There are several existing closed loop heat transfer technologies, including both passive and active methods. The passive methods are generally limited by heat load, transport distance or orientation, while the active methods require an external power source. In applications where an increase in temperature is desired along with the transfer of heat, the external power requirements increase significantly.
Heat pipes are a passive device relying on two-phase heat transfer (evaporation/condensation). The liquid is pumped by capillarity through a continuous wick, from the condenser, to the evaporator. A capillary wicked heat pipe is reversible (condenser and evaporator can be switched). The heat load and distance are most frequently limited by the capillarity of the wick, but can also be limited by the sonic limit, nucleation limit, and entrainment limit. The heat transport in this device is nearly isothermal.
Looped heat pipes are similar to heat pipes (passive, two-phase heat transfer), where the condensate is returned to the evaporator through capillarity. The wick structure is only located in the evaporator, and the condensate is returned through tubes, which allows for further transport length. Special considerations for start-up are needed to ensure liquid is continuous from the condenser to the evaporator. The heat transport in this device is also nearly isothermal.
Thermosyphons are another passive two-phase heat transfer device. The condensate is returned to the evaporator via gravity. The operation of a thermosyphon is not-reversible, since the condenser must be higher, with respect to gravity, than the evaporator. The transport distance can be very high in these devices. Once again, the heat transfer in this device is nearly isothermal.
Pumping a liquid through a closed heat transfer loop is one of the most common, and oldest, closed loop heat transfer methods. It involves a pump, a heat input heat exchanger (air/liquid, liquid/liquid, refrigerant/liquid, or generically heat source/liquid), and a heat rejection heat exchanger. The pump needs power delivered from an external engine or motor. The heat transfer in this method relies on sensible heating, therefore, the liquid temperature increases and decreases in the heat absorption and rejection processes, respectively.
Similar to a pumped liquid loop, a pumped two-phase cooling loop, uses a pump, evaporator and a condenser. Condensate is pumped from the condenser to the evaporator. The pump is powered by a motor, converting electricity into mechanical energy. The heat transfer in this loop is nearly isothermal, when its operation is under low pressure differentials.
A heat pump can take a heat input and elevate the temperature of the heat output by means of a compressor which is driven by a motor. The power needed to drive the motor can increase the energy into this system by twenty percent or more.
Embodiments of the present invention are directed to a mechanism that enables linear valve actuation on a reciprocating steam engine for use in thermally activated closed loop heat transfer systems. No external power, other than heat load, is needed for the system to operate. Additionally, the system is self-starting, which is created by a directional preference of the inlet and exhaust valve switches on the reciprocating engine. The engine may be applied in at least two distinct forms: a reciprocating heat transfer engine and a reciprocating heat transformer. In each form, power is transferred by the engine to one or more additional pistons via a shaft through linear motion.
In various embodiments of the reciprocating heat transfer engine, the engine drives a reciprocating pump, and the engine's power is derived from the available energy between the heat input to the evaporator and the heat rejected through the condenser. All of the power created by the engine is used to overcome the hydrodynamic losses of the fluid flow as well as frictional losses of the pistons. This system may achieve nearly isothermal closed loop heat transfer.
In various embodiments of the reciprocating heat transformer, the engine drives both a reciprocating pump and compressor. Part of the heat load can be rejected at a higher temperature than the heat input, which is considered to be transformed. All of the engine's power is utilized to overcome the hydrodynamic losses, friction of the pistons, and the work required to drive the compressor. In this system, there are two condensers, a low temperature condenser and a high temperature condenser. While, a nearly isothermal heat transfer loop can be employed by the heat transfer engine, the heat transformer requires a larger temperature difference between the evaporator and low temperature condenser to allow for power to be available to drive the compressor. The linear valve actuation in the engine is best suited for temperature differences of less than 30° C. In this temperature range, a reasonable percentage of the available energy may be converted to work by the engine.
The foregoing has outlined rather broadly certain aspects of the present invention in order that the detailed description of the invention that follows may better be understood. Additional features and advantages of the invention will be described hereinafter which form the subject of the claims of the invention. It should be appreciated by those skilled in the art that the conception and specific embodiment disclosed may be readily utilized as a basis for modifying or designing other structures or processes for carrying out the same purposes of the present invention. It should also be realized by those skilled in the art that such equivalent constructions do not depart from the spirit and scope of the invention as set forth in the appended claims.
For a more complete understanding of the present invention and the advantages thereof, reference is now made to the following description taken in conjunction with the accompanying drawings in which like reference numerals indicate like features and wherein:
A typical reciprocating pumped two-phase closed loop heat transfer system is presented in
A schematic of one embodiment of the present invention is presented in
Considerations must be taken in selecting a working fluid for the reciprocating heat transfer engine, in order to minimize the temperature difference from the evaporator 101 to the condenser 102. Specifically, the operating pressure of the working fluid in the desired temperature range of the device must be considered versus the hydrodynamic pressure losses and frictional losses associated with the movement of the piston. Both the hydrodynamic losses and friction losses will increase the pressure needed across the engine 106 to induce movement of the piston and pump 104. If the pressure differential needed to move the piston is large relative to the operating pressure, large temperature differentials can be observed from the evaporator 101 to the condenser 102, which can adversely impact the performance of the heat transfer engine or even prevent it from working all together.
