US3474544A - Veneer dryer with plural treating zones - Google Patents

Veneer dryer with plural treating zones Download PDF

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US3474544A
US3474544A US651889A US3474544DA US3474544A US 3474544 A US3474544 A US 3474544A US 651889 A US651889 A US 651889A US 3474544D A US3474544D A US 3474544DA US 3474544 A US3474544 A US 3474544A
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veneer
treating
zone
zones
chamber
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US651889A
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Arthur S Holden Jr
Leon H Stuenkel
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Coe Manufacturing Co
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Coe Manufacturing Co
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00Drying solid materials or objects by processes involving the application of heat
    • F26B3/28Drying solid materials or objects by processes involving the application of heat by radiation, e.g. from the sun
    • F26B3/283Drying solid materials or objects by processes involving the application of heat by radiation, e.g. from the sun in combination with convection
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B13/00Machines and apparatus for drying fabrics, fibres, yarns, or other materials in long lengths, with progressive movement
    • F26B13/10Arrangements for feeding, heating or supporting materials; Controlling movement, tension or position of materials
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00Drying solid materials or objects by processes involving the application of heat
    • F26B3/28Drying solid materials or objects by processes involving the application of heat by radiation, e.g. from the sun
    • F26B3/30Drying solid materials or objects by processes involving the application of heat by radiation, e.g. from the sun from infrared-emitting elements
    • F26B3/305Drying solid materials or objects by processes involving the application of heat by radiation, e.g. from the sun from infrared-emitting elements the infrared radiation being generated by combustion or combustion gases
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00Drying solid materials or objects by processes involving the application of heat
    • F26B3/32Drying 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
    • F26B3/34Drying 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
    • F26B3/343Drying 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 in combination with convection

Definitions

  • FIG. l is a diagrammatic top plan view with parts broken away of a veneer ydryer embodying the present invention.
  • FIG. 2 is a diagrammatic sectional view of the veneer dryer shown in FIG. l approximately on the line 2 2 of FIG. 1;
  • FIGS. 3 to 8 are diagrammatic enlarged sectional views of the dryer shown approximately on the lines 3--3 to 8 8 of FIGS. 1 and 2.
  • the preferred apparatus shown is a single deck dryer, designated by the reference character A, for changing the moisture content, in the present instance, drying sheets of green veneer V moving through the dryer in a linear path.
  • the dryer yas shown, comprises a series of elongated treating or drying areas or zones B, C, D, E and F and a cooling area or zone G, arranged in tandem within a housing 10 of rectangular cross-sectional shape through which veneer is caused to travel along a predetermined horizontal path from left to right, as viewed in FIGS. 1 and 2, on conveyor means or a conveyor system H.
  • the various treating zones or areas are arranged in a certain order and are within a single housing certain of the treating areas or zones shown may be omitted and/or they may be arranged in different orders and/or located in individual housing, etc.
  • the housing designated generally by the reference character 10, is substantially rectangular in cross section and comprises a frame made up of suitable structural members, etc. welded and/or bolted together.
  • the exterior of the housing is sheet metal or like material and includes :a plurality of access doors, not indicated, along opposite sides.
  • the front and rear walls of the housing 10 are designated 13 and 14.
  • the treating areas or zones are in the central portion K of the housing 10 between the oor area 1S and the ceiling 16, see FIGS. 3 to 8.
  • the sides of this portion of the central portion K that is, the treating areas or zones, are more or less dened by the left and right-hand frame structures 17 and 18 which support the conveyor means and other equipment in the treating zones.
  • the central portion K of the housing may be divided into a plurality of compartments by transverse vertical partitions having openings in the central portions thereof to permit the passage of the material being treated therethrough, etc. Dividing the central treating portion K of the apparatus into a plurality of compartments facilitates different treating conditions to be established and maintained in the apparatus, preferably with the highest temperature treating zone at or near the entrance end of the apparatus and the other zones having progressively lower treating temperatures with the lowest temperature zone (cooling) at the exit end.
  • the conveyor means H shown is of the double roll type and comprises a plurality of horizontally spaced pairs of top and bottom rolls 20 and 21, respectively, extending transversely of the length of the housing 10, that is, transversely of the direction in which the material to be treated travels through the dryer. Each pair of rolls is identical and is supported and driven in the same manner.
  • the manner of supporting and driving conveyor rolls is well known in the art and the rolls 20 and 21 may be constructed, supported and driven as are the rolls in Morris, United States Patent No. 3,314,164.
  • conveyor shown is of the double roll type it will be understood that any suitable type of conveyor may be used, for example, a cable-type conveyor, such las, shown in Morris, United States Patent No. 3,334,421, or a foraminous belt-type conveyor such as shown in Quimby et al. United States Patent No. 2,603,004 or Milligan et al. United States Patent No. 3,199,213.
  • a wire mesh belt conveyor with the conveying reach riding on the bottom rolls 21 may be employed for supporting the material.
  • the top rolls 20 or a top belt can -be used in conjunction with the bottom belt to hold the material in place.
  • a wire mesh-type belted conveyor is commonly used in the plywood industry.
  • the conveyor obviously should be made of material such that it will not be detrimentally affected by the heat to which it is subjected to. Provision can be made for cooling the conveyor, if desired, such as circulating cooling water through the pairs of rolls 20 and 21.
