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US2370422A - Dehydrator - Google Patents

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US2370422A
US2370422A US459289A US45928942A US2370422A US 2370422 A US2370422 A US 2370422A US 459289 A US459289 A US 459289A US 45928942 A US45928942 A US 45928942A US 2370422 A US2370422 A US 2370422A
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trays
air
unit
units
cabinet
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US459289A
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Jesse O Reed
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CLAUDE R WICKARD
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CLAUDE R WICKARD
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B25/00Details of general application not covered by group F26B21/00 or F26B23/00
    • F26B25/06Chambers, containers, or receptacles
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/02Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B9/00Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards
    • F26B9/06Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards in stationary drums or chambers
    • F26B9/066Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards in stationary drums or chambers the products to be dried being disposed on one or more containers, which may have at least partly gas-previous walls, e.g. trays or shelves in a stack

Definitions

  • This invention relates to dehydrating apparatus, particularly useful in the dehydration of food products.
  • the cabinet and tunnel types two general types of dehydrators, known as the cabinet and tunnel types.
  • the food products are loaded on open trays which are placed in a closed cabinet, and drying air or other gas is circulated over them to remove the desired amount of vaporizable water. The trays are then removed, and the process is repeated for each batch.
  • the tunnel type the process is continuous rather than in batches.
  • the trays of food products are started at one end of the long timnel, and means is 'provided to move them gradually toward the other end. Drying air or gas is circulated in the tunnel throughout its length so that during the waste both in the heat and in the power required to circulate the air through zones in which no dehydrating is being accomplished.
  • the tunnel type has certain'advantages .over
  • the usual tunnel type also has several disadvantages, however.
  • the air passes lengthwiseof the tunnel from one end to the other, and it cannot be kept at the same temperature or relative humidity throughout. Ordinarily, the tunnel can not operate successfully at the same time upon diflerent types ofproducts requiring diflerent con ditions of temperature and humidity.
  • the entire tunnel must be conditioned when the first trays are started through at the beginning of the run, and maintained until the last trays of the run have passed completely through.
  • This involves a Among the objects of this invention are the provision of a dehydrating apparatus which combines the advantages of both the tunnel type and the cabinet type; the provision of a flexible dehydrating apparatus adapted toluse for dehydrating all types of food products; the provision for obtaining and maintaining all desired conditions which is convertible from a unit type to the tunnel type by the mere addition of similar units; the provision of an apparatus of few parts which can be made into a unit type or a tunnel type at will; and the provision of improvements in cabinet type dehydrators generally.
  • Figure l is a perspective view showing several cabinet units joined together, forming a tunnel
  • Figure 2 is a section ontne line 2-2 of Fi ure 1 h
  • Figure 3 is a section on the line 3-4 of Figure "2, certain parts being brokenaway to illustrate the'st'ructure more clearly.
  • FIG. 4 is a side view of an improvedcabinet type of dehydrator.
  • Figure 5 is an enlarged section on the line 5-5 of Figure 4.
  • Figure 6 is an enlarged section onthe line 6-5 of Figure 4..
  • Figure '1 is a perspective view of a tray suitable for use in any of the dehydrators.
  • Figure 8 is an exploded three-dimensional view of a modified tray and bailie suitable for use in any of the dehydrators.
  • Figure 91 s a sectional view of a few trays and banles of the type shown in Figure 8, showing the manner of operation.
  • Figure. 10 is athree-dimensional view of one of the bailles of Figure 8.
  • the floors of the trays are shown as formed from spaced apart slats l0, although screen may be used.
  • the tops H have solid floors I2 forming a ceiling for the drying chamber. It may be observed, when several individual cabinet units are arranged as shown in Figure 1 and no trucks are present, that a tunnel results.
  • the trucks and trays are of a predetermined definite length relative to the individual cabinet units, so that they may be pushed into the tunnel at one end, and when the rear truck is stopped at its proper location, all other trucks will be properly positioned.
  • flexible flaps I3 acting as seals, are fixed in the chambers at positions near the junctures of the individual cabinet units to engage the ends of the trays when the trucks are properly positioned. These flaps allow the trucks and trays to pass, but they substantially prevent gas circulation between the individual chambers in conjunction, of course, with the end pieces of the trays and the solid floors of the tops.
  • the various cabinet units are secured together with flanges and bolts, as shown at ll.
