultrasonic porous media mixer with a top cover removed.
- FIG. 2 is a plan view of the ultrasonic mixer of FIG. 1 in a first position.
- FIG. 3 is a plan view of the ultrasonic mixer of FIG. 1 in a second position.
- FIG. 4 is a plot showing an initial distribution of two immiscible fluids in the porous media.
- FIG. 5 is a plot showing the direction of liquid A inside the porous media without any acoustic wave applied.
- FIG. 6 is a plot showing the concentration of FIG. 5 and direction of liquid A using the mixer according to the invention.
- FIG. 7 is an exemplary alternative embodiment.
- the invention is an apparatus and method for uniformly mixing together at least two fluids, or reagents, in viscous or gaseous phases, either miscible or immiscible, in a porous medium.
- the invention may be used for any application that requires uniformly mixing fluids.
- the mixer 101 comprises at least one porous medium 103 , such as a porous ceramic used for oxidizing toxic waste, a fluidized bed with catalyst or palladium-coated metal membranes for generating hydrogen, a silica-alumina membrane for dehydrating isopropyl alcohol or synthesizing dimethyl carbonate from carbon dioxide and methanol, a symmetrical hydrophobic nylon 66 membrane for adsorbing enzymes, and other media, contained in a rigid vessel 105 .
- a porous medium 103 such as a porous ceramic used for oxidizing toxic waste, a fluidized bed with catalyst or palladium-coated metal membranes for generating hydrogen, a silica-alumina membrane for dehydrating isopropyl alcohol or synthesizing dimethyl carbonate from carbon dioxide and methanol, a symmetrical hydrophobic nylon 66 membrane for adsorbing enzymes, and other media, contained in a rigid vessel 105 .
- the vessel may be made from materials that transmit acoustic waves and are compatible with the fluids to be mixed, such as but not limited to stainless steel, ceramics, plastics and others.
- the exemplary embodiment is shown as a cubic volume, however, other vessel shapes and configurations may be used according to the mixer application and teachings of the invention.
- the preferred embodiment has two inlets 107 , 109 for admitting reagents A and B to mix together as they interact with the porous media 103 .
- Two outlets 108 , 110 are provided and may be positioned perpendicular to the inlets 107 , 109 .
- the inlets 107 , 109 and outlets 108 , 110 are located on opposing sides of the vessel 105 .
- the inlets 107 , 109 and outlets 108 , 110 may be located on adjacent sides, or on the same side of the vessel 105 , or in any other suitable arrangement.
- actuators 111 , 113 that translate a linear motion from at least one linear motor, such as a piezoelectric transducer 115 , 117 into a controlled compression/expansion wave to effect mixing in the porous media 103 .
- the piezoelectric transducer(s) 115 , 117 may be, for example, interdigitated electroded actuators, oriented multilayer-multifilament stacked piezoelectric composites, piezoelectric wafer actuators, or others.
- the transducers 115 , 117 produce a deformation, or linear excursion in a range of from about 1 to 20% of the porous layer width, which may be in a range from about 0.1 microns to 1.0 cm dependent on the technological task when excited by a variable magnitude control signal.
- the vessel internal volume may contain one mono-layer, a sandwich of more than one type of porous media, or may be completely filled with more than one type of porous media.
- the transducer may vibrate from audible to ultrasonic frequencies.
- the frequency range may be in a range of from about 10 kHz to 100 MHz.
- the piezoelectric transducers 115 , 117 may be electrically coupled to a variable frequency oscillator for excitation (not shown).
- Deformation of a piezoelectric transducer plate generally corresponds to a motion along the axis normal to the plate.
- interdigitated electroded actuators which are typically rectangular, the excursion is in the longitudinal direction.
- the embodiment shown in FIG. 1 uses interdigitated electroded actuators.
- the porous medium 103 is flexible in three dimensions, at least two sidewalls 119 , 121 of the vessel 105 exhibit an acoustical impedance that allow for a controlled waveform to be impressed into the porous medium 103 .
