Patent Application
20220331750
The present disclosure is generally related to nanobubble generators, and more particularly to systems and methods including a vacuum-assisted shear flow nanobubble generator.
A nanobubble is a stable cavity of gas contained within a liquid matrix. At this time, there are no fully validated theories for the balance of forces that allow for stability of nanobubbles in solution. In fact, traditional bubble theory specifically states that nanobubbles are not stable and only have a half-life of microseconds. In reality, nanobubbles have been observed to have extremely long half-lives, allowing the nanobubbles to remain in solution for periods of weeks or even months. In contrast, microbubbles and macrobubbles show greater buoyancy than nanobubbles and tend to separate within a fluid flow, while nanobubbles may remain in solution.
The diameters of nanobubbles in solution may vary and are typically less than 1 micron. Microbubbles may have a diameter of about 1 to 50 microns, and macrobubbles may have diameters greater than 50 microns. The typical radius of a stable nanobubble is around 120 nm. The radius and stability of the nanobubbles have been shown to be influenced by liquid properties such as pH, salinity, temperature, other properties, or any combination thereof.
Nanobubbles have unique properties, which enable various applications. For example, nanobubbles have negative zeta potential (surface charge), which promotes separation of the nanobubbles in solution, improving stability. Smaller nanobubbles may have stronger surface charges than larger bubbles, limiting their coalescence. Further, nanobubbles lack enough buoyancy to reach a surface of the fluid and instead follow Brownian motion, such that the nanobubbles tend to remain suspended in water for long periods of time (weeks or months) until they dissolve, traveling randomly within the solution. The addition of nanobubbles to a liquid has been demonstrated to lower the surface tension of the liquid. Additionally, nanobubbles enable supersaturation with an order of magnitude greater than traditional dissolved gas limits.
There are many methods of generating nanobubbles, such as electrolysis, mechanical shear, filter membranes, porous glass or ceramics, saturation followed by pressure drop, and so on. Generally, nanobubbles are created by a “violent” mixing of gas and water through large pressure drops, high shear rates, or extensive mixing. A majority of industrial nanobubble generators use either pressure drops or gas injection at high shear flows. Both methods require the gas to experience high pressure relative to the liquid at positive fluid pressure that is typically moving at high velocity.
Some gases, such as ozone, are known to have reduced stability at high pressure. Unfortunately, generation of ozone nanobubbles using high pressure and shear forces may result in inefficient bubble formation with low percentage retention of ozone as it recombines to form oxygen at elevated rates at high pressures, as well as undesired aggregation or combination of nanobubbles into larger microbubbles or release of the gas from the fluid mixture.
Embodiments of systems, methods, and devices described below that include a system including a nanobubble generator and a pump. The nanobubble generator may include a first inlet to receive a fluid at a first pressure, a second inlet to receive a gas at a higher pressure, and an outlet. The nanobubble generator may include a porous component over which the fluid may flow. The porous component may include a chamber to receive the gas from the second inlet and a surface having a plurality of gas-permeable openings to inject the gas into the flowing fluid. The pump may include an input coupled to the outlet of the nanobubble generator and may include an output coupled to one or more of a conduit or a tank to pump the solution from the nanobubble generator. The pump may apply a negative pressure at the outlet of the nanobubble generator, producing a negative pressure within the nanobubble generator. The negative pressure may cooperate with the fluid flowing across the plurality of gas-permeable openings to shear the injected gas to facilitate nanobubble production. The negative pressure inside the nanobubble generator may draw the gas into the solution. In some implementations, the negative pressure may enable formation of stable nanobubbles having an expanded size, facilitating bubble formation, and the bubbles may shrink to a more stable nanobubble size when exposed to the higher pressure as the pump pushes the nanobubble solution to the conduit or the tank.