  • Each unit has openings in its opposite end walls for the admission and egress of products-to be dehydrated, and the several units are connected together with the openings matched.
  • the end units are provided on their free ends with suitable doors i5, which can be removed and flanges substituted,if other units are to be added on the ends. If only one cabinet unit is desired, doors are generally provided at both its ends, although the'doors may be omitted.
  • Each cabinet unit is provided with a circulating and heating means.
  • a fan [6, preferably of the forced feed multiple type, is located in compartment I'I above the unit.
  • the fan is driven by a variable speed motor (not shown) and circulates air through a heater l8, which maybe of any desired type, but is preferably a steamheated radiator, a connection of which is shown at ii.
  • the heated air leaves each fan unit through an exhaust duct 20 and is forced through chamber 2
  • the function of the damper system is to control the humidity of the drying air. Any part of the exhaust air may be returned to the heater rather than to the outside atmosphere. Returning larger quantities of the exhaust air to the heater increases the humidity of the drying air.
  • Suitable instruments such as a dry bulb thermometer 30 and a wet bulb thermometer 30', may be positioned in the drying air current for observation, whereby manual adjustments can be made on the heat admitted to the heater for maintaining the desired dry bulb temperature and on the damper system to maintain the desired wet bulb temperature of the circulating air.
  • Each cabinet unit is provided with means rendering it useful for other steps than drying.
  • a perforated steam pipe is provided at 3i, to admit steam for blanching purposes. This pipe may also be used for increasing the relative humidity of the air, as may be necessary at the start of dehydrating a new batch, for example.
  • blanching can be carried out to any desired extent.
  • the chamber can then be immediately aerated and drying started by simply shutting oil? the steam and resetting the damper system.
  • a complete process may be carried out with one cabinet unit, by successively effecting different processing steps on a batch of products loaded in the unit. If, however, it is desirable to operate several units together as a tunnel, each may be set and made to perform any desired step such as blanching, gas treatment or drying.
  • the first cabinet unit may be used for blanching or used for gas treatment to inhibit enzyme reactions, or if separate units are desired for these treatments, the first and second may be thus employed.
  • dry gases may be used and circulated with high velocity, since the food product is heavy at this stage.
  • the drying may be eifected at increasing temperatures and at decreasingly lower air velocities, to prevent blowing the light, dry
  • All units may be operated at the same time on diiferent batches, the trucks being pushed ahead to convey the products from one unit to the next unit.
  • the cabinet type of dehydrator herein shown is generally similar to the cabinet unit used in Figure 1. It provides a processing chamber 40 into which the truck 4
  • the fan- 50 and heater of this dehydrator may be acommercially obtainable heating unit of predetermined capacity, if desired, and if constant heat and air are supplied, the tray capacity can be adjusted to care for varying conditions.
  • a blanching steam admission pipe 52 similar to that described in reference to the first modification, is provided.
  • Air is exhausted from the fan through exhaust duct 53, and passes a set of fin 5454--5l, ad-
  • the air inlet port 55 is controlled by a valve 56, and the air outlet port 51 is controlled by damper 58.
  • the valve and damper are so coupled together that when the valve is opened to admit dry outside air, the damper is set to open the air outlet port and to deflect the air away from the heater and out of the port.
  • Figure 5 shows an extreme setting of the system inwhich all of the air is deflected to the outside.
  • the coupling is provided by a link 89 connecting crank arms 56' and 58' attached to the valve and damper, respectively, at their pivotal axes.
  • a control rod 60 for setting the damper system is attached to the damper crank arm 58.
  • thermometers Observation dry and wet bulb thermometers are shown at 6! and 84, respectively, which may be used in connection with manual control means as described in reference to Figure 3. Automatic control is, however, preferable, and may be provided by the following described means shown schematically.
  • of known type canbe coupled to the control rod, and the damper system regulated automatically to maintain a desired humidity by coupling the motor control to a humidostat or wet bulb control apparatu of wellknown type, located in the box shown at 81.
  • the dry bulb temperature may be controlled by a thermostat or dry bulb control apparatus also automatic control of the dry bulb temperature
  • Inspection windows are provided at 65, 68 and 61.
  • the trays provide for circulating the air over the food products.
  • Figures 8, 9 are directed to an improved tray system in which the air is forced to circulate through the tray floors or screens. with some products, this results in a more unliorm drying, and makes it possible to'load the trays deeper.
