EP0068734B1 - Séchoir à étages multiples pour matière granuleuse comportant un dispositif d'évacuation canalisé - Google Patents

Séchoir à étages multiples pour matière granuleuse comportant un dispositif d'évacuation canalisé Download PDF

Info

Publication number
EP0068734B1
EP0068734B1 EP19820303149 EP82303149A EP0068734B1 EP 0068734 B1 EP0068734 B1 EP 0068734B1 EP 19820303149 EP19820303149 EP 19820303149 EP 82303149 A EP82303149 A EP 82303149A EP 0068734 B1 EP0068734 B1 EP 0068734B1
Authority
EP
European Patent Office
Prior art keywords
drying
column
particulate material
grain
dryer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
EP19820303149
Other languages
German (de)
English (en)
Other versions
EP0068734A3 (en
EP0068734A2 (fr
Inventor
Christianus Marinus Theresia Westelaken
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from US06/275,313 external-priority patent/US4398356A/en
Priority claimed from US06/275,312 external-priority patent/US4423557A/en
Application filed by Individual filed Critical Individual
Priority to AT82303149T priority Critical patent/ATE33306T1/de
Publication of EP0068734A2 publication Critical patent/EP0068734A2/fr
Publication of EP0068734A3 publication Critical patent/EP0068734A3/en
Application granted granted Critical
Publication of EP0068734B1 publication Critical patent/EP0068734B1/fr
Expired legal-status Critical Current

Links

Images

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B17/00—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
    • F26B17/12—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed solely by gravity, i.e. the material moving through a substantially vertical drying enclosure, e.g. shaft
    • F26B17/122—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed solely by gravity, i.e. the material moving through a substantially vertical drying enclosure, e.g. shaft the material moving through a cross-flow of drying gas; the drying enclosure, e.g. shaft, consisting of substantially vertical, perforated walls
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
    • F26B25/001—Handling, e.g. loading or unloading arrangements
    • F26B25/002—Handling, e.g. loading or unloading arrangements for bulk goods

