Patent Application
20070017192
The present invention relates to liquid purification, and more particularly to liquid purification by vapor compression distillation comprising a liquid ring pump with rotatable housing having an internal liquid recovery system.
A dependable source of clean water eludes vast segments of humanity. For example, the Canadian International Development Agency reports that about 1.2 billion people lack access to safe drinking water. Published reports attribute millions and millions of deaths per year, mostly children, to water related diseases. Many water purification techniques are well known, including carbon filters, chlorination, pasteurization, and reverse osmosis. Many of these techniques are significantly affected by variations in the water quality and do not address a wide variety of common contaminants, such as bacteria, viruses, organics, arsenic, lead, mercury, and pesticides that can be found in water supplies in the developing world and elsewhere. Some of these systems require access to a supply of consumables, such as filters or chemicals. Moreover, some of these techniques are only well suited to centralized, large-scale water systems that require both a significant infrastructure and highly trained operators. The ability to produce reliable clean water without regard to the water source, on a smaller, decentralized scale, without the need for consumables and constant maintenance is very desirable, particularly in the developing world.
The use of vapor compression distillation to purify water is well known and can address many of these concerns. However, the poor financial resources, limited technical assets, and low population density that does not make it feasible to build centralized, large-scale water systems in much of the developing world, also limits the availability of adequate, affordable, and reliable power to operate vapor compression distillation systems, as well as hindering the ability to properly maintain such systems. In such circumstances, an improved vapor compression distillation system and associated components increases efficiency and production capability, while decreasing the necessary power budget for system operation and the amount of system maintenance required.
In a first embodiment of the invention a liquid purification system is provided that advantageously may be compact, inexpensive, and easily maintained. One embodiment has a distillation device with a liquid ring pump and a rotatable housing with a single continuous shaft about which the liquid ring pump, motor and rotor rotates, and a second shaft supporting the rotatable housing, with an internal or external combustion engine, having motor rotor and magnets outside the fluid pressure boundary for the distillation system.
Another alternative embodiment has a distillation device with a liquid ring pump encased in a fully rotatable housing within the head vapor space of a still. Systemic heat sources can be redirected through a multi-line heat exchanger to maximize energy efficiency during the vaporization step. Back-wash lines may be directed to the intake from the head chamber of the evaporator/condenser, to keep unique flip-filters in the intake from fouling and to add heat into the heat exchange network. Further, a method of eliminating mist may be incorporated in the liquid ring pump component to eliminate contaminated liquid droplets entrained in the vapor and prevent them from being carried along to the condenser and thereby contaminating the purified product. One particular embodiment of the mist eliminator may have a top, a bottom and a housing wherein liquid is removed from suspension in vapor to an inner surface of the housing, the improvement comprising a plurality of vanes disposed along a diverter cone, wherein the diverter cone is situated at the bottom of said mist eliminator and wherein the vanes are angled to create a rotating motion to the vapor in the housing, a plurality of scales forming an angle α of at least about 15 degrees relative to a longitudinal axis Z of the housing, wherein the scales are situated to entrap liquid removed from suspension in vapor upon contact of the liquid with the scales, and each scale is in fluid communication with a gap between the scale and the inner surface of the housing of a dimension adapted to draw liquid through the gap to a collection area.
In related embodiments, the gap may be between about 0.025 and 0.05 inches, and may comprise a steam output for allowing steam to escape and/or a separator for collecting any liquid passing through the top of the mist eliminator.
Another particular embodiment has a distillation device with a liquid ring pump and a rotatable housing with a single continuous shaft about which the liquid ring pump, motor and rotor rotates, and a second shaft supporting the rotatable housing, with an internal or external combustion engine and siphon pump in a lower reservoir to siphon liquid into the chamber of the liquid ring pump. The result is a highly efficient, easily accessed and maintained, relatively simple and inexpensive system for purifying a liquid.
Yet another embodiment provides a level sensor for controlling fluid flow of a liquid in a liquid distillation system during distillation, the level sensor coupled with a variable flow valve controlled by the fluid level in the system.
Yet another method for removing contaminants from water comprises driving an electric generator by means of a thermal cycle engine for generating electrical power capacity, the thermal cycle engine including a burner for combusting a fuel, employing at least a portion of the electrical power capacity of the electric generator for powering a water purification unit, supplying source water to an input of the water purification unit, conveying heat output of the thermal cycle engine for supplying heat to the water purification unit to reduce the amount of electrical power required to purify the water. Further embodiments may additionally comprise one or all of transferring heat from an exhaust gas of the burner to source water, heating an enclosure surrounding the water purification unit to reduce thermal loss, vaporizing untreated water, and condensing vaporized water into distilled water product.
Another embodiment employs a backpressure regulator comprising a hinged arm having a closed position and a movable stop shaped to cover a port connected to a pressurized conduit, the stop being held by a retainer attached to the arm, and the stop being positioned adjacent to the port when the arm is in the closed position, wherein the arm is away from the closed position when the pressure conduit exceeds a set point, and the arm is in the closed position when the pressure in the conduit is less than the set point.
Additional advantages and specific aspects of the system will be more readily ascertained from the drawings and the accompanying detailed description of the preferred embodiments, below.
The foregoing features of the invention will be more readily understood by reference to the following detailed description, taken with reference to the accompanying drawings, in which:
Definitions. As used in this description and the accompanying claims, the following terms shall have the meanings indicated, unless the context otherwise requires.
The term “purifying” as used herein, and in any appended claims, refers to substantially reducing the concentration of one or more contaminants to less than or equal to specified levels or otherwise substantially altering the concentration of one or more contaminants to within a specified range.
The term “specified levels” as used herein refers to some desired level of concentration, as established by a user for a particular application. One instance of a specified level may be limiting a contaminant level in a fluid to carry out an industrial or commercial process. An example is eliminating contaminant levels in solvents or reactants to a level acceptable to enable an industrially significant yield in a chemical reaction (e.g., polymerization). Another instance of a specified level may be a certain contaminant level in a fluid as set forth by a governmental or intergovernmental agency for safety or health reasons. Examples might include the concentration of one or more contaminants in water to be used for drinking or particular health or medical applications, the concentration levels being set forth by organizations such as the World Health Organization or the U.S. Environmental Protection Agency.
As used herein, the terms rotor and impeller are intended to be used interchangeably, such that a rotor and an impeller perform the equivalent function within the liquid purification system described and claimed herein.
A conceptual flow diagram of an overall system in accordance with one possible embodiment of the present invention is shown in
A power source 800 is used to power the overall system. Power source 800 may be coupled to a motor 150 (not shown) that is used to drive compressor 100, particularly when compressor 100 is a steam pump, such as a liquid ring pump. The power source 800 may also be used to provide electrical energy to the other elements of the system shown in
Alternatively, heat from electrical power generator 800 may be recaptured by channeling the engine exhaust into the insulated cavity that surrounds the still, which lies between fixed housing and the individual still components. In such an embodiment, exhaust blows across a finned heat exchanger that heats source liquid as it enters evaporator 600.
Returning to
Pre-treatment of the liquid to be distilled, preferably water, may be conducted, in which case pre-treatment may occur prior to or within intake 00. Pre-treatment operations may include any or all of gross-filtering; treatment with chemical additives such as polyphosphates, polyacetates, organic acids, or polyaspartates; and electrochemical treatment such as an oscillating magnetic field or an electrical current; degassing; and UV treatment. Additives may be added in liquid form to the incoming liquid stream using a continuous pumping mechanism such as a roller pump or pulsatile pump, including a standard diaphragm pump or piezoelectric diaphragm pump. Alternatively, the additives may be added by a semi-continuous mechanism using, for example, a syringe pump, which would require a re-load cycle, or a batch pumping system, wherein a small volume of the additive would be pumped into a holding volume or reservoir external to the system that uniformly mixes the additive with the liquid before the liquid flows into the system. A volcano valve pump as described in U.S. Pat. No. 6,464,667, hereby incorporated by reference herein, may also be used for the addition of additives. In addition, an FMS pump, as described in U.S. Pat. No. 5,193,990, hereby incorporated by reference herein, may be used for addition of additives. As well, the additives may be added using a fluid system management pump described in U.S. Application Ser. No. 60/792,073 filed Apr. 14, 2006 to inventors Dirk A van der Merwe, James D. Dale, Brian Tracey, Larry B. Gray, Jason A Demers, David E. Altobelli, Dean L. Kamen, N. Christopher Perry, and Kingston Owens, hereby incorporated by reference herein. Such a pump may be a reciprocating positive-displacement pump, as described in more detail below.