In some implementations, the system may include a degassing valve coupled between the output of the nanobubble generator and the input of the pump to remove microbubbles or larger bubbles that might otherwise cause cavitation and damage the pump. The degassing valve may be integrated within the output of the nanobubble generator. In some implementations, the degassing valve may augment the contact time of the liquid with the gas contained in the microbubbles, further increasing efficiency of the system.
In some implementations, a system may include a nanobubble generator and a pump configured to provide a negative pressure to the nanobubble generator. The nanobubble generator may include a fluid inlet to receive a fluid, a gas inlet to receive a gas, a porous component including a plurality of gas-permeable openings to allow gas injection, and an outlet. The fluid may flow across the gas-permeable openings while the fluid flows from the fluid inlet to the outlet. The pump may include an inlet coupled to the outlet of the nanobubble generator and may include an outlet to provide a nanobubble solution to one or more of a conduit or a tank. The fluid pressure from the fluid and the negative pressure provided by the pump may cooperate to shear nanobubbles from the plurality of gas-permeable openings to form the nanobubble solution. In some aspects, a filter may be provided to remove bubbles that are larger than nanobubbles from the solution before the solution is provided to the inlet of the pump.
In other implementations, a system may include a pump, a nanobubble generator, and a filter. The pump may include an inlet coupled to an output of the nanobubble generator and may include an outlet coupled to one or more of a conduit or a tank. The nanobubble generator may include one or more fluid inlets to receive a fluid, a gas inlet to receive a gas, and the outlet coupled to the inlet of the pump to receive a negative pressure. The nanobubble generator may include a porous component including a chamber coupled to the gas inlet and including a plurality of gas-permeable openings through which the gas may be injected and across which the fluid flows from the one or more fluid inlets to the outlet. The filter may be disposed between the porous component and the inlet of the pump and may be configured to remove bubbles larger than nanobubbles. A fluid pressure from the fluid and a negative pressure provided by the pump may cooperate to shear nanobubbles from the plurality of gas-permeable openings to form a bubble solution that passes through the filter to produce a nanobubble solution.
In still other implementations, a system may include a pump and a nanobubble generator. The nanobubble generator may include a fluid inlet to receive a fluid, a gas inlet to receive gas from a gas source, and an outlet. The nanobubble generator may include a porous component including a chamber to receive the gas and a surface including a plurality of gas-permeable openings. The fluid may flow from the fluid inlet to the outlet across the surface. The pump may include an inlet coupled to the outlet of the nanobubble generator and may include an outlet to supply a nanobubble solution to a conduit or a tank. The pump may supply a negative pressure to the porous component and the fluid may flow across the surface to shear the gas from the openings to form the nanobubble solution.
The detailed description is set forth with reference to the accompanying figures. In the figures, the left most digit(s) of a reference number identifies the figure in which the reference number first appears. The use of the same reference numbers in different figures indicates similar or identical items or features.
While implementations are described in this disclosure by way of example, those skilled in the art will recognize that the implementations are not limited to the examples or figures described. It should be understood that the figures and detailed description thereto are not intended to limit implementations to the particular form disclosed, but on the contrary, the intention is to cover all modifications, equivalents, and alternatives falling within the spirit and scope as defined by the appended claims. The headings used in this disclosure are for organizational purposes only and are not meant to limit the scope of the description or the claims. As used throughout this application, the work “may” is used in a permissive sense (in other words, the term “may” is intended to mean “having the potential to”) instead of in a mandatory sense (as in “must”). Similarly, the terms “include”, “including”, and “includes” mean “including, but not limited to”.
