US2293728A

US2293728A - Dehydrating method and apparatus

Info

Publication number: US2293728A
Application number: US339860A
Authority: US
Inventors: Berthold G Freund
Original assignee: Individual
Current assignee: Individual
Priority date: 1940-06-11
Filing date: 1940-06-11
Publication date: 1942-08-25
Anticipated expiration: 1959-08-25

Description

25, 1942- B. G. FREUND DEHYDRATING METHOD AND APPARATUS Filed June 11, 1940 3 Sheets-Sheet 1 INVENTOR. BERTHOLD 5. FREUA/D h, ha/14M ATTORNEYS Aug'. 25, 1942. B. a. FREUND 2,293,723

DEHYDRATING METHOD AND APPARATUS V Filed June 11, 1940 s Sheeks-Sheet 2 I INVENTOR. BERT/ OLD 6. FREl/IVO ATTORNEYS Patented, Aug. 25, 1942 UNl-TED STATES PATENT" OFFICE 2,293,728 DEHYDRATING ME'rnon AND APPARATUS Bcrthold G. Freund, New York, N. Y. Application June 11, 1940, Serial No. 339,860 20 Claims. (01. 99-199)- The invention relates to a method and apparatus for dehydrating or desiccating materials,

such as cellulose products, like alfalfa, green sawdust, wood flour,'etc., and food products, including fish, meats, vegetables, fruits, and the like, for instance, brewery mash.

The processes and apparatus of .the prior art for the dehydrating or drying of these materials involve the exposure of the product to be dried to a comparatively high and uniform temperature. In contradistinction to this prior art method and apparatus, the products of which uated drying can be properl and most eflicaciously applied, whereupon the exact amount of heat necessary to remove a specific "quantity of the moisture contained in the material is ap lied at each stage of the drying process, The drying at each stage, in accordance with the present in vention, is controlled to prevent excessive drying, both from the point of view of the time element and the quantity of heatapplied, so as to prevent scorching oi the produc In accordance with the present invention, the I gradual drying, in stages, of the material, is accomplished by controlled temperature and air circulation producing a grading of the heat apeach stage being exactly in proportion to the amount of moisture still contained in and tobe removed from the material. The material to be dried is first subjected to a predehydrating step temperature of the heat being applied, the first degree of heat being efiective to open th pores of the material, so as to permit the subsequent uniform application of the final drying heat to the material. a

' In its broadest aspecta'the present invention" consists in the provision of an apparatus whereby the material to be dried, whether a cellulose product or a food product, is first disintegrated by a rotary cutter or mill into substantially uniformly sized particles. whichuniformly sized particles are then conducted through an automatically feeding. and'automatically discharging prefinally .dehydratirig device, from which it is conducted-55 capable of receiving the comparatively high dcto a hopper disposed above the main dehydrating unit of the apparatus, through which unit the material is gradually passed in succeeding levels constituted of a series of discs and circular. platforms and stationary scraping devices, the material being passed in sequence from a section of the. dehydrating apparatus, in which a certain amount of heat and circulation is applied to the material, tea-second section in which a heat of a uniform temperature of lesser degree is applied to the materiahand finally to a sectionof the apparatus in which the degree of heat applied is 'still less. In each of the sections of the main dehydrating unit, the degree of heat being applied to the material is controlled by a suitable apparatus, the air, circulation involved in the application of such heat 'being similarly controlled by suitable devices attached to the unit.

By certain novel features of the apparatus and by the combination of a series of steps in the carrying out of the dehydrating process, there is secured, in accordance with the present invention, a substantially complete control of the temperature and of the air circulation resulting in 5 a uniform graduation of the heat being-applied to the material in order to dry it, with the distribution' of the heat at the various stages being dependent upon or in proportion to the amount of moisture, which is still contained in the material at the specific stage,'and it is, therefore,

to be removed at such stage, and each of the subsequent stages. For securing the proper and uniform application of this graduated heat and-air circulation, I provide novel means for automati- 5 cally agitating the material to be dried in order plied to the material, th heat. thus applied at to expose, during the heat treatment, all of the parts and surfaces of the'material and the minute particles thereof uniformly to the heat and to the air circulation.