It is also envisioned that the user could simply drop a prescribed volume of the additive into, for example, a bucket containing the liquid to be purified. Liquid additives may be loaded as either a lifetime quantity (i.e., no consumables for the life of the machine), or as a disposable amount requiring re-loading after consumption.
Additives could also be added in solid form, wherein such additives could be embedded in a time-release matrix inserted into the flow-through channel of intake 00. In this particular embodiment, replacement additive would need to be inserted periodically by the user. In yet another embodiment, a powder form of an additive could be added in a batch system wherein the powder is added, for example in tablet form, to an external reservoir containing water to be purified wherein the additive is uniformly mixed, similar to the batch system for adding liquid additives described above.
Post-treatment of the distilled product, preferably water, may occur, in which case post-treatment may occur preferably within an external output region (not shown). Post-treatment operations may include taste additives such as sugar-based additives for sweetening, acids for tartness, and minerals. Other additives, including nutrients, vitamins, stabilized proteins such as creatinine, and fats, and sugars may also be added. Such additives may be added either in liquid or solid form, whether as a time-release tablet through which the output liquid flows, or a powder added to an external reservoir such as through a batch system. Alternatively, the additive may be added to the output liquid via an internal coating of a separate collection reservoir or container, for example, by leaching or dissolution on contact. In such embodiments, the ability to detect purified liquid with and without the additive is preferred. Detection systems in accordance with embodiments of the present invention include pH analysis, conductivity and hardness analysis, or other standard electrical-based assays. Such detection systems allow for replacement of additives, as needed, by triggering a signal mechanism when the additive level/quantity is below a pre-set level, or is undetectable.
In another embodiment, liquid characteristics, such as for example water hardness, is monitored in the output and may be coupled with an indicator mechanism which signals that appropriate additives should be added.
In yet another embodiment, ozone is systemically generated using, for example, electric current or discharge methods, and added to the output product for improved taste. Alternatively, air pumped through a HEPA filter may be bubbled through the output liquid to improve palatability of the final purified product.
It is envisioned that other embodiments may include means for detecting nucleic acids, antigens and bio-organisms such as bacteria. Examples of such detection means include nanoscale chemistry and biochemistry micro-arrays known in the field and currently commercially available. Such arrays may also be used to monitor the presence and/or absence of nutrients and other additives in the purified product, as discussed above.
In another embodiment, UV treatment may be used post-purification, for example in a storage barrel or other container, to aid in maintenance of the purified product.
In another particular embodiment, a Stirling engine generator which produces exhaust high in CO2 content is used as the power source 800 to power the overall system. In such an embodiment, the exhaust from the Stirling engine is funneled back to intake 00 and used to acidify the water to be purified as one means of pre-treatment. The acidification of the incoming water supply would result from the forced dissolution of the CO2 (under pressure) in the exhaust, and the acidification may reduce any scaling, such as lime build-up, that occurs in the system. Alternatively, the CO2 exhaust may be channeled into the purified product as a means for post-treatment acidification.
The system provided in accordance with embodiments of the present invention has two basic functional components that may be combined within a single integral unit or may be capable of separate operation and coupled as described herein for the purpose of local water purification.
Thermal cycle engines are limited, by second law of thermodynamics, to a fractional efficiency, i.e., a Carnot efficiency of (TH−TC)/TH, where TH and TC are the temperatures of the available heat source and ambient thermal background, respectively. During the compression phase of a heat engine cycle, heat must be exhausted from the system in a manner not entirely reversible, thus there will always be a surfeit of exhaust heat. More significantly, moreover, not all the heat provided during the expansion phase of the heat engine cycle is coupled into the working fluid. Here, too, exhaust heat is generated that may be used advantageously for other purposes. The total heat thermodynamically available (i.e., in gas hotter than the ambient environment) in the burner exhaust is typically on the order of 10% of the total input power. For a power unit delivering on the order of a kilowatt of electrical power, as much as 700 W of heat may be available in an exhaust stream of gas at temperatures in the vicinity of 200° C. In accordance with embodiments of the present invention, the exhaust heat, as well as the electrical power generated by an engine-powered generator, are used in the purification of water for human consumption, thereby advantageously providing an integrated system to which only raw water and a fuel need be provided.
Moreover, external combustion engines, such as Stirling cycle engines, are capable of providing high thermal efficiency and low emission of pollutants, when such methods are employed as efficient pumping of oxidant (typically, air, and, referred to herein and in any appended claims, without limitation, as “air”) through the burner to provide combustion, and the recovery of hot exhaust leaving the heater head. In many applications, air is pre-heated, prior to combustion, nearly to the temperature of the heater head, so as to achieve the stated objectives of thermal efficiency. However, the high temperature of preheated air, desirable for achieving high thermal efficiency, complicates achieving low-emission goals by making it difficult to premix the fuel and air and by requiring large amounts of excess air in order to limit the flame temperature. Technology directed toward overcoming these difficulties in order to achieve efficient and low-emission operation of thermal engines is described, for example, in U.S. Pat. No. 6,062,023 (Kerwin, et al.) issued May 16, 2000, and incorporated herein by reference.
External combustion engines are, additionally, conducive to the use of a wide variety of fuels, including those most available under particular local circumstances, however the teachings of the present description are not limited to such engines, and internal combustion engines are also within the scope of the present invention. Internal combustion engines, however, impose difficulties due to the typically polluted nature of the exhausted gases, and external combustion engines are preferably employed.
An embodiment of a power unit 2010 is shown schematically in
As shown in
Generator 2102 is coupled to a crankshaft (not shown) of Stirling engine 2101. It should be understood to one of ordinary skill in the art that the term generator encompasses the class of electric machines such as generators wherein mechanical energy is converted to electrical energy or motors wherein electrical energy is converted to mechanical energy. The generator 2102 is preferably a permanent magnet brushless motor. A rechargeable battery 2113 provides starting power for the power unit 2010 as well as direct current (“DC”) power to a DC power output 2112. In a further embodiment, APU 2010 also advantageously provides alternating current (“AC”) power to an AC power output 2114. An inverter 2116 is coupled to the battery 2113 in order to convert the DC power produced by battery 2113 to AC power. In the embodiment shown in
Utilization of the exhaust gas generated in the operation of power unit 2010 is now described with reference to the schematic depiction of an embodiment of the invention in
In accordance with alternate embodiments of the invention, adding heat to exhaust stream 2502 is within the scope of the invention, whether through addition of a post-burner (not shown) or using electrical power for ohmic heating.
During initial startup of the system, power unit 2010 is activated, providing both electrical power and hot exhaust. Warm-up of water purification unit 2012 is significantly accelerated since finned heat exchanger 2506 is initially below the dew point of the moisture content of the exhaust, since the exhaust contains water as a primary combustion product. All the heat of vaporization of this water content is available to heat source water as the water condenses on the fins of the heat exchanger. The heat of vaporization supplements heating of the fins by convection of hot gas within the still cavity. Heating of the fins by convection continues even after the fins reach the dew point of the exhaust.
In accordance with other embodiments of the present invention, power unit 2010 and water purification unit 2012 may be further integrated by streaming water from the purification unit through the power unit for cooling purposes. The use of source water for cooling presents problems due to the untreated nature of the water. Whereas using the product water requires an added complexity of the system to allow for cooling of the power unit before the purification unit has warmed up to full operating conditions.