- the transducers 115 , 117 are coupled to a stationary support and to the actuators 111 , 113 .
- a transducer 115 , 117 excursion is transferred to a respective actuator 111 , 113 which may be hinged allowing for reciprocal movement.
- FIG. 2 Shown in FIG. 2 is a view of the mixer 101 with two transducers 115 , 117 where a compression wave 203 is applied to one half of the porous media and a reciprocal expansion wave 201 to the other half of the porous media.
- FIG. 3 shows the alternating nature of the applied force when the transducers 115 , 117 are at a positive excursion.
- Each actuator 111 , 113 alternately imparts a compression 203 /expansion 201 wave.
- Each transducer 115 , 117 excitation is in unison with each other.
- the actuators 111 , 113 transfer the linear excursion from the transducers 115 , 117 into a compression 203 /expansion 201 wave indirectly to the porous media 103 via the sidewalls 119 , 121 .
- Each actuator employs at least two acoustic coupling points 205 , 207 , 209 , 211 separated by a predefined distance corresponding to the actuator 111 , 113 .
- the points 205 , 207 , 209 , 211 provide and act as the point source of acoustical energy from the transducers 115 , 117 to the porous media 103 .
- FIG. 4 Shown in FIG. 4 is a plot of initial reactant location within the mixer 101 .
- the initial concentrations of reactants A and B are located at their respective inlet 107 , 109 sides of the mixer.
- the plot shows gradual diffusion at the vessel 105 midpoint with no vibration. They slowly diffuse inwards toward the middle of the porous media.
- the reactant A slowly diffuses into the volume occupied by the reactant B and vise versa such that the concentrations of A and B reach equilibrium values about 1 ⁇ 2 way uniformly across the vessel.
- the dimensions of the mixer are as required to achieve the desired productivity.
- the plot of FIG. 5 shows gradual diffusion at the vessel 105 midpoint with no vibration.
- the fluids slowly diffuse inwards toward the middle of the porous media.
- the reactant A slowly diffuses into the volume occupied by the reactant B and vise versa such that the concentrations of A and B reach equilibrium values about 1 ⁇ 2 way uniformly across the vessel 105 .
- the dimensions of the mixer are as required to achieve the desired productivity.
- FIG. 6 Shown in FIG. 6 is a plot showing the same reactant concentrations as in FIG. 5 , with the compression/expansion wave applied by the invention 101 frozen in time.
- the transducers 115 , 117 are excited using a frequency of 10 MHz.
- the plot shows enhanced mixing of the reactants when the compression/expansion wave is applied, with no additional mechanical manipulation.
- the parameters of the porous medium 103 shown in FIGS. 5 and 6 are those of Torrey paper.
- Torrey paper is a porous material used in fuel cell applications.
- Porosity is a non-dimensional quantity being the ratio of free space to the total volume of the material.
- the concentration change toward equilibration in the porous media 103 is calculated as 1.8*10 ⁇ 7 per one period of vibration. The value indicates that during the time equal to one vibration period, the concentration in non-dimensional units (the ratio of the volume occupied by A or B to the total volume) has changed by 1.8*10 ⁇ 7 .
- the value 0.00000018 is small, however, the period,
- V 1 /t
- V is the frequency and t is the period, of a 10 MHz vibration is very short and substantial changes in concentration may be reached in the short time for frequencies of 10 MHz and higher.
- FIG. 6 shows the concentration change toward equilibrium in the porous media 103 when using the mixer 101 as 0.4*10 ⁇ 5 per one period of vibration.
- mixing acceleration is approximately 22 times greater for a chosen porous media using a 10 MHz excitation having an amplitude equal to 0.1 of the sample width.
- the concentration change towards equilibrium is approximately 22 times faster than without the vibration (ratio of 0.4*10 ⁇ 5 to 1.8*10 ⁇ 7 ).
