With the availability of heat engines utilizing a fully regenerative phase-change thermodynamic cycle, it is possible to convert the thermal energy contained in a uniform-temperature environment directly to mechanical or electrical energy (see PCT/US11/41289 Thermal Engine Capable of Utilizing Low-Temperature Sources of Heat, inventor Neil Tice, and U.S. Pat. No. 7,816,601 Device and method for converting thermal energy into electrical energy, inventor David Reginald Carver) without the need for an additional reservoir of a cooler temperature in which to dump waste heat. The key component of this type of engine is a working medium consisting of a material which undergoes a first phase change while absorbing latent heat of transformation, then undergoes a return phase change to complete the cycle.
Any phase change from one state to another, including from one solid state to another solid state, for example, can be used to convert heat to another form of energy. Many of the potential phase transitions involve a change from one fluid state to another fluid state. Fluid in this sense means the ability to flow, and is not restricted to liquids. Examples may include liquid to vapor, liquid to liquid, and vapor to vapor. Additional possibilities may involve compound mediums, such as a liquid with solid particles blended into a slurry, with one or both undergoing a phase change which results in a change in volume or pressure. Any compound which undergoes a change in volume or pressure as a result of one or more phase changes, and remains fluid in all relevant states, is a candidate for use in the present invention.
One inefficiency experienced in heat engines, in general, is that in the transition from the high-enthalpy gas to the low-enthalpy liquid state and the return transition from gas to liquid state (in, for example, an engine driven by the liquid to gas transition), either the work performed by the transition from low enthalpy to high enthalpy is not captured, or the latent heat energy released by the transition from high enthalpy to low enthalpy is wasted. Efficiencies may be gained by utilizing the latent heat expressed during the high- to low-enthalpy phase change and capturing the work output of the low- to high-enthalpy phase change.
Patent application PCT/US11/41289, submitted Jun. 21, 2011, is hereby incorporated by reference as if fully set forth herein.
The key component of a fully-regenerative heat engine cycle is the use of a working medium which undergoes a full cycle of phase changes during the heat engine cycle, returning to its original state at the end of the cycle. The working medium must be a material which, during the course of its phase change cycle, converts a portion of its latent heat of transformation from thermal energy to mechanical energy through a change in pressure, volume, or both. During the cycle, the working medium undergoes a phase change from a low-enthalpy state to a high-enthalpy state while absorbing its latent heat of transformation, and subsequently undergoes a phase change from a high-enthalpy state back to a low-enthalpy state. During the latter phase change it expels its latent heat of transformation, less the portion which of the latent thermal energy which was converted to mechanical energy.
In order to convert the latent heat from thermal to mechanical energy, the working medium must act on a mechanical device simultaneously with its phase change and consequent change in pressure, volume, or simultaneous change in pressure and volume.
If the mechanical work done during the phase change is non-zero, the internal energy (the latent heat) of the working medium must be reduced by an amount greater than or equal to the mechanical work done during the phase change, pursuant to the First Law of Thermodynamics.
Any implementation of the fully-regenerative engine using a working medium that undergoes liquid-vapor phase change requires that the fluid medium undergo its phase change within a defined, albeit changing, volume. The volume must vary in a defined relationship to the thermal energy absorbed by the fluid medium, such that the product of the partial pressure and the molar volume of the vaporous working medium remains constant as the working medium vaporizes or condenses. If the volume varies according to this principle, then the work done on the variable-volume chamber (defined as W=PΔV) must be a conversion of the latent heat to mechanical energy, rather than a conversion of sensible heat to mechanical energy as in the Rankine cycle or other similar engines.
The present invention offers a practical method of capturing the mechanical work done by a fluid medium which undergoes a liquid to vapor, liquid to liquid, or vapor to vapor phase change. By capturing energy at each phase transition, the preferred embodiment captures a greater proportion of available energy than currently available systems.
