US20070243059A1

US20070243059A1 - Techniques for movement through gas or liquid or liquid without a velocity boundary layer

Info

Publication number: US20070243059A1
Application number: US11/231,536
Authority: US
Inventors: Scott Davis
Original assignee: Forced Physics LLC
Current assignee: Forced Physics LLC
Priority date: 2002-12-19
Filing date: 2005-09-20
Publication date: 2007-10-18
Also published as: AU2003303154A8; JP2006511758A; US20050002776A1; AU2003300960A8; US20050022974A1; US6932564B2; AU2003299640A8; AU2003300960A1; WO2004059147A3; EP1618299A2; WO2004059265A3; US7008176B2; WO2004059265A2; EP1581742A4; WO2004057260A3; US20050135919A1; EP1581742B1; AU2003303154A1; EP1618299A4; WO2004057260A2

Abstract

A technique of generating a flow from a gas. The technique includes the steps of selecting molecules from the gas on a nanoscopic or microscopic scale, and generating the flow from the selected molecules. The gas can be air. In one embodiment, the molecules are selected based on the direction of movement of the molecules. In another embodiment, the molecules are selected based on the velocities (i.e., direction and speed) of the molecules. Also, devices that implement the technique.

Description

CROSS REFERENCE TO RELATED APPLICATIONS

This application claims priority from application Ser. No. 10/737,535, “Molecular

Inventor Citizenship Residence City and State

Scott DAVIS United States Foothill Ranch, CA
Speed and Direction Selection,” filed Dec. 16, 2003, in the name of inventor Scott Davis; from “Provisional Application No. 60/434852, “Air Flow, Heat Exchange, and Molecular Selection Systems,” filed Dec. 19, 2002, in the name of inventors Scott Davis and Art Williams; from Provisional Application No. 60/499,066, “Molecular Speed Selection, Flow Generation, Adiabatic Cooling, and Other Heteroscopic Technologies,” filed Aug. 29, 2003, in the name of inventors Scott Davis and Art Williams; and U.S. patent application Ser. No. 10/693,635, “Heteroscopic Turbine,” filed Oct. 24, 2003, in the name of inventor Scott Davis. These applications are incorporated by reference as if fully set forth herein.

BACKGROUND OF THE INVENTION

1. Field of the Invention
This invention relates to selecting molecules from air or other gaseous or liquid matter based on the speed or direction of those molecules and generating bulk flows from the selected molecules.
2. Description of the Related Art
Molecules in air (and other gaseous matter) are in constant motion, continuously colliding with each other. This molecular motion is constantly occurring, even if the bulk velocity of the air is zero.
The speed of the molecules between collisions is the thermal velocity for the air. The average distance between collisions is the mean free path distance. The overall bulk velocity of the air is the air's transport velocity. Theoretically, the maximum transport velocity that can be imparted to an airflow is the thermal velocity of the underlying air molecules.
Several conventional apparatuses exist for generating a flow of air. Examples include fans and turbomolecular pumps.
Fans force air to flow in bulk with rotating fan blades. Even highly efficient fans cannot achieve very high transport velocities compared to the underlying molecular motion of the air. In particular, even good fans can only achieve transport velocities that are on the order of a hundredth to a thousandth of the thermal velocity of the air molecules.
Because high-velocity (i.e., comparable to thermal velocity) bulk air flow cannot be achieved with conventional fans, larger fans must be used to move significant amounts of air. As a result, fan size often becomes a limiting design factor for anything that requires airflow, cooling, or the like.
Another device for moving air (and other gaseous matter) is the turbomolecular pump. Turbomolecular pumps can be used as absorbers or consumers of air molecules. These pumps typically are used to draw molecules from a high vacuum environment in order to create an even “higher” vacuum.
Turbomolecular pumps use rotating turbine blades to select molecules from air. Molecules that randomly cross the tops of the blades are captured and whisked away.
In order for existing turbomolecular pumps to operate, collisions between air molecules must be avoided. If such collisions occur, the molecules can bounce away from the blades before they can be captured, defeating the operation of the pump.
Typical existing turbomolecular pumps use macroscopic turbine blades rotating at extremely high speeds, for example 75,000 RPM. These high speeds are used so that molecules that cross the path of the rotor blades do not have time to collide with other molecules before being whisked away.
Collisions are also prevented by ensuring that the mean free path distance for the molecules is not too small compared to the container or feed tube for the pump. The ratio between container or feed tube length and mean free path distance is the Knudsen number.
Typical existing turbomolecular pumps only operate effectively if the Knudsen number is no greater than approximately 10. This Knudsen number can only be achieved in a high vacuum, and then with only relatively small containers or feed tubes. Obviously, a significant air flow cannot be generated by pumping from a high vacuum through a small container or feed tube. As a consequence, existing turbomolecular pumps do not generate significant air flow.
All of these problems also exist when generating a flow from any other gas or gas mixture besides air.
Generation of flows from gasses is of interest because such flows are ubiquitous in modern technology. For example, heating and cooling applications generally utilize some type of bulk flow in their operation. Examples of these applications include cooling units for computers, radiators for cars, air conditioners, refrigerators, heaters, industrial cooling units for large machinery, and innumerable other devices.
Conventional techniques for exchanging heat with air involve forced convection. In forced convention, air is forced to flow over or through some heating or cooling element. For example, air can be blown over or through a heated or cooled substrate, duct or grille. The purpose of these arrangements can be to heat or cool either the air or the substrate, duct or grille.
In all of these arrangements, a boundary layer forms over the surface of the substrate, duct or grille. In particular, air molecules in contact with the surface tend to “stick” to the surface. These air molecules in turn impede the motion of adjacent air molecules in the air flow, which in turn impede other air molecules. Thus, a region of slow-moving air molecules forms over the surface. This region is known as a velocity boundary layer.
The velocity boundary layer limits the number of air molecules that come into contact with the surface. Actual heat transfer only occurs at this surface. As a result, once heat is transferred to or from the molecules in the boundary layer, further transfer of heat is largely blocked. More heat can only be transferred once the molecules in the boundary layer are dragged away from the surface by the viscosity of the air, which is an intrinsically inefficient process. Molecular collisions also can drive the molecules away from the surface, but this is an even more inefficient process. As a result, the velocity boundary layer is accompanied by a thermal boundary layer.
The thermal boundary layer greatly impedes the transfer of heat between the forced air and the substrate, duct or grille. In addition, the forcing elements (e.g., fans) for conventional heat transfer devices must be powerful enough to overcome the viscosity of the air. Otherwise, little heat transfer will occur. Because of these factors, heating and cooling units tend to be fairly large devices with large footprints. These large footprints are the limiting design factors in many modern devices.
One alternative technique that has been explored with little success is heating or cooling the blades of fans that force (i.e., blow) air. However, in this approach, a thermal boundary layer forms on a fan's blades. As a result, this approach is no more efficient than forcing air over or through a substrate, duct or grille. All of these problems also exist when transferring heat to or from any other gas or gas mixture besides air.