  • the veneer V is passed between a plurality of pairs of top and bottom high frequency infra-red radiant heat transmitters or generators, preferably panel-type gas red commercially available infra-red radiant heat generators 22 and 23, interposed between the pairs of conveyor rolls in the area or zone.
  • the radiant heat transmitter or panels 22 and 23 are, like the rolls 20 and 21, extended transversely of the direction of travel of the material being treated and are supported at opposite ends in the frame structures 17 and 18 in any suitable manner.
  • the respective pairs of radiant heat panels can be individually controlled and are preferably operated at temperatures which will emit radiant energy at the Wave length range most readily absorbed by the veneer taking into consideration its moisture content, etc. Temperatures in the order of 700 F. to about 2300 F. have been used. The preferred source or face temperature of the infrared radiant heat generators is in the order of 1200 F. to 1650 F. While gas fired direct radiant heat panels are used in the preferred embodiment herein described and are preferred, because of the high B.t.u. per hour output per square foot of burner surface and the fact that much of the energy generated is high frequency energy, it is to be understood that other types of radiation generators, for example, electric radiation generators, can be used.
  • Air may be circulated about the radiation generators and the material being treated in any suitable amounts and at any desired velocity. Velocities up to about 6000 feet per minute are contemplated to assist in controlling the temperatures in the treating zone and to carry away the moisture removed from the veneer by a stack 25 having a motor driven fan 26 therein.
  • the latent heat of Vevaporation will assist in maintaining the temperature of the veneer within the desired range.
  • the linear speed of the sheet must be correlated with the number and size of the infra-red generators, the temperatures at which they are operated and their spacing from the veneer, etc.
  • the second treating area C is essentially the same as the first treating area with the exception of the fact that provision is made for circulating cooling air closely around each of the radiant heaters or heating panels at relatively high velocity, preferably, at velocities from about 2000 to about 6000 feet per minute.
  • a motor driven fan, design-ated generally as 27, is provided in a cylindrical duct 28 which is in constant communication with a chamber 29 which in turn communicates with the lower portion of the housing. Air circulated by the fan 27 passes into the treating chamber through pairs of upper and lower ducts 30 and 31 somewhat similar to the upper and lower ducts shown in Morris Patent No. 3,314,164 or Morris Patent No.
  • the air ducts 30 and 31 in treating area or zone C can be supported in a manner similar to that in which the air ducts in Morris Patent No. 3,314,164 or Morris Patent No. 3,334,421 are supported.
  • the left-hand wall 18 in this treating zone or area is preferably constructed similar to the corresponding right-hand wall in Morris Patent No. 3,314,164. It is, therefore, solid or closed except for the openings into the pairs of air ducts 30 and 31.
  • the veneer is subjected to drying by the imrpingement of jets of heated air against opposite sides of the veneer which air strikes the veneer at high velocity, for example, from about 2000 to about 6000 feet per minute, preferably at about 3000 feet per minute. If the temperature of the Veneer entering the zone is greater than that of the air striking the veneer the air will have a cooling effect on the veneer.
  • the construction of this area or zone and the manner of heating the air circulated therethrough can be similar to that shown in the Morris Patent No. 3,314,164.
  • the left-hand Wall structure 18, as viewed in FIG. 5, is a solid wall with the pairs of upper and lower air ducts 36 and 37 communicating therewith.
  • the air is circulated by a fan 38 and is heated to a desired temperature of about 350 or more, by steam pipes 40 or other suitable heating means, for example, direct gas or oil tiring, in a chamber 41 located immediately above the treating area or zone D. From the chamber 41 the air travels into the left-hand or rear end of the treating area or zone, travels through the pairs of air ducts 36 and 37 and is returned to the chamber 41 from the righthand or front end of the zone.
  • the chamber 41 is provided with a vent stack 42 having a control damper 43 therein.
  • the veneer is treated in a manner similar to that in which it is treated in zone D with the exception of the fact that the heated air for zone E is obtained from zone B in which the veneer is subjected to radiant heat by conduit means 50 connected to the stack 25 opening into the top of zone B and the left-hand or rear side of zone E.
  • the conduit means 50 includes a damper 52 which with a damper 53 located in the stack 25 can be used to direct the heated air from zone B either to atmosphere or to zone E, as desired. It will also be understood that by proper manipulation of the dampers 52, 53, the temperature of the air supplied to zone E from zone B can be controlled.
  • Air from zone B is exhausted to atmosphere or forced through the conduit means 50 by the motor-driven fan 26 located in the lower -part of the stack 25, the lower end of which is directly connected to the housing 10y and in continuous communication with a chamber 56 above the treating chamber B, which chamber 56 is in communication with opposite ends of the treating area or zone B.
  • conduit 50 is connected with a chamber 57 in communication with a chamber 58 at the rear side of treating area or zone E.
  • Air is supplied to treating area or zone E from chamber 58 through pairs of upper and lower ducts 59 and 60 similar to the air ducts 36 and 37 in treating zone D. Heated air is exhausted from zone E by a motor driven electric fan 61 located on a stack 62 in communication lwith a chamber 63 within the housing 10 and into which the right or front side of the treating chamber E opens.
  • the temperature of the air or gas obtained from zone B is not suiciently high, the temperature thereof may be increased by the use of supplemental heating means, such as, steam pipes or burners 64 located in duct 50.
  • supplemental heating means such as, steam pipes or burners 64 located in duct 50.
  • the veneer is subjected to high frequency electromagnetic energy below the infrared frequency range, preferably in the dielectric and microwave frequency ranges.