  • the tray 10 is provided with side and end walls H and 12, resp ctively, of the same height, and a perforated floor I3, herein shown as a screen.
  • a baflle 14 positioned between each pair of screens, is provided with solid end walls II of the same height and a solid floor 18. Each products loaded on the trays.
  • side wall of the baille is open above the floor on one side and below the floor on the other side, as shown at 11, but is otherwise closed by pieces II.
  • the trays and battles are alternately stacked, as shown in Figure 9. Due to this arrangement, the air is forced to travel as shown by the arrows, and is forced through the tray floors and food Strips may be fastened to the end walls 15 of baffles 14 so as to hold said bailles in spaced apart position, and the trays Ill may be slid between the ballles.
  • a dehydrating apparatus comprising at least two separate, similar, individual cabinet units, each unit having an opening in each of its end walls for the admission andegress of products to be dehydrated and each unit being provided with means for effecting a first gas-processing step and with means for effecting at least one more gas-processing step different from that of gether with the openings matched to form a tunnel type dehydrator, whereby when so connected together the first unit may be employed to eflect the first processing step on a first batch of prod-' ucts loaded in the first unit, following which the first batch of products may be conveyed into the second unit and a second batch of products placed in the first unit and the second unit may be em-' ployed to effect the second processing step on the first batch of products while the first unit is circulation between the individual units when the said units are connected together.
  • a dehydrating apparatus comprising at least two separate, similar, individual cabinet units,
  • each unit having an opening in each of its end walls for the admission and egress of products to be dehydrated, trays having closed ends so constructed that when the trays are stacked on each other the ends form a closed wall, each unit being provided with means for eflecting a first gasprocessing step and with means for efiecting at least one more gas-processing stepdifferent from that of the first-mentioned means, whereby a single unit may be employed to effect the first processing step followed by effecting the next processingstep on a batch of products loaded on the trays imthe unit, and means for detachably connecting the'units together with the openings matched to form a; tunnel type dehydrator, whereby when so connected together the first unit may be employed to effect the first processing step on a batch of products loaded in the first unit, following which the first batch of products may be conveyed into the second unit and a second batch or products placed in the first unit and the second unit may be employed to effect the second processing step on the first batch of products while the first unit is effecting the first
  • a tray system comprising removable trays each having a perforated floor and solid side and end walls, said side and end walls being of the same height, and removable baflles corresponding in size to the trays, said bailles each comprising a solid floor, solid end walls extending above and below the floor, one.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Drying Of Solid Materials (AREA)

Description

Feb. 27, 1945.
J. O. REED DEHYDRATORS Filed Sept. 22, 1942 5 Sheets-Sheet 1 5 mmmi INVENTOR I J.0.REED ,g/Q 9 m,
QM. law Y ATTORNEYS Feb. 27,1945. J. o. REED 2,370,422-
DEHYDRATORS Filed Sept. 22,19 42 5 Sheets-Sheet 2 INVENTOR J'.O.REED
AT ORNEYS l I I I I I I I I I I I I I I l I I I I I J. o. REED Feb. 27, 1945.
DEHYDRATORS 5 Sheets-Sheet 3 Filed Sept. 22, 1942 INVENTOR J .O-REED A TORNEYS Feb. 27, 1945. ED 2,370,422
DEHYDRA'IORS Filed Sept. 22, 1942 5 Sheets Sheet-4 I HUM-g INVENTOR J.O.REED
Feb. 27, 1945.
J. o. fiEED 2,370,422
DEHYDRATORS Filed Sept. 22, 1942 5 Sheets-Sheet 5 ATTORNEYS Patented Feb. 27, .1945
UNITED STATES PATENT OFFICE Jesse 0. 41. 12532? minor to Claude it. Wiokard, as Secretary of Agriculture of the United States. of America, and hi moeslcrs inoilice (Granted under the act of March 3,
ms. at
April 30, 1 9 28; 370 0. G. 75'!) 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 the Government of the United States of America for governmental purposes without the payment to me of any royalty thereon.
This invention relates to dehydrating apparatus, particularly useful in the dehydration of food products.