- the acoustic perturbation of the porous material 103 using the compression/expansion wave of the invention accelerates the mixing of the reactants to more than 20 times that of natural diffusion.
- Multiphase flow in the porous medium 103 when subjected to the compression/expansion wave show dramatic enhancement of mixing compared to natural diffusion of the two reacting fluids inside the porous sample.
- FIG. 1 The exemplary embodiment shown in FIG. 1 is one instance of the general approach to accelerating and controlling the mixing of at least two reactants inside at least one porous medium.
- FIG. 7 Shown in FIG. 7 is an alternate embodiment of the invention 701 .
- the alternative embodiment employs 4 pairs of transducer/actuators 705 , 707 , 709 , 711 , 713 , 715 , 717 , 719 .
- the wave imparted by the transducer/actuators 705 , 707 , 709 , 711 , 713 , 715 , 717 , 719 exert force on two opposing surfaces of at least one porous medium 721 containing, at an initial stage, separate liquids A through I introduced through a micro-channel plenum (not shown).
- the motion of the invention is synchronized such that each transducer excursion is in unison.
- Transducer/actuators 705 , 709 , 713 , 717 and 707 , 711 , 715 , 719 may be a lower and an upper part of the same transducer assembly, respectively.
- transducers that exert force synchronously may be designed as one entity, as N/2, rather than requiring N separate transducers (one transducer for each actuator), such that one source of ultrasonic energy is divided and channeled to the required point sources of application by which synchronization is achieved.
- Modifications to the acoustic perturbation wave shape applied to the porous medium and to the frequency may be used to optimize the rate of mixing in any porous medium structure geometry.
- hybridization of the transducer syncing may further optimize mixing efficiency, where each pair of transducer/actuators 705 / 707 , 709 / 711 , 713 / 715 , 717 / 719 may not be in complete synchronicity, or phase, with other pairs, but with each operating at a predetermined phase shift from other pairs.
- various embodiments of the invention may be employed, for example, to mix methanol and water in a reformed hydrogen fuel cell and/or a direct methanol fuel cell. Additionally, various embodiments of the invention have demonstrated the capability to mix a variety of fluids including, for example, gases, liquids, gas-liquid mixtures, etc. Other representative applications may include the mixing of fuels supplying a micro-reactor and/or micro-combustion chamber.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Dispersion Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Mixers With Rotating Receptacles And Mixers With Vibration Mechanisms (AREA)
Abstract
Apparatus and methods are disclosed for uniformly mixing fluid phases entrained in a porous material.
Description
- The invention relates generally to the field of combining fluids. More specifically, the invention relates to apparatus and methods for uniformly mixing fluid phases entrained in a porous medium.
- The mixing of fluids is frequently needed to perform chemical reactions. Most chemical reactions require a controlled and homogeneous mixing of reagents.
- A conventional means of mixing two or more miscible liquids is mechanical manipulation to stir and exploit fluidic forces to produce localized regions corresponding to relatively high fluid flow rates. The flow rates operate to produce localized turbulent forces within the fluid field. The turbulence provides a contact surface between the liquids such that diffusion of the fluid components into each other produces a homogeneous mixture.
- Mixing also includes homogeneous compositions of immiscible fluids such as oil and air, typically used in oil jet pumps for gear lubrication. Oil and air are not miscible in a chemical sense, but may be combined in a mechanical sense. The term frequently used for mixing immiscible substances is homogenization.
- Ultrasonic mixers use piezoelectric transducers to generate vibrations. High power output may be required to maintain the desired amplitude and intensity under conditions of increased load such as high viscosity or immiscibility.
- When a porous medium, such as a polymer membrane, is used to contain reagents, equilibrium diffusion is problematic. While ultrasonic mixers have been employed to provide bulk mixing of liquid and gas, they have not been successfully employed for porous materials. Typically, the only known approach for mixing intensification inside porous bodies has been mechanical manipulation which might not be feasible or desirable in every case.
