This invention relates generally to low temperature or cryogenic refrigeration such as refrigeration generated by a pulse tube cryocooler.
A recent significant advancement in the field of generating low temperature refrigeration is the development of cryocoolers such as the pulse tube cryocooler system wherein pulse energy is converted to refrigeration using an oscillating gas. Such systems can generate refrigeration to very low levels sufficient, for example, to liquefy helium. One important application of the refrigeration generated by such cryocooler systems is in magnetic resonance imaging systems. Other such cryocooler systems are Gifford-McMahon cryocoolers and Stirling cryocoolers.
One problem with conventional cryocooler systems is a potential inefficiency due to a mismatch between the most efficient operating frequency of the cryocooler system and the most efficient operating frequency of the oscillating gas generating system.
Accordingly it is an object of this invention to provide an improved cryocooler system which has more efficient operation.
The above and other objects, which will become apparent to those skilled in the art upon a reading of this disclosure, are attained by the present invention, one aspect of which is:
A method for operating a cryocooler system comprising:
Another aspect of the invention is:
A frequency modulated cryocooler system comprising:
As used herein the term “regenerator” means a thermal device in the form of porous distributed mass or media, such as spheres, stacked screens, perforated metal sheets and the like, with good thermal capacity to cool incoming warm gas and warm returning cold gas via direct heat transfer with the porous distributed mass.
As used herein the term “thermal buffer tube” means a cryocooler component separate from the regenerator and proximate the cold heat exchanger and spanning a temperature range from the coldest to the warmer heat rejection temperature for that stage.
As used herein the term “indirect heat exchange” means the bringing of fluids into heat exchange relation without any physical contact or intermixing of the fluids with each other.
As used herein the term “direct heat exchange” means the transfer of refrigeration through contact of cooling and heating entities.
As used herein the term “frequency modulating mechanical resonator” means a combination of one or more of a mass member, spring, and piston system that is designed to modulate the operating frequency of a cryocooler to an improved level of performance.
The numerals in the Drawings are the same for the same or similar elements.
The invention comprises the use of a low loss frequency modulating mechanical resonator positioned between an electrically driven pressure wave generator and a cryocooler to drive the low frequency cryocooler without losing any power rating of the electric motor which is operating at the natural AC frequency. A mechanical resonator is an energy transmission device, thus it is expected to have relatively low loss. A low loss mechanical resonator is a device having losses that are much smaller than a comparable fluid resonator, i.e. long pipe.
The invention will be described in greater detail with reference to the Drawings. Referring now to
The oscillating gas generated by the pressure wave generator passes in line 15 to low loss frequency modulating mechanical resonator 1 which is located between pressure wave generator 10 and the cryocooler. Frequency modulating mechanical resonator 1 has a solid piston or mass 2 and is designed to convert the operating frequency of the pressure wave generator into the operating frequency of cryocooler regenerator 20 and thermal buffer tube 40; in other words, the frequency modulating mechanical resonator replicates the dynamic conditions of the cryocooler at the warm end of its regenerator 20. Suspension member shown as 3 are linear suspension elements that provide stability to solid piston movement. A well-designed frequency modulating mechanical resonator will minimize losses due to friction and drag.
The frequency modulating mechanical resonator serves to reduce the frequency of the oscillating gas to produce lower frequency oscillating gas which has a frequency which is lower than the resonant frequency of the pressure wave generator and which is closer to the preferable operating frequency of the cryocooler. The lower frequency oscillating gas generally has a frequency less than 40 hertz, typically has a frequency less than 30 hertz, preferably less than 10 hertz, most preferably less than 5 hertz. Referring back now to
The lower frequency oscillating gas applies a pulse to the hot end of regenerator 20 thereby generating an oscillating working gas and initiating the first part of the pulse tube sequence. The pulse serves to compress the working gas producing hot compressed working gas at the hot end of the regenerator 20. The hot working gas is cooled, preferably by indirect heat exchange with heat transfer fluid 22 in heat exchanger 21, to produce warmed heat transfer fluid in stream 23 and to cool the compressed working gas of the heat of compression. Examples of fluids useful as the heat transfer fluid 22, 23 in the practice of this invention include water, air, ethylene glycol and the like. Heat exchanger 21 is the heat sink for the heat pumped from the refrigeration load against the temperature gradient by the regenerator 20 as a result of the pressure-volume work generated by the pressure wave generator.