Some specific embodiments of the present invention may improve upon the basic design of the liquid ring pump, particularly with respect to increasing overall energy efficiency by reducing frictional losses. A preferred embodiment of the present invention having a fully rotatable housing, that provides maximum reduction in frictional loss yet maintains simplicity of design and cost-effectiveness of production is shown in
Stator 9 has support structures 26 in the input and output regions, as seen in
Preferably, a liquid ring pump in accordance with the present invention is designed to operate within a fairly narrow range of input and output pressure, such that generally, the system operates in the range of from 5 to 15 psig. System pressure may be regulated using check valves to release steam from chamber 3 of
An alternative embodiment for a liquid ring pump is shown in
Another alternative embodiment of a liquid ring pump, wherein the interface between rotatable housing 10 and stator 9 is conical rather than cylindrical, is seen in
In addition, there may be either a conical or axial seal 13 present between stationary sections 6 and 7 and rotor 8. In the conical embodiment seen most clearly in
In alternative embodiments there is provided a vertical fixed housing having an inner rotatable housing (described above as rotatable housing 10) such as the cylindrical rotatable housing shown in
In related embodiments, the stationary housing 2810 is tapered and within it sits a tapered rotatable housing 2820 designed to be just smaller than fixed housing 2810 having fins/ribs 2830 such that there is a thin film of water under housing 2820, in the fixed housing. Examples of this embodiment are shown in
There may also be a (jewel) bearing pair 2910 between fixed housing 2810 and rotatable housing 2820, one half of the bearing pair 3010 rising up from the base of the fixed housing to an apex, the other half of the bearing pair being a convex point 3310 matched to the apex of the fixed housing so that the rotatable housing rests upon the fixed housing at this apex/convex point interface 2910 (see
For proper function, the bearing pair 2910 must stay wet, so the fluid level between the fixed housing and the rotatable housing must stay higher than the rotatable housing bottom. To help maintain a sufficient fluid level, a pitot tube 3320A (see
In addition, as the rotatable housing spins, the tapered sides may draw liquid up the sides of the rotatable housing, requiring a fluid return 3410 (see
In other related embodiments, the fins/ribs are vertically disposed along the inner surface of the rotatable housing, attached at a downwardly tapered angle and designed to offset the taper angle of the rotatable housing, thus providing fins that are effectively parallel to a true vertical (see
One particular embodiment of the cylindrical rotatable housing is designed to be mounted with a horizontal axis, as traditionally seen when hydrodynamic bearings are used. Another particular embodiment provides a cylindrical rotatable housing designed to be mounted with a vertical axis, as shown in
Embodiments described above, wherein the rotating housing acts as a large hydrodynamic bearing, eliminate the need for seals, bearings and a shaft for the rotatable housing, which in turn also dramatically reduces stress on the rotatable housing by eliminating overhang load. This enables the use of inexpensive manufacturing processes and simplifies liquid ring pump assembly.
In related embodiments, an impeller 3800 having multiple vanes 3810 and stacked annular horizontal cross-plates 3820 intersecting across the multiple vanes for stability (see
As can be seen in
The stacked annular horizontal cross-plates 3820 greatly decreases drag of multiple vanes 3810 along the liquid ring in rotatable housing improves the rigidity, and thus durability, of impeller 3800, and decreases root stress. Although the cross-plates extend to the end of the vanes in the embodiments depicted in
A top view of an assembled impeller 3800 with stop 4210 and valve plate 4400 within a rotatable housing (not visible) and a rotatable housing cover 2820 for the rotatable housing is shown in
During operation, impeller vanes 3810 cut off air flow during rotation, pressure builds, and a compression ratio is formed for controlling pressure in and out of impeller 3800. A variable compression ratio is achieved by controlling pressure into and out of impeller 3800, using flapper valves (not shown).
In another embodiment, a volcano valve may be used to automatically add water to maintain the liquid ring in the liquid ring pump automatically. In this embodiment, when the liquid ring no longer covers the volcano valve, the valve will automatically open, thereby allowing water to flow into the liquid ring. When the ring fills up, the volcano valve will become fully or at least partially covered and stop the flow of water into the liquid ring.
During operation, it may be desirable to measure the depth of the liquid ring in the compressor, to optimize performance. In the embodiments herein disclosed, liquid ring pump housing 10 rotates with the liquid ring in the pump, and the temperature of the liquid is typically around 110° C. Methods of measuring ring depth include any one of the usual methods, such as using ultra-sound, radar, floats, fluid conductivity, and optical sensors. Because of the complexities of the rotating housing, use of a capacitive sensor is a preferred embodiment for this measurement, wherein as the depth of the liquid in the capacitor changes, the capacitance of the capacitor also changes. As shown in
Alternatively, in another particular embodiment in accordance with the invention, it can be envisioned that a regenerative blower might be used in place of a liquid ring pump for compressor 100. An example of a possible regenerative blower that could be used instead of a liquid ring pump is the commercially available REGENAIR® R4 Series by GAST (e.g. models R4110-2/R4310A-2 et seq.), capable of operating at 52″ H2O maximum pressure, 92 cfm open flow, or 48″ H2O maximum pressure, 88 cfm open flow, respectively. See Appendix A, incorporated by reference herein.
To prevent contaminated liquid droplets from being entrained and carried along with vapor to condenser 200, pump 100 may be designed as shown in the alternative embodiment of
A particular embodiment of the mist eliminator is shown in
In other particular embodiments, the diverter cone may not be present, replaced by an input, which imparts rotating motion to the vapor entering the housing of the mist eliminator. For example, the input may have a thread-like inner surface such that as vapor is forced into the mist eliminator and wherein the threads impart rotational motion to the vapor. Other designs for the input may also impart rotational motion to entering vapor, such as a circular tunnel or corkscrew-like input designed for the entering vapor.
There is also a plurality of scales along the inner surface of the housing, forming an angle α of at least about 15 degrees relative to a longitudinal axis Z of the housing. The scales are situated to entrap liquid removed from suspension in vapor upon contact of the liquid with the scales. In one particular embodiment, the scales may be envisioned to be situated like inverted siding on a house, such that the top of each scale, angled 15° away from the vertical surface of the housing, overlaps the base of the scale above it. In addition, each scale is in fluid communication with a gap, or trough created by the overlap between the scale and the inner surface of the housing of a dimension adapted to draw liquid through the gap to a collection area. In particular embodiments, the gap may be between about 0.025 and 0.05 inches. Particular embodiments of the mist eliminator may also comprise a steam output for allowing steam to escape and/or a separator for collecting any liquid passing through the top of the mist eliminator. The plurality of scales may be attached to the inner surface of the housing by any attaching means, such as screws, brads, staples, adhesive resin, or any other suitable attaching means. Alternatively, the scales may be a feature of the surface of the inner housing, created by a molding process or other manufacturing process as a single piece. In yet another embodiment, the scales may be angled downward, like the siding on a house.
In a preferred embodiment, there may also be an actuator 150, such as a motor, for driving compressor/pump 100, as shown in
In one embodiment, motor 150 is a motor of the type designed to be run in steam and water, eliminating the need for shaft couplings and mechanical seals, thereby reducing drag and complexity in the mechanical components, and simultaneously allowing better recovery of motor power loss. In such an embodiment, motor rotor 37 (see
In a more preferred embodiment, motor rotor 37 is a solid material rotor such as pure iron or stainless steel, for example, a high-chromium content steel such as 446 stainless steel. The iron or steel rotors 37 may be nickel-plated, as may be magnets 37A. Pure iron rotors have the best magnetic properties, and improved torque relative to laminated rotors. Alternatively, solid stainless steel rotors with nickel-plated magnets may be used. Preferably the stainless steel has a high chromium content, thereby creating a coating of chrome oxide on the surface of rotor 37, which protects the iron content in the rotor from rust. As with pure iron rotors, stainless steel rotors also have improved torque over laminated rotors.
In yet another embodiment, the high-chromium content stainless steel rotor may be passivated to remove surface iron, creating a thick chromium oxide coating for enhanced corrosion protection. Other applied coatings may be used to aid in corrosion resistance. In addition, the nickel-plated magnets may be curved surface magnets, which will further increase motor torque and reduce manufacturing costs.
As shown in
A lower reservoir 30 containing a level of liquid, connects to a drain/fill fluid line (not shown), and houses siphon pump 32 and rotating housing bearings 52 about rotating housing shaft 53. Siphon pump 32 redirects liquid, preferably water, from lower reservoir 31 up siphon pump line 35 and continuing through siphon feed line 36 into chamber 12. As rotor 8 and liquid ring 19 rotate, water droplets 20 are flung by centrifugal force outwards, through a liquid ring overflow opening (not shown), against fixed housing 25, and then run down fixed housing wall 25 and back into lower reservoir 30.
Similarly,
A detailed view of siphon pump 32 can be seen in
Another specific embodiment of the present invention is designed to improve overall energy efficiency of the system, and is shown in
From exchanger 400, the intake line may continue in a cooling loop about motor 150, and then continue into core evaporator/condenser 600 wherein condenser 200 has a top core plate 48 and a bottom core plate 50. Within core evaporator/condenser 600 may be multiple parallel tubes 49, typically made of copper-nickel alloy or other heat-transferable material, having head manifold openings 56 to allow core tubes 49 to communicate with head 300, and having sump manifold openings 55 to allow tubes 49 to communicate with sump 500. Core tubes 49 are the heat exchange surface through which the latent heat of evaporation is transferred in the evaporation/condensation cycle. The rate at which heat can be exchanged between the condensing steam, outside the tubes, and evaporating water, inside the tubes, is a key factor in output rate and efficiency. If the thermal resistance of the heat exchange surface is low, better heat exchange occurs and output volume and efficiency increases. Any air impinged against the condensing surface becomes an insulator that inhibits transfer of heat. To prevent this, any air present in the system is continuously vented out of the system, via, for example, air vent 01, volatile mixer 23, or other venting outlets as required.