An ozone nanobubble solution may be used to purify water for numerous applications including cleaning applications (automotive, carpet, industrial equipment, and so on), organic cleaning solutions (vegetable baths, fruit baths, and so on), water reclamation (black water recycling, fracking fluid reclamation, and so on), and other applications. Typically, in cleaning solution applications, cleaning fruits, vegetables, or other objects in a nanobubble solution may require submersion of the object to be cleaned for a period of time. However, nanobubble production in which high velocity fluid is forced across the porous component to shear the gas bubbles may produce a highly turbulent bubble solution comprised of nanobubbles, microbubbles, and larger gas bubbles. The turbulence may cause a longer pathway through a fluid chamber allowing some of the bubbles to collide and aggregate to form larger bubbles, which may reduce the nanobubble concentration within the solution and which may reduce the overall efficiency of the nanobubble production process. Moreover, ozone gas has reduced stability at high pressure, and the high pressure required to overcome the backpressure from the fluid results in rapid decay of ozone before reaching injection location. The reduced gas stability coupled with the turbulence of the solution reduces the efficiency of ozone nanobubble production.
Embodiments of the present disclosure include a system including a vacuum-assisted, shear flow nanobubble generator that utilizes shear flow from a fluid and a vacuum supplied by a pump to shear gas from a surface of a porous component to form a plurality of stable nanobubbles. The nanobubble generator is configured to produce bubbles under negative pressure.
In some implementations, the nanobubble generator may include an enclosure with a fluid inlet, a gas inlet, and an outlet. Within the enclosure, the nanobubble generator may include a porous component including a chamber to receive a gas from the gas inlet and a plurality of gas-permeable openings through which the gas may be injected into the enclosure. A negative pressure is applied to the enclosure. As fluid flows across the porous component from the fluid inlet to the outlet, the negative pressure may cause the gas to be drawn into the fluid as it passes through the gas-permeable openings, facilitating shearing of the gas and formation of nanobubbles.
Generally, larger bubbles are easier to shear from the gas-permeable openings than smaller bubbles, requiring lower fluid flow rates and injected gas pressures (i.e., less shearing force). The diameter of a stable nanobubble may be larger at low or negative pressures than the diameter of the same bubble at a higher pressure due to the balance of internal and external pressure forces on the bubble surface. By forming bubbles at negative pressures, the vacuum allows the gas to form larger diameter bubbles, assisting the fluid flow to shear the gas from the gas-permeable openings. The bubble sizes may change as the pressure is increased (i.e., when the bubble solution passes through a pump) without adversely effecting stability of the bubbles. In an example, the bubble formed in the vacuum within the enclosure of the nanobubble generator may have a diameter of 200 nm or greater and the diameter of the bubble may shrink to a size of 120 nm or less when a positive external pressure is applied by surrounding fluid, producing a stable nanobubble solution.
In some implementations, a system may include a nanobubble generator and a pump. The nanobubble generator may include an inlet to receive a fluid at a first pressure, a gas input to receive a selected gas (such as ozone gas), and an output to provide a nanobubble solution to an inlet of a pump. The pump may apply a negative pressure to the outlet of the nanobubble generator, supplying a vacuum to assist in the formation of the nanobubbles. The pump may be configured to move the nanobubble solution from the nanobubble generator into a conduit or a tank at a second pressure that is greater than the first pressure.
It is generally undesirable to inject gas into a liquid stream at the input of a pump, since the injected gas may cause cavitation. Cavitation is a phenomenon in which bubbles within the fluid flow may collapse and generate shock waves, which may result in wear to mechanical parts within the pump. Embodiments of the present disclosure introduce a nanobubble solution to an inlet of the pump. The nanobubbles in the solution may shrink under pressure but otherwise remain stable and substantially homogenous within the solution, allowing the pump to move the solution without problems due to cavitation. If larger size bubbles are introduced into the fluid before a pump, these bubbles may be removed by a degassing filter.