SUMMARY OF THE INVENTION

Accordingly, great benefit could be derived from devices and methods that more efficiently generate bulk flows from a gas, for example for heating and cooling applications.
The invention addresses this need with a device that exploits the physics of molecular movement on a microscopic or nanoscopic scale to select molecules based on their directions or directions and speeds. The selected molecules are then aggregated into one or more bulk flows useful on a macroscopic scale. The use of microscopic or nanoscopic principles to generate macroscopic effects is referred to as “heteroscopic” in this disclosure.
The heteroscopic nature of the device helps improve efficiency. The microscopic or smaller (e.g., nanoscopic) structures allow segregation of molecules in a gas based on the thermal speed of those molecules. The segregation can occur with little or no work done on the selected molecules. Thus, the process of segregation expends a relatively low amount of energy, especially compared to traditional heating and cooling techniques. Aggregation of selected molecules into bulk flows permits application of the invention to real-world macroscopic heating and cooling applications.
If the molecules are selected based on speed as well as direction, in other words based on velocity, then the generated flow can be significantly cooler or hotter than the gas from which the flow is generated. Thus, the invention provides a viable alternative to inefficient heating and cooling techniques such as forced convection.
Accordingly, one embodiment of the invention is a technique of generating a flow from a gas. The technique includes the steps of selecting molecules from the gas on a nanoscopic or microscopic scale, and generating the flow from the selected molecules. The gas can be air.
In one embodiment, the molecules are selected based on the direction of movement of the molecules. In another embodiment, the molecules are selected based on the velocities (i.e., direction and speed) of the molecules.
Preferably, the molecules are selected from the gas at higher than near-vacuum pressure, for example at atmospheric pressure.
The molecules can be selected by nanoscopic or microscopic blades moving at a velocity comparable to a mean thermal velocity of the molecules in the gas. In one embodiment, the blades are mounted on or in a rotating structure such as a circular airfoil. In another embodiment, the blades are mounted on or in a surface movable substantially linearly through the gas such as a radiator of a vehicle.
The blades can be protruding blades or alternatively can be formed from microscopic or nanoscopic holes in a substrate. Other types of blades and/or edges can be used.
The invention also encompasses devices that implement the foregoing methods.
This brief summary has been provided so that the nature of the invention may be understood quickly. A more complete understanding of the invention may be obtained by reference to the following description of the preferred embodiments thereof in connection with the attached drawings.

BRIEF DESCRIPTION OF THE DRAWINGS

FIGS. 1A and 1B show rotating surfaces that can be used to implement the invention.
FIG. 2 shows surfaces that move substantially linearly through a gas to implement the invention.
FIG. 3 shows a possible arrangement of blades for direction selection of molecules.
FIG. 4 shows forced convention in the arrangement show in FIG. 3.
FIG. 5 shows blades formed from holes in a surface of a rotor or other structure.
FIG. 6 shows another possible arrangement of blades for direction selection of molecules.
FIGS. 7 to 9 show possible ducting arrangements.
FIGS. 10A to 10C show a possible arrangement of blades for selecting molecules based on velocity (i.e., direction and speed). FIGS. 10A to 10C are referred to collectively as FIG. 10.
FIGS. 11A and 11B show some possible variations on the arrangement shown in FIG. 10. FIGS. 11A and 11B are referred to collectively as FIG. 11.
FIGS. 12 to 14 show more possible arrangements of blades that perform velocity sorting of molecules in a gas.
FIG. 15 shows a potential problem caused by hotter molecules moving laterally across blades in a device that performs velocity sorting.
FIGS. 16 to 18 show possible solutions to the problem shown in FIG. 15.
FIG. 19 shows a possible aggregation and ducting arrangement for use with rotor-based speed selection.
FIGS. 20 and 21 show possible modifications for blade arrangements that perform speed selection.
FIGS. 22A to 22D illustrate an embodiment that includes a rotor (disk) arranged between two stators. FIGS. 22A to 22D are referred to collectively as FIG. 22.
FIG. 23 shows a possible variation of the arrangement shown in FIG. 22.
FIGS. 24A to 24C show possible features for an output stator for a device that performs velocity sorting. FIGS. 24A to 24C are referred to collectively as FIG. 24.
FIG. 25 shows a possible aggregation and ducting arrangement for the rotor/stator embodiment.
FIGS. 26 to 28 show possible variations of the rotor/stator embodiment.