At present, two general types of dehydrators, known as the cabinet and tunnel types, are in use. In the cabinet type, the food products are loaded on open trays which are placed in a closed cabinet, and drying air or other gas is circulated over them to remove the desired amount of vaporizable water. The trays are then removed, and the process is repeated for each batch. 'In the tunnel type the process is continuous rather than in batches. The trays of food products are started at one end of the long timnel, and means is 'provided to move them gradually toward the other end. Drying air or gas is circulated in the tunnel throughout its length so that during the waste both in the heat and in the power required to circulate the air through zones in which no dehydrating is being accomplished.
'of dehydrating: the provision pf an apparatus type dehydrator.
passage of the trays the food products are de- 1 hydrated.
The tunnel type has certain'advantages .over
the cabinet type. In large scale operations, a continuous process is more desirable than a batch process. The flow of materials in a continuous process is more even and regular-and fewer operations are necessary. v
The usual tunnel type also has several disadvantages, however. The air passes lengthwiseof the tunnel from one end to the other, and it cannot be kept at the same temperature or relative humidity throughout. Ordinarily, the tunnel can not operate successfully at the same time upon diflerent types ofproducts requiring diflerent con ditions of temperature and humidity. Also, in dehydrating certain food products, it is desirable to subject them at some point in the process to treatments other than dehydrating, such as blanching. This can be accomplished with some types of cabinet dehydrators, but not with usual tunnel dehydrators, since all the food products in the tunnel are operated upon simultaneously with respect to one operation or another. There is also loss in the starting and stopping of'the tunnel type of dehydrators. The entire tunnel must be conditioned when the first trays are started through at the beginning of the run, and maintained until the last trays of the run have passed completely through. This involves a Among the objects of this invention are the provision of a dehydrating apparatus which combines the advantages of both the tunnel type and the cabinet type; the provision of a flexible dehydrating apparatus adapted toluse for dehydrating all types of food products; the provision for obtaining and maintaining all desired conditions which is convertible from a unit type to the tunnel type by the mere addition of similar units; the provision of an apparatus of few parts which can be made into a unit type or a tunnel type at will; and the provision of improvements in cabinet type dehydrators generally.
Other objects of the invention will be apparent I from the following detailed description and attached, drawings, in which,
Figure l is a perspective view showing several cabinet units joined together, forming a tunnel Figure 2 is a section ontne line 2-2 of Fi ure 1 h I Figure 3 is a section on the line 3-4 of Figure "2, certain parts being brokenaway to illustrate the'st'ructure more clearly.
' Figure 4 is a side view of an improvedcabinet type of dehydrator. I
Figure 5 is an enlarged section on the line 5-5 of Figure 4.
Figure 6 is an enlarged section onthe line 6-5 of Figure 4..
Figure '1 is a perspective view of a tray suitable for use in any of the dehydrators.
' Figure 8 is an exploded three-dimensional view of a modified tray and bailie suitable for use in any of the dehydrators.
Figure 91s a sectional view of a few trays and banles of the type shown in Figure 8, showing the manner of operation.
Figure. 10 is athree-dimensional view of one of the bailles of Figure 8.
Referring to the drawings, and in particula to the apparatus of Figures 1, 2 and '3, similar. separable individual cabinet, units l, 2 and 3 are shown. coupled together in Figure 1. Three units I are shown, although the apparatus is adapted to any number, and may have as many as six or more for carrying out the most complete process.
The various constructional details which are obcabinet dehydrator in itself. It provides a drying or processing chamber 4 into which a truck 5 loaded with trays 6 may be pushed. Guide rails I, provided on the floor in the drying chamber, properly position the truck. Each tray shown in detail in Figure '7 is provided with end pieces 8 and open side pieces 9. Figure 3 shows a double row of trays stacked one on the other, with the end pieces forming partitions which close the ends of th drying chamber. Air to pass over the trays is admitted and exhausted through the open side pieces 9, which restrict the area and, act as a grille to control the delivery of air over the trays. The total inlet and total exhaust areas provided by the open side pieces should be substantially equal to the cross-sectional area of the fan exhaust duct to maintain a substantially constant air velocity.
The floors of the trays are shown as formed from spaced apart slats l0, although screen may be used. The tops H have solid floors I2 forming a ceiling for the drying chamber. It may be observed, when several individual cabinet units are arranged as shown in Figure 1 and no trucks are present, that a tunnel results.
