US3845270A - Microwave heating and vapor condensing apparatus - Google Patents
Microwave heating and vapor condensing apparatus Download PDFInfo
- Publication number
- US3845270A US3845270A US00390155A US39015573A US3845270A US 3845270 A US3845270 A US 3845270A US 00390155 A US00390155 A US 00390155A US 39015573 A US39015573 A US 39015573A US 3845270 A US3845270 A US 3845270A
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- Prior art keywords
- energy
- enclosure
- microwave
- vapors
- heating
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-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B3/00—Drying solid materials or objects by processes involving the application of heat
- F26B3/32—Drying solid materials or objects by processes involving the application of heat by development of heat within the materials or objects to be dried, e.g. by fermentation or other microbiological action
- F26B3/34—Drying solid materials or objects by processes involving the application of heat by development of heat within the materials or objects to be dried, e.g. by fermentation or other microbiological action by using electrical effects
- F26B3/347—Electromagnetic heating, e.g. induction heating or heating using microwave energy
-
- H—ELECTRICITY
- H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
- H05B—ELECTRIC HEATING; ELECTRIC LIGHT SOURCES NOT OTHERWISE PROVIDED FOR; CIRCUIT ARRANGEMENTS FOR ELECTRIC LIGHT SOURCES, IN GENERAL
- H05B6/00—Heating by electric, magnetic or electromagnetic fields
- H05B6/64—Heating using microwaves
- H05B6/80—Apparatus for specific applications
-
- H—ELECTRICITY
- H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
- H05B—ELECTRIC HEATING; ELECTRIC LIGHT SOURCES NOT OTHERWISE PROVIDED FOR; CIRCUIT ARRANGEMENTS FOR ELECTRIC LIGHT SOURCES, IN GENERAL
- H05B2206/00—Aspects relating to heating by electric, magnetic, or electromagnetic fields covered by group H05B6/00
- H05B2206/04—Heating using microwaves
- H05B2206/046—Microwave drying of wood, ink, food, ceramic, sintering of ceramic, clothes, hair
Definitions
- the oven enclosure walls include means for the circulation of a fluid medium to condense substantially all vapors released by the treated material.
- the condensed fluids are collected in the lower section of the apparatus by gravity and are either recirculated or removed.
- the microwave energy generator means is suitably isolated by energy permeable means, as well as, a warm air circulation system to minimize attenuation of the energy by the condensed vapors.
- Perforated partition means are provided in the collector region to substantially inhibit the escape of microwave energy from the oven enclosure.
- the microwave energy is radiated within an enclosure which is dimensioned to support a plurality of modes at the assigned operating frequency.
- the energy is distributed in multimode energy patterns by such means as paddletype mode stirrers and the like.
- the term microwave is defined as electromagnetic energy in the region of the spectrum having wavelengths in the order of 1 meter to l millimeter and frequencies in the order of 300 MHz to 300 GHz.
- An example of a prior art processing technique is the deposition of a platinum catalyst on such materials as ceramic cores which requires the carrying of the platinum material in a solution of hydrochloric acid.
- the acid solution is driven off as a vapor before the high temperature firing is undertaken.
- Prior art apparatus employed in such techniques involves long gas-fired ovens, lined with special low-corrosion high-temperature metals and the corrosive vapors are conducted away by means of water curtains or condensed to effectively scrub" such vapors.
- the removal of vapors during the heating and/or drying operations becomes of importance and, particularly, in processing of products which result in the release of corrosive or toxic vapors.
- means are provided for the efficient removal of substantially all of the released vapors from products being processed with microwave energy. Condensation on the fluid impervious walls defining the oven enclosure is encouraged by the provision of suitable heat transfer media in close proximity to the walls.
- Such means include cooling coils coupled to the walls together with forced circulation of any liquid coolant having sufficient flow and thermal absorbing capacity to condense substantially all of the vapors released by the material being dried or heated on the oven interior walls. The condensation is conducted by gravity to the lower section of the microwave heating apparatus where it is collected and can be either reused or disposed of by appropriate means.
- Other moisture removal means include the flow of air or other fluids within the cavity walls or other absorbing media to encourage the condensation of the liberated vapors.
- the condensation on the walls of the enclosure takes place in the region where the microwave electric fields are minimal and, therefore, there is little or no coupling or loss of energy to the condensate formed on the enclosure walls.