By using a combination of a negative pressure and a shearing force due to the fluid flow, the fluid velocity in the fluid chamber can be reduced which increases nanobubble formation efficiency, and the resulting bubble solution is less turbulent than in conventional nanobubble generators. While it is widely believed that high pressure gas is needed to form the nanobubbles, the high gas pressure requires high velocity fluid flow to produce shearing effects, resulting in highly turbulent flow in a fluid chamber, encouraging collisions between the bubbles, and reduces overall efficiency of nanobubble formation. In the context of ozone nanobubbles, the high pressure of injected gas adversely impacts the stability of pressure sensitive gases prior to injection. By using fluid flow and negative pressure to encourage nanobubble formation, overall efficiency of nanobubble formation is improved and the bubbles in the resulting solution are produced more efficiently than in conventional systems, particularly with respect to gas bubbles formed from pressure sensitive gases such as ozone. Additionally, the flow speed is reduced with reduction in overall turbulence of the nanobubble solution is reduced, enhancing stability of the bubbles due to less aggregation.
In some implementations, a filter may be used to remove microbubbles and other bubbles that are larger than nanobubbles, producing a nanobubble solution including only nanobubbles and dissolved gas to flow into the pump. The filter may be implemented as an outgassing valve, a spin down filter, a membrane, another type of filter, or any combination thereof, which may be configured to remove bubbles larger than nanobubbles from the solution. The filter may be included within the nanobubble generator or may be provided between the nanobubble generator and the pump, depending on the implementation. By removing or degassing microbubbles and larger bubbles from the solution, the remaining nanobubbles may remain stable in the solution and may flow through the pump without causing cavitation. By increasing the contact time of the fluid with the larger bubbles, additional efficiencies can be obtained, such as sanitization of water moving though system with ozone gas injected.
In some implementations, the nanobubble generator 104 may include one or more fluid channels 114, through which the fluid may flow. The one or more fluid channels 114 may extend across a surface of one or more porous components 116. The surface of the porous component 116 may include a plurality of gas-permeable openings. The porous surfaces may be flat or cylindrical in shape. The porous component 116 may include a chamber configured to receive the gas from the second inlet. The fluid may flow across the openings at an angle that is generally orthogonal to the surface of the porous components 116. Each porous component 116 is arranged such that the gas introduced into a lumen or chamber of the porous component 116 is forced through or otherwise is drawn through the gas-permeable openings. The fluid flow across the openings in conjunction with a negative-pressure introduced by a pump 110 may cooperate to shear the gas to form nanobubbles and to draw the nanobubbles into the inlet of the pump 110.
The one or more filters 108 may be positioned between the nanobubble generator 104 and the pump 110. The one or more filters 108 may be configured to remove microbubbles and larger bubbles from the solution, so that the solution provided to the pump 110 includes dissolved gas and nanobubbles. In some implementations, the filter 108 may be implemented as a degassing valve configured to remove gas bubbles that are larger than a nanobubble using gravity and buoyancy of the larger bubbles, a porous membrane with nanobubble-sized openings, another type of filter, or any combination thereof, which allows only the nanobubbles and dissolved gas to be provided to the pump inlet. The one or more filters 108 are shown in phantom because they may be external to the nanobubble generator 104 or may be integrated within the nanobubble generator 104, depending on the implementation.
The fluid pressure at the fluid inlet of the nanobubble generator 104 may be less than the pressure at the outlet of the pump 110. In some implementations, the fluid source 102 may be a tank of water and the pressure in the nanobubble generator 104 is under vacuum with negative pressure. Other implementations are also possible.
In the illustrated example of
The nanobubble generator 104 may be manufactured to have a variety of different form factors, including cylindrical form factors, rectangular form factors, and so on. One example of a rectangular form factor is described below with respect to
In some implementations, the nanobubble generator 104 may include an optional bypass opening 208. In such implementations, there may be a bypass portion of flow that allows for some of the fluid to transit directly through the nanobubble generator 104, which may be used as stabilizing pressure force applied after shearing of nanobubbles. The fluid may flow between the openings (inlet 204 and outlet 206) and across the porous component 116. The porous component 116 may include a chamber or lumen coupled to a gas inlet to receive the gas from a gas source 106 and may include a plurality of gas-permeable openings to allow the gas to seep through the openings to be sheered into nanobubbles by the fluid flowing across the surface of the porous component 116. The pump 110 may supply a negative pressure to the solution outlet 206 (or the fluid inlet 204, depending on the configuration). The negative pressure may facilitate bubble formation in conjunction with the fluid flow. The nanobubble generator 104 may have been originally designed to work under positive pressures installed after a pump. However, as previously discussed, by installing the nanobubble generator 104 in front of the pump 110 (i.e., before in the inlet of the pump 110), the nanobubbles can be produced in a negative pressure at relatively low fluid flow rates and relatively low gas pressures to produce a stable nanobubble solution with improved efficiency.