DESCRIPTION OF THE PREFERRED EMBODIMENT

Lexicography
Nanoscopic: Having lengths or dimensions less than or equal to a billionth of a meter.
Microscopic: Having lengths or dimensions less than or equal to one millimeter.
Macroscopic: Having lengths or dimensions greater than or equal to one millimeter, and numbers greater than about one hundred.
Heteroscopic: Characterized by use of microscopic or nanoscopic principles to generate macroscopic effects.
Transport speed: The mean speed of an flow of gaseous matter moving in bulk. Also called bulk speed.
Mean thermal velocity: The speed of molecules in gaseous matter.
Mean free path distance: The average distance that molecules in gaseous matter travel between collisions with other molecules in the gaseous matter.
Hotter molecules: In reference to a given gas, hotter molecules consist of an aggregation of molecules selected from the gas that have a mean thermal velocity faster than the mean thermal velocity of the gas. In reference to individual molecules, a so-called hotter molecule is expected, on average, to be faster and therefore hotter than a so-called cooler molecule, but exceptions can occur.
Cooler molecules: In reference to a given gas, cooler molecules consist of an aggregation of molecules selected from the gas that have a mean thermal velocity slower than the mean thermal velocity of the gas. In reference to individual molecules, a so-called cooler molecule is expected, on average, to be slower and therefore cooler than a so-called hotter molecule, but exceptions can occur.
Near vacuum conditions: Pressures less than or equal to 0.001 atmospheres.
Knudsen number: A ratio of pump container or feed tube size to mean free path distance. (Sometimes in scientific literature, the Knudsen number is expressed as the opposite ratio.)
Blade: Broadly, any edge that is moved through air. This term encompasses both flat blades and tops of holes in a moving surface.
Comparable: In this application, speeds and distances are comparable if they are within an order of magnitude of each other. For example, if air molecules have a mean thermal velocity of 500 meters per second, blades moving at 50 to 5,000 meters per second would be moving at speeds comparable to the mean thermal velocity of the air molecules. Throughout this disclosure, the term “on an order of” is synonymous to “comparable to.”
Heteroscopic Effects
The techniques of the invention simultaneously operate on two different scales. First, molecules are selected or segregated from a gas on a microscopic or nanoscopic scale. In particular, the structures that select the molecules have dimensions comparable with the mean free path distance of the molecules in the gas. In normal operating conditions, for example regular atmospheric pressure, these dimensions are somewhere between microscopic and nanoscopic. The invention is not limited to such operating conditions.
Second, macroscopic effects are used. For example, the segregated molecules converge or are directed to generate a bulk flow. The bulk flow can be created from the segregated molecules by the arrangement of the segregating structures, by use of macroscopic structures such as flow ducts, by some combination of these arrangements, or by some other structures or techniques.
The invention preferably operates with a Knudsen number less than ten and preferably between one half and two (i.e., near unity). Thus, blades or edges used to select molecules are preferably about a mean free path distance high and spaced apart by about the mean free path distance. The mean free path distance is for a gas at a pressure at which the device is intended to operate. According to the invention this gas and pressure can be, but is not limited to, air at normal atmospheric pressure.
In more efficient embodiments of the invention, the microscopic or nanoscopic structures do little or no actual work while segregating molecules based on their speeds. Instead, molecules on an input side moving within a particular range of speeds and directions can pass through the structures, while other molecules collide with the structures or are otherwise repelled.
On an output side, a bulk flow generated by the aggregation of the selected molecules serves to push other ambient molecules out of the way. In systems that do not generate such bulk flows, “infidel” molecules entering from the output side can force the systems to do significant extra work. In the invention, the momentum of molecules comprising the bulk flow pushes would-be infidels away from the output side, thereby helping to prevent those molecules from colliding with the structures and forcing them to do work.
In the preferred embodiment, this bulk flow is aggregated molecular flow at thermal speeds. This differs from conventional prior art systems, in which the bulk flow is caused by fan or turbine blades actually pushing and therefore working on the molecules. Thus, by pushing away infidels, the bulk flow of the invention reduces one of the only remaining sources of work for the blades to perform, greatly improving efficiency.
The combination of microscopic or nanoscopic selection with aggregation into a macroscopic bulk flow can lead to extremely high efficiency. This efficiency arises in part from a lack of a velocity boundary layer at an interface between a gas and the blades. This leads to lower viscous losses. The invention is not limited to embodiments that lack such a boundary layer, although the preferred embodiment does lack the boundary layer.
Until recently, the combination of a large number of microscopic and smaller segregating structures has been limited to fields that deal with electricity, light, or other energy. One example of such heteroscopic devices is a computer chip.
In sum, the heteroscopic nature of the invention enables high efficiency without creating significant barriers to production. Such efficiency should have important ramifications for applications such as generating bulk flows, including for example applications where fans and jets are used, and heating and cooling other devices and elements. The invention is not limited to these applications—other applications exist.
Macroscopic Mounting
FIGS. 1A and 1B show rotating structures (i.e., rotors) on or in which blades or edges can be mounted for direction or velocity selection of molecules from a gas. Such a rotor could be, but is not limited to, a heteroscopic turbine. In these figures, the rotors spin about an axis extending out of the figures.
In FIG. 1A, rotor 1 in a shape of a disk or annulus contains chips 2. The chips contain the microscopic or nanoscopic blades.