- a thin layer of a corrosion-resistant plastic material such as that available under the trademark TEFLON will protect the metal walls without hindering microwave energy distribution.
- a microwave permeable panel is provided and warm air circulated adjacent to the panel to inhibit condensation.
- means in the form of a perforated partition will permit the passage of condensation without the coupling or escape of the microwave energy from the apparatus.
- the apparatus 10 comprises a microwave oven enclosure delineating the confined area 12 defined by fluid impervious conductive sidewalls 14, top wall 16 and tapered bottom wall 18.
- a door which may be provided in one of the sidewalls l4'has purposely been omitted in order to aid in the understanding of the invention.
- the enclosure is radiated by a microwave energy from a source 20, such as a magnetron, with a probe-type antenna 22 extending through the top wall 16.
- a high voltage supply 24 provides for the energization of the magnetron.
- the described energy source is directly coupled to the apparatus and, if desired, the source may be mounted at a remote location with a waveguide transmission line coupled directly to the top wall 16.
- This energy coupling structure has not been illustrated since it will be obvious to one skilled in the art.
- the input energy section 30 is isolated from the remaining enclosure area by means of a microwave permeable panel 26 that is also impervious to fluids. A heated medium from source 28 may be circulated within the isolated region 30 to thereby inhibit condensation formation on the panel which would affect microwave energy passage.
- the sidewalls 14 are provided with convoluted coils 32 containing a forced circulating coolant fluid medium provided from a source 34, and egress means 36.
- the flow rate is controlled to provide the most efficient condensation of vapors released within the enclosure 12.
- the product to be processed is supported by a dielectric plate member 40 which is in turn supported on a pedestal 42 of a dielectric material to provide for the radiation of the load 38 uniformly on all sides.
- a partition member 44 having a plurality of perforations 46 is disposed in the bottom portion of the enclosure and supports the pedestal 42.
- the perforations 46 are disposed in an array to substantially prevent the escape of any microwave energy through the condensate collection region
- Condensation droplets 50 formed along the inner portions of sidewalls 14 are permitted to pass through the partition member 44 perforations 46 into the collection region 48 defined by tapered walls 18 by means of gravity and are directed to the outlet passage 52.
- a drain or pump means 54 provide for the removal of the condensate or reuse if desired.
- sidewalls 14, as well as bottom wall 18 may be provided with a thin layer of any suitable corrosion-resistant material 56.
- This layer provides for the protection of the metallic sidewalls and will not hinder the distribution of the microwave energy within the enclosure.
- the invention is particularly useful where the liberated vapors are of a corrosive or toxic nature.
- the described apparatus will eliminate the need for prior art systems providing flow of a hot or warm fluid media to maintain the released vapors at the appropriate temperature for transport from the microwave apparatus to an exterior location.
- the effective cooling of the oven enclosure walls encourages substantial condensation and the means for the conduction of released vapors as a fluid to an exterior location.
- Other condensation and removal systems may be incorporated such as the circulation of heat transfer media in the enclosure walls or the provision of other absorbing and conversion means for the transporting of the heating vapors to an exterior location. It is intended that the foregoing description of the illustrative embodiment be considered broadly and not in a limiting sense.
- Microwave heating apparatus comprising:
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Electromagnetism (AREA)
- Life Sciences & Earth Sciences (AREA)
- Microbiology (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Biotechnology (AREA)
- Molecular Biology (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Drying Of Solid Materials (AREA)
Abstract
Microwave apparatus together with an intergral vapor condensation collection system is disclosed for any heating and/or drying application. The oven enclosure walls include means for the circulation of a fluid medium to condense substantially all vapors released by the treated material. The condensed fluids are collected in the lower section of the apparatus by gravity and are either recirculated or removed. The microwave energy generator means is suitably isolated by energy permeable means, as well as, a warm air circulation system to minimize attenuation of the energy by the condensed vapors. Perforated partition means are provided in the collector region to substantially inhibit the escape of microwave energy from the oven enclosure.
Description
United States Patent [1 1 Widugris, Jr. 1
[451 Oct. 29, 1974 MICROWAVE HEATING AND VAPOR CONDENSING APPARATUS [75] Inventor: William Widugris, Jr., Weston,
Mass.
[73] Assignee: Raytheon Company, Lexington,
Mass.