Heat transfer may also be adversely affected when water forms sheets as it condenses and coats the exterior of the tubes as it runs down to the bottom of the condenser chamber, a phenomenon known as “skinning.” The extent to which the water “skins” on the surface of the condenser is determined largely by the surface energy (hydrophobicity) of the heat transfer surface. In an embodiment of the present invention, hydrophobic coatings may be applied to cause condensing water to bead-up rather than skin, thereby leaving more of the heat transfer surface exposed for efficient heat transfer. Examples of suitable hydrophobic coatings include a coating manufactured by Ocular Technologies, or any other hydrophobic coating that imposes little to no thermal resistance itself.
Steam 21 from the evaporator section 600B of evaporator/condenser 600 may also feed into a volatile mixer 23 where volatile gases may be released from the system.
The system maintains a constant blowdown water flow to prevent scaling and other accumulation in the system. Water level 19 in head chamber 300 is adjusted through a feedback control loop using level sensor L1, valve V1, and source pump 00, to maintain proper water flow through the blowdown stream 43. The three-way source pump fill valve 29 is set to pump water into sump 500, which causes water level 19 in head chamber 300 to rise. As liquid level 19 rises in head chamber 300, liquid overflows past a dam-like barrier 302 into blowdown control chamber 301 containing blowdown level sensor L1. As required, blowdown valve V1 is controlled to allow water flow from blowdown control chamber 301 through heat exchanger 400, to extract heat and cool blowdown stream 43, and flow out valve V1, through volatile mixer 23 allowing cooling of hot gases and steam 21 from the evaporator section 600B, and then completing the blowdown stream, out to waste 43A.
The system also maintains proper product flow. Product level 502 builds up in condenser chamber 600C, and enters into product control chamber 501, where product level sensor L2 is housed. Using a feedback control loop with level sensor L2 and valve V2, product stream 41 is controlled to flow from product control chamber 501 through heat exchanger 400, to extract heat and cool product stream 41, then through valve V2 and on out to complete the product stream as product water outlet 41A.
The system may preferably be configured to maintain proper liquid ring pump water level by the use of a liquid recovery system to replenish liquid loss. There are several ways that liquid from the ring pump may be depleted during system operation, including leakage into lower reservoir 30, expulsion through exhaust port 6, and evaporation. The leakage and expulsion losses can be large depending on operational parameters, such as the speed of rotation and liquid ring pump throughput. These leakage and expulsion losses could require total replacement of the fluid in the pump several times per hour. The evaporation loss is typically small.
Liquid level in the ring pump can be maintained by adding additional source water, product water, or preferably by re-circulating liquid water lost from the liquid ring pump for improved system efficiency. In one preferred embodiment, the liquid level in the ring pump is primarily maintained by re-circulation of the liquid accumulated in lower reservoir 30 in
A minimum depth of water is preferably maintained in the lower reservoir for the siphon pump 32 to perform properly. In one preferred embodiment, liquid ring pump control chamber 101, which houses liquid ring pump level sensor L3 can be used to control the liquid ring pump level and control the level of water in the lower reservoir 30, as shown in
If re-circulated water from lower reservoir 30 is not primarily used to maintain the fluid level in the liquid ring pump, then either cold source water or product water could to be used. In the event source water were used, the introduction of cold water (which could be approximately 85 degrees C. colder than system temperature) may require the use of a pre-heater. Alternatively, product water can be used to maintain liquid ring pump fluid level, which would not adversely affecting the system temperature, although it could decrease production level. At startup, the initial fluid level for the liquid ring pump is preferably supplied from source water.
In one embodiment, the start-up time may be reduced by using an external connecting valve 43AA between source 39 and blowdown 43 fluid lines, located adjacent to heat exchanger 400, on the cold side, as shown in
The concentration of solids in blowdown stream 43 may be monitored and controlled to prevent precipitation of materials from solution and thus clogging of the system. Also during start-up, circulating pump 43BB can circulate water through heat exchanger 400 to pre-heat the heat exchanger to the proper temperature for normal operation. A conductivity sensor (not shown) may be used to determine total dissolved solid (TDS) content by measuring the electrical conductivity of the fluid. In a particular embodiment, the sensor is an inductive sensor, whereby no electrically conductive material is in contact with the fluid stream. If the TDS content in blowdown stream 43 rises above a prescribed level, for example, during distillation of sea water, the fluid source feed rate is increased. Increasing the fluid source feed rate will increase the rate of blowdown stream 43, because distilled water production changes only slightly as a function of fluid feed rate, and an increased blowdown stream rate results in reduced concentration of TDS, thereby maintaining overall efficiency and productivity of the system.
Another specific embodiment of the present invention is shown in
From exchanger 400, the source liquid 139 continues in a cooling loop about motor 150, and then continues into core evaporator/condenser 600 wherein condenser 200 has a top core plate 148 and a bottom core plate 150. Within core evaporator/condenser 600 may be multiple parallel tubes 149, typically made of copper-nickel alloy or other heat-transferable material, having head manifold openings 156 to allow core tubes 149 to communicate with head 300, and having sump manifold openings 155 to allow tubes 149 to communicate with sump 500. Core tubes 149 are the heat exchange surface through which the latent heat of evaporation is transferred in the evaporation/condensation cycle. The rate at which heat can be exchanged between the condensing steam, outside the tubes, and evaporating water, inside the tubes, is a key factor in output rate and efficiency. If the thermal resistance of the heat exchange surface is low, better heat exchange occurs and output volume and efficiency increases. Any air impinged against the condensing surface becomes an insulator that inhibits transfer of heat. To prevent this, any air present in the system is continuously vented out of the system, via, for example, vent 011, volatile mixer 123, or other venting outlets as required. Steam 121 from the evaporator section 600B of evaporator/condenser 600 may also feed into a volatile mixer 123 where volatile gases may be released from the system.
Heat transfer may also be adversely affected when water forms sheets as it condenses and coats the exterior of the tubes as it runs down to the bottom of the condenser chamber, a phenomenon known as “skinning.” The extent to which the water “skins” on the surface of the condenser is determined largely by the surface energy (hydrophobicity) of the heat transfer surface. In an embodiment of the present invention, hydrophobic coatings may be applied to cause condensing water to bead-up rather than skin, thereby leaving more of the heat transfer surface exposed for efficient heat transfer. Examples of suitable hydrophobic coatings include a coating manufactured by Ocular Technologies, or any other hydrophobic coating that imposes little to no thermal resistance itself.
The system maintains a constant blowdown liquid flow to prevent scaling and other accumulation in the system. Liquid level 119 in head chamber 300 is adjusted through a feedback control loop using level sensor L1, valve V1, and source pump 001, to maintain proper liquid flow through the blowdown stream 143. The three-way source pump fill valve V7 is set to pump liquid through source check valve V0 into sump 500, which causes liquid level 119 in head chamber 300 to rise. As liquid level 119 rises in head chamber 300, liquid overflows past a dam-like barrier 302 into blowdown control chamber 301 containing blowdown level sensor L1. As required, blowdown valve V1 is controlled to allow liquid flow from blowdown control chamber 301 through heat exchanger 400, to extract heat and cool blowdown stream 143, and flow out valve V1, through volatile mixer 123 allowing cooling of hot gases and steam 121 from the evaporator section 600B, and then completing the blowdown stream, out to waste 143A.
The evaporation/condensation level between liquid sump 500 and vapor in head 300 is maintained/adjusted through a feedback control loop using level sensor L2, vent check valve V2, and vent 011, to maintain proper liquid/vapor ratios in evaporator/condenser 600. Liquid from sump 500 flows over barrier 703 into evaporator level sensor chamber 701 containing evaporator level sensor L2. As needed, vapor either flows over barrier 702 into head 300, or is vented via vent line 011 by vent check valve V2 or directed to volatile mixer 123 via condenser vent valve V8.
The system also maintains proper product flow. Product level 502 builds up in condenser chamber 600C, and enters into product control chamber 501, where product level sensor L2 is housed. Using a feedback control loop with level sensor L2 and valve V2, product stream 141 is controlled to flow from product control chamber 501 through heat exchanger 400, to extract heat and cool product stream 141, then through valve V2 and on out to product divert valve V6, where product is removed as product outlet stream 141A, or as diverted product outlet stream 141B.
