|Publication number||US3048928 A|
|Publication date||Aug 14, 1962|
|Filing date||Apr 27, 1959|
|Priority date||Apr 27, 1959|
|Publication number||US 3048928 A, US 3048928A, US-A-3048928, US3048928 A, US3048928A|
|Inventors||David A Copson, Edward Z Krajewski|
|Original Assignee||Raytheon Co|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (4), Referenced by (28), Classifications (9)|
|External Links: USPTO, USPTO Assignment, Espacenet|
1962 D. A. COPSON ET AL FREEZE-DRYING APPARATUS Filed April 27, 1959 OSC/LLATO REFRIGERA T/0N 0 0000000 0000 on o ouoooo 0o P HA m K N sw a w: n ,0 A R k Z. p0 Y/ My 3 31,048,928 Patented Aug. 14, 1962 Filed Apr. 27, 1959, Ser. No. 809,304 3 Claims. (Cl. 341) This invention relates to the use of microwave energy for the freeze-drying of material such as foods.
Drying by sublimation of such materials as foods, tissues and cultures of organisms that have first been frozen has proved to be a useful preservation process particularly for heat l-abile substances. However, many materials are not amenable to this treatment because of their dimensions or structures. For example, as beefsteak or bone tissue is freeze-dried, the highest surface at which sublimation occurs steadily recedes behind a dried portion of the substance that acts as a poor conductor for "heat. As the process goes on, more and more heat is dissipated in the dried portion of the material before reaching the vaporizing surface to cause sublimation.
An improved technique over the application of heating utilizes the fact that many materials in the dry state absorb little electromagnetic energy at radio or microwave frequencies compared to the energy absorbed by the same material in a moist frozen state. The result is that microwave energy applied to moist frozen material is absorbed almost entirely by the moist frozen portion of the material. By this process, little or no energy is lost in transmission through the dried material, making the drying process far more efiicient. In fact, a given sized piece of beefsteak can be dried by microwave energy in about one-third of the time required to dry it in other forms of heating under the same conditions.
It is important that the sublimed water be removed from the place where the heat of sublimation is applied. Heretofore it has been considered necessary to physically separate the place of sublimation from a place of desublimation where refrigeration is provided so that the condensate will not flow back to the place of sublimation and to pump the moisture in vapor form from the place of sublimation to the place of desublimation where the moisture is collected thereby effecting dehydration of the material being processed. However, the expansion of water in its sublimation from ice is several orders of mag ni-tude, i.e., one pound of water at 1 mm. pressure occupies a volume of about 14,300 cu. ft. This substantial increase in volume has heretofore required the use of high capacity motors and pumps and suction pipe lines of large dimensions even when moderate quantities of water are to be removed. Further the efliciency of freeze-drying systems depends to a large extent, particularly during the initial drying phase, on the unimpeded flow of vapor from the region of sublimation or high vapor pressure to the region of low vapor pressure or the desublimator. As pointed out heretofore the place where the heat of sublimation is applied was separated from the desublimator where refrigeration occurs, so that the condensate will not flow back into the system.
The present invention contemplates a single vacuum chamber enclosing an RF still constructed in the form of an RF choke and comprised of screen material opaque to radio and microwave frequency energy while providing a large number of passages in combination with coils or the like containing a refrigerant surrounding and enclosing the RF still. Conventional means are provided to supply microwave energy to the interior of the still, lower the temperature of the condenser coils to about --30 to 40 C. and evacuate the vacuum chamber to about 0.5-1 mm. pressure. Upon reduction of the temperature of the coils and the pressure in the chamber to the desired operating temperature and pressure, and provision of microwave energy to the still or container containing the frozen material to be treated, water in the frozen material is sublimated and collected on the coils and noncondensable gases are eliminated by the vacuum pump. Due to the location of the condenser coils in close proximity to the frozen material being dried, the large area of cold surface provided by the condenser coils and the large number of passages in the radio frequency screen, there is provided at all times a highly efficient and very short and substantially unimpeded vapor path from the region of high vapor pressure in the still to the low vapor pressure at the condenser coils thereby greatly increasing the efiiciency of freeze-drying systems and simplifying their construction and manufacture.
Other and further features and advantages of the invention will become apparent from the following description taken in connection with the accompanying drawing illustrating the invention which shows a perspective view with parts broken away of an apparatus for carrying out the invention.