[22] Filed: Aug. 20, 1973 [21] Appl. No.: 390,155
[52] US. Cl. 219/1055, 34/1 [51] Int. Cl. H05b 9/06 [58] Field of Search 219/1055; 34/1 [56] References Cited UNITED STATES PATENTS 3,048,928 8/1962 Copson 219/1055 3,505,490 4/1970 Gorn 219/1055 3,748,421 7/1973 Peterson 219/1055 The? VOLTAGE HEATED MEDIUM COOLANT COOLANT OUT Primary Examiner-4. V. Truhe Assistant Examiner-Hugh D, .laeger Attorney, Agent, or Firm-Edgar O. Rost; Joseph D. Pannone; Harold A. Murphy [5 7 ABSTRACT Microwave apparatus together with an intergral vapor condensation collection system is disclosed for any heating and/or drying application. The oven enclosure walls include means for the circulation of a fluid medium to condense substantially all vapors released by the treated material. The condensed fluids are collected in the lower section of the apparatus by gravity and are either recirculated or removed. The microwave energy generator means is suitably isolated by energy permeable means, as well as, a warm air circulation system to minimize attenuation of the energy by the condensed vapors. Perforated partition means are provided in the collector region to substantially inhibit the escape of microwave energy from the oven enclosure.
2 Claims, 1 Drawing Figure VPAIENIEUIINZS m4 45270 VHIGH VOLTAGE SUPPLY /6 l/i/ TTM:III HEATED MEDIUM COOLANT N COOLANT OUT I DRAIN BACKGROUND OF THE INVENTION 1. Field of the Invention The invention relates to microwave heating and, in particular, to the removal of moisture released within confined areas during the application of the microwave energy.
2. Description of the Prior Art Processing with microwave heating has become widely accepted for a large number of domestic and industrial products due to the rapid heating times provided by electromagnetic energy generated from such sources as the magnetron. Heating with microwaves provides the so-called dielectric heating phenomenon descriptive of the high frequency oscillatory movements of the molecules within the material by combined interaction with the electric and magnetic fields associated with absorbed electromagnetic energy. A rapid rise in material temperatures cause heating by essentially molecular friction. The electromagnetic energy is typically radiated within an enclosure defining a confined area within which the article is disposed or transported by means of a conveyor. The energy conventionally operates in the region of the electromagnetic energy spectrum having frequencies of 915 i 13 MHz and 2,450 i 50 MHz in the industrial, scientific and medical band assigned for such heating apparatus by the Federal Communications Commission. The microwave energy is radiated within an enclosure which is dimensioned to support a plurality of modes at the assigned operating frequency. The energy is distributed in multimode energy patterns by such means as paddletype mode stirrers and the like. For the purposes of the present description, the term microwave is defined as electromagnetic energy in the region of the spectrum having wavelengths in the order of 1 meter to l millimeter and frequencies in the order of 300 MHz to 300 GHz.
All materials have differing values of dielectric constant and loss tangent characteristics which control the rate of absorption of energy and, therefore, the rate of heating becomes a varying factor. In certain processing operations frozen products as well as products having a considerable amount of moisture are treated which results in the release of a considerable amount of trapped vapors. To render the processing with microwave more efficient the rapid removal of the moisture is desired to prevent any attenuation of the energy radiated within the confined area. In certain processes the released vapors resulting from the drying or heating operation may be corrosive or toxic and in prior art heating techniques rather costly methods and/or equipment are used to neutralize and/or dispose of such vapors.
An example of a prior art processing technique is the deposition of a platinum catalyst on such materials as ceramic cores which requires the carrying of the platinum material in a solution of hydrochloric acid. The acid solution is driven off as a vapor before the high temperature firing is undertaken. Prior art apparatus employed in such techniques involves long gas-fired ovens, lined with special low-corrosion high-temperature metals and the corrosive vapors are conducted away by means of water curtains or condensed to effectively scrub" such vapors. In the more effective utilization of microwave energy the removal of vapors during the heating and/or drying operations becomes of importance and, particularly, in processing of products which result in the release of corrosive or toxic vapors.
SUMMARY OF THE INVENTION In accordance with the teachings of the invention means are provided for the efficient removal of substantially all of the released vapors from products being processed with microwave energy. Condensation on the fluid impervious walls defining the oven enclosure is encouraged by the provision of suitable heat transfer media in close proximity to the walls. Such means include cooling coils coupled to the walls together with forced circulation of any liquid coolant having sufficient flow and thermal absorbing capacity to condense substantially all of the vapors released by the material being dried or heated on the oven interior walls. The condensation is conducted by gravity to the lower section of the microwave heating apparatus where it is collected and can be either reused or disposed of by appropriate means.