Types of Pumps and their Operation
The controlled-volume characteristic required of a mechanism for converting the latent heat of a fluid medium to mechanical energy (or the reverse, converting mechanical energy to latent heat) can be achieved by allowing the fluid medium to absorb latent heat as it passes through a pump. For the purposes of the present invention, the mechanism referred to as a pump may operate as either a pump or an engine, either imparting energy to a fluid or converting the energy of a fluid to another form of energy.
The pump mechanism may be any type of pump, so long as the correct relationship between volume, pressure, and absorption or release of latent heat may be maintained. This includes the positive-displacement type of pumps (for example reciprocating pumps, gear pumps, screw pumps, or gerotors) as well as dynamic pumps such as centrifugal pumps or impeller turbines. For ease of explanation, this document will primarily refer to positive-displacement pumps as the preferred embodiments.
Behavior of Liquid-Vapor Phase Change in a Variable-Volume Chamber
The behavior of a working medium undergoing a liquid to vapor phase change while being harnessed to do mechanical work will be used as a representative case for a regenerative engine utilizing a fluid working medium. The same or similar methods may be utilized with any phase change which goes from one fluid state to another fluid state, causing a change in volume while doing so.
The phase change and subsequent expansion of a liquid into a vapor, while confined within the chamber of a positive displacement pump, shares some characteristics with a type of boiling-liquid expanding-vapor explosion (BLEVE). The volume, though it may change rapidly, remains controlled rather than changing in a violent and uncontrolled manner.
The pertinent type of BLEVE is the result of a situation in which a pressure vessel contains a nonflammable liquid-vapor mixture. In this case, the entire liquid-vapor mass is held at a temperature above its boiling point temperature at ambient pressure, due to elevated pressure inside the pressure vessel. The trouble starts when the pressure vessel is breached. Even a small breach can lower the internal pressure enough to cause the liquid to boil rapidly, generating large amounts of vapor at high pressures. The high overpressure wave causes a further breach of the pressure vessel, boiling the remaining liquid and releasing large amounts of mechanical work—potentially destroying the pressure vessel.
Like the BLEVE, the controlled conversion of the latent heat of vaporization to mechanical work relies on the ability of a boiling liquid to increase the volume of vapor at the same time as pressure is rising. Unlike the BLEVE, the liquid temperature is controlled to provide a predictable rate of vapor production, and the chamber expands so as to accommodate the increased vapor volume.
The cycle starts as a liquid or a liquid-vapor combination is introduced to a variable-volume chamber, such as a cylinder containing a movable piston, as shown in
The liquid absorbs heat from the chamber walls 111, such that it begins to boil. The resulting production of vapor 105 increases the chamber pressure until it reaches a pressure sufficient to move the piston 113. As the piston begins to move, causing the chamber to expand (
At the end of the cycle all the liquid will ideally have been converted to vapor and the piston will be in its maximum-volume configuration (
Behavior of Vapor to Liquid Phase Change in Reciprocating Piston System
A similar process may be made to occur when vapor undergoes a vapor to liquid phase change, as shown in
Once the intake 109 is closed off or occluded (
At the end of the cycle, ideally all of the vapor will have condensed to liquid and the piston will be nearly at its minimum-volume condition. The liquid can then be expelled from the chamber through an outlet 115 and the cycle can begin again (
Single-Acting or Dual-Acting Pistons
The power density of the cylinder plus reciprocating piston design can be improved if a piston design known to those skilled in the arts as a “double-acting piston” is used instead of a single-acting piston. The double-acting piston uses the piston to divide the cylinder into two chambers, one at each end, with a set of intake and exhaust valves for each chamber. The valves are actuated such that the two chambers operate on identical but opposed cycles. Thus, when one chamber is at its maximum volume, the other is at its minimum volume, and vice-versa.
An advantage of the double-acting piston when used for the fully-regenerative cycle is that one chamber will be at its maximum pressure while the other is at its minimum pressure. This will increase the net work done on the piston over a single-acting piston where the non-chamber side of the piston faces a constant pressure.