  • This energy is applied to the veneer by high frequency electromagnetic transmitters or generators 70, 71 interposed between the pair of rolls 20 and 21 in zone F.
  • the members 70, 71 may be plates of a dielectric heating device or a wave gui-de of a microwave heating device.
  • Air is circulated about the veneer to prevent condensation of the vapor on the surface of the veneer and to withdraw the heated moist air from treating zone or area F by motor-driven electric fans 72 and 73 located in stacks 74 and 75 in communication with a chamber 76 in the top of the housing 10 which chamber communicates with both ends of the treating area or zone F.
  • zone G the veneer is subjected to cooling air circulated therethrough by motor-driven fans and 81 located in conduits 82 and 83 in communication with a chamber 84 which chamber in turn communicates with a chamber 85, the left-hand or rear side of the treating chamber G.
  • the construction of this chamber below the ceiling 16 is similar to that of the construction in chambers D and E.
  • the air circulated by the fans 80 and 81 is conducted through transversely extending pairs of top and bottom conduits 86 and 87, and is impinged against opposite sides of the veneer at high velocity.
  • the cooling air may strike the veneer at any suitable velocity, preferably, at velocities of about 3000 to 4000 feet per minute.
  • From the treating area or zone G the air is exhausted through Stacks 90 and 91 in communication with a chamber 92 which chamber in turn communicates with the right-hand or front part of the treating chamber G.
  • the veneer dryer which forms the preferred embodiment of the invention is capable of receiving green veneer having a high moisture content at the left-hand or green end of the dryer and reducing the moisture content to a desired uniform content usually in the neighborhood of about 4% to 8% as the veneer emerges from the dry or right-hand end of the dryer.
  • the speed of the veneer must be correlated with the number and size of the radiation generators, the temperatures at which they are operated and their spacing with respect to the veneer, etc.
  • the moisture content of Ms Southern Pine can be reduced from 100% to 10% by a radiant gas burner of the type herein contemplated operating at a surface temperature in the neighborhood of 1200 F. to 1400 F., in slightly less than three minutes.
  • the speed of l/s Southern Pine veneer through the dryer illustrated should be such that any given section of the Veneer would not be exposed to the radiant heat or remain in the radiant heat treating areas more than a minute or two. Most of the remaining moisture is removed in the convection heating zone or zones and the final desired moisture content of approximately 4% to 5% being arrived at in the last or terminal high frequency treating zone F. If one or more of the convection heating zones or areas are omitted, preferably more of the moisture is removed in the radiant heating zone. As will be understood, the lengths of the respective zones and the temperatures therein can be regulated to remove almost any desired amount of moisture in any given zone or area.
  • the moisture content of the veneer can be reduced to the desired amount solely by the use of high frequency radiant heaters or the major part of the moisture removed either by high frequency radiant heating and/or convection heating and the iinal moisture content arrived at by using high frequency heating in the microwave and/or dielectric heating frequency regions or ranges.
  • the present process and apparatus provide an way of reducing veneer of any moisture content to a desired lessercontent under controlled conditions and in minimum time.
  • One of the advantages of radiant or infra-red heat is the rapidity with which it can be used to remove moisture from the veneer.
  • One of the principal advantages of high frequency heat in the microwave and/or dielectric heating frequency regions or ranges is the fact that it produces a uniform moisture content in the veneer Since its effectiveness is the function of the moisture in various parts of the Veneer.
  • the high frequency treatment in the microwave and/or dielectric heating frequency regions or ranges is used when the veneer has reached a moisture content closely approaching the ultimate desired level, or with veneer that is already of low moisture content.
  • High frequency treatment in the microwave and/0r dielectric heating frequency regions or ranges is ideal for carrying out finish drying operations regardless of how the initial drying was accomplished.
  • a method of treating veneer to change its moisture content the steps of moving veneer to be treated in a predetermined path through a plurality of treating zones in at least one of which the veneer is moved between at least one infra-red radiation heater located closely adjacent to each opposite side of said path, in another of which zones the veneer is moved between at least one conduit adjacent to each opposite side of said path and which conduits have apertures therein facing said path and through which a gaseous medium is circulated with the gaseous medium being discharged from said conduits through said apertures and against opposite sides of said veneer, and in a third of which zones the veneer is moved by at least one high frequency transmitter operating at a heating frequency range below infra-red located adjacent to said path.
  • an apparatus having a plurality of zones for treating veneer to change its moisture content, means for moving veneer to be treated in a predetermined path through a plurality of said zones, at least one infra-red radiation heater in one of said zones located closely adjacent to each opposite side of said path, at least one conduit in a second of said zones adjacent to each opposite side of said path, said conduits having apertures therein facing said path, means for circulating a gaseous medium through said conduits with the gaseous medium being discharged from said conduits through said apertures, and at least one high frequency source in a third of said zones operable at a heating frequency below infra-red located adjacent to said path.