The trucks and trays are of a predetermined definite length relative to the individual cabinet units, so that they may be pushed into the tunnel at one end, and when the rear truck is stopped at its proper location, all other trucks will be properly positioned. In order to isolate theindividual chambers of the several cabinet units from each other, flexible flaps I3, acting as seals, are fixed in the chambers at positions near the junctures of the individual cabinet units to engage the ends of the trays when the trucks are properly positioned. These flaps allow the trucks and trays to pass, but they substantially prevent gas circulation between the individual chambers in conjunction, of course, with the end pieces of the trays and the solid floors of the tops.
The various cabinet units are secured together with flanges and bolts, as shown at ll. Each unit has openings in its opposite end walls for the admission and egress of products-to be dehydrated, and the several units are connected together with the openings matched. The end units are provided on their free ends with suitable doors i5, which can be removed and flanges substituted,if other units are to be added on the ends. If only one cabinet unit is desired, doors are generally provided at both its ends, although the'doors may be omitted.
Each cabinet unit is provided with a circulating and heating means. A fan [6, preferably of the forced feed multiple type, is located in compartment I'I above the unit. The fan is driven by a variable speed motor (not shown) and circulates air through a heater l8, which maybe of any desired type, but is preferably a steamheated radiator, a connection of which is shown at ii. The heated air leaves each fan unit through an exhaust duct 20 and is forced through chamber 2| which is provided with deflecting fins 22 to distribute the air evenly over the sides of the trays.
After the air passes over the trays and has gathered moisture from the food products, it enters exhaust duct 23 from which it is directed partiall or wholly to the outside atmosphere by a suitable damper system. An air inlet port is provided at 24, the opening of which is controlled by a valve 25, which may be held set in a selected position by adjusting means 26. An air outlet port is provided at 21, the opening of which is controlled by damper 28, which may be held set in a selected position by adjusting means 20. Damper 28 also acts as a deflector to direct the air into the outlet port. As can be seen in Figure 3, the damper in one extreme setting will direct all th outlet air to the outside, and in the opposite extreme setting will direct it all 'back into the heater.
The function of the damper system is to control the humidity of the drying air. Any part of the exhaust air may be returned to the heater rather than to the outside atmosphere. Returning larger quantities of the exhaust air to the heater increases the humidity of the drying air.
Suitable instruments, such as a dry bulb thermometer 30 and a wet bulb thermometer 30', may be positioned in the drying air current for observation, whereby manual adjustments can be made on the heat admitted to the heater for maintaining the desired dry bulb temperature and on the damper system to maintain the desired wet bulb temperature of the circulating air.
Each cabinet unit is provided with means rendering it useful for other steps than drying. A perforated steam pipe is provided at 3i, to admit steam for blanching purposes. This pipe may also be used for increasing the relative humidity of the air, as may be necessary at the start of dehydrating a new batch, for example. By completely closin ports 24 and 21 and admitting steam, blanching can be carried out to any desired extent. The chamber can then be immediately aerated and drying started by simply shutting oil? the steam and resetting the damper system.
If it is desired to treat the food products with flue gas or sulphur dioxide, as is necessary in some cases to inhibit nzyme reactions, such gases are admitted through the inlet port 24.
The adaptability of this-apparatus to a wide variety of conditions and uses is apparent. A complete process may be carried out with one cabinet unit, by successively effecting different processing steps on a batch of products loaded in the unit. If, however, it is desirable to operate several units together as a tunnel, each may be set and made to perform any desired step such as blanching, gas treatment or drying. To illustrate, the first cabinet unit may be used for blanching or used for gas treatment to inhibit enzyme reactions, or if separate units are desired for these treatments, the first and second may be thus employed. In the next unit dry gases may be used and circulated with high velocity, since the food product is heavy at this stage. In the next two units, the drying may be eifected at increasing temperatures and at decreasingly lower air velocities, to prevent blowing the light, dry
products oil! the trays. All units may be operated at the same time on diiferent batches, the trucks being pushed ahead to convey the products from one unit to the next unit.
Referring to the modified type of Figures 4, 5 and 6, the cabinet type of dehydrator herein shown is generally similar to the cabinet unit used in Figure 1. It provides a processing chamber 40 into which the truck 4| i pushed. The truck in this instance is provided with guide wheels 42 at its centerrunning between rails 43. The trays 6 are the same as those described above.