Rotating Positive Displacement Pumps
While a system consisting of a cylinder plus a piston is easily understood, it may not be the most practical arrangement for a fully-regenerative engine. A cylinder plus piston is also known as a “positive displacement pump”, and there are many other types of positive displacement pumps, any of which may be employed in a fully regenerative engine. Rotating positive displacement pumps can offer a more consistent flow with fewer moving parts, greater efficiency, and higher power density. Possible choices for the pumps in a fully-regenerative engine are gear pumps, roots-type pumps, or gerotors.
A representative case of a design is a thermally conductive pump utilizing a gerotor. A gerotor consists of an inner and outer rotor. The inner rotor has N teeth (generally with a trochoidal shape), and the outer rotor has N+1 teeth (made up of circular arcs which mesh with the inner rotor teeth). The inner rotor is placed off-center from the outer rotor such that the rotors partition the volume between them into N chambers.
The outlet of the gerotor 137 is in the portion of the rotor wherein the chamber volume is decreasing. When the rotors move such that the chamber is exposed to the outlet, the fluid is forced out of the chamber through the outlet. At the end of the rotor cycle, the chamber volume is close to zero, the outlet is occluded, and the cycle can begin again.
Multiple-Ganged Pumps
Although the simplest design case is for each of the pump functions to be carried out within a single pump chamber, it is desirable in some instances to utilize multiple pumps in parallel, with inputs and outputs all connected to the same fluid medium passages and all connected to a power transmission element (such as a drive shaft, or electric motor/generators connected by appropriate power routing devices) such that they work in concert. Multiple pumps ganged together in this manner may result in reduced fluid flow rate or torque pulsations as compared to a single pump chamber.
Multiple-Ganged Engines
Another design that has some advantages is to use multiple-ganged engines, with pairs of pumps connected by fluid medium passages, and all the pairs of pumps connected by a power transmission element. The paired pumps may have reduced flow resistance through the fluid medium passages while still having lower torque ripple due to the multiple pairs of pumps.
Discussion of Complete Heat Engine Assemblies
Referring to
The thermally conductive phase-change pump 1 incorporates a chamber that brings the working medium directly or indirectly into thermal contact with a heat exchanger 13a, allowing the working medium to undergo its liquid-to-vapor phase change and transmitting the energy of that change to a power transmission element 19. The working medium exits the phase-change pump 1 via a passage 17 and proceeds to a restrictive cooling element 21 composed of expansion valve 3 and a “restrictive cooling element,” acting as a heat exchanger 5 and subsequently to a passage 15. A restrictive cooling element is one in which the working medium flow is restricted to the level at which the phase change to the low enthalpy state is completed for all fluid that passes through. Expansion valve 3 allows the working medium into heat exchanger 5 at a rate to maintain working medium within heat exchanger 5 at a partial pressure which allows it to release its residual latent heat which is conveyed from heat exchanger 5 to heat exchanger 13b, as the working medium transitions from a high to a low enthalpy state.
Heat exchanger 13b imparts the residual latent heat to the heat pump medium, which then passes through an expansion valve 9 heat exchanger 13a and compressor 11, to complete a vapor-compression heat pump cycle. Compressor 11 draws its power from power transmission element 19. The heat pump cycle has the effect of removing the remaining latent heat from the working medium at heat exchanger 5 and supplying it to the working medium in thermally conductive pump 1.
The working medium exits heat exchanger 5 in its liquid state with substantially lowered or zero vapor content and is conveyed via passage 15 to heat exchanger 7, where it absorbs heat from an external source 8. The working medium then is conveyed to thermally conductive pump 1 to begin the cycle again. In one preferred embodiment, external heat source 8 is also used to heat thermally conductive pump 1, in addition to heat exchanger 13a.
Power-routing element 25 allows an external power source or sink 23 to either drive or be driven by power transmission element 19.