Description

Oct. 28, 1969A A. s. HOLDEN, JR, ETAL VENEER DRYER WITH FLURAL TREATING ZONES 4 sheets-sheet 1 Filed July v, 1967 Oct. 28, 1969 v A. s. HOLDEN, JR., ET AL 3,474,544
VENBER DRYER WITH PLURAL TREAIING ZONES Filed July T, '1967 4 Sheets-Sheet 2 (uI j E F103 /IS B I6j I7/ |4` l:e2
K, .Cv 23 ISN Oct. 28, 1969 A, 5, HOLDEN, JR" ETL 3,474,544
VENEER DRYER WITH PLURAL TREATING ZONES Fild'July 7, 196'? 4 Sheets-Sheet 5 Oct. 23. 1969l A. s. HOLDEN, JR.. ET AL 3,474,544
' "/ENEER AI'JR'ELH WITH PLURL TREITING ZNESA y Filed July 1967 4 Sheets-Shet 4 United States Patent O 3,474,544 VENEER DRYER WITH PLURAL TREATING ZONES Arthur S. Holden, Jr., and Leon H. Stuenkel, Painesville,
Ohio, assignors to The Coe Manufacturing Company,
Painesville, Ohio, a corporation of Ohio Filed July 7, 1967, Ser. No. 651,889 Int. Cl. F26b 3/04, 3/30, 3/36 U.S. Cl. 34-1 2 Claims ABSTRACT F THE DISCLOSURE Method and apparatus for the changing the moisture content of material in sheet form, especially material which is relatively light and apt to be warped or otherwise irregular in shape and/or to become so, or more so, during treatment, such as veneer, wherein the material is moved continuously through two or more treating areas or zones in at least one which the material being treated is heated by high frequency electromagnetic energy, preferably in the dielectric, microwave or infra-red ranges.
Technical Field Description of invention The invention resides in certain operations, constructions and combinations and arrangements of parts, and further objects and advantages will be apparent to those skilled in the art to which the invention relates from the following description of the preferred equipment or apparatus for practicing the invention described with reference to the accompanying drawings forming a part of this specification and in which:
FIG. l is a diagrammatic top plan view with parts broken away of a veneer ydryer embodying the present invention;
FIG. 2 is a diagrammatic sectional view of the veneer dryer shown in FIG. l approximately on the line 2 2 of FIG. 1; and
FIGS. 3 to 8 are diagrammatic enlarged sectional views of the dryer shown approximately on the lines 3--3 to 8 8 of FIGS. 1 and 2.
Although the illustrative equipment will be described in detail, it is to be understood that the invention is not limited to the use of equipment having the construction and arrangement shown and described, but is capable of being otherwise practiced and carried out in various ways. It is also to be understood that the pharseology or terminology employed herein is for the purpose of description and not of limitation, `and that there is no intention to thereby limit the invention beyond the requirements of the prior art.
Referring to the drawings, the preferred apparatus shown is a single deck dryer, designated by the reference character A, for changing the moisture content, in the present instance, drying sheets of green veneer V moving through the dryer in a linear path. The dryer, yas shown, comprises a series of elongated treating or drying areas or zones B, C, D, E and F and a cooling area or zone G, arranged in tandem within a housing 10 of rectangular cross-sectional shape through which veneer is caused to travel along a predetermined horizontal path from left to right, as viewed in FIGS. 1 and 2, on conveyor means or a conveyor system H. While in the apparatus shown the various treating zones or areas are arranged in a certain order and are within a single housing certain of the treating areas or zones shown may be omitted and/or they may be arranged in different orders and/or located in individual housing, etc.
The housing, designated generally by the reference character 10, is substantially rectangular in cross section and comprises a frame made up of suitable structural members, etc. welded and/or bolted together. The exterior of the housing is sheet metal or like material and includes :a plurality of access doors, not indicated, along opposite sides. The front and rear walls of the housing 10 are designated 13 and 14. In the particular embodiment shown, the treating areas or zones are in the central portion K of the housing 10 between the oor area 1S and the ceiling 16, see FIGS. 3 to 8. The sides of this portion of the central portion K, that is, the treating areas or zones, are more or less dened by the left and right- hand frame structures 17 and 18 which support the conveyor means and other equipment in the treating zones.
The central portion K of the housing, if desired, may be divided into a plurality of compartments by transverse vertical partitions having openings in the central portions thereof to permit the passage of the material being treated therethrough, etc. Dividing the central treating portion K of the apparatus into a plurality of compartments facilitates different treating conditions to be established and maintained in the apparatus, preferably with the highest temperature treating zone at or near the entrance end of the apparatus and the other zones having progressively lower treating temperatures with the lowest temperature zone (cooling) at the exit end.
The conveyor means H shown is of the double roll type and comprises a plurality of horizontally spaced pairs of top and bottom rolls 20 and 21, respectively, extending transversely of the length of the housing 10, that is, transversely of the direction in which the material to be treated travels through the dryer. Each pair of rolls is identical and is supported and driven in the same manner. The manner of supporting and driving conveyor rolls is well known in the art and the rolls 20 and 21 may be constructed, supported and driven as are the rolls in Morris, United States Patent No. 3,314,164.
While the conveyor shown is of the double roll type it will be understood that any suitable type of conveyor may be used, for example, a cable-type conveyor, such las, shown in Morris, United States Patent No. 3,334,421, or a foraminous belt-type conveyor such as shown in Quimby et al. United States Patent No. 2,603,004 or Milligan et al. United States Patent No. 3,199,213. When thin or fragile material is to be handled a wire mesh belt conveyor with the conveying reach riding on the bottom rolls 21 may be employed for supporting the material. The top rolls 20 or a top belt can -be used in conjunction with the bottom belt to hold the material in place. A wire mesh-type belted conveyor is commonly used in the plywood industry. The conveyor obviously should be made of material such that it will not be detrimentally affected by the heat to which it is subjected to. Provision can be made for cooling the conveyor, if desired, such as circulating cooling water through the pairs of rolls 20 and 21.