The rotor can include ports or ducts (not shown) below each chip 2 to permit airflow from the chips to pass through the rotor. Ports or ducts also can extend radially for speed selection embodiments (see below). Alternatively, the arrangements of the blades themselves could result in such bulk flows without a need for ducting.
The Knudsen number for the rotor in FIG. 1A preferably is less than ten, for example between one half and two. Each of the blades has a height comparable to the mean free path distance for the gas in which the device operates, and the blades spaced apart by a distance comparable to the mean free path distance. In operation, the rotor preferably rotates fast enough so that the blades move through the surrounding gas at a speed comparable to the mean thermal velocity of the gas.
For example, in air at normal atmospheric conditions, the mean free path distance is 6.91E−08 meters. In one embodiment, the gap between blades is 3.455E−08 meters, and the height of the blades is also 3.455E−08 meters. In this embodiment, if the annulus has a circumference of 4 meters, then in operation it would preferably rotate at 7,500 RPM. Somewhere on the order of 1.75E+13 such blades could easily by placed on the annulus shown in FIG. 1A, resulting in significant aggregate flow from the blades. The invention is not limited to these particular numeric values, which are only provided as an example of a preferred embodiment.
The arrangement in FIG. 1A permits the blades to be fabricated on the chips, for example using technology developed for computer chip manufacturing. Then, the chips can be attached to the rotor. One benefit of this arrangement is that a manufacturing defect in one chip only ruins that chip, not the entire rotor. This can greatly reduce manufacturing costs.
FIG. 1B shows another embodiment of a rotating structure (i.e., rotors) on or in which blades or edges can be mounted for direction or velocity selection of molecules from a gas. In this embodiment, the blades are attached directly in or on the rotor 3. The locations of blades are represented by the dashes around the periphery of the rotor or disk. The advantage of this arrangement is that far more blades might be attached or manufactured into the rotor.
In both FIGS. 1A and 1B, the blades preferably are arranged on the outer portion of the rotor or disk to take advantage of higher linear velocities that occur there as compared to nearer the axis of the rotor or disk. Other arrangements can be used, including ports or other input structures placed over the entire surface of the rotor or disk.
FIGS. 1A and 1B define conventions for “radial view” and “tangential view” used throughout this disclosure. Namely, a “radial view” is a view, possibly a cross-section, along a radius of the rotor or disk. A “tangential view” is a view, possibly a cross-section, parallel to a tangent to the rotor or disk.
FIG. 2 shows surfaces 4 that move substantially linearly through a gas, as represented by the arrow in the figure, to select or sort molecules based on direction or speed (velocity). The term “substantially linearly” is intended to represent movement on the scale of the structures themselves. For example, if the structures were part of or mounted on a radiator in a vehicle, the movement of the vehicle down a roadway would be “substantially linear,” despite turns or curves in the roadway.
The locations of blades mounted in or on these surfaces are represented by dashes on the surfaces. In an alternative embodiment, the blades could be mounted on chips that are in turn mounted on or in the surfaces.
The structures in FIG. 2 can include ports or ducts (not shown) below the blades to permit airflow from the chips to pass through. These ducts or ports can be used to aggregate selected molecules into bulk flows. Alternatively, the arrangements of the blades themselves could result in such bulk flows without a need for ducting.
The Knudsen number for the arrangement in FIG. 2 also preferably is less than ten, for example between one half and two. Each of the blades has a height comparable to the mean free path distance for the gas in which the device operates, and the blades spaced apart by a distance comparable to the mean free path distance. In operation, the surfaces preferably are moved through a gas at a speed comparable to the mean thermal velocity of the gas, although this need not be the case.
Direction Selection
FIG. 3 shows a possible arrangement of blades for direction selection of molecules. The number and arrangement of blades in FIG. 3, as well as throughout the rest of this application, are not to scale.
The blades in FIG. 3 could be mounted on the chips, rotors, or surfaces shown in FIGS. 1A, 1B and 2, or on some other devices that moves through a gas, either rotationally or translationally. If the blades are mounted on a rotor, then FIG. 3 is a radial view.
In FIG. 3, blades 5 are of approximately equal height. The blades are on an order of a mean free path distance high and are on an order of a mean free path distance apart. The Knudsen number for these blades preferably is near unity.
When the blades move through a gas at a speed comparable to the mean thermal velocity of the gas, molecules that move past the tops of the blades are captured. Molecules moving away from the tops are not captured. Thus, the tops of the blades form direction selection plane 6.
Molecules captured by blades 5 either pass through the blades untouched or are pushed by the blades to below the blades. The aggregation of these molecules generates bulk flow 7.
While the flow generated by each blade is small, the aggregation of all of the flows can be very significant. In fact, depending on the particular embodiment, the bulk flow can be much stronger than would be generated by a similar sized conventional fan or turbine. In theory, the flow can even be strong enough to provide jet propulsion for a vehicle from even a relatively small device.
The momentum of molecules comprising the bulk flow pushes would-be infidels away from the output side of the blades (i.e., bottoms in FIG. 3), thereby helping to prevent those molecules from colliding with the structures and forcing them to do (more) work.
FIG. 4 shows forced convention that can result from direction selection. As molecules are captured from the top side of blades 5, other molecules move via Brownian motion to take their place. Hotter molecules are faster and therefore more likely to take the place of captured molecules. As a result, more hotter molecules tend to be captured, resulting in flow 7 including a disproportionate number of hotter molecules (i.e., a hotter flow is generated). This process is called “forced convection” and may have many useful applications, for example cooling gas above the device or warming gas below the device.