Other moisture removal means include the flow of air or other fluids within the cavity walls or other absorbing media to encourage the condensation of the liberated vapors. The condensation on the walls of the enclosure takes place in the region where the microwave electric fields are minimal and, therefore, there is little or no coupling or loss of energy to the condensate formed on the enclosure walls. Where the process involves the liberation of toxic or corrosive vapors a thin layer of a corrosion-resistant plastic material such as that available under the trademark TEFLON will protect the metal walls without hindering microwave energy distribution. To substantially prevent the attenuation of the microwave energy in the input region a microwave permeable panel is provided and warm air circulated adjacent to the panel to inhibit condensation. In the collection region in the lower portion of the apparatus, means in the form of a perforated partition will permit the passage of condensation without the coupling or escape of the microwave energy from the apparatus. Numerous alterations, modifications and variations of the embodiment to be described will be apparent to those skilled in the art.
DESCRIPTION OF THE PREFERRED EMBODIMENT Referring to the single FIGURE shown, the invention will now be described in detail. The apparatus 10 comprises a microwave oven enclosure delineating the confined area 12 defined by fluid impervious conductive sidewalls 14, top wall 16 and tapered bottom wall 18. A door which may be provided in one of the sidewalls l4'has purposely been omitted in order to aid in the understanding of the invention. The enclosure is radiated by a microwave energy from a source 20, such as a magnetron, with a probe-type antenna 22 extending through the top wall 16. A high voltage supply 24 provides for the energization of the magnetron. The described energy source is directly coupled to the apparatus and, if desired, the source may be mounted at a remote location with a waveguide transmission line coupled directly to the top wall 16. This energy coupling structure has not been illustrated since it will be obvious to one skilled in the art. The input energy section 30 is isolated from the remaining enclosure area by means of a microwave permeable panel 26 that is also impervious to fluids. A heated medium from source 28 may be circulated within the isolated region 30 to thereby inhibit condensation formation on the panel which would affect microwave energy passage.
The sidewalls 14 are provided with convoluted coils 32 containing a forced circulating coolant fluid medium provided from a source 34, and egress means 36. The flow rate is controlled to provide the most efficient condensation of vapors released within the enclosure 12.
The product to be processed, indicated generally as load 38, is supported by a dielectric plate member 40 which is in turn supported on a pedestal 42 of a dielectric material to provide for the radiation of the load 38 uniformly on all sides. In addition a partition member 44 having a plurality of perforations 46 is disposed in the bottom portion of the enclosure and supports the pedestal 42. The perforations 46 are disposed in an array to substantially prevent the escape of any microwave energy through the condensate collection region Condensation droplets 50 formed along the inner portions of sidewalls 14 are permitted to pass through the partition member 44 perforations 46 into the collection region 48 defined by tapered walls 18 by means of gravity and are directed to the outlet passage 52. A drain or pump means 54 provide for the removal of the condensate or reuse if desired.
Where corrosive or toxic vapors are involved sidewalls 14, as well as bottom wall 18, may be provided with a thin layer of any suitable corrosion-resistant material 56. The provision of this layer provides for the protection of the metallic sidewalls and will not hinder the distribution of the microwave energy within the enclosure.
There is thus disclosed a unique microwave apparatus which provides an integral vapor condensing and collector system for substantially all microwave heating and drying applications. The invention is particularly useful where the liberated vapors are of a corrosive or toxic nature. The described apparatus will eliminate the need for prior art systems providing flow of a hot or warm fluid media to maintain the released vapors at the appropriate temperature for transport from the microwave apparatus to an exterior location. The effective cooling of the oven enclosure walls encourages substantial condensation and the means for the conduction of released vapors as a fluid to an exterior location. Other condensation and removal systems may be incorporated such as the circulation of heat transfer media in the enclosure walls or the provision of other absorbing and conversion means for the transporting of the heating vapors to an exterior location. It is intended that the foregoing description of the illustrative embodiment be considered broadly and not in a limiting sense.
l claim:
1. Microwave heating apparatus comprising:
a source of electromagnetic energy;
an enclosure defined by fluid impervious top, bottom and sidewall members;
means for coupling said energy to said enclosure;
means for disposing a load within said enclosure;
means for circulation of a heat transfer fluid medium over a substantial portion of said sidewalls to con- ..dense vapors on the interior walls of said enclosure;
and
means for collecting and removing said condensation from said enclosure.