- What is desired is a controlled acceleration of mixing in porous media. This would result in smaller physical component packaging for synthesizing units housing porous media such as those used for chemical reactors, fuel cells, and the like.
- Although there are various types of mechanical manipulation mixing apparatus, such mixers are not completely satisfactory for porous media. The inventor has discovered that it would be desirable to have apparatus and methods for uniformly mixing fluid phases entrained in porous media.
- One aspect of the invention provides a porous material mixer. Mixers according to this aspect of the invention comprise a vessel for holding at least one porous medium, at least one actuator acoustically coupled with at least one wall of the vessel for generating a wave, and at least one inlet in the vessel for admitting at least two fluids for combining, wherein the wave effects mixing of the at least two fluids.
- Another aspect of the invention is a method for mixing at least two fluids in a porous material. Methods according to this aspect begin with introducing the fluids into a mixing vessel, the mixing vessel comprising at least one inlet, at least one linear motor coupled to at least one actuator wherein the actuator is acoustically coupled to a wall of the vessel, exciting the at least one linear motor with a control signal of predetermined frequency, and forming a compression/expansion wave determined by the actuator acoustic coupling and the predetermined frequency wherein fluid motion within the vessel is effected.
- The details of one or more embodiments of the invention are set forth in the accompanying drawings and the description below. Other features, objects, and advantages of the invention will be apparent from the description and drawings, and from the claims.
-
FIG. 1 is a perspective view of an exemplary ultrasonic porous media mixer with a top cover removed. -
FIG. 2 is a plan view of the ultrasonic mixer ofFIG. 1 in a first position. -
FIG. 3 is a plan view of the ultrasonic mixer ofFIG. 1 in a second position. -
FIG. 4 is a plot showing an initial distribution of two immiscible fluids in the porous media. -
FIG. 5 is a plot showing the direction of liquid A inside the porous media without any acoustic wave applied. -
FIG. 6 is a plot showing the concentration ofFIG. 5 and direction of liquid A using the mixer according to the invention. -
FIG. 7 is an exemplary alternative embodiment. - Embodiments of the invention will be described with reference to the accompanying drawing figures wherein like numbers represent like elements throughout. Further, it is to be understood that the phraseology and terminology used herein is for the purpose of description and should not be regarded as limiting. The use of “including,” “comprising,” or “having” and variations thereof herein is meant to encompass the items listed thereafter and equivalents thereof as well as additional items. The terms “mounted,” “connected,” and “coupled” are used broadly and encompass both direct and indirect mounting, connecting, and coupling. Further, “connected” and “coupled” are not restricted to physical or mechanical connections or couplings.
- The invention is an apparatus and method for uniformly mixing together at least two fluids, or reagents, in viscous or gaseous phases, either miscible or immiscible, in a porous medium. The invention may be used for any application that requires uniformly mixing fluids.