After the bubbles are sheared off of the surface of the porous component 116, the bubble solution flows into the volume expansion area 310, which may help the bubbles to separate from one another and to restore the pressure and velocity of the solution to levels that correspond to the flow rate and pressure of the fluid and the fluid inlet 204. In some instances, the volume expansion area 310 may assist in stabilizing the bubbles after formation and may operate to allow the bubbles to separate from one another, homogenizing the bubble solution.
The pump 110 may apply a negative pressure such that the fluid channel 114 within the nanobubble generator 104 is at a negative pressure. The negative pressure may assist the shear flow in tearing the bubbles away from the gas-permeable openings 308. Additionally, the gas bubble may expand into the negative pressure, creating larger diameter but stable nanobubbles in the vacuum. As pressure is increased when the nanobubble solution passes through the pump 110, the diameters of the nanobubbles may decrease while remaining stable and without cavitation.
In the example of
As the nanobubbles are formed by the shearing fluid flow, the transition flow 404(1) transitions into a turbulent flow as indicated at 406, as the nanobubbles flow into the volume expansion area 310. As the nanobubble solution 304 flows toward and into the outlet 206, the turbulent flow 406 may transition back into a transition flow 404(2) and possibly a laminar flow.
At 430, the gas has pushed further into the fluid flow producing a larger gas dome, as shown at 432. The viscous sublayer flow 402 further deforms the gas dome 432, and the gas dome 432 causes some transition flow 404. The negative pressure from the pump 110 and the shear force of the viscous sublayer fluid flow 402 cooperate to further deform the gas dome at 432.
At 434, the viscous sublayer fluid flow 402 may shear the gas from the opening 308, producing a bubble 442. The bubble 442 may move into the fluid flow and separate from a new gas dome 424 that is forming at the opening 308.
In the examples above, nanobubbles are formed by the interaction of the fluid flowing across the surface of the porous component 116 and the negative pressure applied by the pump 110. The size of bubble created is controlled by the balance of forces of pressure injected behind the gas bubble, back pressure in the fluid chamber, shear force from the fluid flow, and surface tension of the gas-liquid interface. The surface charge may tend to expand the diameter of the bubble. Additionally, under negative pressure, there is little or no backpressure to oppose expansion of the bubble, allowing the gas to expand into the fluid flow to produce bubbles that may contract as fluid pressure increases. An illustrative example of the formation, separation, and contraction of the bubbles is described below with respect to
In a pull stage 506, the gas bubble expands into the fluid chamber as a result of the negative pressure pulling on the gas bubble. As the gas dome is drawn into the fluid chamber by the negative pressure it deformed by the shearing force produced by the viscous sublayer fluid flow (402 in
In a cut stage 508, the fluid flow cuts the gas dome to form a nanobubble 442. At 508(1), the viscous sublayer fluid flow may deform a portion of the gas dome near the surface of the porous component 116. At 508(2), the viscous sublayer fluid flow may shear the gas dome from the opening to produce the nanobubble. In general, the fluid flow rate does not need to be as fast as in conventional nanobubble generators because the fluid pressure does not drive the gas back into the porous medium.
In a separate stage 510, the turbulence of the fluid flow, the negative pressure in the fluid chamber, the positive pressure in the gas bubble, and the surface charge of the nanobubble 442 cooperate to separate the nanobubble 442 from the porous component 116 and from other bubbles in the fluid solution. The turbulent flow may prevent aggregation and facilitate separation of the nanobubbles 442 from one another.