FIG. 5 shows blades formed from holes in a surface of a rotor or other structure. These holes could be in the chips, rotors, or surfaces shown in FIGS. 1A, 1B and 2, or on some other structure that moves through a gas, either rotationally or translationally. If the holes are in a rotor, FIG. 5 is a radial view, and the rotor surface is moving from left to right.
The edges and sides of holes 9 in FIG. 5 form blades. In a preferred embodiment, the size of holes 9 is greater than a molecular size for the gas in which the device operates and less than a mean free path distance for that gas.
The holes in FIG. 5 can be bored using any of a great number of existing technologies, including but not limited to e-beam and photographic lithography, sputtering, laser drilling, mechanical drilling, ion beam drilling, chemical etching, and other technologies.
FIG. 6 shows another possible arrangement of blades for direction selection of molecules from a gas. Blades 11 in this embodiment are formed from angled planes projecting from the surface of the rotor or other structure. Molecules captured by blades 11 exit through openings 12 at angles formed between the planes and the surface.
FIGS. 7 to 9 show possible ducting arrangements for use with the blades and other structures shown herein. FIG. 7 has ducts 13 that collect captured molecules for radially exit from a rotator-based device on which the blades are mounted. FIG. 8 has ducts 14 that collect captured molecules for axial (downward) exit from such a device. Other ducting arrangements are possible, some of which are shown in other figures in this disclosure.
FIG. 9 shows a twisted of curved duct that can be used with some of the ducting arrangements. This duct forces molecules that pass through it to collide with the walls of the duct. The result can be to slow the molecules down, thereby cooling them. Molecules can even be slowed down by one or more collisions with the blades.
Speed Selection
In general, the term speed refers to a scalar quantity, while velocity refers to a vector that incorporates both speed and direction. However, in some instance in this application, the term “speed selection” is used interchangeably with “velocity selection,” with both terms meaning selection, sorting or segregation of molecules from a gas based on their velocities.
When molecules are selected from a gas based on their velocities, the aggregations of those molecules can result in flows with different temperatures. Thus, techniques and devices of the invention can be used to generate hotter or cooler flows from a gas. These embodiments can be extremely efficient.
In mathematical terms, let ΔW be an amount of work done on molecules in a gas, and let ΔV be a mean difference in speed between “hot” and “cold” molecules in hot and cold bulk flows generated by these embodiments. In the more efficient preferred embodiments, ΔW/ΔV can be less than 3.1. Before the invention, a device that achieved this relationship between work and molecular speed had not been realized. Of course, the invention is not limited to embodiments that exhibit this high efficiency.
FIGS. 10A to 10C show a possible arrangement of blades for selecting molecules based on velocity and therefore temperature. FIGS. 10A to 10C are referred to collectively as FIG. 10.
Briefly, the blades in FIG. 10 have at least two different heights. When the blades are moved through a gas, tops of the blades having a first height form a direction selection plane that filters molecules that cross the plane, and tops of blades having a second height form a speed selection plane that filters molecules based on thermal velocity.
In FIG. 10, blades 30 and 31 preferably are microscopic or even nanoscopic in size. Blades 30 and 31 preferably are mounted on a rotor or other structure and are angled in a direction of blade movement through a gas. Some of the blades are longer than others. In FIG. 10, blades 30 are longer than blades 31.
If the blades are mounted on a rotor or disk (e.g., turbine), that rotor or disk preferably rotates fast enough such that the blades are moved through the gas at a speed comparable to the mean thermal velocity of the gas. The spacing between blades preferably is comparable to the mean free path distance of the molecules in the gas. Thus, the arrangement of blades on a particular rotor preferably is matched to a range of molecular speeds and mean free path distances corresponding to a particular range of temperatures and pressures of a gas.
The angle of the blades preferably is chosen based on the mean speed of molecules in the gas, which in turn is dependent upon the temperature and pressure of the gas, and the speed at which the blades move through the gas. In some embodiments, the ambient temperature and pressure of the gas can be controlled to best match the angles of the blades.
The tops of the longer blades form a direction selection plane. Molecules of a gas that cross this plane will be whisked away by the blades. Likewise, the shorter blades form a speed selection plane. Only molecules traveling with a certain vertical speed (and therefore temperature) will be cross this plane in time to be captured by the shorter blades. Stated differently, only molecules moving fast enough to have a sufficiently short time of flight from the direction selection plane to the speed selection plane will be selected by the shorter blades.
FIG. 10 shows direction selection plane 32 and speed selection plane 33. Also shown in FIG. 10 are two molecules represented by small circles. The empty circle represents a hotter and therefore faster (at least in the vertical direction) molecule. The filled circle represents a cooler and therefore slower (at least in the vertical direction) molecule.
In FIG. 10A, neither of the molecules has crossed the direction selection plane. In FIG. 10B, the molecules have traveled sufficiently far downward that they have crossed direction selection plane 32. Of the two molecules, only the hotter molecule has enough downward speed to cross speed selection plane 33 before the closest smaller blade 31 passes by due to motion of the blades (i.e., spinning of the rotor holding the blades). Thus, slower (cooler) molecules and faster (hotter) molecules are segregated as shown in FIG. 10C.
In operation, some faster molecules will be moving in a direction that takes them to the same side of the shorter blade as slower molecules. Thus, the cooler molecules might be “contaminated” with at least some hotter molecules. However, only hotter molecules will have sufficient speed to pass the speed selection plane in time to be grouped on the hotter molecule side. Thus, the mean speed (temperature) of the hotter molecules will tend to be higher than that of the cooler molecules despite any contamination.