Additional consideration may be taken in selecting the working fluid for the reciprocating heat transfer engine, depending on the desired effect of the heat transfer engine. For instance, if a nearly isothermal performance is desired, a pure or an azeotropic working fluid should be chosen, since evaporation and condensation will happen at a constant temperature with a fixed pressure. If said device is intended to be used as an intermediate heat transfer system between a hot and cool fluid stream, than a zeotropic or non-azeotropic working fluid may be selected. During evaporation, the temperature of a zeotropic or non-azeotropic working fluid will increase as the vapor quality increases, which is referred to as “temperature glide.” The reverse is true during the condensation process. In this scenario, the working fluid selection should also account for the desired temperature drop of the hot fluid as well as the temperature rise of the cool fluid.
A schematic of a typical heat pump utilizing reciprocating compressor is presented in
Another embodiment of the present invention is presented in
In order for the heat transformer to operate, the net force supplied by the engine 106, must be greater than the force necessary to drive both the pump 104 and the compressor 109. Therefore, the overall displacement ratio of the heat transformer must be greater than unity.
The variables P and A denote the pressure and cross-section area of the respective piston, respectively. The subscripts Evap, Cond,L, and Cond,H represent the evaporator, low temperature condenser and high temperature condenser, respectively. In the heat transformer, a relatively high vapor quality fluid leaves the evaporator, and flows in parallel to both the engine 106 and the compressor 109. During start-up, the evaporator 101 temperature may temporarily be higher than the high temperature condenser's 110 temperature. Because of this condition, along with the fact that the engine 106 and compressor 109 are implemented in parallel to each other, the check valves 105f and 105e must have a cracking pressure that is high enough to compensate for the maximum pressure differential of the evaporator 101 with respect to the high temperature condenser 110 during start-up. If a setting is not accounted for, vapor may bypass the engine 106 entirely, and the system will not operate. Alternately, an on/off valve may be placed upstream of the check valves 105f and 105e, that can be off, until the pressure in the high temperature condenser 110 section of the system is higher than that of the evaporator 110.
The degree in which the temperature of the high temperature condenser 110 is elevated, relative to the evaporator 101, depends on the proportion of fluid that is driven through the compressor 109 versus how much fluid flow drives the engine 106 less the flow driven by the pump 104. This concept may be observed mathematically in the definition of the heat transformer displacement ratio in EQ 1. Generally, the less fluid that is driven by the compressor 109, and the more fluid that drives the engine 106, the higher the degree of heat transformation in the high temperature condenser 110. Also, the higher the temperature and pressure difference between the evaporator 101 and the low temperature condenser 102, the greater the degree of heat transformation in the high temperature condenser 110.
Since there are two condensers in the heat transformer, rejecting heat at different temperatures, there are two options for coolant passing by these condensers, as presented in
In both embodiments discussed, an inlet valve switch and outlet valve switch was represented in a schematic. The mechanical implementation of the inlet valve switch is presented in
The outlet valve switch is presented in
The inlet and outlet valve switches in the present invention allow for the relative high pressure from the evaporator 101 to be exposed to one side of the piston 201, and the relative low pressure of the condenser 102 to be exposed to the opposing side of the piston 201 for the entire stroke of the piston 201. This mechanism is best used for relative low temperature differentials, for example less than 30 C, between the evaporator and the low temperature condenser. When this temperature differential is low, it is possible to convert a reasonable percentage of the available energy to work. At higher temperature differentials, the percentage of available energy that can be converted to work decreases because the valve switches do not allow for expansion of the vapor during each stroke.
Additional considerations also must be taken when designing the system's displacement ratio (engine to pump or heat transformer displacement ratio), since the reversal process of the inlet and outlet valve switch in the engine 106 takes a finite amount of time, which allows for vapor to directly flow from the evaporator 101 to the condenser 102. Additionally, the minimum clearance volume must also be accounted for when sizing the pistons of these systems.
While the present system and method has been disclosed according to the preferred embodiment of the invention, those of ordinary skill in the art will understand that other embodiments have also been enabled. Even though the foregoing discussion has focused on particular embodiments, it is understood that other configurations are contemplated. In particular, even though the expressions “in one embodiment” or “in another embodiment” are used herein, these phrases are meant to generally reference embodiment possibilities and are not intended to limit the invention to those particular embodiment configurations. These terms may reference the same or different embodiments, and unless indicated otherwise, are combinable into aggregate embodiments. The terms “a”, “an” and “the” mean “one or more” unless expressly specified otherwise. The term “connected” means “communicatively connected” unless otherwise defined.
When a single embodiment is described herein, it will be readily apparent that more than one embodiment may be used in place of a single embodiment. Similarly, where more than one embodiment is described herein, it will be readily apparent that a single embodiment may be substituted for that one device.
In light of the wide variety of methods for transferring heat known in the art, the detailed embodiments are intended to be illustrative only and should not be taken as limiting the scope of the invention. Rather, what is claimed as the invention is all such modifications as may come within the spirit and scope of the following claims and equivalents thereto.
None of the description in this specification should be read as implying that any particular element, step or function is an essential element which must be included in the claim scope. The scope of the patented subject matter is defined only by the allowed claims and their equivalents. Unless explicitly recited, other aspects of the present invention as described in this specification do not limit the scope of the claims.
This application claims priority under 35 U.S.C. §119 based upon prior U.S. Provisional Patent Application Ser. No. 61/931,759, filed Jan. 27, 2014, in the name of Jeremy Rice, entitled “IMPROVED RECIPROCATING STEAM ENGINE,” the disclosure of which is incorporated herein in its entirety by this reference.
Number | Date | Country | |
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61931759 | Jan 2014 | US |