The system may preferably be configured to maintain proper liquid ring pump water level by the use of a liquid recovery system to replenish liquid loss. There are several ways that liquid from the ring pump may be depleted during system operation, including leakage into lower reservoir 30 (not shown in
Thus, the liquid level in the ring pump may be maintained by adding additional source water, product water, or preferably by re-circulating liquid water lost from the liquid ring pump for improved system efficiency. In one preferred embodiment shown in
In another preferred embodiment, the liquid level in the ring pump is primarily maintained by re-circulation of the liquid accumulated in lower reservoir 30 (shown in
A minimum depth of water is preferably maintained in the lower reservoir for the siphon pump 32 to perform properly. In one preferred embodiment, liquid ring pump control chamber 101, which houses liquid ring pump level sensor L3 can be used to control the liquid ring pump level and control the level of water in the lower reservoir 30, as shown in
If re-circulated water from lower reservoir 30 is not primarily used to maintain the fluid level in the liquid ring pump, then either cold source water or product water could to be used. In the event source water were used, the introduction of cold water (which could be approximately 85 degrees C. colder than system temperature) to the liquid ring pump may require use of a pre-heater. Alternatively, the use of product water can be used to maintain the fluid level in the liquid ring pump 100, as shown in
As discussed in relationship to
Flow rate through the variable flow control valves and from the input pump can be determined using an in-situ calibration technique. The level sensors and associated level sensor volume can be used to determine the fill or empty rate of the sensor volume. By appropriately configuring the control valves, the flow rate calibration of each valve and also of the source pump can be determined. For example, one embodiment employs a self-calibrating level sensor, which has a built-in non-constant geometry so that discontinuity can be detected using a constant (or nearly constant) rate fill. With prior knowledge of the expected geometry, the fill rate may not need to be precisely controlled.
In a particular embodiment of the invention, a valve block (not shown) may be utilized to consolidate all control valves for the system into a single part, which may be integrated with the fluid flow manifold. A control system comprising a sensor for total dissolved solids and blowdown stream may also be incorporated, as well as a float valve or other device for controlling the height/level of liquid in the head.
As shown in
Further, there may be a heater 900 with heating element 60 for heating cold liquid to boiling at start-up, and for maintaining sufficient heat during operation of the still to continuously convert liquid to steam. In one embodiment of the invention, the distillation system may operate at steady-state without thermal input from the heater 900 after system start up. Alternatively, a second heater (not shown) may be used to maintain sufficient heat during operation; the heater may run continuously, in a pulsed mode, or be controlled by a controller.
In one particular embodiment, evaporator/condenser 600 is evaporator/condenser 600A having elastomer tube and shell seals 54A and 54B for core tubes 49, as shown in
In yet another particular embodiment in accordance with the invention there may be an evaporator/condenser 650, as shown in
In addition, another particular embodiment in accordance with the invention may include fluid distribution manifold 675, shown in
Finally,
In such a particular embodiment, a fluid distribution manifold 675 is capable of eliminating most plumbing in a liquid purification system, advantageously incorporating various functionality in one unit, including flow regulation, mist removal, and pressure regulation, thereby simplifying manufacture and significantly reducing overall component parts. The core plates and manifolding may be made of, for example, plastic, metal, or ceramic plates, or any other non-corrosive material capable of withstanding high temperature and pressure. Methods of manufacture for the core plates and manifolding include brazing and over-molding.
For either core 600 having core tubes 49, or core 650 having parallel core layers 92 and 94, the geometry of the core tubing or layer channels may be cylindrical, square, rectangular, and the like. In still another specific embodiment in accordance with the present invention, core configurations may be selected to increase the net phase change rate of the liquid, and may include core inserts, which are more fully detailed in U.S. patent application Ser. No. 10/636,303 filed Aug. 7, 2003 entitled “Method and Apparatus for Phase Change Enhancement,” the contents of which are hereby incorporated by reference herein.
Scale control may be achieved using chemical treatments such as with polyphosphates or polyaspartates, via plasma coating of appropriate components through the use of galvanic or electrochemical processes, by treatment with acids such as an organic acid, or through the use of electric and/or magnetic fields.
Other particular embodiments of the present invention may advantageously improve energy efficiency of the overall system by including, for example, highly efficient heat exchangers 400A and 400B as shown in
Alternatively, a single multi-channel heat exchanger 400B such as depicted in
As discussed above, tube bundle heat exchanger technology detailed in U.S. Pat. No. 4,520,868 may be utilized for the heat exchangers in accordance with the present invention, wherein elastomeric end plates may be used to seal the tubes in a fixed orientation, in place of metal or otherwise inelastic end plates soldered or brazed to the heat exchanger tubes.
As discussed above with respect to
If an external drive shaft motor is utilized, the overall system may employ an additional “cold” fluid pump of the gear-, diaphragm-, or “ram-” pump variety inline with cold intake line. In a particular embodiment, such a pump will be driven off the same rotor drive shaft as the liquid ring pump. Other particular embodiments of the present invention may also be envisioned without a fluid intake pump, whereby a gravity-feed mechanism or creation of a vacuum is used to drive the fluid through the system.
In another particular embodiment, sump 500 may employ a pre-heater or supplemental heater, wherein a switch and temperature sensor with relay monitor is employed to regulate heat input and temperature of the water in the sump. Other fluid reservoirs may also contain temperature sensors. For example, a temperature sensor in the sump could be used to determine optimum conditions for the initiation of distillation as the still heats up. Temperature sensors may also be employed to detect changes in water temperature, thereby allowing adjustment of fluid flow rates to maintain overall still production.
In one embodiment, shown in
Still another embodiment of the present invention is designed to increase the purity of the final purified liquid product by incorporating a filtering mechanism within intake 00, as shown in
In another embodiment, the multi-unit flip filter may be a multi-sected circular filter 80B, shown schematically in
Alternatively, a manual valve 85, such as shown schematically in
In another particular embodiment, not shown, there may be an external system including a holding tank with a pump for waste discharge, if circumstances require.
The particular embodiments described above generally operate above atmospheric pressure, typically around 10 psig. Such a system advantageously provides higher steam density at the higher pressure, thereby allowing more steam to be pumped through a positive displacement pump than at lower pressure. The resulting higher throughput provides overall improved system efficiency. Further, the higher throughput and higher system pressure reduces the power needed for compressor 100, and eliminates the need for two additional pumps—one for pumping condensed product 41 and another for pumping blowdown stream 43. Overall construction is simplified, as many shapes withstand internal pressure better than external pressure. Importantly, operating at super-atmospheric pressure reduces the impact of minor leaks on the overall efficiency and performance. Non-condensable gases such as air inhibit the condensation process, and would be magnified at sub-atmospheric pressure, where minor leaks would serve to suck in air, something which will not occur in a system operating at super-atmospheric pressure.
When embodiments of the invention operate above atmospheric pressure, the use of a novel backpressure regulation may serve to control the operating pressure of the system.
In operating the embodiment shown in
In the embodiment of
Adjustment of the backpressure regulator set point may be useful, when the backpressure regulator is utilized in systems at higher altitudes. When the atmospheric pressure is lower, the system operating pressure is commensurately lower. As a result, the temperature of the distillation apparatus is lowered, which may adversely affect system performance. As well, such adjustment allows one to identify set points for the backpressure regulator that are desired by the end user. The use of a counter mass to apply the closing force may also lower cost of the backpressure regulator and reduce component fatigue. In a particular embodiment of the invention, the adjustable counter mass is designed to allow a range of set points with a lowest set point substantially less than or equal to 10 psig. and a highest set point substantially greater than or equal to 17 psig. Thus embodiments of the invention allow for precise system pressure regulation, unlike devices, which act simply as safety relief valves.
In another embodiment of the invention shown in
In an embodiment of the invention shown in
The backpressure regulator may be configured to allow a small leakage rate below the set point in order to purge the build up of volatile gases that act to insulate heat exchange and suppress boiling in a system; the regulator is designed, however, to allow pressure to build in the pressurized conduit despite this small leakage. In an embodiment of the invention, release of volatile components from a pressurized conduit, below the set point of the backpressure regulator, may also be achieved through a specifically-designed leak vent while the arm of the backpressure regulator is in the closed position. The leak vent is configured to allow a certain leakage rate from the port or the orifice while the pressure in the conduit is below the set point. Such leak vent may be designed by a variety of means known to those skilled in the art. Non-limiting examples include specific positioning of the stop and port to allow a small opening while the arm is in the closed position; designing the port such that a small opening, not coverable by the stop, is always exposed; specifying a particular rigid, non-compliant seal configuration between the stop and port when the arm is in the closed position; and configuring the orifice leading to the port to have a small opening to allow leakage of fluids.