In the rst treating area or zone B, the veneer V is passed between a plurality of pairs of top and bottom high frequency infra-red radiant heat transmitters or generators, preferably panel-type gas red commercially available infra-red radiant heat generators 22 and 23, interposed between the pairs of conveyor rolls in the area or zone. The radiant heat transmitter or panels 22 and 23 are, like the rolls 20 and 21, extended transversely of the direction of travel of the material being treated and are supported at opposite ends in the frame structures 17 and 18 in any suitable manner.
The respective pairs of radiant heat panels can be individually controlled and are preferably operated at temperatures which will emit radiant energy at the Wave length range most readily absorbed by the veneer taking into consideration its moisture content, etc. Temperatures in the order of 700 F. to about 2300 F. have been used. The preferred source or face temperature of the infrared radiant heat generators is in the order of 1200 F. to 1650 F. While gas fired direct radiant heat panels are used in the preferred embodiment herein described and are preferred, because of the high B.t.u. per hour output per square foot of burner surface and the fact that much of the energy generated is high frequency energy, it is to be understood that other types of radiation generators, for example, electric radiation generators, can be used. Air may be circulated about the radiation generators and the material being treated in any suitable amounts and at any desired velocity. Velocities up to about 6000 feet per minute are contemplated to assist in controlling the temperatures in the treating zone and to carry away the moisture removed from the veneer by a stack 25 having a motor driven fan 26 therein. The latent heat of Vevaporation will assist in maintaining the temperature of the veneer within the desired range. The linear speed of the sheet, however, must be correlated with the number and size of the infra-red generators, the temperatures at which they are operated and their spacing from the veneer, etc.
The second treating area C is essentially the same as the first treating area with the exception of the fact that provision is made for circulating cooling air closely around each of the radiant heaters or heating panels at relatively high velocity, preferably, at velocities from about 2000 to about 6000 feet per minute. For this purpose a motor driven fan, design-ated generally as 27, is provided in a cylindrical duct 28 which is in constant communication with a chamber 29 which in turn communicates with the lower portion of the housing. Air circulated by the fan 27 passes into the treating chamber through pairs of upper and lower ducts 30 and 31 somewhat similar to the upper and lower ducts shown in Morris Patent No. 3,314,164 or Morris Patent No. 3,334,- 421 except that they are deeper and the sides thereof adjacent to the veneer path are open and have loca-ted therein radiant heaters 32 and 33 similar to the radiant heaters 22 and 23 in treating area or zone B. The sides of the air ducts 30 and 31 are slightly wider than the radiant heaters located therein thus providing space through which cooling air can circulate or travel around or about the heaters into the treating zone or area proper. The construction is such that the radiant heat generators are located in the open sides of a plenum chamber formed by the ducts 30 and 31. The air travels through the treating chamber or area C from left to right, as vlewed 1n FIG. 4, and is exhausted to atmosphere through a st ack 34 connected to the top of a chamber 35 in communication with the right-hand or front side of the treating area. The air ducts 30 and 31 in treating area or zone C can be supported in a manner similar to that in which the air ducts in Morris Patent No. 3,314,164 or Morris Patent No. 3,334,421 are supported. The left-hand wall 18 in this treating zone or area is preferably constructed similar to the corresponding right-hand wall in Morris Patent No. 3,314,164. It is, therefore, solid or closed except for the openings into the pairs of air ducts 30 and 31.
In the treating area D the veneer is subjected to drying by the imrpingement of jets of heated air against opposite sides of the veneer which air strikes the veneer at high velocity, for example, from about 2000 to about 6000 feet per minute, preferably at about 3000 feet per minute. If the temperature of the Veneer entering the zone is greater than that of the air striking the veneer the air will have a cooling effect on the veneer. The construction of this area or zone and the manner of heating the air circulated therethrough can be similar to that shown in the Morris Patent No. 3,314,164. In this event the left-hand Wall structure 18, as viewed in FIG. 5, is a solid wall with the pairs of upper and lower air ducts 36 and 37 communicating therewith. In this zone the air is circulated by a fan 38 and is heated to a desired temperature of about 350 or more, by steam pipes 40 or other suitable heating means, for example, direct gas or oil tiring, in a chamber 41 located immediately above the treating area or zone D. From the chamber 41 the air travels into the left-hand or rear end of the treating area or zone, travels through the pairs of air ducts 36 and 37 and is returned to the chamber 41 from the righthand or front end of the zone. The chamber 41 is provided with a vent stack 42 having a control damper 43 therein.
In the zone E, the veneer is treated in a manner similar to that in which it is treated in zone D with the exception of the fact that the heated air for zone E is obtained from zone B in which the veneer is subjected to radiant heat by conduit means 50 connected to the stack 25 opening into the top of zone B and the left-hand or rear side of zone E. The conduit means 50 includes a damper 52 which with a damper 53 located in the stack 25 can be used to direct the heated air from zone B either to atmosphere or to zone E, as desired. It will also be understood that by proper manipulation of the dampers 52, 53, the temperature of the air supplied to zone E from zone B can be controlled. Air from zone B is exhausted to atmosphere or forced through the conduit means 50 by the motor-driven fan 26 located in the lower -part of the stack 25, the lower end of which is directly connected to the housing 10y and in continuous communication with a chamber 56 above the treating chamber B, which chamber 56 is in communication with opposite ends of the treating area or zone B.