Once the molecules have been segregated, like molecules can be aggregated using macroscopic ducts to generate bulk flow. Alternatively, like molecules selected by many blades can simply exit in the same direction, for example below a rotor with the blades, thereby creating a bulk flow without the need for any ducts. In any case, further ducting can be used to aggregate or redirect any flow.
A very large number of blades preferably select molecules for each flow. In a preferred embodiment, on the order to 10ˆ12 or more blades can be used. For example, and without limitation, one preferred embodiment uses 1.75E+13 blades. The invention is not limited to this number of blades.
In terms of “slip,” the device in FIG. 10 can be modeled as a perfect or nearly perfect absorber of molecules that cross the direction selection plane. Therefore, no (or few) molecules stick to the blades, ensuring adequate slip between the blades and the gas molecules. Slip not a concern at the output (not shown) of the device due to the bulk nature of the output flow.
FIGS. 11A and 11B show some possible variations on the arrangement shown in FIG. 10. FIGS. 11A and 11B are referred to collectively as FIG. 11.
FIG. 11A shows capture duct 34 for cooler molecules, and capture duct 35 for hotter molecules. Capture duct 35 in turn feeds macroscopic duct 36 for aggregating and transporting the hotter molecules away. Transportation of the cooler molecules is not illustrated in FIG. 11A.
In some cases, only hotter or cooler bulk flows are desired. In this case, a reflection surface can be added to the device to block undesired molecules. Reflection surface 37 adjoining the trailing blade in FIG. 11B is such a surface. In the embodiment shown in FIG. 11B, no ducting is used to aggregate the selected molecules. Rather, the hotter molecules selected by many blades aggregate below the rotor or other element on which the blades are mounted. Of course, ducting can be used if so desired.
FIGS. 12 to 14 show more possible arrangements of blades that perform speed selection of molecules in a gas.
FIG. 12 shows blades formed from angles planes. Hotter molecules pass the direction selection plane formed by the tops of taller blades 40 and pass through the blades before being blocked off by shorter blades 41. Thus, hotter molecules can exit below the blades. Cooler molecules can be directed by a channel formed between each blade 40 and each blade 41 for exit radially from the blades.
FIG. 13 shows blades formed from angled planes with bases. The blades are stacked in layers. Blades 43 on a top layer preferentially capture cooler molecules. Blades 44 on a bottom layer preferentially capture hotter molecules. Ducting can be provided to transport the molecules away, for example for aggregation into bulk flows.
FIG. 14 shows blade 46 formed from an angled planes projecting from a surface, akin to the blade shown in FIG. 6. This blade has openings 47 for cooler molecules to pass at angles formed between the planes and the surface, and openings 48 for hotter molecules to pass through the surface.
Other blade arrangements can be used to perform speed selection of molecules in gas.
FIG. 15 shows a potential problem caused by hotter molecules moving laterally across blades during sorting. In FIG. 15, hotter molecule 50 that moves laterally across the blades passes into an area that is supposed to sort out cooler molecules. FIGS. 16 to 18 show possible solutions to this problem.
In FIG. 16, baffles 52 between rows of blades help prevent lateral motion of hotter molecules into cooler molecule areas.
In FIG. 17, three rows of blades that capture hotter molecules are surrounded by rows of blades that capture cooler molecules. Thus, any laterally moving molecules will tend to be captured by the blades for hotter molecules.
To combine the arrangements in FIGS. 16 and 17, baffles could be placed between sets of rows of blades such as those shown in FIG. 17. In other words, every five (or some other number) of rows of blades could be separated by baffles.
Yet another solution is to curve the blades concavely in a direction of their motion through a gas. This solution is illustrated in FIG. 18, which shows curved blades 53. The curved sides of the blades would tend to reflect laterally moving molecules, as illustrated by the angled arrow in the figure.
Other solutions and arrangements are possible without departing from the invention.
FIG. 19 shows a possible aggregation and ducting arrangement for use with rotor-based speed selection.
In FIG. 19, molecules are segregated by blades on rotor 54. Ducting or other structures redirect the molecules based on their speed (i.e., temperature). Output stator 55 includes preferably macroscopic ducting to aggregate and to transport faster (i.e., hotter) molecules below rotor 54. Output stator 55 also includes preferably macroscopic ducting to aggregate and to transport slower (i.e., cooler) molecules radially from rotor 54.
FIGS. 20 and 21 show possible modifications for blade arrangements that perform speed selection.
In the foregoing speed selection embodiments, molecules are segregated into two groups: hotter and cooler. However, molecules can be segregated into plural different groups based on their velocities. To this end, FIG. 20 shows plural blades 65 to 69 of different heights disposed between blades 70 that define a direction selection plane. When these blades move, for example by rotation of a rotor on which they are mounted, the blades will select plural different speeds of molecules. Only the fastest molecules will reach the leading shorter blade 65. The slowest will reach the trailing longer blades, possibly contaminated with faster molecules. When the molecules are aggregated, those caught by leading shorter blades will tend to be faster and therefore hotter than those caught by trailing longer blades.
Again, the angle of these blades preferably is chosen based on the mean speed of molecules in the gas, which in turn is dependent upon the temperature and pressure of the gas. In some embodiments, the ambient temperature and pressure of the gas can be controlled to best match the angles of the blades.
One problem that can arise when performing direction or speed selection is backflow from inside the device out of the input ports or past the turbine blades. One solution to this problem is to arrange the input ports and blades to reduce outflow. In FIG. 21, blades 72 are thickened at their bases to create funnel-shaped channels that help prevent outflow.