In a particular embodiment of the invention directed toward the leakage of volatiles below the set point of the backpressure regulator, the port 1410 has a small notch 1420 as shown in
Various features of a backpressure regulator consistent with embodiments of the invention may be altered or modified. For example, stops to be used with backpressure regulators may have any shape, size, or mass consistent with desired operating conditions, such stops need not be ball-shaped as shown in some embodiments of the invention discussed herein. As well, stops of different weight but similar sizes may be utilized with the retainer to alter the set point of the regulator. Similarly, counter masses of different sizes, shapes and masses may be utilized with embodiments of the invention as long as they are accommodated by the axis and arm configurations (compare 1180 in
Embodiments of the invention may optionally utilize the drain orifice feature described earlier. Also, embodiments of the invention may not utilize the counter mass force adjustment feature, relying on the specific properties of a stop to provide the set point for the backpressure regulator.
Other embodiments of the invention may not utilize a vessel, but rely on orifices that are intrinsically part of the system. In such instances, the backpressure regulator arm may be directly attached to a portion of the system such that the arm, stop, and counter mass are appropriately oriented for the operation of the regulator.
Cassettes suitable for use in the present liquid distillation system include valve cassettes disclosed in U.S. Pat. No. 6,464,667 the entire contents of which are incorporated by reference herein. The valve cassette, which is preferably pneumatically operated by a control assembly, includes various combinations of membrane-based chambers and valves. The cassette preferably includes, along the fluid passage through the cassette, one or more membrane based valves. A first and second rigid member are in an open position with respect to each other, with a sealing member defining an aperture through which fluid communication is provided. The membrane defines the valving chamber and the second membrane-based valve is preferably resilient, so that the valving chamber may provide a supply of pressurized fluid, when the valve is closed.
In the preferred embodiment valve stations are closed on the back side of the cassette, except that each valve station includes a pair of through holes for ports. One port communicates with a selected liquid path on the back side of the cassette, the other port communicates with another selected liquid or pneumatic path on the back side of the cassette.
It is preferred that the valve be made by molding a resilient material about and to the second rigid member so as to form an aperture sealing member about the port on the complementing surface of the second rigid member, and then assembling the first and second rigid members, which are preferably molded out of a rigid material, so as to bring the complementing surfaces adjacent each other and so that the sealing member is urged against the complementing surface of the first rigid surface.
In a preferred version of the cassette, which is primarily made out of rigid material, the membrane for the membrane-based valves is disposed adjacent the housing, such that the rigid housing and the membrane define a valving chamber. One passage enters the valving chamber at a first mouth located at the end of a protrusion of the rigid housing and the valving chamber toward the membrane and the valve may prevent the flow of fluid therethrough when the membrane is forced against the first mouth, by the control unit.
Embodiments described in the above references pump fluid using a valve cassette such as shown in
As can be seen in
The pump cassette 5602 is typically designed to interface with the control assembly in one or more directions, as needed. Pump cassette 5602 depicted in
The various valves 5620-5626 depicted in
A control assembly capable of operating the pump cassette 5602 is utilized in conjunction with pump cassette 5602. The control assembly includes pneumatic pathways that interface with a receiving surface through which pump cassette 5602 is operated. The receiving surface may be, without limitation, a bezel gasket that is part of a bezel assembly. During operation, pump cassette 5602 is aligned and pressed against the bezel gasket by a movable member. Air lines connected to the bezel assembly are controlled pneumatically, and used to displace membranes of the bezel gasket to operate the various valves and chambers of pump cassette 5602.
Alternative embodiments of the system may employ fluid management system pumps, such as reciprocating positive-displacement pumps wherever an accessory pump is required or desired. For example, siphon pump 32 (see
In one embodiment the pod pump is a reciprocating positive-displacement pump with a hemispherical rigid chamber wall; a flexible membrane attached to the rigid chamber wall, so that the flexible membrane and rigid chamber wall define a pumping chamber; an inlet for directing flow through the rigid chamber and an outlet for directing flow through the rigid chamber wall out of the pumping chamber. A reciprocating positive-displacement pump is provided comprising a rigid hemispherical chamber wall; a flexible membrane attached to the rigid chamber wall, so that the flexible membrane and rigid chamber wall define a pumping chamber; an inlet for directing flow through the rigid chamber wall into the pumping chamber in a direction that is substantially tangential to the rigid chamber wall; and an outlet for directing flow through the rigid chamber wall out of the pumping chamber in a direction that is substantially tangential to the rigid chamber wall. In other embodiments, the reciprocating positive-displacement pump also includes a rigid limit structure for limiting movement of the membrane and limiting the maximum volume of the pumping chamber, the flexible membrane and the rigid limit structure defining an actuation chamber. The rigid limit structure is preferably adapted to limit movement of the flexible membrane such that, when the pumping chamber is at maximum volume, the rigid chamber and the flexible membrane (which will be urged against the rigid limit structure) define the pumping chamber as a spherical volume. The rigid limit structure is preferably a hemispherical limit wall that, together with the flexible membrane, defines a spherical actuation chamber when the pumping chamber is at minimum volume.
As described above, various embodiments of this invention may advantageously provide a low-cost, easily maintained, highly efficient, portable, and failsafe liquid purification system that can provide a reliable source of drinking water for use in all environments regardless of initial water quality. The system of the present invention is intended to produce a continuous stream of potable water, for drinking or medical applications, for example, on a personal or limited community scale using a portable power source and moderate power budget. As an example, at the desired efficiency ratio, it is envisioned that the present system may be utilized to produce approximately 10 gallons of water per hour on a power budget of approximately 500 watts. This may be achieved through a very efficient heat transfer process and a number of sub-system design optimizations.
Knowledge of operating temperatures, TDS, and fluid flows provides information to allow production of potable water under a wide range of ambient temperatures, pressures, and dissolved solid content of the source water. One particular embodiment may utilize a control method whereby such measurements (T, P, TDS, flow rates, etc) are used in conjunction with a simple algorithm and look-up table allowing an operator or computer controller to set operating parameters for optimum performance under existing ambient conditions.
Embodiments of the present invention may be described and used as indicated in the following listing, which is neither exhaustive nor limiting:
1. An improved mist eliminator having a top, a bottom and a housing wherein liquid is removed from suspension in vapor to an inner surface of the housing, the improvement comprising:
a plurality of vanes disposed along a diverter cone, wherein the diverter cone is situated at the bottom of said mist eliminator and wherein the vanes are angled to create a rotating motion to the vapor in the housing;
a plurality of scales forming an angle α at least about 15 degrees relative to a longitudinal axis Z of the housing, wherein the scales are situated to entrap liquid removed from suspension in vapor upon contact of the liquid with the scales, each scale in fluid communication with a gap between the scale and the inner surface of the housing of a dimension adapted to draw liquid through the gap to a collection area.
2. An improved mist eliminator having a top, a bottom and a housing wherein liquid is removed from suspension in vapor to an inner surface of the housing, the improvement comprising;
an input which imparts rotating motion to the vapor entering the housing of the mist eliminator;
a plurality of scales situated to entrap liquid removed from suspension in vapor upon contact of the liquid with the scales, each scale being disposed at an angle at least about 15 degrees relative to a longitudinal axis Z of the housing and having a protruding edge and a bottom edge, wherein the protruding edge forms a gap between the scale and the inner surface of the housing, each scale in fluid communication with the gap, and wherein the gap is of a dimension adapted to draw liquid through the gap to a collection area.
3. A mist eliminator according to claim 1 or 2, wherein the dimension of the gap between each of the plurality of scales and the inner surface of the housing is between about 0.025 to about 0.050 inches.
4. A mist eliminator according to claim 1 or 2, further comprising steam output for allowing steam to escape.
5. A mist eliminator according to claim 1 or 2, further comprising a separator for collecting any liquid passing through the top of the mist eliminator.
6. A method for eliminating entrained liquid from vapor comprising:
contacting the vapor with a mist eliminator having a plurality of vanes on a diverter cone within a housing situated to create a rotating motion to the vapor;
discharging rotating vapor from the plurality of vanes on the diverter cone;
entrapping the liquid from the discharged vapor on a plurality of scales within the housing, each scale forming an angle α relative to a longitudinal axis Z of the housing;
propelling the liquid from the plurality of scales through a gap between each scale and the inner surface of the housing to a collection area.