Heat pump 10 pumps a greater quantity of heat energy than the quantity of mechanical energy that is used to drive the compressor 11. Less latent heat is extracted from the working medium by heat exchanger 5 than is absorbed by the working medium in thermally conductive pump 1, because some of the latent heat is converted to work by pump 1. Therefore, in order to supply all of the thermal energy required for the working medium to complete its phase change within thermally conductive pump 1, the working medium must exit heat exchanger 5 at a lower temperature than it enters thermally conductive pump 1. But heat exchanger 7, driven by external source 8, warms up the working medium so that it is approaching the temperature at which it changes phase when it reaches thermally conductive pump 1, thereby permitting heat engine 10 to supply all of the latent heat required to cause the working medium to change phase within thermally conductive pump 1.
The thermally conductive pump 1 incorporates a chamber that brings the working medium directly or indirectly into thermal contact with a heat exchanger 13a, allowing the working medium to undergo its liquid-to-vapor phase change and transmitting the energy of that change to a power transmission element 19. The working medium exits the phase-change pump 1 via a passage 17 and proceeds to a second thermally conductive pump 27 and subsequently to passage 15. Pump 27 allows the working medium to release its residual latent heat which is conveyed to heat exchanger 13b, and also shares power with power transmission element 19 via a power summation element 25.
Heat exchanger 13b imparts the residual latent heat to the heat pump medium, which then passes through an expansion valve 9 heat exchanger 13a and compressor 11, to complete a vapor-compression heat pump cycle. Compressor 11 draws its power from power transmission element 19. The heat pump cycle has the effect of removing the remaining latent heat from the working medium at heat exchanger 5 (
The working medium exits pump 27 in its liquid state with substantially lowered or zero vapor content and is conveyed via passage 15 to heat exchanger 7, where it absorbs heat from an external source. The rate of heat absorption is moderated by a layer of conductive material 14 which has reduced thermal conductivity compared to the heat exchanger, such as a heat spreader composed of steel or cast iron. The purpose of this layer is to reduce the heat flow into exchanger 7, and allow the use of a heat source having a high temperature relative to the desired temperature of the fluid as it leaves exchanger 7. The working medium then is conveyed to thermally conductive pump 1 to begin the cycle again.
A power summation element 25 allows an external power source or sink 23 to either drive or be driven by power transmission element 19.
In this embodiment, the heat pump fluid medium undergoes its liquid to vapor phase change in thermally conductive pump 33, absorbing its latent heat of vaporization from pump 27. The heat pump fluid medium then traverses passage 29 to pump 35. Within thermally conductive pump 35, the heat pump fluid medium undergoes its vapor to liquid phase change and releases its latent heat of vaporization to pump 1 before traversing passage 31 back to pump 33 to complete the cycle. At a minimum, the use of pumps 35 and 33 helps to move the heat pump fluid medium through its cycle. Depending on the amount of latent heat absorbed from the working medium in pump 27 and absorbed by the working medium in pump 1, mechanical energy may be taken from or supplied to power transmission element 19.
Heat is conducted to heat exchanger 7 through heat pipe 12. In this embodiment, the heat pipe is a variable-conductance heat pipe which uses a variable quantity of non-condensing gas held in reservoir 16 to control the heat flow through the pipe. This is a device that will be familiar to skilled persons and may be acquired from a number of different sources. By varying the amount of non-condensing gas in the main body of the pipe, the amount of heat flow through the pipe and therefore into heat exchanger 7 can be adjusted to match the energy required by heat engine 60.
The embodiment of
The heat pump may also be arranged using thermally conductive pumps, similar to the heat pump arrangement using pumps 35 and 33.
Skilled persons will readily appreciate that other permutations of inventive elements are possible, without departing from the scope of the invention.
This application is a continuation-in-part of application Ser. No. 13/860,485 filed Apr. 10, 2013, which claims priority from application Ser. No. 61/622,356, filed on Apr. 10, 2012 and application Ser. No. 61/622,347, filed on Apr. 10, 2012 which are incorporated by reference as if fully set forth herein.
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Child | 15007428 | US |