Rotor/Stator Based Speed Selection Embodiments

FIGS. 22A to 22D illustrate a two stator and one rotor device that can generate hotter flows, cooler flows, or both from a gas. FIGS. 22A to 22D are referred to collectively as FIG. 22.
FIG. 22 shows a device that generates a hotter flow, cooler flow, or both hotter and cooler flows from a gas. The device includes structures that segregate molecules in the gas on the basis of the speed of those molecules, and structures that aggregate at least some of the segregated molecules into a bulk flow. The device is heteroscopic in that at least some of the structures that segregate the molecules are microscopic or smaller, while the segregated molecules are aggregated into a macroscopic bulk flow.
In FIG. 22, the structures that segregate the molecules include input stator 81, rotor 82, and output stator 83. The stators preferably are disks that are positioned coaxially with the rotor.
In a preferred embodiment, rotor 82 flies over at least one of the stators due to Eckman airflow, similar to how a disk head flies over a disk in a computer disk drive. Alternatively, magnetic repulsion from one or both of the stators can be used to keep the rotor in place. Normal mechanical mounting and other techniques also can be used.
The input stator includes plural microscopic or smaller input ports, one of which is shown as port 84. The small size of the ports permits selection of molecules moving only in a limited set of directions. Preferably, a very large number of input ports are arranged on the device.
Rotor 82 preferably is, is mounted on, or is part of a rotating structure such as the rotors in FIGS. 1 and 2. FIG. 22 shows the rotor in cross section. The arrow to the right of rotor 82 shows the direction of movement of the rotor as the structure rotates.
Rotor 82 includes plural channels for molecules that enter the input ports. Channel 85 is such a channel. The rotor channels can be larger than the input ports. Preferably, though, the channels are microscopic size or smaller.
This disk or rotor preferably rotates fast enough such that the input ports are moved through the gas at a speed comparable to the mean thermal velocity of the gas. The size of the input ports preferably is comparable to the mean free path distance of the molecules in the gas. Thus, the arrangement of a particular rotor preferably is matched to a range of molecular speeds and mean free path distances corresponding to a particular range of temperatures and pressures of a gas.
The output stator includes at least one barrier arranged such that hotter molecules pass through the channels to one side of the barrier and cooler molecules pass through the channels to an other side of the barrier. One of these barriers is shown as barrier 86. Representative hotter molecules are shown with small empty circles, and representative cooler molecules are shown by small filled circles.
In the device shown in FIG. 22, one or more macroscopic ducts aggregate the hotter molecules, the cooler molecules, or both the hotter and the cooler molecules into separate bulk flows. Macroscopic duct 87 represents one of these ducts.
Each subfigure in FIG. 22 illustrates different steps in segregating and aggregating gas molecules according to this embodiment of the invention.
In FIG. 22A, unsorted molecules are present above input stator 81. These molecules are undergoing normal thermal motion, which is random motion in all directions.
Molecules possessing downward speed pass through port 84 of input stator 81 in FIG. 22B. These molecules can then enter channel 85 of rotor 82.
Depending on the molecules' velocities in the downward direction (i.e., the direction of the axis of rotor 82), the molecules take different amounts of time to pass through the channels in the rotor. Hotter molecules tend to have higher downward velocities, so the hotter molecules tend to pass through the channels faster. Cooler molecules tend to have lower downward velocities, so the cooler molecules tend to pass through the channel slower.
Barrier 86 is positioned so that hotter molecules that exit the channel faster pass to one side of the barrier, while cooler molecules that exit the channel slower pass to another side of the barrier. Thus, as shown in FIG. 22D, hotter (faster) molecules exit to one side of barrier, and cooler (slower) molecules exit to the other side of barrier. Macroscopic ducts 87 aggregate like molecules, preferably from a very large number of channels, and transport those molecules to one or more output ports (not shown). As a result, bulk flows with different temperatures are generated.
One concept useful for understanding the operation of the device shown in FIG. 22 is “slip.” Slip is relative motion between a spinning rotor and gas molecules in contact with the rotor. In some systems, no slip occurs because gas molecules in contact with the rotor tend to stick to the rotor. However, in FIG. 22, input stator 81 prevents the gas molecules from sticking to rotor 82. As a result, slip occurs, and the molecules can pass into the channels of the rotor.
At the output (not shown) of the device in FIG. 22, the macroscopic ducts preferably generate a bulk flow of gas molecules. Because of this bulk flow, slip considerations are less important at the output.
The device shown in FIG. 22 segregates molecules primarily on the basis of their downward (i.e., vertical) velocities. However, gas molecules also might have horizontal (e.g., along the rotor radius) velocities, even after passing through channels in the rotor. The output stator can include extra barriers to segregate and aggregate molecules based on their radial velocities.
Thus, FIG. 23 shows an arrangement wherein the output stator includes barriers 89 arranged in pairs. Each pair is arranged such that hotter molecules pass through the rotor to outside of the pair of barriers and cooler molecules pass through the rotor to between the pair of barriers.
In more detail, slower and therefore cooler molecules with smaller radial velocities tend not to travel far in the radial direction. These molecules aggregate between barriers 89 of the output stator.
Faster and therefore hotter molecules with larger radial velocities can travel beyond barriers 89. Thus, these molecules aggregate on either side of the barriers.
Macroscopic ducting can be used to redirect the cooler and hotter aggregated molecules to desired output ports (not shown).
FIGS. 24A to 24C show possible features for an output stator for a device that performs speed selection. FIGS. 24A to 24C are referred to collectively as FIG. 24.
In FIG. 24, stator 101 is an output stator akin to output stator 83 in FIG. 22. Likewise, barrier 102 is a barrier akin to barrier 86 shown in FIG. 22. Thus, faster (i.e., hotter) molecules pass to the left of barrier 102, and slower molecules pass to the right of barrier 102.
The faster molecules pass through downward directed port 103 for aggregation and output below stator 101, as shown in FIG. 24C. In one embodiment, the molecules are aggregated simply by passing out of many ports such as port 103. In another embodiment, macroscopic ducts 104 situated in or below the stator can aggregate the molecules from plural such ports.
Slower (i.e., cooler) molecules are redirected by angled surface 105 into a radial direction, as shown in FIG. 24B. The impact with the angled surface also can slow the molecules, possibly cooling them further. The redirected slower molecules pass through radially directed port 106 for aggregation and output radially from stator 101, as shown in FIG. 24C. In one embodiment, the molecules are aggregated simply by passing out of many ports such as port 106. In another embodiment, macroscopic ducts 107 situated in or beside the stator can aggregate the molecules from plural such ports.
In a preferred embodiment, output stator 101 includes macroscopic ducting to transport aggregated cooler molecules into bulk flows radially away from the device. Likewise, output stator 101 preferably includes macroscopic ducting to transport aggregated hotter molecules into bulk flows downward from the device.
The arrangement shown in FIGS. 24A to 24C can be modified so that cooler molecules exit downward, while hotter molecules exit radially. For example, the angled surface could be placed on the left in FIG. 24A.
FIG. 25 shows a possible aggregation and ducting arrangement for the rotor/stator embodiment.
In FIG. 25, molecules enter input stator 108 (akin to input stator 81 in FIG. 22), pass through rotor 109 (akin to rotor 82 in FIG. 22), and are segregated and aggregated by output stator 110 using structures such as those shown in FIG. 24. Other different structures can be use without departing from the invention.
FIGS. 26 to 28 show possible variations of the rotor/stator embodiment.
In the embodiments shown in FIGS. 22 to 25, molecules are segregated into two groups: hotter and cooler. However, molecules can be segregated into plural different groups based on their velocities. Thus, FIG. 26 shows input stator 121, rotor 122, and output stator 123 configured to generate plural different flows.
Input stator 121 is akin to the input stators already discussed. Rotor 122 can also be of the same type as those discussed above. However, FIG. 26 shows an alternative construction, in which the rotor includes plural blades spaced apart to form channels. The angle of these blades preferably is chosen based on the mean speed of molecules in the gas, which in turn is dependent upon the temperature and pressure of the gas, and the speed at which the blades move through the gas. In some embodiments, the ambient temperature and pressure of the gas can be controlled to best match the angles of the blades.
Output stator 123 includes plural different output paths. Faster molecules reach one of these paths after less travel distance for the rotor blades, while slower molecules reach one of the paths after more travel distance for the rotor blades. In FIG. 26, the rotor is moving from left to right (indicated by the arrow). Thus, faster (hotter) molecules exit more leftward output paths in stator 123, and slower (cooler) molecules exit more rightward output paths in stator 123. The arrangement of paths preferably is periodic, repeating relative to each input port for input stator 121.
FIG. 27 is arranged in a somewhat similar manner as FIG. 26, except that input stator 124 includes plural input ports. Rotor 125 again is constructed from blades that form channels, and output stator 126 includes plural output paths. Relative speeds of molecules output by the paths are represented by arrows, with longer arrows representing faster molecules.
Another feature shown in FIG. 27 is that input stator 124 has longer angled parallel input ports 127. Preferably, these ports are angled in the direction of rotor movement and have a length on the order of the mean free path distance for the gas being processed. This arrangement restricts input molecules to those already moving in the direction of the rotor, which improves the degree of segregation of molecules by the device. Restriction of the input molecules in this fashion is referred to as “collimation.”
One problem that can arise with the heteroscopic devices is backflow from inside the device out of the input ports or past the blades. One solution to this problem is to arrange the input ports and turbine blades to reduce outflow. For example, in FIG. 28, input port 130 is funnel shaped to help prevent outflow.
Interchangeability of Features
Each of the embodiments discussed herein can benefit from structures and arrangements described for the other embodiments.