Regenerator 20 contains regenerator or heat transfer media. Examples of suitable heat transfer media in the practice of this invention include steel balls, wire mesh, high density honeycomb structures, expanded metals, lead balls, copper and its alloys, complexes of rare earth element(s) and transition metals. The pulsing or oscillating working gas is cooled in regenerator 20 by direct heat exchange with cold regenerator media to produce cold pulse tube working gas.
Thermal buffer tube 40 and regenerator 20 are in flow communication. The flow communication includes cold heat exchanger 30. The cold working gas passes in line 60 to cold heat exchanger 30 and in line 61 from cold heat exchanger 30 to the cold end of thermal buffer tube 40. Within cold heat exchanger 30 the cold working gas is warmed by indirect heat exchange with a refrigeration load thereby providing refrigeration to the refrigeration load. This heat exchange with the refrigeration load is not illustrated. One example of a refrigeration load is for use in a magnetic resonance imaging system. Another example of a refrigeration load is for use in high temperature superconductivity.
The working gas is passed from the regenerator 20 to thermal buffer tube 40 at the cold end. Preferably, as illustrated in
Cooling fluid 44 is passed to heat exchanger 43 wherein it is warmed or vaporized by indirect heat exchange with the working gas, thus serving as a heat sink to cool the compressed working gas. Resulting warmed or vaporized cooling fluid is withdrawn from heat exchanger 43 in stream 45. Preferably cooling fluid 44 is water, air, ethylene glycol or the like.
In the low pressure point of the pulsing sequence, the working gas within the thermal buffer tube expands and thus cools, and the flow is reversed from the now relatively higher pressure reservoir 52 into the thermal buffer tube 40. The cold working gas is pushed into the cold heat exchanger 30 and back towards the warm end of the regenerator while providing refrigeration at heat exchanger 30 and cooling the regenerator heat transfer media for the next pulsing sequence. Orifice 50 and reservoir 52 are employed to maintain the pressure and flow waves in appropriate phases so that the thermal buffer tube generates net refrigeration during the compression and the expansion cycles in the cold end of thermal buffer tube 40. Other means for maintaining the pressure and flow waves in phase which may be used include inertance tube and orifice, expander, linear alternator, bellows arrangements, and a work recovery line connected back to the compressor with a mass flux suppressor. In the expansion sequence, the working gas expands to produce working gas at the cold end of the thermal buffer tube 40. The expanded gas reverses its direction such that it flows from the thermal buffer tube toward regenerator 20. The relatively higher pressure gas in the reservoir flows through valve 50 to the warm end of the thermal buffer tube 40. In summary, thermal buffer tube 40 rejects the remainder of pressure-volume work generated by the compression system as heat into warm heat exchanger 43.
The expanded working gas emerging from heat exchanger 30 is passed in line 60 to regenerator 20 wherein it directly contacts the heat transfer media within the regenerator to produce the aforesaid cold heat transfer media, thereby completing the second part of the pulse tube refrigeration generation sequence and putting the regenerator into condition for the first part of a subsequent pulse tube refrigeration generation sequence.
Although the invention has been described in detail with reference to certain preferred embodiments, those skilled in the art will recognize that there are other embodiments of the invention within the spirit and the scope of the claims. For example, a Gifford-McMahon cryocooler or a Stirling cryocooler may be used rather than the pulse tube cryocooler illustrated in
Number | Name | Date | Kind |
---|---|---|---|
5129232 | Minas et al. | Jul 1992 | A |
5363077 | Herd et al. | Nov 1994 | A |
5904046 | Kawano | May 1999 | A |
6374617 | Bonaquist et al. | Apr 2002 | B1 |
6378312 | Wang | Apr 2002 | B1 |
6434947 | Zhu et al. | Aug 2002 | B2 |
6578364 | Corey | Jun 2003 | B2 |
6604363 | Corey et al. | Aug 2003 | B2 |
6640553 | Kotsubo et al. | Nov 2003 | B1 |
6644038 | Acharya et al. | Nov 2003 | B1 |
Number | Date | Country |
---|---|---|
09296965 | Nov 1997 | JP |