An important feature of my invention is the which is itself completely controlled as to the.-

provision of the predehydrating unit which is effective to bring the material, prior to its introin just the proper state conducive to the gradual,

uniform, and complete dehydration thereof. The function of such pre-dehydrating unit, which, just like the main. dehydrating unit, must be carefully controlled with respect to the amount and the degree of heat being applied to the ma- J-Vidllfll particles, so that when the material reaches the main dehydrating unit, it is gree of heat applied at the first stage of the main dehydrating process without the danger of scorching the material a has been frequently.

the difiiculty with the processes and apparatus of the prior art, in which the high degree of heat abruptly applied to the material sought tobe dehydrated has caused a destruction of the cellular structure of the material and the scorching of the outer surfaces of the individual particles while leaving the interior portions substantially moist.

My novel dehydrating apparatus is character.

ized also by the provision of a series of rotating supporting surfaces for the material to be dried within the main dehydrating unit, constituting platforms upon which the material is exposed to the necessary amount and degree of heat for tending substantially throughout the length thereof. Along the inner surface of the cylindrical casing I8 is provided insulation 2| of approximately one inch thickness. The entire pre-dejust the proper duration of time, with the agitation of the individual particles of the mass of material being accomplished by fixed scrapers which scrape the material, after the Proper degree of exposure to ,the heat and air circulation, to the next platform and thus sequentially throughout the extent of the main dehydrating unit to the discharge outlet thereof.

My apparatus is characterized also by the disposition of the air circulation producing units or blowers which, together with the suitably disposed heating elements, controlled by thermostats, provide the application of the graduated degree and quantity of heat and air circulation necessary to produce a properly and completely dried product.

A specific embodiment of an apparatus constructed in accordance with my invention, and which is suitable for carrying out my novel prochydrating unit is approximately 15 inches in diameter.

From the pre-dehydrating unit I5, the material to be further dried is conducted through the pipe It to a hopper 25, the progress of thematerial through the pre-dehydrating unit and the pipe it into the hopper 25 being enhanced by the air suction device 26. From the hopper 2| the material enters the main dehydrating unit which will now be described:

The unit is housed in a chamber 21 through the center of which extends a vertical shaft ll rotated by gearing connected to pulley 2! rotated by means of a belt 30 by a motor 3| through the speed regulation of which the speed of .rotation ess, is illustrated in the accompanying drawings,

in which Fig. 1 is a front view of the complete apparatus, including the cutting mill, the predehydrating unit, and the main dehydrating unit; Fig. 2 is a vertical section through the main dehydrating unit; Fig. 3 is a horizontal sectionthrough the main dehydrating unit; 8. 4 is,a vertical longitudinal section through the pre-dehydrating unit; and Fig. 5 is a vertical transverse section through said pre-dehydrating unit.

'Referrin'g more particularly to the drawings, in which similar reference characters identify similar parts in the several views, the material disintegrating unit of my novel apparatus comprises a cutter or mill III of conventional construction mounted upon a table I l with a gravitational delivery pipe l2 connected to the cutter from which the material to be dehydratedin fine, uniform particles is sucked by blower fan l3. to pipe ll leading to the pre-dehydrating unit. The

cutter Ill is-operated by a system of belts and.

unit. generally designated end and an outlet pipe I8 of slightly larger diameter extending from the opposite end of the casing, both of the pipes l1 and it being centrally disposed longitudinally of the casing. The

' This screening l9 forms a cylinder which is apof the shaft 28 is controlled. Surrounding and secured to the shaft 28 in any convenient man ner, for instance, by being keyed thereto, is a pipe 32 from which extend four radial supports to which is secured a fiat disc 24. Above the upper surface of each disc are positioned two series of

blades

35 and 36, depending from supports 22, extending from two opposite corners of the chamber, the first series of blades extending in one direction from the pipe 32, and the second in the diametrically opposite direction from such pipe. Intermediate each of two adjacent discs 34 is a circular platform 31 supported upon radial brackets extending from the pipe 32 and having their peripheral edges bound by an upwardly extending flange-l8. Each of the circular platforms 3! has a central aperture 38 immediately surrounding the pipe 22.