The opposite end of conduit 50 is connected with a chamber 57 in communication with a chamber 58 at the rear side of treating area or zone E. Air is supplied to treating area or zone E from chamber 58 through pairs of upper and lower ducts 59 and 60 similar to the air ducts 36 and 37 in treating zone D. Heated air is exhausted from zone E by a motor driven electric fan 61 located on a stack 62 in communication lwith a chamber 63 within the housing 10 and into which the right or front side of the treating chamber E opens.
If the temperature of the air or gas obtained from zone B is not suiciently high, the temperature thereof may be increased by the use of supplemental heating means, such as, steam pipes or burners 64 located in duct 50.
In the treating chamber F the veneer is subjected to high frequency electromagnetic energy below the infrared frequency range, preferably in the dielectric and microwave frequency ranges. This energy is applied to the veneer by high frequency electromagnetic transmitters or generators 70, 71 interposed between the pair of rolls 20 and 21 in zone F. The members 70, 71 may be plates of a dielectric heating device or a wave gui-de of a microwave heating device. Air is circulated about the veneer to prevent condensation of the vapor on the surface of the veneer and to withdraw the heated moist air from treating zone or area F by motor-driven electric fans 72 and 73 located in stacks 74 and 75 in communication with a chamber 76 in the top of the housing 10 which chamber communicates with both ends of the treating area or zone F.
In the last treating zone shown, that is, zone G, the veneer is subjected to cooling air circulated therethrough by motor-driven fans and 81 located in conduits 82 and 83 in communication with a chamber 84 which chamber in turn communicates with a chamber 85, the left-hand or rear side of the treating chamber G. The construction of this chamber below the ceiling 16 is similar to that of the construction in chambers D and E. In other words, the air circulated by the fans 80 and 81 is conducted through transversely extending pairs of top and bottom conduits 86 and 87, and is impinged against opposite sides of the veneer at high velocity. The cooling air may strike the veneer at any suitable velocity, preferably, at velocities of about 3000 to 4000 feet per minute. From the treating area or zone G the air is exhausted through Stacks 90 and 91 in communication with a chamber 92 which chamber in turn communicates with the right-hand or front part of the treating chamber G.
The veneer dryer which forms the preferred embodiment of the invention is capable of receiving green veneer having a high moisture content at the left-hand or green end of the dryer and reducing the moisture content to a desired uniform content usually in the neighborhood of about 4% to 8% as the veneer emerges from the dry or right-hand end of the dryer. As previously stated, the speed of the veneer must be correlated with the number and size of the radiation generators, the temperatures at which they are operated and their spacing with respect to the veneer, etc. As an illustration, the moisture content of Ms Southern Pine can be reduced from 100% to 10% by a radiant gas burner of the type herein contemplated operating at a surface temperature in the neighborhood of 1200 F. to 1400 F., in slightly less than three minutes. From this it will -be apparent that the speed of l/s Southern Pine veneer through the dryer illustrated should be such that any given section of the Veneer would not be exposed to the radiant heat or remain in the radiant heat treating areas more than a minute or two. Most of the remaining moisture is removed in the convection heating zone or zones and the final desired moisture content of approximately 4% to 5% being arrived at in the last or terminal high frequency treating zone F. If one or more of the convection heating zones or areas are omitted, preferably more of the moisture is removed in the radiant heating zone. As will be understood, the lengths of the respective zones and the temperatures therein can be regulated to remove almost any desired amount of moisture in any given zone or area. It will also be apparent that one or more of the treating zones can be eliminated, for example, the moisture content of the veneer can be reduced to the desired amount solely by the use of high frequency radiant heaters or the major part of the moisture removed either by high frequency radiant heating and/or convection heating and the iinal moisture content arrived at by using high frequency heating in the microwave and/or dielectric heating frequency regions or ranges. The present process and apparatus provide an eficient way of reducing veneer of any moisture content to a desired lessercontent under controlled conditions and in minimum time.
While a preferred embodiment of the invention has been illustrated and described, it is to be understood, as previously Stated, that the invention is not limited to the use of the equipment shown, for example, any one or more of the treating zones and equipment described therein could be used for the purposes of changing the moisture content of veneer so long as one of the zones utilities high frequency heating in the infra-red, microwave or dielectric frequency ranges.
One of the advantages of radiant or infra-red heat is the rapidity with which it can be used to remove moisture from the veneer. One of the principal advantages of high frequency heat in the microwave and/or dielectric heating frequency regions or ranges is the fact that it produces a uniform moisture content in the veneer Since its effectiveness is the function of the moisture in various parts of the Veneer. Preferably the high frequency treatment in the microwave and/or dielectric heating frequency regions or ranges is used when the veneer has reached a moisture content closely approaching the ultimate desired level, or with veneer that is already of low moisture content. High frequency treatment in the microwave and/0r dielectric heating frequency regions or ranges is ideal for carrying out finish drying operations regardless of how the initial drying was accomplished.
From the foregoing description it will be apparent that the objects and others heretofore enumerated have been accomplished and that there has been provided novel and improved methods and apparatus for changing the moisture content of material in sheet form and especially veneer.