7. A method according to claim 6, wherein the gap has a diameter of between about 0.025 and about 0.05 inches.
8. A method according to claim 6, wherein the angle α of each scale relative to the Z axis of the inner surface of the housing is at least about 15 degrees.
9. A method according to claim 6, further comprising recycling liquid from the collection area to the mist eliminator.
10. A method according to claim 6, further comprising venting steam from the mist eliminator.
11. A method according to claim 6, further comprising providing a vapor/liquid separator coupled with the mist eliminator.
12. A mist eliminator according to claim 6, wherein the plurality of scales are made of plastic.
13. A liquid distillation system comprising:
an input for receiving untreated liquid;
a vaporizer coupled to the input for transforming the liquid to vapor;
a vapor pump for compressing the vapor;
a condenser in communication with the vapor pump fro transforming compressed vapor into a distilled liquid product; and
a mist eliminator having a diverter cone within a housing, the diverter cone having a plurality of vanes, wherein the housing has a plurality of scales for entrapping liquid and removing it from the vapor.
14. A liquid distillation system operating at a thermal steady-state after start-up, the system comprising:
an input for receiving untreated liquid;
a vaporizer coupled to the input for transforming the liquid to vapor;
a vapor pump for compressing the vapor;
a condenser in communication with the vapor pump for transforming compressed vapor into a distilled liquid product; and
a motor for driving the vapor pump, wherein heat supplied to the vaporizer originates in the motor.
15. A liquid distillation system comprising:
an input for receiving untreated liquid;
a vaporizer coupled to the input for transforming the liquid to vapor;
a liquid ring vapor pump for compressing the vapor;
a condenser in communication with the vapor pump for transforming compressed vapor into a distilled liquid product;
a shaft located inside a rotating housing for the system;
internal bearings.
16. A system according to claim 15, further comprising a motor can and motor stator located outside the pressure and fluid boundary for the system.
17. A system according to claim 15, further comprising a single shaft spanning from the motor to the pump.
18. A system according to claim 13, wherein the system comprises a rotatable housing inside the fixed housing, the fixed housing and rotatable housing each having a diameter such that the diameter of the rotatable housing is smaller than the diameter of the fixed housing.
19. A system according to claim 18, further comprising a bearing between the rotatable housing and the fixed housing.
20. A system according to claim 19, wherein the bearing is a hydrodynamic bearing.
21. A system according to claim 19, wherein the bearing is a jewel bearing.
22. A system according to claim 19, wherein the bearing comprises an annular shelf between an exterior surface at the bottom of the rotatable housing and an interior surface at the bottom of the fixed housing.
23. A system according to claim 19, wherein a thin film of water between the rotatable housing and the housing elevates the rotatable housing and acts as the hydrodynamic bearing for the rotatable housing and fixed housing as the rotatable housing rotates.
24. A system according to claim 18, wherein the rotatable housing and the housing are tapered, decreasing from top to bottom.
25. A system according to claim 18, further comprising an apex rising from an interior surface of the bottom of the housing and a convex point on an exterior surface of the bottom of the rotatable housing, the convex point of the rotatable housing resting on the apex of the fixed housing such that during rotation, the rotatable housing rotates about a single point of contact between the convex point of the rotatable housing and the apex of the fixed housing.
26. A system according to claim 25, wherein the convex/apex point of contact comprises a jewel bearing between the fixed housing and the rotatable housing.
27. A system according to claim 22, wherein the bearing is plastic or ceramic.
28. A system according to claim 18, wherein the rotatable housing has an interior surface comprising a plurality of vertical fins.
29. A system according to claim 18 further comprising an impeller within the rotable housing, wherein the impeller has a plurality of vanes designed to engage the vertical fins of the rotatable housing.
30. A system according to claim 29, wherein the plurality of vanes are oblique to a central axis of rotation for the impeller.
31. A system according to claim 29, wherein the impeller further comprises at least one annular horizontal cross-plate intersecting the plurality of vanes.
32. A system according to claim 29, wherein the impeller is mechanically connected to a shaft which rotates the impeller and the impeller further comprises a stop to prevent the impeller from riding up the shaft during rotation.
33. A system according to claim 32, wherein the shaft further comprises a seal, a collar, a spring or any combination thereof above the impeller.
34. A system according to claim 33, wherein the shaft further comprises a seal below the impeller.
35. A system according to claim 29, wherein the rotatable housing further comprises a rotatable housing cover.
36. A system according to claim 18, wherein the housing is fixed.
37. A system according to claim 36, further comprising a pitot tube connecting to an exterior wall of the housing into the liquid ring pump at a height determined to be a minimum level for a liquid ring during operation of the liquid ring pump.
38. A system according to claim 36, further comprising a pitot tube connecting to an exterior surface at the bottom of the rotatable housing.
39. A liquid distillation system according to any of claims 13-38 further comprising a fluid management system pump driven by any of vapor, air or liquid for controlling scale, pressure, liquid level in the vapor pump and/or for pre-treating the untreated liquid.
40. A level sensor for controlling fluid flow of a liquid in a liquid distillation system during distillation, the level sensor coupled with a variable flow valve controlled by fluid level in the system.
41. A level sensor according to claim 40 wherein the sensor is a self-calibrating level sensor for maintaining a liquid level in a liquid distillation system, the self-calibrating sensor having a sensor level and a non-constant geometry a known distance from the sensor level [for comparing fill rate versus distance to the sensor level].
42. A level sensor according to claim 40 or 41 wherein the level sensor is a capacitive level sensor.
43. A level sensor according to claim 40 further comprising a pre-set control sensor level.
44. A method of monitoring conductivity of a liquid during distillation, the method comprising:
measuring the conductivity of the liquid during distillation at a particular point in time to obtain a magnitude of the conductivity of the liquid at the particular point in time;
comparing the magnitude of the conductivity of the liquid at the particular point in time to a pre-determined target magnitude for the conductivity.
45. A method of monitoring conductivity in a distilled liquid product according to claim 44, the method further comprising:
adjusting the conductivity of the liquid during distillation until the magnitude of the conductivity is within an acceptable range of the pre-determined target magnitude for the conductivity.
46. A method according to claim 44, wherein the magnitude of the conductivity of the liquid at the particular point in time is indicative of total dissolved materials in the liquid at the particular point in time.
47. A method according to any of claims 44-46 wherein monitoring conductivity is coupled with using a level sensor.
48. A system according to claim 47, wherein the vapor pump is a liquid ring pump and the fluid management system pump controls fluid in the liquid ring pump.
49. A method of controlling fluid in a vapor pump of a liquid distillation system, the method comprising:
driving a fluid management system pump with vapor from the distillation system;
controlling pressure within the vapor pump with at least one valve;
adding liquid to the vapor pump with the fluid management system pump as needed.
50. A method according to claim 49, further comprising determining the amount of liquid to add to the vapor pump with a level sensor.
51. A fluid distribution manifold coupled to a liquid distillation system, the manifold comprising means for regulating flow of fluid within the system.
52. A fluid distribution manifold coupled to a liquid distillation system, the manifold comprising means for eliminating liquid entrained in a vapor within the system.
53. A fluid distribution manifold coupled to a liquid distillation system, the manifold comprising means for controlling pressure within the system.
54. A fluid distribution manifold coupled to a liquid distillation system, the manifold comprising means for regulating flow of fluid with the system;
means for eliminating liquid entrained in a vapor with the system; and
means for controlling pressure within the system.
55. A liquid distillation system comprising:
an input for receiving untreated liquid;
a vaporizer coupled to the input for transforming the liquid to vapor;
a head chamber for collecting vapor from the vaporizer;
a vapor pump for compressing the vapor, the vapor pump comprising:
an internal drive shaft; and
an impeller within a rotatable housing;
fixed housing for the rotatable housing; and
a condenser in communication with the vapor pump for transforming compressed vapor into a distilled liquid product.
56. The liquid distillation system as in claim 55 wherein the impeller further comprises a plurality of vanes separated by chambers, each chamber having an intake and an exit.
57. A liquid distillation system according to claim 55 wherein the input is coupled to at least one heat source.
58. A liquid distillation system according to claim 55 further comprising a sump wherein liquid from the vaporizer may be preheated at start-up.
