Search Images Maps Play YouTube News Gmail Drive More »
Sign in
Screen reader users: click this link for accessible mode. Accessible mode has the same essential features but works better with your reader.


  1. Advanced Patent Search
Publication numberUS2360108 A
Publication typeGrant
Publication dateOct 10, 1944
Filing dateAug 29, 1942
Priority dateAug 29, 1942
Publication numberUS 2360108 A, US 2360108A, US-A-2360108, US2360108 A, US2360108A
InventorsAlfred Christie
Original AssigneeClaude R Wickard
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
High-frequency desiccator
US 2360108 A
Abstract  available in
Previous page
Next page
Claims  available in
Description  (OCR text may contain errors)

Oct. 10, 1944. c ams-1 15 2,360,108


A ORNEYS Patented Oct. 10, 1944 HIGH-FREQUENCY nasrcca'roa Alfred Christie, Washington Grove, MIL, assignor to Claude R. Wickard, as Secretary of Agriculture of the United States of America, and his successors in oifice Application August 29, 1942, Serial No. 458,720

1 Claim.

(Granted under the act of March 3, 1883, as amended April 30, 1928; 3'10 0. G. 757) This application is made under the act of March 3, 1883, as amended by the act of April 30, 1928, and the invention herein described, if patented, may be manufactured and used by or for th Government of the United States of America for governmental purposes without the payment to me of any royalty thereon.

This invention relates to the art of dehydrating samples of materials for the purpose of testing them, and to a desiccator suitable for this purpose. Many materials such as grains, flour, self-rising flour, etc., if dried in an ordinary heated desiccator will be additionally affected by the high temperature employed. This is obviously objectionable.

An object of the invention is to provide a method and a desiccator whereby samples may be dehydrated without other material changes. A further object is to provide a desiccator which will simultaneously dehydrate a plurality of samples.

A high frequency capacity heater may be advantageously used for dehydrating a sample. Such a device comprises essentially a pair of plates connected in the circuit of a high frequency oscillator and enclosed in a chamber which is partially evacuated. The plates are so positioned that a sample may be placed between them and internally heated due to the dielectric hysteresis loss of the material of the sample when it is subjected to an alternating electrostatic field.

A particular means for dehydrating samples is illustrated in the accompanying drawing, in which:

Figure 1 is a side view of a desiccator unit shown partially in section; and

Figure 2 is a cross section of the line 22 of Figure 1, and showing a very high frequency oscillator circuit in diagram.

The desiccator comprises a base I supporting a cup 2 and a cover 3 forming an enclosing chamber 4. These parts are formed from ceramics or other suitable non-conducting materials. The cover is provided with an evacuating tube 5 and a shut-off valve 6. Evacuation may be carried to a point just under that of production of a glow discharge. The chamber contains a ceramic platform I on which the crucibles 8, I, I, etc., for containing the samples, are seated. These crucibles are made from a dielectric material which is not substantially heated by reason of its location in an alternating electrostatic field, i. e., a material having a low dielectric hysteresis loss. Fused silica has ben found suitable for this purpose. The plates 9 and ID are elongated, rectangular, flat, metallic plates arranged face to face in spaced capacity relationship to each other and so positioned in the chamber that the 5 crucibles 8 may be placed between them.

The plates are energized by a very high frequency oscillator shown in diagram at the left of Figure 2. Any oscillator which will supply the desired energy to the desiccator plates at the proper frequency may be used. The particular oscillator herein shown comprises a pair of tubes l I and I2 arranged in push-pull, the filaments of which are heated by current supplied by a suitable transformer iii. The cathode current is supplied from any suitable direct voltage source H, fed to the filaments through the variable resistance l5 and a center tap on the secondary of the transformer l3, and fed to the plates through a very high frequency choke l8 and the center tap on a plate inductance ll. A feed-back to the tube grids is provided through the very high frequency choke I8 and the center tap of a grid inductance l9. Very high frequency chokes are added at 20, 2| to prevent feed-back of the very high frequency to the power line. The end taps of the plate inductance I! are connected with suitable lead conductors to the plates 9 and ID with sealed lead-ins at 22 and 23.

The power and frequency supplied by the oscillator will depend on the dimensional values employed. For a desiccator having 6 crucibles of 1%;"diameter and plates 8%" by 1%" spaced 1 apart, a plate outlet of substantially 250 watts at 112 megacycles frequency is satisfactory. Substantially such is provided by use of 'I'W-150 (Taylor Tube Co.) tubes with a plate voltage of 1,475 volts, with 15 equal to 700 ohms, with 16, 18, 20 and 21 formed from 24 turns of bare No. 14 wire, diameter, spaced A6" apart, with 19 formed from a single turn of 4" copper tubing, 8" in diameter, and with 17 formed from a single turn of copper tubing, 14" in diameter.

An important feature of the desiccator-relates to the manner of electrically connecting the plates to the oscillator. As seen in Figure 2, one lead conductor from the oscillator is connected to plate 9 at its end 22, and the other 50 lead conductor is connected to plate III at its end 23 opposite end 22, rather than at the end adjacent end 22. The purpose of this will be apparent from the following discussion.

When various samples of the same type of ma- 55 terial are totally dehydrated in a very high frequency capacity desiccator, experience has shown that the time of dehydrating is not dependent on the original moisture content within the range of moisture contents encountered in testing procedure, provided the power supply is constant. The rate of drying at any instant is proportional to the moisture content at that instant. Thus, the higher the moisture content of the sample, the faster the moisture is given off. When the time required to remove completely the free moisture from a particular kind of material is once determined, this time may be used for any sample of the same type of material, regardless of itsoriginal moisture content.