- Shown in
FIG. 1 is amixer 101 for combining reagents introduced into aporous media 103. Themixer 101 comprises at least oneporous medium 103, such as a porous ceramic used for oxidizing toxic waste, a fluidized bed with catalyst or palladium-coated metal membranes for generating hydrogen, a silica-alumina membrane for dehydrating isopropyl alcohol or synthesizing dimethyl carbonate from carbon dioxide and methanol, a symmetrical hydrophobic nylon 66 membrane for adsorbing enzymes, and other media, contained in arigid vessel 105. The vessel may be made from materials that transmit acoustic waves and are compatible with the fluids to be mixed, such as but not limited to stainless steel, ceramics, plastics and others. The exemplary embodiment is shown as a cubic volume, however, other vessel shapes and configurations may be used according to the mixer application and teachings of the invention. - The preferred embodiment has two
107, 109 for admitting reagents A and B to mix together as they interact with theinlets porous media 103. Two 108, 110 are provided and may be positioned perpendicular to theoutlets 107, 109. In the exemplary embodiment, theinlets 107, 109 andinlets 108, 110 are located on opposing sides of theoutlets vessel 105. However, the 107, 109 andinlets 108, 110 may be located on adjacent sides, or on the same side of theoutlets vessel 105, or in any other suitable arrangement. - Located on opposite sides of the vessel are
actuators 111, 113 that translate a linear motion from at least one linear motor, such as a 115, 117 into a controlled compression/expansion wave to effect mixing in thepiezoelectric transducer porous media 103. The piezoelectric transducer(s) 115, 117 may be, for example, interdigitated electroded actuators, oriented multilayer-multifilament stacked piezoelectric composites, piezoelectric wafer actuators, or others. In embodiments, the 115, 117 produce a deformation, or linear excursion in a range of from about 1 to 20% of the porous layer width, which may be in a range from about 0.1 microns to 1.0 cm dependent on the technological task when excited by a variable magnitude control signal. The vessel internal volume may contain one mono-layer, a sandwich of more than one type of porous media, or may be completely filled with more than one type of porous media. When a control signal of fixed or variable frequency is impressed, the transducer may vibrate from audible to ultrasonic frequencies. The frequency range may be in a range of from about 10 kHz to 100 MHz. Thetransducers 115, 117 may be electrically coupled to a variable frequency oscillator for excitation (not shown).piezoelectric transducers - Deformation of a piezoelectric transducer plate generally corresponds to a motion along the axis normal to the plate. For interdigitated electroded actuators, which are typically rectangular, the excursion is in the longitudinal direction. The embodiment shown in
FIG. 1 uses interdigitated electroded actuators. - Since the
porous medium 103 is flexible in three dimensions, at least two 119, 121 of thesidewalls vessel 105 exhibit an acoustical impedance that allow for a controlled waveform to be impressed into theporous medium 103. In the preferred embodiment, the 115, 117 are coupled to a stationary support and to thetransducers actuators 111, 113. A 115, 117 excursion is transferred to atransducer respective actuator 111, 113 which may be hinged allowing for reciprocal movement. - Shown in
FIG. 2 is a view of themixer 101 with two 115, 117 where atransducers compression wave 203 is applied to one half of the porous media and areciprocal expansion wave 201 to the other half of the porous media.FIG. 3 shows the alternating nature of the applied force when the 115, 117 are at a positive excursion. Eachtransducers actuator 111, 113 alternately imparts acompression 203/expansion 201 wave. Each 115, 117 excitation is in unison with each other.transducer - The
actuators 111, 113 transfer the linear excursion from the 115, 117 into atransducers compression 203/expansion 201 wave indirectly to theporous media 103 via the 119, 121. Each actuator employs at least two acoustic coupling points 205, 207, 209, 211 separated by a predefined distance corresponding to thesidewalls actuator 111, 113. The 205, 207, 209, 211 provide and act as the point source of acoustical energy from thepoints 115, 117 to thetransducers porous media 103. - Shown in
FIG. 4 is a plot of initial reactant location within themixer 101. The initial concentrations of reactants A and B are located at their 107, 109 sides of the mixer. The plot shows gradual diffusion at therespective inlet vessel 105 midpoint with no vibration. They slowly diffuse inwards toward the middle of the porous media. The reactant A slowly diffuses into the volume occupied by the reactant B and vise versa such that the concentrations of A and B reach equilibrium values about ½ way uniformly across the vessel. The dimensions of the mixer are as required to achieve the desired productivity. - The plot of
FIG. 5 shows gradual diffusion at thevessel 105 midpoint with no vibration. The fluids slowly diffuse inwards toward the middle of the porous media. The reactant A slowly diffuses into the volume occupied by the reactant B and vise versa such that the concentrations of A and B reach equilibrium values about ½ way uniformly across thevessel 105. The dimensions of the mixer are as required to achieve the desired productivity. - Shown in
FIG. 6 is a plot showing the same reactant concentrations as inFIG. 5 , with the compression/expansion wave applied by theinvention 101 frozen in time. The 115, 117 are excited using a frequency of 10 MHz. The plot shows enhanced mixing of the reactants when the compression/expansion wave is applied, with no additional mechanical manipulation.transducers - The parameters of the
porous medium 103 shown inFIGS. 5 and 6 are those of Torrey paper. Torrey paper is a porous material used in fuel cell applications. Porosity is a non-dimensional quantity being the ratio of free space to the total volume of the material. The concentration change toward equilibration in theporous media 103 is calculated as 1.8*10−7 per one period of vibration. The value indicates that during the time equal to one vibration period, the concentration in non-dimensional units (the ratio of the volume occupied by A or B to the total volume) has changed by 1.8*10−7. The value 0.00000018 is small, however, the period, -
V=1/t, (1) - where V is the frequency and t is the period, of a 10 MHz vibration is very short and substantial changes in concentration may be reached in the short time for frequencies of 10 MHz and higher.