Having thus described our invention, what we claim is:
1. In a method of treating veneer to change its moisture content, the steps of moving veneer to be treated in a predetermined path through a plurality of treating zones in at least one of which the veneer is moved between at least one infra-red radiation heater located closely adjacent to each opposite side of said path, in another of which zones the veneer is moved between at least one conduit adjacent to each opposite side of said path and which conduits have apertures therein facing said path and through which a gaseous medium is circulated with the gaseous medium being discharged from said conduits through said apertures and against opposite sides of said veneer, and in a third of which zones the veneer is moved by at least one high frequency transmitter operating at a heating frequency range below infra-red located adjacent to said path.
2. In an apparatus having a plurality of zones for treating veneer to change its moisture content, means for moving veneer to be treated in a predetermined path through a plurality of said zones, at least one infra-red radiation heater in one of said zones located closely adjacent to each opposite side of said path, at least one conduit in a second of said zones adjacent to each opposite side of said path, said conduits having apertures therein facing said path, means for circulating a gaseous medium through said conduits with the gaseous medium being discharged from said conduits through said apertures, and at least one high frequency source in a third of said zones operable at a heating frequency below infra-red located adjacent to said path.
References Cited UNITED STATES PATENTS 2,384,990 9/ 1945 French 34-18 XR 2,576,519 l1/l95l Kopp 34-1 XR FOREIGN PATENTS 1,033,104 4/1953 France.
722,116 1/ 1955 Great Britain.
CARLTON R. CROYLE, Primary Examiner A. D. HERRMANN, Assistant Examiner U.S. Cl. X.R.
34-l8, 68, 155, 216; 2l9-l0.47, 10.71
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Cited By (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3578069A (en) * 1968-02-19 1971-05-11 Pechiney Apparatus for firing carbon-containing products
US3704523A (en) * 1970-01-14 1972-12-05 Int Standard Electric Corp Microwave dryer for ceramic articles
US3732048A (en) * 1970-02-18 1973-05-08 Int Standard Electric Corp Apparatus for casting of ceramics
US3744147A (en) * 1968-09-06 1973-07-10 J Pless Artificial seasoning of timber
US3831288A (en) * 1970-11-24 1974-08-27 Furnace L Dev Ltd Drying and sterilising apparatus
US3902253A (en) * 1973-01-17 1975-09-02 Nippon Musical Instruments Mfg Lumber drying apparatus
US4026037A (en) * 1975-02-18 1977-05-31 Adolf Buchholz Apparatus for steam drying
US4062127A (en) * 1974-07-01 1977-12-13 Klockner-Humboldt-Deutz Aktiengesellschaft Method for the continuous drying of wet, granular and/or lumpy materials and device for carrying out the method
FR2367998A1 (en) * 1976-10-12 1978-05-12 Bayer Ag DRYING POLYCHLOROPRENE SHEETS, AND THE CORRESPONDING DRYER
US4121350A (en) * 1975-02-18 1978-10-24 Adolf Buchholz Sheet dryer apparatus using deflectors for steam drying
US4127945A (en) * 1976-06-01 1978-12-05 Bayer Aktiengesellschaft Process and a dryer for drying polychloroprene sheets
US4127946A (en) * 1975-02-18 1978-12-05 Adolf Buchholz Method for steam drying
US4146973A (en) * 1977-04-14 1979-04-03 Georgia-Pacific Corporation Method and apparatus for drying veneer
US4148346A (en) * 1976-06-14 1979-04-10 Scarnecchia O Vincent Method of and apparatus for drying and debarking logs
US4179820A (en) * 1977-04-14 1979-12-25 Georgia-Pacific Corporation Apparatus for drying veneer
US4417406A (en) * 1980-08-09 1983-11-29 Babcock-Bsh Aktiengesellschaft Arrangement for drying plate-shaped wood products
EP0268774A2 (en) * 1986-11-22 1988-06-01 BABCOCK-BSH AKTIENGESELLSCHAFT vormals Büttner-Schilde-Haas AG Continuous veneer dryer
US5107602A (en) * 1988-07-15 1992-04-28 Loeoef Nils Oskar T Method and an apparatus for drying veneer and similar products
US5298707A (en) * 1991-06-07 1994-03-29 Tgtbt, Ltd. Apparatus for preparing fat free snack chips
US5309650A (en) * 1991-08-29 1994-05-10 Abb Flakt, Inc. Method and apparatus for ventilating a paint baking oven
US5423260A (en) * 1993-09-22 1995-06-13 Rockwell International Corporation Device for heating a printed web for a printing press
US5858431A (en) * 1996-11-25 1999-01-12 International Machinery, Inc. Method and apparatus for preparing fat free snack chips using hot air impingement, microwaving, and hot air drying
US20050217136A1 (en) * 2004-03-24 2005-10-06 Apollo Hardwoods Company Method and apparatus for drying materials including veneers
WO2015058027A1 (en) * 2013-10-17 2015-04-23 Triglia Joseph P Jr System and method of removing moisture from fibrous or porous materials using microwave radiation and rf energy
WO2016001456A1 (en) * 2014-07-04 2016-01-07 Das Tech Solutions, S.L.U. Device and method for product drying