At 520, the nanobubbles separate from one another and spread out within the solution in the volume expansion area 310 of the nanobubble generator 104. In this stage, the turbulence of the fluid flow and the surface charge of each nanobubble cooperate to mix the nanobubbles within the solution to produce a relatively homogenous fluid solution. Within the volume expansion area 310, the nanobubbles 442 are further separated from one another and may stabilize as the fluid pressure is slightly higher but still negative in the volume expansion area 310.
At 530, the pressurization by the pump 110 may cause the nanobubbles 442 to contract to form smaller-diameter stable nanobubbles 532. In general, during the production stage at 502 and during the separation and homogenization stage 520, the nanobubbles 442 are under a negative pressure in which there is little or no backpressure to oppose gas expansion. As pressure is applied by the pump 110, the fluid pressure applies a backpressure that may cause the nanobubbles to contract to a smaller-diameter state in which the nanobubbles 532 are at equilibrium with respect to opposing gas and fluid pressures, producing a stable nanobubble solution.
As previously discussed, the solution outlet 206 of the nanobubble generator 104 may be coupled to the input of the pump 110, which may provide a negative pressure to the nanobubble generator 104. The fluid flow from the inlet 204 to the outlet 206 across the surface of the porous component 116 that includes a plurality of gas-permeable openings 308. The combination of the fluid flow and the negative pressure may facilitate nanobubble formation. In particular, the negative pressure may cause the gas volume to increase, making it easier for the fluid flow to shear the bubbles away from the surface of the porous component.
Unlike conventional nanobubble generators that require a high pressure (80 PSI or greater) fluid flow to shear the nanobubbles, the nanobubble generator 104 may generate nanobubbles at lower gas pressures (e.g., 5-30 psi) and lower fluid shear flow velocities (e.g., 1.5 m/s to 2.0 m/s). The negative pressure applied by the pump 110 may enhance the efficiency of nanobubble formation, enabling reduced requirements for fluid flows and gas pressures while still enabling nanobubble formation. Additionally, a pure nanobubble solution may be produced which may be beneficial for certain applications where the floatation provided by larger bubbles is disadvantageous to the application.
At 702, the method 700 may include providing fluid from a fluid source 102 to a fluid inlet 204. In some implementations, the fluid may include water, which may be distilled or purified. In other implementations, the fluid may be selected based on desired fluid properties, such as viscosity, chemical content, and so on. The fluid may be provided to the fluid inlet 204 of the nanobubble generator 104. However, in some implementations, the nanobubble generator 104 may be bidirectional such that the fluid source may be coupled to the inlet 204 or the outlet, and the pump 110 may be coupled to the other of the outlet 206 or the inlet 204.
At 704, the method 700 may include applying a negative pressure to an outlet 206 of the nanobubble generator 104. The negative pressure may be applied by a pump 110 drawing the fluid or the fluid solution 304 through the outlet 206. In some implementations, by changing the rate of the pump 110, the negative pressure may be increased or decreased to provide a selected negative pressure. As the rate of the pump 110 is increased, the negative pressure increases. The negative pressure may facilitate nanobubble formation within the nanobubble generator 104.
At 706, the method 700 may include providing a gas to a porous component 116 within an enclosure 202 of a nanobubble generator 104. The gas may include one or more of oxygen, ozone, carbon dioxide, hydrogen, nitrogen, another gas, or any combination thereof. In some implementations, the gas may be provided by connecting a gas source 106 to a gas inlet 202 of the nanobubble generator 104 and opening a valve to allow the gas from the gas source 106 to flow to the gas inlet 202. The gas may be provided at a relatively low pressure of 5-30 PSI.