Furthermore, it several similar samples are dehydrated in a desiccator of the type herein described, except that the lead conductors be connected to adjacent ends of the plates 9 and II), it has been found that the rate of drying is no longer proportional to the moisture content at any instant, but that the samples positioned nearer the terminal connections dry more rapidly than expected. This shows that the power supplied is not the same at all regions between the plates, but is greatest at or near the terminal connections. This phenomenon may be due to the use of very high frequency resulting in a lag of charge distribution on the plates, suiiicient to prevent equal distribution of charge on all areas of the plates in the one-half interval of the cycle. That is, assuming that phase of the cycle in which plate 9 is being charged negatively, electrons will tend to pile up on that end of the plate near the terminal 22, while the positive charges will tend to pile up on plate i near its terminal connection. Therefore, if the terminal connections are on adjacent ends of the plates, the amplitude of field intensity is greater between the end of the plates having the connections than between their opposite ends.

If, however, the terminal connections be made at opposite ends of the plates, as shown in Figure 2, it has been found that the rate of drying at any instant at all regions between the plates is proportional to the moisture content of the sample at that instant. This indicates that the theory 01' charge distribution lag is correct. It negative charges pile up near terminal 22, a similar piling up of positive charges will occur near terminal 23. Due to symmetry of the arrangement, the potential difference between any point on one plate and an adjacent point on the other plate is substantially uniform at any instant throughout the plate areas, and the field intensity is the same at all regions between the plates.

It therefore follows that a desiccator constructed in accordance with this invention can be used to simultaneously dehydrate a plurality oi samples of similar material, without regard to their original moisture content, within the range of moisture contents ordinarily encountered in testing procedure, by placing the several samples between the plates and applying the very high frequency power to them for the interval of time required to remove completely the free moisture for the particular kind of material.

The foregoing description is intended to show but one embodiment of this invention, and is not to be taken as limiting the invention, except as is required by the appended claim.

Having thus described my invention, I claim:

The method of simultaneously totally removing the free moisture from a plurality of samples of similar dielectric material for moisture content testing purposes, comprising placing the several simples between a pair of elongated, substantially rectangular, flat, metallic plates arranged face to face in spaced capacity relationship, and applying very high frequency power to the plates with an oscillator having one of its lead conductors connected to one end of one plate and its other lead conductor connected to the opposite end of the other plate, whereby substantially the same field intensity exists at all regions between the plates, for an interval of time corresponding to that required to remove completely the free moisture from the particular kind of material without regard to its original moisture content.


Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US2427786 *Oct 3, 1944Sep 23, 1947Rca CorpApparatus for concentrating drugs
US2428615 *Dec 30, 1944Oct 7, 1947Skenandoa Rayon CorpMethod and apparatus for drying yarn packages in an electrostatic field
US2442114 *Apr 27, 1944May 25, 1948Rca CorpMethod of and apparatus for subjecting materials to a radio-frequency field
US2488839 *Oct 4, 1945Nov 22, 1949American Smelting RefiningProcess for drying selenium with high-frequency electric current
US2501776 *Jul 17, 1947Mar 28, 1950Kuljian Harry AsdourMethod of and apparatus for drying
US2502129 *Jul 29, 1944Mar 28, 1950American Viscose CorpMethod of treating filamentary materials
US2512311 *Sep 1, 1948Jun 20, 1950Gen ElectricHigh-frequency heating apparatus
US2521442 *Apr 5, 1944Sep 5, 1950Dehydration IncFood dehydration
US2529862 *Jun 22, 1943Nov 14, 1950Steinway & SonsDiaphragm unit and method of fabricating same
US2555450 *Nov 29, 1943Jun 5, 1951Lee Foundation For NutritionalHigh-frequency dehydrating method and apparatus
US2585825 *Sep 23, 1946Feb 12, 1952Nyrop Johan ErnstMethod of drying, concentrating by evaporation, or distilling heatsensitive substances
US2918728 *Oct 30, 1956Dec 29, 1959Buehler Ag GebApparatus for the drying of spaghetti and the like
US3041435 *Oct 13, 1958Jun 26, 1962American Mach & FoundryDielectric drying of materials
US3280470 *Jul 23, 1964Oct 25, 1966Kuntz Robert LMethod and apparatus for oven dehydrating compounds
US5367786 *Nov 6, 1990Nov 29, 1994Jennings; Thomas A.Method and apparatus for monitoring the processing of a material
US6098306 *Oct 27, 1998Aug 8, 2000Cri Recycling Services, Inc.Cleaning apparatus with electromagnetic drying
US6225611Nov 15, 1999May 1, 2001Hull CorporationMicrowave lyophilizer having corona discharge control
US7732211 *Oct 12, 2001Jun 8, 2010Avantium International B.V.Method and apparatus for screening of polycondensation catalysts
DE1125360B *Feb 27, 1957Mar 8, 1962Magnetic Heating CorpKammer zum Trocknen fester Gueter im kapazitiven Hochfrequenzfeld
U.S. Classification34/255, 34/92, 219/774
International ClassificationB01L1/00, B01L1/02
Cooperative ClassificationB01L1/02
European ClassificationB01L1/02