-
FIG. 6 shows the concentration change toward equilibrium in theporous media 103 when using themixer 101 as 0.4*10−5 per one period of vibration. With this invention, mixing acceleration is approximately 22 times greater for a chosen porous media using a 10 MHz excitation having an amplitude equal to 0.1 of the sample width. In other words, by applying a 10 MHz vibration with an amplitude equal to 1/10 of the vessel thickness, the concentration change towards equilibrium is approximately 22 times faster than without the vibration (ratio of 0.4*10−5 to 1.8*10−7). - The acoustic perturbation of the
porous material 103 using the compression/expansion wave of the invention accelerates the mixing of the reactants to more than 20 times that of natural diffusion. Multiphase flow in theporous medium 103 when subjected to the compression/expansion wave show dramatic enhancement of mixing compared to natural diffusion of the two reacting fluids inside the porous sample. - The exemplary embodiment shown in
FIG. 1 is one instance of the general approach to accelerating and controlling the mixing of at least two reactants inside at least one porous medium. Shown inFIG. 7 is an alternate embodiment of theinvention 701. The alternative embodiment employs 4 pairs of transducer/ 705, 707, 709, 711, 713, 715, 717, 719.actuators - The wave imparted by the transducer/
705, 707, 709, 711, 713, 715, 717, 719 exert force on two opposing surfaces of at least oneactuators porous medium 721 containing, at an initial stage, separate liquids A through I introduced through a micro-channel plenum (not shown). The motion of the invention is synchronized such that each transducer excursion is in unison. Transducer/ 705, 709, 713, 717 and 707, 711, 715, 719 may be a lower and an upper part of the same transducer assembly, respectively. This means that the transducers that exert force synchronously may be designed as one entity, as N/2, rather than requiring N separate transducers (one transducer for each actuator), such that one source of ultrasonic energy is divided and channeled to the required point sources of application by which synchronization is achieved.actuators - Modifications to the acoustic perturbation wave shape applied to the porous medium and to the frequency may be used to optimize the rate of mixing in any porous medium structure geometry. Moreover, hybridization of the transducer syncing may further optimize mixing efficiency, where each pair of transducer/
actuators 705/707, 709/711, 713/715, 717/719 may not be in complete synchronicity, or phase, with other pairs, but with each operating at a predetermined phase shift from other pairs. - In other representative and exemplary applications, various embodiments of the invention may be employed, for example, to mix methanol and water in a reformed hydrogen fuel cell and/or a direct methanol fuel cell. Additionally, various embodiments of the invention have demonstrated the capability to mix a variety of fluids including, for example, gases, liquids, gas-liquid mixtures, etc. Other representative applications may include the mixing of fuels supplying a micro-reactor and/or micro-combustion chamber.
- One or more embodiments of the present invention have been described. Nevertheless, it will be understood that various modifications may be made without departing from the spirit and scope of the invention. Accordingly, other embodiments are within the scope of the following claims.