59. A liquid distillation system according to claim 58 wherein the vaporizer has a plurality of parallel tubes, each tube having a first open end in communication with the sump and a second open end in communication with the head chamber.
60. A liquid distillation system according to claim 59 further comprising a regulator for maintaining a liquid level sufficient to permit both purification of liquid from the core vaporizer tubes.
61. A liquid distillation system according to claim 55, the system further comprising a regulator for maintaining and controlling pressure in the condenser.
62. A liquid distillation system according to claim 55 further comprising an output for collection of condensed liquid product and further in connection with the input for recycling the blowdown stream.
63. A liquid distillation system according to claim 55 further comprising a pre-treatment assembly coupled to the intake.
64. A liquid distillation system according to claim 63 wherein the liquid pre-treatment assembly performs at least one of a plurality of treatments including filtering, degassing, chemical modification, UV light exposure, treatment with polyphosphates, polyacetates, polyaspartates, organic acids, acidification including addition of CO2 from an external engine, exposure to an oscillating electric field, and any other suitable pre-treatment process.
65. A liquid distillation system according to claim 55, the system further comprising a heating unit for heating intake liquid upon startup.
66. A liquid distillation system according to claim 65, the system further comprising a switch including a thermostatic switch, pressure-sensing switch or related thermal or pressure transducer for signaling completion of the heating phase and turning off the heating unit.
67. A liquid distillation system according to claim 55 further comprising a heat exchanger for receiving liquid from the input such that heat from at least one source is exchanged with the input liquid.
68. A liquid distillation system according to claim 67 wherein the at least one heat source includes the product stream, the blowdown stream, system waste heat, vapor pump waste heat, motor waste heat, engine exhaust heat from a power source, and an external heat source.
69. A liquid distillation system according to claim 67 wherein the heat exchanger is a multi-line exchanger for exchanging heat from a plurality of sources with the input liquid.
70. A liquid distillation system according to claim 55 wherein the drive includes an electric motor.
71. A liquid distillation system according to claim 55 wherein the vaporizer includes an electrical heater.
72. A liquid distillation system according to claim 55, the system further comprising a multi-unit filter having at least two units in the input for filtering the liquid before the liquid is received by the vaporizer.
73. A liquid distillation system according to claim 72 wherein the filter is a flip-filter.
74. A liquid distillation system according to claim 72 further comprising a diverter whereby the filter is back-washed by a blowdown stream diverted from the head chamber.
75. A liquid distillation system according to claim 73 further comprising a regulator coupled to the diverter for providing the minimum flow rate of blowdown stream necessary to back-wash the filter.
76. A liquid distillation system according to claim 73, the system further comprising a mechanism for periodically rotating the flip-filter at appropriate intervals for back-washing filter units to prevent fouling.
77. A liquid distillation system according to claim 74, the system further comprising a switch for changing the direction and source of liquid flowing through the filter for back-washing to prevent fouling.
78. A liquid distillation system according to claim 55 further comprising a power source coupled to the system wherein the power source is a clean-burning generator.
79. A liquid distillation system according to claim 69 wherein the at least one of a plurality of heat sources includes the product stream, the blowdown stream, system waste heat, vapor pump waste heat, motor waste heat, exhaust heat from a power source, and an external heat source.
80. A liquid distillation system comprising:
an input for receiving untreated liquid;
a vaporizer coupled to the input for transforming the liquid to vapor;
a head chamber for collecting vapor from the vaporizer;
a vapor pump for compressing the vapor, the vapor pump comprising:
a condenser in communication with the vapor pump for transforming compressed vapor into a distilled liquid product.
81. A method for distilling a liquid using a system as claimed in any of claims 55-80, the method comprising:
vaporizing untreated liquid in a vaporizer to form a vapor in such a way as to fill a head chamber;
compressing the vapor by rotating the vapor within the head chamber using an internal drive shaft and impeller within a rotatable housing; and
condensing the compressed vapor into a distilled liquid product.
82. A method of distilling a liquid according to claim 81, further comprising using a pod pump for any one of: regulating the internal pressure of the condenser; maintaining a super-atmospheric pressure; maintaining a liquid level in the head chamber sufficient to permit purification of liquid; regulating a blowdown stream from the head chamber; priming the system before start-up; adjusting a source feed rate of untreated liquid if total dissolved material is above a prescribed level; pumping untreated liquid into the vaporizer; venting air on an outlet side of the pump; and re-priming the pump when the evaporator is pressurized.
83. A method of distilling a liquid according to claim 82, further comprising eliminating entrained liquid droplets from the vapor in the vapor pump
84. A method of distilling a liquid according to claim 82, further comprising using a vaporizer connected to a sump, said vaporizer having a plurality of parallel tubes, each tube having a first end in communication with the sump and a second end in communication with the head chamber.
85. A liquid distillation system according to claim 81 wherein the vapor pump further comprises a liquid ring pump and the system further comprises a volatile mixer to cool hot gases and release volatiles.
86. A liquid distillation system according to claim 55 or 80, further comprising:
a pump for pumping untreated liquid into the vaporizer;
an air vent on an outlet side of the pump; and
a valve;
wherein the pump, air vent, and valve are configured in a loop permitting re-priming of the pump when the evaporator is pressurized, the pump is a volcano pump or pod pump, and the valve is a volcano valve or flapper valve.
87. A liquid distillation system according to any one of claims 13, 18-38, or 55-80, further comprising an accessory pump for maintaining sufficient liquid in a sump wherein the pump is a volcano pump or pod pump.
88. A liquid distillation system according to any one of claims 13, 18-38, or 55-80, further comprising an accessory pump for pumping liquid from the input, wherein the pump is a volcano pump or pod pump.
89. A liquid distillation system according to any one of claims 13, 18-38, or 55-80, further comprising an accessory pump for circulating liquid in the distillation system wherein the pump is a volcano pump or pod pump.
90. A liquid distillation system according to any one of claims 13, 18-38, or 55-80, further comprising an accessory pump for pumping a blowdown stream wherein the pump is a volcano pump or pod pump.
91. A liquid distillation system according to any one of claims 13, 18-38, or 55-80, further comprising an accessory pump for pumping condensed product wherein the pump is a volcano pump or pod pump.
92. A liquid distillation system according to any one of claims 13, 18-38, or 55-80, further comprising an accessory pump for circulating liquid in the distillation system wherein the pump is a volcano pump or pod pump.
93. A liquid distillation system according to any one of claims 13, 18-38, or 55-80, further comprising an accessory pump for pumping volatile gases from a volatile mixer wherein the pump is a volcano pump or pod pump.
94. A liquid distillation system according to any one of claims 13, 18-38, or 55-80, further comprising an accessory pump for pumping air through a filter wherein the pump is a volcano pump or pod pump.
95. A liquid distillation system according to any one of claims 13, 18-38, or 55-80, further comprising an accessory pump for pumping liquid in fluid communication with a fluid distribution manifold wherein the pump is a volcano pump or pod pump.
96. A liquid distillation system according to any one of claims 13, 18-38, or 55-80, further comprising an accessory pump for adding liquid to the liquid ring pump wherein the pump is a volcano pump or pod pump.
97. A liquid distillation system according to any one of claims 13, 18-38, or 55-80, further comprising an accessory pump to aid in pressure control in the liquid ring pump wherein the pump is a volcano pump or pod pump.
98. A liquid distillation system according to any one of claims 13, 18-38, or 55-80, further comprising an accessory pump to aid in scale control in the liquid distillation system wherein the pump is a volcano pump or pod pump.
Furthermore, while the invention has been described in connection with specific embodiments thereof, it will be understood that it is capable of further modification as will be apparent to those skilled in the art. All such variations and modifications are intended to be within the scope of the present invention as defined in the specification.
This application is a continuation-in-part of U.S. patent application Ser. No. 10/713,617 filed Nov. 13, 2003 which claims priority from U.S. Provisional Patent Application Ser. No. 60/425,820 filed Nov. 13, 2002 and U.S. Provisional Patent Application Ser. No. 60/490,615 filed Jul. 28, 2003 and U.S. Provisional Patent Application Ser. No. 60/518,782 filed Nov. 10, 2003, each of which is incorporated herein by reference.
| Number | Date | Country | |
|---|---|---|---|
| 60425820 | Nov 2002 | US | |
| 60490615 | Jul 2003 | US | |
| 60518782 | Nov 2003 | US |
| Number | Date | Country | |
|---|---|---|---|
| Parent | 10713617 | Nov 2003 | US |
| Child | 11480294 | Jun 2006 | US |