At 708, the method 700 may include directing the fluid across the porous component 116 within the enclosure 202 to shear gas bubbles from openings 302 of the porous component 116 to form a bubble solution 304. The fluid may be directed across the porous component 116 by providing one or more fluid channels 114 through which fluid may flow. In some implementations, the fluid may flow parallel to and across a surface of the porous component 116 that includes the openings 302 to shear the bubbles.
At 710, the method 700 may include filtering bubbles larger than nanobubbles from the bubble solution 304 to produce a nanobubble solution. In some implementations, filtering may be performed by one or more of gravity or a filter. The filter may include one or more of a degassing valve, a membrane with nanobubble sized pores, another type of filter, or any combination thereof. The filter may be configured to separate microbubbles and larger bubbles from the solution 304, leaving a nanobubble solution comprised of dissolved gas and nanobubbles, which may be provided to the fluid outlet 206.
At 712, the method 700 may include providing the nanobubble solution to an inlet of a pump 110. The nanobubble solution may be provided to the pump 110 by coupling the pump 110 to the outlet 206 and activating the pump 110. The pump 110 may apply a negative pressure to draw the nanobubble solution from the outlet 206 of the nanobubble generator 104 into an inlet of the pump 110. Other implementations are also possible.
As mentioned above, the operations described in the method 700 may occur substantially simultaneously. For example, upon activation of the system 100, the fluid may be provided to the fluid inlet 204, the gas may be provided to the gas inlet, and the negative pressure be applied to the outlet 206 by the pump 110. Upon providing of the fluid and the gas, the fluid may flow across the porous component 116 producing bubbles and the filtering of bubbles larger than nanobubbles from the solution may begin. Thus, the operations described in 702-708 may occur substantially concurrently followed by the filtering at 710 and the receiving of the nanobubble solution 304 at the inlet of the pump 110.
The method 700 is illustrative only and is not intended to be limiting. In some implementations, operations may be combined or may be omitted without departing from the scope of the disclosure. For example, the filtering of the bubbles may be performed by the geometry of the nanobubble generator 104 without a separate filtering step. Other implementations are also possible.
In conjunction with the systems, devices, and methods described above with respect to
In some implementations, the filter 108 may be incorporated in the nanobubble generator 104. In other implementations, the filter 108 may be external to the nanobubble generator 104.
By providing the nanobubble generator 104 in front of the pump 110, the negative pressure supplied by the pump 110 may assist in the nanobubble formation process by forming nanobubbles in a vacuum. Further, the flow of the fluid at the inlet 204 may be lower than that of conventional nanobubble generators because the negative pressure from the pump 110 assists the bubble formation, unlike conventional devices that form nanobubbles using only the shearing force. Further, the injected gas pressure at the gas inlet 302 may be lower than in conventional nanobubble generators. In an example, a conventional nanobubble generator may require injected gas pressures of 50 PSI or greater, while the nanobubble generator 104 may produce nanobubbles under vacuum (e.g., 1-10 mm Hg), enabling low gas injection pressures of 10 to 30 PSI.
While it is generally undesirable to inject gas at the inlet of the pump 110 because cavitation from the bubbles may damage the pump 110, by filtering the microbubbles and larger bubbles from the bubble solution using the filter 108, the nanobubbles within the resulting nanobubble solution remain stable and do not cause cavitation, allowing the pump 110 to move the nanobubble solution reliably and without damage from the bubbles. Further, the negative pressure may facilitate nanobubble production by enabling larger size nanobubbles at low pressure, which may shrink in response to increasing pressure without collapsing. The required gas injection pressure is low, allowing the method to be efficient with pressure sensitive gases. Further, the lower shear speed fluid flow and the negative pressure produce a nanobubble solution with less turbulence than the higher pressure conventional systems, which allows for a more stable nanobubble solution and a more efficient nanobubble production process.
Although the present invention has been described with reference to preferred embodiments, workers skilled in the art will recognize that changes may be made in form and detail without departing from the scope of the invention.