Claims (30)
1. A porous material mixer comprising:
a vessel for holding at least one porous material;
at least one actuator acoustically coupled with at least one wall of said vessel for generating a wave; and
at least one inlet in said vessel for admitting at least two fluids for combining, wherein said wave effects mixing of said at least two fluids.
2. The mixer according to claim 1 further comprising a linear motor coupled to said actuator wherein, when excited by a control signal, said motor exhibits an excursion.
3. The mixer according to claim 2 wherein said excursion applies a force against said actuator.
4. The mixer according to claim 3 wherein said excursion and said actuator acoustic coupling shapes said wave.
5. The mixer according to claim 4 wherein said actuator acoustic coupling is provided by at least two points separated by a predefined distance.
6. The mixer according to claim 5 wherein said force is coupled through said vessel wall into said at least one porous material.
7. The mixer according to claim 6 wherein said actuator alternately applies force to each said point.
8. The mixer according to claim 7 wherein said linear motor is a piezoelectric transducer.
9. The mixer according to claim 8 wherein said excitation control signal alternates at a frequency in a range of from about 1 to 20 MHz.
10. The mixer according to claim 9 wherein a difference between alternate force applications corresponds to about 180 degrees.
11. The mixer according to claim 10 wherein said wave within said at least one porous material is a compression/expansion wave that corresponds with said alternate force applications.
12. The mixer according to claim 11 wherein said at least one porous material is one mono-layer.
13. The mixer according to claim 11 wherein said at least one porous material is a sandwich of more than one type of porous material.
14. A method for mixing at least two fluids in a porous material comprising:
introducing the fluids into a mixing vessel, said mixing vessel comprising:
at least one inlet;
at least one linear motor coupled to at least one actuator wherein said actuator is acoustically coupled to a wall of said vessel;
exciting said at least one linear motor with a control signal of predetermined frequency; and
forming a compression/expansion wave determined by said actuator acoustic coupling and said predetermined frequency wherein fluid motion within said vessel is effected.
15. The method according to claim 14 wherein said predetermined frequency is in a range of from about 1 to 20 MHz.
16. The method according to claim 15 wherein said linear motor is a piezoelectric transducer.
17. A porous material mixer comprising:
a vessel for holding at least one porous material;
a plurality of actuator pairs, wherein each actuator pair comprises two member actuators and each actuator pair member is acoustically coupled with an opposing side of said vessel for generating a wave; and
at least one inlet in said vessel for admitting at least two fluids for combining, wherein said wave effects mixing of said at least two fluids.
18. The mixer according to claim 17 wherein each pair of actuators further comprises a linear motor wherein, when excited by a control signal, said motor exhibits an excursion.
19. The mixer according to claim 18 wherein said excursion applies a force against each actuator pair member.
20. The mixer according to claim 19 wherein said excursion and said actuator pair member acoustic coupling shapes said wave.
21. The mixer according to claim 20 wherein each actuator acoustic coupling is provided by at least two points separated by a predefined distance.
22. The mixer according to claim 21 wherein said force is coupled through said vessel wall into said at least one porous material.
23. The mixer according to claim 22 wherein each said actuator alternately applies force to each said point.
24. The mixer according to claim 23 wherein said linear motor is a piezoelectric transducer.
25. The mixer according to claim 24 wherein said control signal alternates at a frequency in a range of from about 1 to 20 MHz.
26. The mixer according to claim 25 wherein a difference between alternate force applications corresponds to about 180 degrees and generates a compression/expansion wave that corresponds with said alternate force applications.
27. The mixer according to claim 26 wherein said alternating force application of each actuator pair member is synchronized with its other pair member such that said compression/expansion wave generated by an actuator pair is reinforced.
28. The mixer according to claim 27 wherein each pair of said plurality of actuator pairs is in synchronism with each other and shares a common control signal.