2. Apparatus according to claim 1 wherein said energy coupling means are substantially isolated from said enclosure by a panel member impervious to fluids and permeable to said energy disposed between said top and bottom wall members to form an input energy region.
Claims (2)
1. Microwave heating apparatus comprising: a source of electromagnetic energy; an enclosure defined by fluid impervious top, bottom and sidewall members; means for coupling said energy to said enclosure; means for disposing a load within said enclosure; means for circulation of a heat transfer fluid medium over a substantial portion of said sidewalls to condense vapors on the interior walls of said enclosure; and means for collecting and removing said condensation from said enclosure.
2. Apparatus according to claim 1 wherein said energy coupling means are substantially isolated from said enclosure by a panel member impervious to fluids and permeable to said energy disposed between said top and bottom wall members to form an input energy region.
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US00390155A US3845270A (en) | 1973-08-20 | 1973-08-20 | Microwave heating and vapor condensing apparatus |
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US00390155A US3845270A (en) | 1973-08-20 | 1973-08-20 | Microwave heating and vapor condensing apparatus |
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Cited By (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4079522A (en) * | 1976-09-23 | 1978-03-21 | Rca Corporation | Apparatus and method for cleaning and drying semiconductors |
FR2393252A1 (en) * | 1976-10-07 | 1978-12-29 | Sagami Chem Res | METHOD AND DEVICE FOR DEHYDRATING AND INCINERATE SAMPLES |
FR2487692A1 (en) * | 1980-07-29 | 1982-02-05 | Daimler Benz Ag | METHOD FOR SEPARATING MIST OF PAINT AIR PAINT MIST FROM PAINT FACILITIES |
WO1982001411A1 (en) * | 1980-10-15 | 1982-04-29 | Nils O Loeoef | A method for drying wooden products |
WO1982001766A1 (en) * | 1980-11-14 | 1982-05-27 | Risman Per O | A method of carrying out the drying of wooden objects |
DE3106236A1 (en) * | 1981-02-20 | 1982-09-02 | Paul 8000 München Hirsch | ADDITIONAL DEVICE FOR MICROWAVE DEVICES |
US4547642A (en) * | 1983-01-03 | 1985-10-15 | General Electric Company | Combination microwave and thermal self-cleaning oven with an automatic venting arrangement |
US4567340A (en) * | 1985-01-09 | 1986-01-28 | Phillips Petroleum Company | Apparatus and method for drying solid materials |
EP0174587A2 (en) * | 1984-09-13 | 1986-03-19 | Agfa-Gevaert AG | Process and appartus for the remelting of gelled colloids, especially photographic emulsions |
FR2634007A1 (en) * | 1988-07-05 | 1990-01-12 | Valeo | Method for drying a porous product containing a solvent, with recovery of the solvent |
US4963709A (en) * | 1987-07-24 | 1990-10-16 | The United States Of America As Represented By The Department Of Energy | Method and device for microwave sintering large ceramic articles |
US5216216A (en) * | 1990-06-30 | 1993-06-01 | Samsung Electronics Co., Ltd. | Equipment for discharging overflows in a microwave oven |
US5338409A (en) * | 1990-11-30 | 1994-08-16 | Mls Mikrowellen-Labor-Systeme Gmbh | Apparatus for distilling liquids in a vacuum |
US5512737A (en) * | 1994-05-09 | 1996-04-30 | Henny Penny Corporation | Oven liner for dielectric oven |
WO1998016965A1 (en) * | 1996-10-16 | 1998-04-23 | Widia Gmbh | Microwave oven and components therefor |
US5843304A (en) * | 1993-04-28 | 1998-12-01 | Wastech International, Inc. | Filtration and treatment system |
US5853579A (en) * | 1996-11-26 | 1998-12-29 | Wastech International Inc. | Treatment system |
