Patent Application
20100058783
This application relates to a refrigerant system that utilizes an expander to provide a more efficient expansion process and to recover at least a portion of energy from this expansion process, and wherein at least partially expanded refrigerant is injected back into the compression process to reduce discharge temperature.
Refrigerant systems utilize a refrigerant that is usually circulated through a closed-loop refrigerant cycle to condition a secondary fluid, such as air, water or glycol solution, to be delivered to a climate controlled environment. Typically, in a basic refrigerant system, a compressor compresses the refrigerant and delivers it to a first heat exchanger, which is a condenser, for subcritical applications, and a gas cooler, for transcritical applications. In the first heat exchanger, heat is rejected from the refrigerant and is absorbed by another secondary fluid, such as ambient air. Refrigerant, from that first heat exchanger, passes through an expansion process, during which its pressure and temperature are reduced. Downstream of the expansion device, a refrigerant passes through a second heat exchanger, or so-called evaporator, and then back to the compressor. In the second heat exchanger, the refrigerant is evaporated and typically superheated, while cooling a secondary fluid to be delivered to a climate controlled environment.
Expansion devices can be of a so-called passive or active type. Passive expansion devices are typically represented by an orifice or a valve. The refrigerant expansion through these devices follows an inefficient isenthalpic thermodynamic process. One option that is known in refrigerant systems is the use of an active expansion device or an expander, which follows more thermodynamically efficient isentropic process and can be a turbine, a piston expander (a free-piston type or a linked-piston type), a scroll expander, a screw expander or any other type expander expanding the refrigerant from a higher pressure to a lower pressure. The expander typically recovers at least portion of energy from the expansion process, and that portion of energy is utilized, at least partially, to drive other components, such as, for example, one of the refrigerant system components, such as a compressor, a fan or a pump. Expanders increase performance (efficiency and capacity) of a refrigerant system by recovering this portion of energy and by utilizing a more thermodynamically efficient isentropic expansion process.
Another feature utilized in refrigerant system designs is the injection of a portion of refrigerant back into the compression process. The refrigerant injected into the compression process is typically a two-phase mixture of vapor and liquid. The liquid-vapor mixture cools the compressor elements as well as the main flow of compressed refrigerant. The cooling of the main refrigerant flow occurs as this cooler two-phase mixture undergoes evaporation and mixing process with the hotter main refrigerant vapor.
The refrigerant injection cooling feature becomes even more important for high-pressure refrigerant systems, and specifically for refrigerant systems operating in a transcritical cycle, such as C02 refrigerant systems. These refrigerants operate at higher pressures and often higher pressure ratios than formerly used conventional refrigerants, thus promoting higher discharge temperatures. Additionally, in most cases, the transcritical cycle is less efficient than the conventional subcritical cycle, requiring even higher discharge pressures or other means of performance enhancement, such as, for instance, a liquid-suction heat exchanger, both increasing refrigerant discharge temperatures. Specifically, C02 refrigerant has a higher value of a polytropic exponent (than other conventional refrigerants), also undesirably affecting the discharge temperature. On the other hand, in the transcritical cycle, pressure and temperature are essentially independent from each other, so discharge temperature reduction may find additional benefits of performance optimization, operational envelope extension and reliability improvement.
The use of this injected refrigerant is known in the art, and a worker skilled in this art would recognize when and how much injected refrigerant would be desirable. For instance, the refrigerant may be injected into the compression process to maintain a compressor discharge temperature, to control discharge or suction superheat, etc.
However, a refrigerant system has never been proposed, which has utilized the expander in combination with this -refrigerant injection cooling, especially in conjunction with C02 applications that can operate in a transcritical cycle.
In the disclosed embodiment of this invention, a refrigerant system incorporates an expander that is utilized to efficiently expand refrigerant from a higher pressure to a lower pressure, and recover at least a portion of energy from that expansion process to assist in driving one of the refrigerant system components. In a disclosed embodiment, the expander assists in driving of at least one compressor associated with the refrigerant system. At the same time, a portion of refrigerant that has been at least partially expanded in the expander is injected into the compression process to reduce the discharge temperature of the main refrigerant flow compressed in the compressor. In the prior art, the injected refrigerant was diverted from the location upstream of the expansion device, thus the diverted refrigerant was not expanded (even partially, through the expander), therefore less expansion could be recovered from the expansion process in the prior art refrigerant systems then in this invention.
In one disclosed embodiment, a portion of refrigerant is taken from an intermediate point in the expansion process in the expander and returned to a suction line leading to a single-stage or multi-stage compressor. In another embodiment, a portion of refrigerant is tapped from an intermediate point in the expansion process in the expander and returned to an intermediate point in the compression process that can be located inside one of the compression stages or in between compression stages.
In yet another embodiment, a portion of refrigerant is taken downstream of the expander and injected into compressor suction. In all cases, an evaporator is bypassed by this portion of injected refrigerant.