US11143454B2 (en) 2013-10-17 2021-10-12 Joseph P. Triglia, Jr. System and method of removing moisture from fibrous or porous materials using microwave radiation and RF energy
US11384980B2 (en) 2013-10-17 2022-07-12 Joseph P. Triglia, Jr. System and method for reducing moisture in materials or plants using microwave radiation and RF energy

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US2384990A (en) * 1944-05-11 1945-09-18 French John Robert Drier
US2576519A (en) * 1949-01-11 1951-11-27 Philip E Kopp Apparatus and method for clay baking
FR1033104A (en) * 1950-05-22 1953-07-08 Device for drying wet textile fibers
GB722116A (en) * 1952-02-14 1955-01-19 Vickers Electrical Co Ltd Improvements relating to the drying of materials

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2384990A (en) * 1944-05-11 1945-09-18 French John Robert Drier
US2576519A (en) * 1949-01-11 1951-11-27 Philip E Kopp Apparatus and method for clay baking
FR1033104A (en) * 1950-05-22 1953-07-08 Device for drying wet textile fibers
GB722116A (en) * 1952-02-14 1955-01-19 Vickers Electrical Co Ltd Improvements relating to the drying of materials

Cited By (31)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3578069A (en) * 1968-02-19 1971-05-11 Pechiney Apparatus for firing carbon-containing products
US3744147A (en) * 1968-09-06 1973-07-10 J Pless Artificial seasoning of timber
US3704523A (en) * 1970-01-14 1972-12-05 Int Standard Electric Corp Microwave dryer for ceramic articles
US3732048A (en) * 1970-02-18 1973-05-08 Int Standard Electric Corp Apparatus for casting of ceramics
US3831288A (en) * 1970-11-24 1974-08-27 Furnace L Dev Ltd Drying and sterilising apparatus
US3902253A (en) * 1973-01-17 1975-09-02 Nippon Musical Instruments Mfg Lumber drying apparatus
US4062127A (en) * 1974-07-01 1977-12-13 Klockner-Humboldt-Deutz Aktiengesellschaft Method for the continuous drying of wet, granular and/or lumpy materials and device for carrying out the method
US4026037A (en) * 1975-02-18 1977-05-31 Adolf Buchholz Apparatus for steam drying
US4121350A (en) * 1975-02-18 1978-10-24 Adolf Buchholz Sheet dryer apparatus using deflectors for steam drying
US4127946A (en) * 1975-02-18 1978-12-05 Adolf Buchholz Method for steam drying
US4127945A (en) * 1976-06-01 1978-12-05 Bayer Aktiengesellschaft Process and a dryer for drying polychloroprene sheets
US4148346A (en) * 1976-06-14 1979-04-10 Scarnecchia O Vincent Method of and apparatus for drying and debarking logs
FR2367998A1 (en) * 1976-10-12 1978-05-12 Bayer Ag DRYING POLYCHLOROPRENE SHEETS, AND THE CORRESPONDING DRYER
US4179820A (en) * 1977-04-14 1979-12-25 Georgia-Pacific Corporation Apparatus for drying veneer
US4146973A (en) * 1977-04-14 1979-04-03 Georgia-Pacific Corporation Method and apparatus for drying veneer
US4417406A (en) * 1980-08-09 1983-11-29 Babcock-Bsh Aktiengesellschaft Arrangement for drying plate-shaped wood products
EP0268774A2 (en) * 1986-11-22 1988-06-01 BABCOCK-BSH AKTIENGESELLSCHAFT vormals Büttner-Schilde-Haas AG Continuous veneer dryer
EP0268774A3 (en) * 1986-11-22 1989-05-24 Babcock-Bsh Aktiengesellschaft Vormals Buttner-Schilde-Haas Ag Continuous veneer dryer
US5107602A (en) * 1988-07-15 1992-04-28 Loeoef Nils Oskar T Method and an apparatus for drying veneer and similar products
US5298707A (en) * 1991-06-07 1994-03-29 Tgtbt, Ltd. Apparatus for preparing fat free snack chips
US5309650A (en) * 1991-08-29 1994-05-10 Abb Flakt, Inc. Method and apparatus for ventilating a paint baking oven
US5423260A (en) * 1993-09-22 1995-06-13 Rockwell International Corporation Device for heating a printed web for a printing press
US5858431A (en) * 1996-11-25 1999-01-12 International Machinery, Inc. Method and apparatus for preparing fat free snack chips using hot air impingement, microwaving, and hot air drying
US20050217136A1 (en) * 2004-03-24 2005-10-06 Apollo Hardwoods Company Method and apparatus for drying materials including veneers
US7383643B2 (en) 2004-03-24 2008-06-10 Apollo Hardwoods Company Method for drying veneers
WO2015058027A1 (en) * 2013-10-17 2015-04-23 Triglia Joseph P Jr System and method of removing moisture from fibrous or porous materials using microwave radiation and rf energy
US9879908B2 (en) 2013-10-17 2018-01-30 Triglia Technologies, Inc. System and method of removing moisture from fibrous or porous materials using microwave radiation and RF energy
US10533799B2 (en) 2013-10-17 2020-01-14 Joseph P. Triglia, Jr. System and method of removing moisture from fibrous or porous materials using microwave radiation and RF energy
US11143454B2 (en) 2013-10-17 2021-10-12 Joseph P. Triglia, Jr. System and method of removing moisture from fibrous or porous materials using microwave radiation and RF energy
US11384980B2 (en) 2013-10-17 2022-07-12 Joseph P. Triglia, Jr. System and method for reducing moisture in materials or plants using microwave radiation and RF energy
WO2016001456A1 (en) * 2014-07-04 2016-01-07 Das Tech Solutions, S.L.U. Device and method for product drying

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