Alternative Embodiments

Many of the foregoing embodiments are discussed in the context of rotational motion. Application of many of these concepts to linear motion through a gas would not require any further invention. For instance, the turbine blades could be mounted on an element that moves linearly through the air. An example of such an element would be a radiator of a vehicle.
Throughout this application, the rotor was assumed to be oriented with a vertical axis for ease of discussion. However, the invention is equally applicable to any other orientation. If another orientation is used, terms such as “downward,” “below,” “vertical,” etc. should be read as being re-oriented in accordance with that orientation.
Furthermore, although preferred embodiments of the invention are disclosed herein, many variations are possible which remain within the content, scope and spirit of the invention, and these variations would become clear to those skilled in the art after perusal of this application.

Claims

1-29. (canceled)

30. A method of moving a surface through a gas or liquid, comprising:

disposing nanoscopic or microscopic blades or edges on or in the surface; and

moving the surface through the gas or liquid;

whereby the gas or liquid at the surface lacks a velocity boundary layer.

31. A method as in claim 30, wherein the surface moves through the gas or liquid at a velocity comparable to a mean thermal velocity of the molecules in the gas or liquid.

32. A method as in claim 30, wherein the gas or liquid is air.

33. A method as in claim 30, wherein the surface is a rotating structure.

34. A method as in claim 30, wherein the surface moves linearly through the gas or liquid.

35. A method as in claim 30, wherein the blades or edges are formed from microscopic or nanoscopic holes in the surface.

36. A method as in claim 30, wherein the blades or edges are funnel shaped.

37. A method as in claim 30, wherein baffles separate groups of the blades.

38. A device, comprising:

a surface; and

nanoscopic or microscopic blades or edges on or in the surface;

wherein when the surface moves through a gas or liquid, the gas or liquid at the surface lacks a velocity boundary layer.

39. A device as in claim 38, wherein the surface moves through the gas or liquid at a velocity comparable to a mean thermal velocity of the molecules in the gas or liquid.

40. A device as in claim 38, wherein the gas or liquid is air.

41. A device as in claim 38, wherein the surface is a rotating structure.

42. A device as in claim 38, wherein the surface moves linearly through the gas or liquid.

43. A device as in claim 38, wherein the blades or edges are formed from microscopic or nanoscopic holes in the surface.

44. A device as in claim 38, wherein the blades or edges are funnel shaped.

45. A device as in claim 38, wherein baffles separate groups of the blades.