Extending from the two other corners of the chamber 21 and disposed to saddle the radius of each of the circular platforms 21, is' a bracket 40 from which depend a series of blades ll, with one series, on one half of a platform 21 extending in one direction and the series overlying the other half of the same platform extending in the diametrically opposite direction.

Each of the discs 34 is provided with a plurality of apertures 42 indiscriminately disposed throughout the surface of the disc for the purpose her'einafter described. Each of such discs,"

which there may be conveniently positioned a window 45 to permit visual observation of the operation of the unit.

On one side of the chamber 21 is an auxiliary chamber 46, in which may conveniently be housed

electric heaters

41 and 48 and companion air circulating devices,"for instance, fans 4! and a 50. The motors 5| and 52 for these fans may be conveniently positioned outside of the chamber but supported upon the wall thereof. Disposed between the

heaters

41 and 48 approximately ing portion of the dehydrating unit. of depending upon the shovelling of the material centrally of the vertical extent of the chamber 46 is a rheostat 53 controlled by a dial or knob 54 extending outside of the chamber. I

On the opposite side of the chamber 21 is a second auxiliary chamber 55 within which approximately centrally of the vertical extent. of the chamber are disposed the heater 56 and fan 51, the latter operated by electric motor 58, mounted exteriorly on the wall of the chamber. Be-

low the heater 56 is a rheostat 59 and its control knob 60, extending outside of thechamber and above such heater is rheostat GI and its control knob 62.

The entire unit, including the front and rear faces of the main chamber 21 and the exterior walls of the

auxiliary chambers

46 and 55 are provided with insulation 63.

From the top of the chamber 21 extends the exhaust outlet 64 with a damper control knob 65, while the material after dehydration issues throughan outlet conduit 68.

As the material to be dried passes through the main chamber with the progressive dehydration thereof as hereafter described, it first encounters the heat'impinged against it by the circulation caused by the fan 50, the heat emanat- 8' temperature of approximately 180 F.; at the next stage of the dehydration, the material is acted upon by the blasts of heated air circulated by the fan' 51 and emanating from the heaters 56, maintaining a temperature of approximately 140 F.; and thereafter in the third or final stage of the dehydration process, the material is acted the disc to the next succeeding platform and I from the platform to the next succeeding disc is repeated throughout the extent of the rotatto the peripheral edge of each of the discs, each of suchdiscs as shown in Fig. 3 is provided with fromelectric heaters 48, maintaining a Instead aplurality, of staggered holes of approximately" one inch in diameter throughout the face of the disc, through which holes the material can drop through the disc to the next succeeding platform. I have found that approximately 24.

of these staggered holes in each disc are capable of providing a smooth continuity of operation with excellent results as to the dehydration of the material being treated. It will be noted that the alternate batteries of discs and platforms are divided into three seriesor stages, the first of which is supplied with hotair by means of the topmost blower and electric heat element, the

air being impinged against the material beingdried being heated to between 160 to 200 F'., the medium of 180 being given hereinabove as illuse trative. I have found that after the'pre-dehy drating process to which the material has. been subjected prior to the introduction into the-main dehydrating unit, this quantity. of heatis as much as the material will stand without destroying its cellular structure. The next battery of between 100 and 120. The moisture taken out of the material by the'heated air is dissipated by an exhauster, the saturated air being let out of the chamber by means of the suction fan 61, positioned at the top ofthe chamber within'the pipe 68 and controlled by a damper 69. It" will be understood by those skilled in the art that a condenser of conventional construction may be used for this purpose.

I have found that there is a certain relationship between the angularity of the blades, their arcuate disposition and the efliciency with which the complete dehydration of the material acted.

upon is accomplished. The angularity of the blades must be such that at one complete revolution of the disc, the entire surface of such disc has been scraped by the blades. I have found by experimentation that this angularity of the blades to the vertical is approximately 70.

The purpose of the blades is to automatically stir or agitate the particles of the material being dried, which material forms a layer of approximately inch in thickness upon the discs during the heat treatment so as to expose all surfaces and parts of the individual particles of the material substantially uniformly tothe heat being applied thereto.