It may be desirable to run various size batches, and means in this form provides for blocking oi! air from the part of the chamber not occupied if the truck is loaded to less than its full capacity.
as a weight at its free hanging end. The other end of the curtain, provided with a stifl'ener 41,
is attached to a pull rope 48, which extends outside the dehydrator, and is wound on a bracket 49. When the truck is in position, the operator can readilyadjust the curtain to block oil all the air inlet area above the top tray.
The fan- 50 and heater of this dehydrator may be acommercially obtainable heating unit of predetermined capacity, if desired, and if constant heat and air are supplied, the tray capacity can be adjusted to care for varying conditions.
A blanching steam admission pipe 52, similar to that described in reference to the first modification, is provided.
Air is exhausted from the fan through exhaust duct 53, and passes a set of fin 5454--5l, ad-
justably mounted on axes 54-54'--54' to direct the air over the sides of the trays.
In the damper system of this modification, the air inlet port 55 is controlled by a valve 56, and the air outlet port 51 is controlled by damper 58. The valve and damper are so coupled together that when the valve is opened to admit dry outside air, the damper is set to open the air outlet port and to deflect the air away from the heater and out of the port. Figure 5 shows an extreme setting of the system inwhich all of the air is deflected to the outside. The coupling is provided by a link 89 connecting crank arms 56' and 58' attached to the valve and damper, respectively, at their pivotal axes. A control rod 60 for setting the damper system is attached to the damper crank arm 58.
Observation dry and wet bulb thermometers are shown at 6! and 84, respectively, which may be used in connection with manual control means as described in reference to Figure 3. Automatic control is, however, preferable, and may be provided by the following described means shown schematically.
A modulating motor control 6| of known type canbe coupled to the control rod, and the damper system regulated automatically to maintain a desired humidity by coupling the motor control to a humidostat or wet bulb control apparatu of wellknown type, located in the box shown at 81.
' The dry bulb temperature may be controlled by a thermostat or dry bulb control apparatus also automatic control of the dry bulb temperature,
a very efiicient heat consumption is obtained, as no excess air is heated or exhausted.
Inspection windows are provided at 65, 68 and 61.
In the embodiments thus far described, the trays provide for circulating the air over the food products. Figures 8, 9 and are directed to an improved tray system in which the air is forced to circulate through the tray floors or screens. with some products, this results in a more unliorm drying, and makes it possible to'load the trays deeper. The tray 10 is provided with side and end walls H and 12, resp ctively, of the same height, and a perforated floor I3, herein shown as a screen. A baflle 14, positioned between each pair of screens, is provided with solid end walls II of the same height and a solid floor 18. Each products loaded on the trays.
side wall of the baille, however, is open above the floor on one side and below the floor on the other side, as shown at 11, but is otherwise closed by pieces II.
The trays and baiiles are alternately stacked, as shown in Figure 9. Due to this arrangement, the air is forced to travel as shown by the arrows, and is forced through the tray floors and food Strips may be fastened to the end walls 15 of baffles 14 so as to hold said bailles in spaced apart position, and the trays Ill may be slid between the ballles.
Having thus described the invention, what is claimed is:
1. A dehydrating apparatus comprising at least two separate, similar, individual cabinet units, each unit having an opening in each of its end walls for the admission andegress of products to be dehydrated and each unit being provided with means for effecting a first gas-processing step and with means for effecting at least one more gas-processing step different from that of gether with the openings matched to form a tunnel type dehydrator, whereby when so connected together the first unit may be employed to eflect the first processing step on a first batch of prod-' ucts loaded in the first unit, following which the first batch of products may be conveyed into the second unit and a second batch of products placed in the first unit and the second unit may be em-' ployed to effect the second processing step on the first batch of products while the first unit is circulation between the individual units when the said units are connected together.
2. A dehydrating apparatus comprising at least two separate, similar, individual cabinet units,
each unit having an opening in each of its end walls for the admission and egress of products to be dehydrated, trays having closed ends so constructed that when the trays are stacked on each other the ends form a closed wall, each unit being provided with means for eflecting a first gasprocessing step and with means for efiecting at least one more gas-processing stepdifferent from that of the first-mentioned means, whereby a single unit may be employed to effect the first processing step followed by effecting the next processingstep on a batch of products loaded on the trays imthe unit, and means for detachably connecting the'units together with the openings matched to form a; tunnel type dehydrator, whereby when so connected together the first unit may be employed to effect the first processing step on a batch of products loaded in the first unit, following which the first batch of products may be conveyed into the second unit and a second batch or products placed in the first unit and the second unit may be employed to effect the second processing step on the first batch of products while the first unit is effecting the first processing step on the second batch of products, and inwardly extending flexible flaps fixed in the tunnel near the ,junctures of the individual units, the flaps engaging the stacked trays and forming with the closed wall means for preventing gas circulation between the individual units and permitting the trays to be conveyed from the first unit into the second unit.