In still another disclosed embodiment, a portion of refrigerant is tapped upstream of the expander and injected into the compressor suction or into an intermediate point in the compression process, either inside one of the compression stages or in between the compression stages. Although a single tap point and a single injection point are associated with each embodiment, a combination of the above tap and injection locations is feasible and within the scope of invention.
In all cases considered above, the refrigerant injected into the compression process is at a lower temperature and, in many cases, is a two-phase mixture. Thus, the refrigerant can cool the compressor elements as well as the main flow of compressed refrigerant vapor. The refrigerant injection cooling feature is even more important for high-pressure refrigerant systems, and specifically for refrigerant systems operating in a transcritical cycle, such as C02 refrigerant systems, that operate at higher pressures and higher pressure ratios, promoting higher discharge temperatures. Additionally, a less efficient transcritical cycle requires even higher discharge pressures or other means of performance enhancement, such as, for instance, a liquid-suction heat exchanger, both further increasing refrigerant discharge temperatures. Specifically, C02 refrigerant has a higher value of a polytropic exponent, also undesirably affecting the discharge temperature. On the other hand, in the transcritical cycle, pressure and temperature are independent from each other, so discharge temperature reduction may find additional benefits of performance optimization, operational envelope extension and reliability improvement.
In other features, a refrigerant flow control device, such as a valve, may be incorporated onto the refrigerant return line, and can be controlled to achieve desired conditions in the compression process. As an example, the amount of injected refrigerant can be controlled to achieve a desired discharge temperature, discharge superheat, suction superheat, etc. As an example, the valve may be an on/off valve or may be controlled by one of pulsation or modulation techniques, or it can be a valve with an adjustable opening to control the amount of injected refrigerant based on measured operational characteristics of a refrigerant system (such as, for example, a discharge temperature or suction superheat). Again, a worker in this art would recognize how much refrigerant to inject, and when it would be desirable to do so. It is the use of the expander in combination with the refrigerant injection cooling that is inventive here. These and other features of the present invention can be best understood from the following specification and drawings, the following of which is a brief description.
Downstream of the expander 26, the refrigerant passes through an evaporator 34, and then returns to the compressor 22.
The invention incorporates the refrigerant return line 30 that returns at least a portion of partially expanded refrigerant (in this embodiment) through a control valve 32, to a suction line leading to the compressor 22. This returned refrigerant is at a lower temperature than the refrigerant flowing to the compressor 22 from the evaporator 34. Various benefits from supplying this colder refrigerant could include reducing the temperature of the refrigerant leaving and/or entering the compressor 22 as well as provide cooling to the elements of the compressor 22. Further, by controlling the amount of refrigerant passing through the control valve 32, these temperatures can be tailored as desired.
A control 23 operates the control valve 32 to control the amount of returned refrigerant to adjust desired operational characteristics, such as, for instance, discharge temperature, suction superheat and discharge superheat, for the refrigerant system 20. The control valve 32 may be provided with a pulse width modulation control such that it can be rapidly opened and closed by the control 23 to exactly tailor the amount of injected refrigerant. Pulse width modulation controls for valves are known, however, they have not been incorporated into a refrigerant system 20 having both the expander 26 and the cooling refrigerant return line 30. The control valve 32 can also have an adjustable opening to precisely meter the amount of injected refrigerant as desired.
Furthermore, as mentioned above, since the partially expanded injection refrigerant is diverted to the compressor from an intermediate location in the expander, the diverted partially expanded refrigerant participates part-way through the expansion process, therefore increasing the amount of energy that can be recovered from the expansion process.
While in the embodiments shown in
Although a single tap point and a single injection point are associated with each embodiment, a combination of the above tap and injection locations is feasible and within the scope of invention. Also, it should be pointed out that, for refrigerant systems employing tandem compressors, refrigerant injection, as well as recovered energy connection, may be provided to all tandem compressors or only to some compressors operating in tandem.
As stated above, the refrigerant injection cooling feature is even more important for high-pressure refrigerant systems, and specifically for refrigerant systems operating in a transcritical cycle, such as C02 refrigerant systems, that operate at higher pressures and higher pressure ratios, promoting higher discharge temperatures. Additionally, a less efficient transcritical cycle requires even higher discharge pressures or other means of performance enhancement, such as, for instance, a liquid-suction heat exchanger, both further increasing refrigerant discharge temperatures. Specifically, C02 refrigerant has a higher value of a polytropic exponent, also undesirably affecting the discharge temperature. On the other hand, in the transcritical cycle, pressure and temperature are independent from each other, providing additional flexibility and design opportunities to a refrigerant system designer. Therefore, discharge temperature reduction provided by the refrigerant injection of this invention, along with cycle enhancement opportunities provided by the expander, is more critical and more advantageous in these applications for performance optimization, operational envelope extension and reliability improvement.
Although preferred embodiments of this invention have been disclosed, a worker of ordinary skill in this art would recognize that certain modifications would come within the scope of this invention. For that reason, the following claims should be studied to determine the true scope and content of this invention.
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/US06/49201 | 12/26/2006 | WO | 00 | 5/19/2009 |