While I have described a specific embodiment of my invention, and particularly one specific form of an apparatus for carrying out my novel process, it is obvious that modifications therein, particularly in the arrangement and configura-, tion of the several parts (if such apparatus, and in the steps of the process may be made without departing from my invention.

I claim: 1. Process for dehydrating cellulose products,

foods, and the like, which comprises disintegrating the material into substantially uniformly sized minute particles, subjecting the material to pre -dehydration to a degree removing only a small quantity of the moisture contained therein, and then completely drying the material in a plurality of drying stages by means of controlled heat of difierent degrees for each stage. 7

, 2. Process for dehydrating celluloseproducts, foods, and the like, which comprises disintegrating the material into. substantially uniformly sized minute particles} subjecting the material to predehydration to a degree removing only a small quantity of the moisture contained therein, and

then completely drying the material in a plurality of drying stages by means of controlled-heat,

of different degrees for each stage, the first drying stage being conducted at :a comparatively temperature, suflicient to remove a quantity of the moisture contained in the material discs and platforms receive heat atbetween 140 an 1 6o F., 140" beinggiven as illustrative herewithout destroying its cellular structure, the intermediate stage-:at' somewhat lower tempera-.

ture, and the final stage at astill lower tem perature.

3. Process for dehydrating cellulose products,

foods, and thelike, which comprisesdisintegrating the material: into substantially uniformly sized minute particles, subjecting the material to' raredehydration to, a degree removing .only a small quantity .of the moisture contained there-: in, and then completely drying the material in a plurality of drying stages by providing controlled heated air of different degrees for each stage in proximity to the material, and circulating said heated air through said is-being agitated. I I

4. Process for dehydrating cellulose products,

inabovawhile the last-battery receives heat at foods,1and the like, winch comprisesdisintegrat material while it ing the material into substantially uniformly sized minute particles, subjecting the material to pre-dehydration to a degree removing only a small quantity of the moisture contained therein, and then completely drying the material in a plurality of drying stages by providing controlled heated air of different degrees for each stage in proximity to the material, and circulating said heated air through said material while it is being agitated, the first drying stage being conducted at a comparatively high temperature suiiicient to remove a quantity of the moisture contained in the material without destroying its cellular structure, the intermediate stage at somewhat lower temperature, and the final stage at a still lower temperature.

5. The method of dehydrating cellulose products, foods, and the like, which comprises disin- -tegrating the material into uniformly minute particles thereof uniformly to the drying'heat,

said drying being carried out by means of con;

- of controlled heat of different degrees for each stage, said pre-dehydrating means comprising a cylindrical casing, a plurality of tubular screens surrounding the path of the material through dehydrating means comprising a cylindrical casing, a plurality of tubular screens surrounding the path of the material through said casing, a plurality of heating elements disposed longitudinally of the casing and surrounding said tubular screens and means for controlling the temperature of the heat from said heaters.

- 11. In an apparatus for dehydratingcellulose products, food's, and the like, means for subjecting the material to pre-dehydration prior to the I final, complete drying of the material, said predehydrating means comprising a cylindrical casing, a plurality of tubular screens surrounding the path of the material through said casing, said screens being successively, from the center of the casing outwardly, of finer-mesh, a plurality of trolled heat of difierent degrees of temperature for each stage, the first drying stage being conducted at a comparatively high temperature, the intermediate stage at somewhat lower temperature, and the final stage at a still lower temperature, the material being fed from one drying stage to the next succeeding stage after completion of the degree of agitation and application of suiiiheating elements disposed longitudinally of the casing and surrounding said tubular screens, and

a means for controlling the temperature of the heat emanating from said heaters.

12. Apparatus for dehydrating cellulose prod- "ucts, foods, and the like, which comprises means for disintegrating the material into substantially cient heat to remove a quantity of moisture from stages.