3. In a dehydrator, a tray system comprising removable trays each having a perforated floor and solid side and end walls, said side and end walls being of the same height, and removable baflles corresponding in size to the trays, said bailles each comprising a solid floor, solid end walls extending above and below the floor, one.
US459289A 1942-09-22 1942-09-22 Dehydrator Expired - Lifetime US2370422A (en)

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Cited By (28)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2443924A (en) * 1945-01-24 1948-06-22 Wolverine Equipment Co Slasher hood
US2549070A (en) * 1951-04-17 Apparatus for scalding poultry
US2757920A (en) * 1952-06-14 1956-08-07 Coe Mfg Co Veneer dryer
US2855839A (en) * 1953-03-09 1958-10-14 D M Russell Method of treating perishable onions in storage
US3075297A (en) * 1958-10-27 1963-01-29 Argabrite Apparatus for processing leather
US3192645A (en) * 1959-10-07 1965-07-06 Leybold Aulagen Holding A G Apparatus and method for vacuum freeze drying substances in a tunnel dryer having sealing locks
US3240340A (en) * 1965-06-25 1966-03-15 Paul M Hayes Chromatography apparatus
US3263337A (en) * 1962-01-08 1966-08-02 Chemet Entpr Method and apparatus for dehydrating foam
US3362087A (en) * 1966-12-20 1968-01-09 Singer Co Dryers for carpets and the like
US3402481A (en) * 1965-09-24 1968-09-24 Sargents Sons Corp C G Driers and components thereof
US3421638A (en) * 1966-11-14 1969-01-14 Ibm Processing system for handling articles supported on holders
US3940860A (en) * 1973-12-18 1976-03-02 Pretema A.G. Method and apparatus for drying a hygroscopic material possessing fibrous structure
US4100682A (en) * 1975-04-10 1978-07-18 Corrigan John H Treatment of commodities through contact with fluid media
US4139953A (en) * 1977-03-18 1979-02-20 Pako Corporation Method and apparatus for drying photographic strip material
US4268974A (en) * 1977-04-05 1981-05-26 Greenbank-Cast Basalt Engineering Co. Limited Hoods for the cylinder drying section of paper making machines and other cylinder drying machines
US4782214A (en) * 1986-02-05 1988-11-01 Rene Voegtlin Indirect-heating truck-type bakery oven
US5025570A (en) * 1990-10-19 1991-06-25 Moffat William A Modular convective oven with anti-contamination features
US5471907A (en) * 1992-01-03 1995-12-05 Kobelt Manufacturing Co. Ltd. Marine steering apparatus
EP0709634A2 (en) * 1994-10-26 1996-05-01 Shin Kiyokawa Apparatus for drying objects
FR2732100A1 (en) * 1995-03-23 1996-09-27 Photomeca Egg Drying of photopolymer plates by accelerated evaporation
WO1999004209A1 (en) * 1997-07-18 1999-01-28 Dtl S.A. A mobile modular production system including a drying tunnel
WO1999023430A1 (en) * 1997-11-04 1999-05-14 Plestenjak Joze A drying device
EP0968396A1 (en) * 1997-01-10 2000-01-05 The Metal Ware Corporation Food dehydrator
NL1014206C2 (en) * 2000-01-27 2001-07-30 Visno Machf B V Drying device for flower bulbs washed with water comprises drying tunnel through which extends transport roller track for conveyance of boxes, cases and similar provided with perforations or other apertures and which carry bulbs
US20070237670A1 (en) * 2006-03-31 2007-10-11 Spx Corporation Dry heat convection sterilization system
EP2803924A1 (en) * 2013-05-14 2014-11-19 Andreas Walter Kraus Process for dehydrating moringa oleifera
DK201470152A1 (en) * 2014-03-26 2015-05-18 Jasopels As Drying room for drying of pelts, drying manifolds and pelt boards
CN110207464A (en) * 2017-07-12 2019-09-06 安徽弘源化工科技有限公司 A kind of blank drying system of Lacquer finish powder processing