29. The mixer according to claim 27 wherein each pair of said plurality of actuator pairs is not in synchronism with each other and does not share a common control signal.
30. The mixer according to claim 29 wherein each control signal for each actuator pair has a predetermined phase shift.
Priority Applications (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US11/507,691 US20080049545A1 (en) | 2006-08-22 | 2006-08-22 | Acoustic acceleration of fluid mixing in porous materials |
| EP07253229A EP1892031A1 (en) | 2006-08-22 | 2007-08-16 | Acoustic acceleration of fluid mixing in porous materials |
| JP2007212539A JP2008049337A (en) | 2006-08-22 | 2007-08-17 | Mixer and method of mixing at least two fluids in porous material |
| US12/607,486 US8408782B2 (en) | 2006-08-22 | 2009-10-28 | Acoustic acceleration of fluid mixing in porous materials |
| US13/832,151 US8789999B2 (en) | 2006-08-22 | 2013-03-15 | Acoustic acceleration of fluid mixing in porous materials |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US11/507,691 US20080049545A1 (en) | 2006-08-22 | 2006-08-22 | Acoustic acceleration of fluid mixing in porous materials |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US12/607,486 Division US8408782B2 (en) | 2006-08-22 | 2009-10-28 | Acoustic acceleration of fluid mixing in porous materials |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US20080049545A1 true US20080049545A1 (en) | 2008-02-28 |
Family
ID=38650077
Family Applications (3)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US11/507,691 Abandoned US20080049545A1 (en) | 2006-08-22 | 2006-08-22 | Acoustic acceleration of fluid mixing in porous materials |
| US12/607,486 Expired - Fee Related US8408782B2 (en) | 2006-08-22 | 2009-10-28 | Acoustic acceleration of fluid mixing in porous materials |
| US13/832,151 Expired - Fee Related US8789999B2 (en) | 2006-08-22 | 2013-03-15 | Acoustic acceleration of fluid mixing in porous materials |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US12/607,486 Expired - Fee Related US8408782B2 (en) | 2006-08-22 | 2009-10-28 | Acoustic acceleration of fluid mixing in porous materials |
| US13/832,151 Expired - Fee Related US8789999B2 (en) | 2006-08-22 | 2013-03-15 | Acoustic acceleration of fluid mixing in porous materials |
Country Status (3)
| Country | Link |
|---|---|
| US (3) | US20080049545A1 (en) |
| EP (1) | EP1892031A1 (en) |
| JP (1) | JP2008049337A (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20100046319A1 (en) * | 2006-08-22 | 2010-02-25 | United Technologies Corporation | Acoustic Acceleration of Fluid Mixing in Porous Materials |
| WO2011091342A1 (en) | 2010-01-25 | 2011-07-28 | Corning Incorporated | Microreactors with microfluidic device and system level application of ultrasound; implementation of chemical reactions within them |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20100046319A1 (en) * | 2006-08-22 | 2010-02-25 | United Technologies Corporation | Acoustic Acceleration of Fluid Mixing in Porous Materials |
| US8408782B2 (en) * | 2006-08-22 | 2013-04-02 | United Technologies Corporation | Acoustic acceleration of fluid mixing in porous materials |
| US8789999B2 (en) | 2006-08-22 | 2014-07-29 | United Technologies Corporation | Acoustic acceleration of fluid mixing in porous materials |
| WO2011091342A1 (en) | 2010-01-25 | 2011-07-28 | Corning Incorporated | Microreactors with microfluidic device and system level application of ultrasound; implementation of chemical reactions within them |
Also Published As
| Publication number | Publication date |
|---|---|
| EP1892031A1 (en) | 2008-02-27 |
| US20130201781A1 (en) | 2013-08-08 |
| US8408782B2 (en) | 2013-04-02 |
| JP2008049337A (en) | 2008-03-06 |
| US20100046319A1 (en) | 2010-02-25 |
| US8789999B2 (en) | 2014-07-29 |
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