8. Apparatus for dehydrating cellulose products, foods, and the like, which'comprises means for distintegrating the material into substantially uniformly sized minute particles, means for preheating the material to pre-dehydrate the same by removing only a small quantity of the moisture contained therein, and means for completely drying the material in a plurality of drying stages, said last named means comprising a plurality of heating units, one for each drying stage,

jecting thematerial to pre-dehydration, and a. multi-stage dehydrating unit for completely drying the material in a plurality of drying stages by means of controlled heat of difierent degrees for each stage, said multi-stage dehydrating unit comprising a heating unit for the first drying stage providing a comparatively high tempera- 5 ture,a second heating unit for the intermediate one of said heating unitsproviding heat at a comparatively high temperature, the heating unit at the intermediate stageproviding heat at a stage providing heat at a somewhat lower temperature, and a third heating unit for the final stage providing heat at a still lower temperature.

multi-stage dehydrating unit for completely dry-- ing the material in a plurality of drying stages by means of controlled heat of different degrees for eachstage, said multi-stage dehydrating unit comprising a heating unit, for the first 'drying stage providing a comparatively high temperature, a second heating unit for the intermediate stage providing heat at a somewhat lower temperature, and a third heating unit for the final stage providing heat at a still lower temperature, said multi-stage dehydrating unit also comprising a chamber, a'plurality of rotatablediscs positioned therein, means for rotating said discs, and scrapers mounted above said discs for agitating the particles of material to be dried and to shovel the same from one discto arr-underlying disc in succession through the chamber from the top to the bottom thereof.

14. Apparatus for dehydrating cellulose produniformly sized minute particles, means for subjecting the material to pre-dehydration, and a multi-stage dehydrating unit for completely drying the material in a plurality of drying stages the vertical extent of the chamber and at differ- 'ent temperatures successively reduced from the by means of controlled heatof different degrees for each stage, said multi-stage dehydrating unit comprising a chamber, a plurality of rotatable discs positioned therein, means for rotating said discs, and scrapers mounted above said discs for agitating the particles of the material to be dried upon rotation of said discs and to shovel the same from one disc to an underlying disc in succession through the chamber from the top to the bottom thereof. 15. Apparatus for dehydrating cellulose products, foods, and'the like, which comprises means for disintegrating the material into substantially uniformlysized-minute particles, means for subfrom the top-t0 the bottom thereof.

top to the bottom of said chamber.-

17. Apparatus for dehydrating cellulose products, foods, and the like, which comprises means for disintegrating the material into substantially uniformly sized minute particles, means for subjecting the material topre-dehydration, and

means forcompletely dehydrating the material in a plurality of drying stages by'controlled heat of different degrees for each stage comprising a chamber, a plurality of rotatable discs positioned therein, means for rotatingsaid discs, a plurality of circular platforms disposed between said discs,

scrapers mounted above said; discs and platforms for agitating the particles of the mateiial to be dried and to shovel the same from one disc to the underlying platform in successive series through the chamber from the top to the bottom 7 I thereof, means for supplying heated streams of air to said material in stages throughout 'the vertical extent of the chamberat different temperatures successively reduced from the'toplto the bottom of said chamben'and a plurality of blower 16. Apparatus for dehydrating cellulose prcducts, foods, and the like, which comprises means for disintegrating the material into substantially uniformly sized minute particles, means for sub- Q jecting the material to pre-dehydration, and a multi-stage dehydrating unit for completely dryby means of controlled heat of different degrees for each stage, saiddehydrating unit comprising a chamber, a plurality of rotatable discs posiunits positioned within the chamber in proximity to, and so as to be effective to directthe heated streams of air against, thematerial to be dried.

18. An apparatus. as claimed in claim 14, in which the scrapers are disposed from brackets extending over the discs, alternate series of said scrapers being disposed so as to shovel the 'material in opposite directions.

19. An apparatus as claimed inclaim 14,- in

I which the scrapers are disposed from brackets 'ing the material in a plurality of drying "stages tioned therein, means for rotating said discs, and

scrapers mounted above said discs for agitating the particles of the material to be dried and to shovel the same from one disc to an underlyingdisc in succession through the chamber from the top .to the bottom. thereof, and means for supplying heat said material in stages throughout extending over the discs, alternate series of said scrapers being disposed so as to shovel the ma,-

terial in opposite directions, said scrapers having 7 an angularity to the vertical of approximate ly '70".

20. An apparatus as claimed in claim 15, in which the scrapers are disposed from brackets extending over the discs and platforms, alternate series of said scrapers being'disposed so asto shove the material in opposite radial directions upon said discs and platforms, respectively;

,nEaTHoLD- G. FaEUNn