FR2770441A1 (en) * | 1997-10-30 | 1999-05-07 | Bernard Dedieu | SHEET DRYING METHOD AND DEVICE FOR IMPLEMENTING THE METHOD |
FR2781710A1 (en) * | 1999-09-28 | 2000-02-04 | Valeurs Bois Ind | Method of drying sawn wood |
FR2793008A1 (en) * | 1999-04-30 | 2000-11-03 | Valeurs Bois Ind | PROCESS FOR THE EXTRACTION OF NATURAL JUICE FROM WOODY PLANT MATERIAL, DEVICE FOR CARRYING OUT THE PROCESS AND USE OF THE PROCESS FOR THE PRODUCTION OF DRY WOODY PLANT |
US6675495B2 (en) | 1997-10-30 | 2004-01-13 | Valeurs Bois Industrie | Method for drying saw timber and device for implementing said method |
US20040045958A1 (en) * | 2001-01-08 | 2004-03-11 | Ekemar Lars S.E. | Tn appliance for the equalisation of heat in a dielectric load heated by an oscillating electric/electromagnetic field |
US20050258173A1 (en) * | 2004-05-21 | 2005-11-24 | Maytag Corporation | Microwave intensification system for a conveyorized microwave oven |
US20120006207A1 (en) * | 2009-03-30 | 2012-01-12 | Hideo Shimoda | Cooking device |
WO2016014320A1 (en) | 2014-07-22 | 2016-01-28 | Ethridge Edwin | Microwave extraction of volatiles from planetary bodies |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3048928A (en) * | 1959-04-27 | 1962-08-14 | Raytheon Co | Freeze-drying apparatus |
US3505490A (en) * | 1966-10-07 | 1970-04-07 | Raytheon Co | Apparatus for thawing of frozen materials |
US3748421A (en) * | 1971-07-29 | 1973-07-24 | Raytheon Co | Microwave melter apparatus |
-
1973
- 1973-08-20 US US00390155A patent/US3845270A/en not_active Expired - Lifetime
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3048928A (en) * | 1959-04-27 | 1962-08-14 | Raytheon Co | Freeze-drying apparatus |
US3505490A (en) * | 1966-10-07 | 1970-04-07 | Raytheon Co | Apparatus for thawing of frozen materials |
US3748421A (en) * | 1971-07-29 | 1973-07-24 | Raytheon Co | Microwave melter apparatus |
Cited By (38)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4079522A (en) * | 1976-09-23 | 1978-03-21 | Rca Corporation | Apparatus and method for cleaning and drying semiconductors |
FR2393252A1 (en) * | 1976-10-07 | 1978-12-29 | Sagami Chem Res | METHOD AND DEVICE FOR DEHYDRATING AND INCINERATE SAMPLES |
FR2487692A1 (en) * | 1980-07-29 | 1982-02-05 | Daimler Benz Ag | METHOD FOR SEPARATING MIST OF PAINT AIR PAINT MIST FROM PAINT FACILITIES |
US4347065A (en) * | 1980-07-29 | 1982-08-31 | Daimler-Benz Aktiengesellschaft | Process for the separation of paint mists from the exhaust air of lacquer painting plants |
WO1982001411A1 (en) * | 1980-10-15 | 1982-04-29 | Nils O Loeoef | A method for drying wooden products |
WO1982001766A1 (en) * | 1980-11-14 | 1982-05-27 | Risman Per O | A method of carrying out the drying of wooden objects |
US4485564A (en) * | 1980-11-14 | 1984-12-04 | Aktiebolaget Edane Komponenter | Method of carrying out the drying of wooden objects |
DE3106236A1 (en) * | 1981-02-20 | 1982-09-02 | Paul 8000 München Hirsch | ADDITIONAL DEVICE FOR MICROWAVE DEVICES |
US4547642A (en) * | 1983-01-03 | 1985-10-15 | General Electric Company | Combination microwave and thermal self-cleaning oven with an automatic venting arrangement |
EP0174587A2 (en) * | 1984-09-13 | 1986-03-19 | Agfa-Gevaert AG | Process and appartus for the remelting of gelled colloids, especially photographic emulsions |
US4673782A (en) * | 1984-09-13 | 1987-06-16 | Agfa Gevaert Aktiengesellschaft | Process and apparatus for microwave melting solidified gel masses, in particular of photographic emulsions |
EP0174587A3 (en) * | 1984-09-13 | 1989-02-01 | Agfa-Gevaert AG | Process and appartus for the remelting of gelled colloids, especially photographic emulsions |
US4567340A (en) * | 1985-01-09 | 1986-01-28 | Phillips Petroleum Company | Apparatus and method for drying solid materials |