In the drawing the reference numeral 10 designates a sealed container or evacuation chamber having a sealable access door 11. Supported within the container as by legs 12 is a second conductive container or heating chamber 13 containing an access door 14. The heating chamber '13 forms a cavity to which propagated electro magnetic radio frequency energy is applied from an oscillator 15 through a transmission line 16 of the wave guide type such as shown, for example, in Patent No. 2,540,036 issued January 30, 1951 to P. L. Spencer. Frequencies which are especially significant for this purpose are those in the microwave range, which may be considered as those lying between 300 megacycles per second and 30,000 megacycles per second. The two most practical frequencies in this range are in the region of 2450 megacycles per second and 915 megacycles per second. In accordance with the invention the heating chamber 13 is adapted to prevent the propagation of electromagnetic energy from its interior to the container 10 while permitting atmospheric communication there-between. This may be achieved by forming the walls 17 of the heating chamber 13 with openings 18 of a diameter small with respect to the wave length of the radio frequency energy to prevent the propagation of the radio frequency energy from the interior of chamber 13 while permitting atmospheric communication. Disposed in close proximity to and substantially enclosing the walls 17 of the heating chamber 13 are condenser coils 19. Condenser coils 19 are connected to suitable refrigeration means 21 adapted to lower the temperature of the condenser coils 19 to about 30 to 40 C. A pipe 22 provides communication between the interior of container 10 and a pump 23. Material 24 in the frozen state to be dried is supported on a centrally located platform 25 of dielectric material formed with suitable openings or slots to permit the free passage of the vapor. The access door 14 is of course closed to prevent leakage of radio frequency energy. As radio frequency energy penetrates the frozen material 24, the ice or other component to be vaporized evaporates without first becoming a liquid, that is it sublim-ates due to the absorption of the radio frequency energy-producing heat. This sublimation produces a region of dried material, represented by the section 24a, and leaves a core of frozen undried material, represented by the section 24b. The dried material 24a offers no appreciable impedance thus permitting the sublimation of the moist material to continue at a substantially uni-form rate. The only precaution that need be taken is to keep the radio frequency energy from being applied fast enough to raise the temperature of any portion of the material above the melting point of the vaporizable portion of the material. Should this be permitted to happen, the liquid, particularly if water, would offer considerably greater impedance to the radio frequency energy and hot spots might develop, which in the case of food, would cause changes affecting the flavor. However, known methods for maintaining the voltage supplied to the oscillator at a predetermined value will accomplish this objective.
The present invention may be used to evaporate out from any material any component that may be evaporated from the solid state. Upon closure of door 11 the evacuation of chamber by pump 23 serves to reduce the partial pressure of the component to be evaporated in the atmosphere of the heating chamber 13. The heating of the material 24 provides a high vapor pressure at the material 24 and the cooling of the condenser coils 19 provide a large low temperature region in close proximity to the material 24. This, in combination with the heating chamber 13 having walls 17 effectively comprising microwave energy chokes, provides at all times a substantially more efficient, very short and unimpeded vapor path from the region of high vapor pressure or material 24 to the low vapor pressure region or condenser coils 19 which rapidly condense and collect in frozen form the vapor sublimated from the material 24 in the heating chamber 13.
Vapor condensed on the coils 19 may be removed during off cycles of the still by raising the temperature of the coils 19 to a point above freezing and removing the vapor as it forms with the pump or other suitable means. This process may be accelerated if the refrigeration means 211 is reversible, i.e., the coils can be heated.
This invention is not limited to the particular details of construction and materials described, as many equivalents will suggest themselves to those skilled in the art. It is accordingly desired that the appended claims be given a broad interpretation commensurate with the scope of the invention within the art.
What is claimed is:
1. Apparatus for removing a vaporizable component by sublimation from material including a solid and said vaporizable component in the solid state comprising: first container means for providing an atmosphere at a pressure substantially lower than atmospheric pressure; pump means communicating with said first container means for maintaining said lower pressure; second container means disposed in said first container means enclosing said material to be treated, a substantial portion of said second container means containing a plurality of passages forming a microwave energy choke for preventing the propagation of microwave energy from the interior of said second container means to the interior of said first container means while permitting substantial atmospheric communication therebetween; a microwave electrical energy generator; a propagated electromagnetic wave-guiding structure coupled to said generator and communicating with said second container means for applying propagated electromagnetic microwave energy to said material to supply the heat of sublimation to sublimate a substantial portion of said component; condenser means having a substantial area substantially enclosing and adjacent said portion of said second container means forming a microwave energy choke for at least assisting in causing said sublimed component to pass outwardly through said choke portion and thereafter to condense on said condenser means; and means for maintaining said condenser means at a temperature substantially lower than freezing whereby there is provided a short substantially unimpeded vapor path between said material and said condenser means and said sublimed component is efiiciently condensed on said condenser means.
2. In combination, means for generating electromagnetic energy having a frequency in the microwave region of the spectrum, a chamber for receiving a frozen aqueous material, waveguide means connected between said generating means and said chamber for coupling said electromagnetic energy to said chamber to sublimate a substantial portion of the water in said material, a sealed container for enclosing said chamber, means for maintaining the pressure within said sealed container at a value substantially lower than atmospheric pressure, a plurality of apertures in a portion of the walls of said chamber for preventing the propagation of said electromagnetic energy from said chamber to said sealed container and for providing atmospheric communication therebetween, and means for condensing water sublimated from said material.
3. In combination, means for generating electromagnetic energy having a frequency in the microwave region of the spectrum, a chamber for receiving a frozen aqueous material, waveguide means connected between said gencrating means and said chamber for coupling said electromagnetic energy to said chamber to sublimate a substantial portion of the water in said material, a sealed container for enclosing said chamber, means for maintaining the pressure within said sealed container at a value substantially lower than atmospheric pressure, a plurality of apertures in a portion of the walls of said chamber for preventing the propagation of said electromagnetic energy from said chamber to said sealed container and for providing atmospheric communication therebetween, condenser means having a substantial area adjacent to and enclosing a substantial portion of said chamber for condensing in frozen form water sublimated from said material, and means for maintaining said condenser means at a low temperature.