Cited By (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2549070A (en) * 1951-04-17 Apparatus for scalding poultry
US2443924A (en) * 1945-01-24 1948-06-22 Wolverine Equipment Co Slasher hood
US2757920A (en) * 1952-06-14 1956-08-07 Coe Mfg Co Veneer dryer
US2855839A (en) * 1953-03-09 1958-10-14 D M Russell Method of treating perishable onions in storage
US3075297A (en) * 1958-10-27 1963-01-29 Argabrite Apparatus for processing leather
US3192645A (en) * 1959-10-07 1965-07-06 Leybold Aulagen Holding A G Apparatus and method for vacuum freeze drying substances in a tunnel dryer having sealing locks
US3263337A (en) * 1962-01-08 1966-08-02 Chemet Entpr Method and apparatus for dehydrating foam
US3240340A (en) * 1965-06-25 1966-03-15 Paul M Hayes Chromatography apparatus
US3402481A (en) * 1965-09-24 1968-09-24 Sargents Sons Corp C G Driers and components thereof
US3421638A (en) * 1966-11-14 1969-01-14 Ibm Processing system for handling articles supported on holders
US3362087A (en) * 1966-12-20 1968-01-09 Singer Co Dryers for carpets and the like
US3940860A (en) * 1973-12-18 1976-03-02 Pretema A.G. Method and apparatus for drying a hygroscopic material possessing fibrous structure
US4100682A (en) * 1975-04-10 1978-07-18 Corrigan John H Treatment of commodities through contact with fluid media
US4139953A (en) * 1977-03-18 1979-02-20 Pako Corporation Method and apparatus for drying photographic strip material
US4268974A (en) * 1977-04-05 1981-05-26 Greenbank-Cast Basalt Engineering Co. Limited Hoods for the cylinder drying section of paper making machines and other cylinder drying machines
US4782214A (en) * 1986-02-05 1988-11-01 Rene Voegtlin Indirect-heating truck-type bakery oven
US5025570A (en) * 1990-10-19 1991-06-25 Moffat William A Modular convective oven with anti-contamination features
US5471907A (en) * 1992-01-03 1995-12-05 Kobelt Manufacturing Co. Ltd. Marine steering apparatus
EP0709634A2 (en) * 1994-10-26 1996-05-01 Shin Kiyokawa Apparatus for drying objects
EP0709634A3 (en) * 1994-10-26 1997-03-12 Shin Kiyokawa Apparatus for drying objects
US5680712A (en) * 1994-10-26 1997-10-28 Shin Kiyokawa System for drying objects to be dried
FR2732100A1 (en) * 1995-03-23 1996-09-27 Photomeca Egg Drying of photopolymer plates by accelerated evaporation
EP0968396A4 (en) * 1997-01-10 2002-01-30 Metal Ware Corp Food dehydrator
EP0968396A1 (en) * 1997-01-10 2000-01-05 The Metal Ware Corporation Food dehydrator
WO1999004209A1 (en) * 1997-07-18 1999-01-28 Dtl S.A. A mobile modular production system including a drying tunnel
WO1999023430A1 (en) * 1997-11-04 1999-05-14 Plestenjak Joze A drying device
NL1014206C2 (en) * 2000-01-27 2001-07-30 Visno Machf B V Drying device for flower bulbs washed with water comprises drying tunnel through which extends transport roller track for conveyance of boxes, cases and similar provided with perforations or other apertures and which carry bulbs
US20070237670A1 (en) * 2006-03-31 2007-10-11 Spx Corporation Dry heat convection sterilization system
US7708960B2 (en) * 2006-03-31 2010-05-04 Spx Corporation Dry heat convection sterilization system
EP2803924A1 (en) * 2013-05-14 2014-11-19 Andreas Walter Kraus Process for dehydrating moringa oleifera
DK201470152A1 (en) * 2014-03-26 2015-05-18 Jasopels As Drying room for drying of pelts, drying manifolds and pelt boards
DK178522B1 (en) * 2014-03-26 2016-05-09 Eikon Technologies Holding S À R L Drying room for drying of pelts
CN110207464A (en) * 2017-07-12 2019-09-06 安徽弘源化工科技有限公司 A kind of blank drying system of Lacquer finish powder processing

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