US4963709A (en) * | 1987-07-24 | 1990-10-16 | The United States Of America As Represented By The Department Of Energy | Method and device for microwave sintering large ceramic articles |
FR2634007A1 (en) * | 1988-07-05 | 1990-01-12 | Valeo | Method for drying a porous product containing a solvent, with recovery of the solvent |
US5216216A (en) * | 1990-06-30 | 1993-06-01 | Samsung Electronics Co., Ltd. | Equipment for discharging overflows in a microwave oven |
US5338409A (en) * | 1990-11-30 | 1994-08-16 | Mls Mikrowellen-Labor-Systeme Gmbh | Apparatus for distilling liquids in a vacuum |
US5843304A (en) * | 1993-04-28 | 1998-12-01 | Wastech International, Inc. | Filtration and treatment system |
US5512737A (en) * | 1994-05-09 | 1996-04-30 | Henny Penny Corporation | Oven liner for dielectric oven |
WO1998016965A1 (en) * | 1996-10-16 | 1998-04-23 | Widia Gmbh | Microwave oven and components therefor |
US5853579A (en) * | 1996-11-26 | 1998-12-29 | Wastech International Inc. | Treatment system |
EP1248059A1 (en) * | 1997-10-30 | 2002-10-09 | Valeurs Bois Industrie | Method for drying sawn timber and device for implementing said method |
FR2770441A1 (en) * | 1997-10-30 | 1999-05-07 | Bernard Dedieu | SHEET DRYING METHOD AND DEVICE FOR IMPLEMENTING THE METHOD |
WO1999023429A1 (en) * | 1997-10-30 | 1999-05-14 | Valeur Bois Industrie | Method for drying saw timber and device for implementing said method |
US6675495B2 (en) | 1997-10-30 | 2004-01-13 | Valeurs Bois Industrie | Method for drying saw timber and device for implementing said method |
US6473994B1 (en) | 1997-10-30 | 2002-11-05 | Valeurs Bois Industrie | Method for drying saw timber and device for implementing said method |
US6581299B1 (en) * | 1999-04-30 | 2003-06-24 | Valeurs Bois Industrie | Method for extracting natural juice of ligneous plant material, device for carrying out said method and use of said method in the production of dried ligneous plants material |
WO2000066960A1 (en) * | 1999-04-30 | 2000-11-09 | Valeurs Bois Industrie | Method for extracting the natural juice of ligneous plant material, device for carrying out said method and use of said method in the production of dried ligneous plant material |
FR2793008A1 (en) * | 1999-04-30 | 2000-11-03 | Valeurs Bois Ind | PROCESS FOR THE EXTRACTION OF NATURAL JUICE FROM WOODY PLANT MATERIAL, DEVICE FOR CARRYING OUT THE PROCESS AND USE OF THE PROCESS FOR THE PRODUCTION OF DRY WOODY PLANT |
FR2781710A1 (en) * | 1999-09-28 | 2000-02-04 | Valeurs Bois Ind | Method of drying sawn wood |
US20040045958A1 (en) * | 2001-01-08 | 2004-03-11 | Ekemar Lars S.E. | Tn appliance for the equalisation of heat in a dielectric load heated by an oscillating electric/electromagnetic field |
US7105789B2 (en) * | 2001-01-08 | 2006-09-12 | Ekemar Lars S E | Appliance for the equalization of heat in a dielectric load heated by an oscillating electric/electromagnetic field |
US20050258173A1 (en) * | 2004-05-21 | 2005-11-24 | Maytag Corporation | Microwave intensification system for a conveyorized microwave oven |
US7081605B2 (en) * | 2004-05-21 | 2006-07-25 | Maytag Corporation | Microwave intensification system for a conveyorized microwave oven |
US20120006207A1 (en) * | 2009-03-30 | 2012-01-12 | Hideo Shimoda | Cooking device |
WO2016014320A1 (en) | 2014-07-22 | 2016-01-28 | Ethridge Edwin | Microwave extraction of volatiles from planetary bodies |
EP3172293A4 (en) * | 2014-07-22 | 2018-07-11 | Ethridge, Edwin | Microwave extraction of volatiles from planetary bodies |
EP3760694A1 (en) * | 2014-07-22 | 2021-01-06 | Ethridge, Edwin | Microwave extraction of volatiles from planetary bodies |
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