References Cited in the file of this patent UNITED STATES PATENTS 2,345,204 Lodwig Mar. 28, 1944 2,513,991 Bradbury July 4, 1950 2,585,825 Nyrop Feb. 12, 1952 2,859,534 Copson Nov. 11, 1958
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US2345204 *||Apr 2, 1942||Mar 28, 1944||Mobile Refrigeration Inc||Interior chamber insulation|
|US2513991 *||Mar 19, 1946||Jul 4, 1950||Lyophile Cryochem Corp||Process for the esiccation of aqueous materials from the frozen state|
|US2585825 *||Sep 23, 1946||Feb 12, 1952||Nyrop Johan Ernst||Method of drying, concentrating by evaporation, or distilling heatsensitive substances|
|US2859534 *||Oct 11, 1956||Nov 11, 1958||Raytheon Mfg Co||Methods and apparatus for radio frequency freeze-drying|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US3205588 *||Oct 17, 1961||Sep 14, 1965||Leybold Anlagen Holding A G||Drying process and apparatus therefor for removing solids from liquid mixtures|
|US3273636 *||Oct 31, 1962||Sep 20, 1966||Space simulation chamber|
|US3276138 *||Sep 21, 1962||Oct 4, 1966||Miwag Mikrowellen Ag||Microwave drying apparatus|
|US3316652 *||Oct 24, 1965||May 2, 1967||Sun Freeze Inc||Continuous dehydrating process|
|US3382585 *||Dec 28, 1965||May 14, 1968||Fmc Corp||Internal sublimation condenser apparatus|
|US3834038 *||Sep 14, 1972||Sep 10, 1974||Gammaflux Inc||Method for drying moldable resins|
|US3845270 *||Aug 20, 1973||Oct 29, 1974||Raytheon Co||Microwave heating and vapor condensing apparatus|
|US3883958 *||Jan 14, 1974||May 20, 1975||Antonio Domingos Filipe||Method and apparatus for accelerated freeze drying|
|US3940885 *||Jan 21, 1975||Mar 2, 1976||Oscar Sam Gray||Process and equipment for treating seeds and product thereof|
|US3955286 *||Oct 9, 1974||May 11, 1976||Rene Anrep||Method of and installation for treating various objects by means of microwaves|
|US4016657 *||Oct 4, 1973||Apr 12, 1977||Passey Now By Change Of Name C||Heat pump freeze drying system|
|US4247988 *||Oct 1, 1979||Feb 3, 1981||Fmc Corporation||Process for removing excess water from active chlorine compounds|
|US4407140 *||Jul 29, 1982||Oct 4, 1983||Kyowa Vacuum Engineering, Ltd.||Vacuum apparatus|
|US4622446 *||Dec 9, 1983||Nov 11, 1986||House Food Industrial Company Ltd.||Microwave drying apparatus and use thereof|
|US4884626 *||Aug 25, 1987||Dec 5, 1989||Filipowski Merle M||Combination refrigerator oven|
|US6148875 *||Jun 18, 1997||Nov 21, 2000||Breen; James||Vacuum food storage system|
|US6225611||Nov 15, 1999||May 1, 2001||Hull Corporation||Microwave lyophilizer having corona discharge control|
|US6920701||Jul 15, 2002||Jul 26, 2005||Steris Gmbh||Chamber for a freeze-drying device|
|US6931754||Apr 10, 2003||Aug 23, 2005||Bayer Aktiengesellschaft||Freeze-drying apparatus|
|US8535542 *||Nov 2, 2009||Sep 17, 2013||Daniel J. Simpson||Filter press with integrated radio frequency heating|
|US8580084||Feb 1, 2010||Nov 12, 2013||Daniel J. Simpson||Desalination method using a filter press|
|US20040250441 *||Jul 15, 2002||Dec 16, 2004||Peter Haseley||Chamber for a freeze-drying device|
|US20100116755 *||Nov 2, 2009||May 13, 2010||Simpson Daniel J||Filter press with integrated radio frequency heating|
|EP1279913A1 *||Oct 9, 2001||Jan 29, 2003||Steris GmbH||Chamber for freeze drying apparatus|
|WO2001036888A1||Nov 15, 2000||May 25, 2001||Hull Corp||Microwave lyophilizer and microwave lyophilization method|
|WO2003012355A1 *||Jul 15, 2002||Feb 13, 2003||Haseley Peter||Chamber for a freeze-drying device|
|WO2003091645A1 *||Apr 15, 2003||Nov 6, 2003||Bayer Ag||Freeze-drying device|
|WO2010062376A1 *||Nov 2, 2009||Jun 3, 2010||Simpson Daniel J||Filter press with integrated radio frequency heating|
|U.S. Classification||34/263, 62/62, 34/92, 219/679, 34/76, 62/268|