Definitions

  • This invention relates generally to gravity flow dryers for particulate material and, more particularly, to a multi-stage gravity flow dryer for particulate material wherein the discharge of the dryer is channelized.
  • the need to dry grain prior to storage has long been recognized in the art and many grain drying systems have been developed to accomplish this purpose.
  • the grain is .heated by air at a predetermined temperature during a first drying process and then the grain is quickly cooled to a desired storage temperature by exposing the grain to a flow of ambient air.
  • One such system is the cross-flow column type grain dryer in which grain flows downwardly by gravity through a column having perforate walls and heated air is forced transversely through the perforate walls of the column to contact the grain to dry the grain or remove moisture.
  • Typical of such cross-flow grain dryers are the grain dryers shown and described in US ⁇ A ⁇ 3238640 and DE-C-717052.
  • Constructional details of the discharge means of a dryer according to Claim 1 are the subject- matter of divisonal application EP-A-0206069.
  • a column type gravity flow dryer for particulate material for example, corn or other type grain.
  • the dryers generally designated 10, includes a generally square-shaped housing 12 comprised of a pair of solid end walls 14 and 16 and a pair of side walls 18 and 20. Each of the side walls 18 and 20 includes solid upper and lower portions 22 and 24, respectively, and a perforate intermediate portion 26.
  • the housing 12 further includes a suitable roof 28 and is supported at the bottom by suitable support means or legs 30.
  • At the top of the housing 12 is a means for introducing moist particulate material or grain into the top portion of the housing, in this embodiment, a suitably sized wet grain inlet 32.
  • the assembly 34 On the outside of the housing 12 adjacent end wall 14, is an assembly or means 34 for providing drying air and cooling air to the housing 12.
  • the assembly 34 which is supported by a suitable support frame 36, generally includes a blower section 38 and a heater section 40.
  • the blower section 38 comprises a pair of blowers or fans 42 and 44 both of which are mounted for rotation on a single shaft 46.
  • the fan shaft 46 extends outwardly through a generally circular cooling air inlet opening 48 in the blower section 38 and is journaled for rotation within a suitable bearing 39.
  • a suitable drive pulley 50 is mounted on the outwardly extending end of the fan shaft 46.
  • the drive pulley 50 is driven to rotation by means of a standard drive belt system 52 which also engages a second drive pulley 54.
  • the drive pulley 54 may be driven by any suitable means, for example, an electric motor or a power takeoff mechanism on a tractor or other vehicle (not shown).
  • the fan 42 which is closest to the cooling air inlet opening 48, is the cool air fan and the fan 44, which is furthest from the air inlet opening 48, is the hot air fan, the fans being separated by a vertical partition 43 to form individual chambers surrounding each fan. Cooling air is drawn in through the inlet opening 48 by the cool air fan 42 and is directed into a pair of cool air ducts 56 which in turn direct the cooling air into the dryer housing 12.
  • the hot air fan 44 draws air in through a second generally rectangular air inlet opening 49 located in the other housing end wall 16 at the opposite end of the housing and the hot air fan 44 directs the flow of air upwardly into the heater section 40.
  • the heater section 40 includes a burner 58 which heats the air received from the fan 44. In the preferred embodiment, the burner 58 may be a standard Maxon gas burner. The heated air from the burner 58 passes into a collector chamber 60 and thereafter is directed into the housing 12 by a pair of generally cylindrical hot air ducts 62.
  • the heater section 40 and the blower section 38 are separated by a generally horizontally disposed partition 64 which contains an airflow control means, comprising in this embodiment, a plurality of adjustable dampers 66.
  • the adjustable dampers 66 are provided to control the flow of air from the hot air fan 44 to the burner 58. In this manner, it is possible to effectively regulate the hot air flow into the housing 12 to efficiently dry a variety of different types of particulate material. For example, it may be desirable to provide a large hot air flow into the housing 12 for drying high moisture content corn and a much smaller hot air flow into the housing 12 for drying lower moisture content rice.
  • the adjustable dampers 66 may be set in a substantially fully open position to apply a large hot air flow to dry corn or in a substantially closed position to apply a small hot air flow when drying rice.
  • the dryer 10 comprises a pair of generally vertical outer drying columns 68, each column being defined by first and second substantially parallel opposed spaced perforate walls 70 and 26.
  • a wet grain hopper 72 is provided at the top portion of the dryer for receiving and temporarily storing the moist grain introduced into the top of the housing 12 through the wet grain inlet 32.
  • the wet grain hopper 72 is defined by the roof panels 28, the side wall upper solid portions 22 and a pair of sloping interior hopper walls 74.
  • the wet grain hopper 72 also functions to distribute the moist grain into the top portions of each of the outer drying columns 68.
  • the columns are tapered outwardly from top to bottom so that the width of each of the columns is greater at the bottom than at the top.
  • the air flow is less restricted at the top of the columns (where the grain is wetter and provides a high air flow rate through the outer columns 68) than at the bottom of the columns (where the grain is drier), thereby providing for a more volume controlled airflow through the columns over their entire length.
  • each of the outer drying columns 68 is a dividing wall means, in the present embodiment a generally vertical partition 76, for dividing the lower portion of each of the drying columns 68 into two generally parallel channels 78 and 80.
  • Each of the channels 78 and 80 preferably contains separate discharge means, in the present embodiment metering rolls 82 and 84, respectively, for discharging particulate material from the channels 78 and 80 at predetermined rates.
  • Both of the metering rolls 82 and 84 are driven by a system of drive belts and pulleys generally designated 85. As shown, the drive pulley for the metering roll 84 is of a smaller diameter than the drive pulley for metering roll 82.
  • metering roll 84 rotates faster than metering roll 82 to thereby discharge grain from the innermost channel 80 at a faster rate than the grain is discharged from the outermost channel 78.
  • the grain from both channels 78 and 80 is discharged by the respective metering rolls 82 and 84 into a receiving hopper 86.
  • heated air from the hot air ducts 62 passes outwardly through the outer drying columns 68 to contact and dry the grain in the columns. Since the heated air enters each of the columns 68 through the inner perforated walls 70, the hottest driest air impinges upon the grain on the side of the drying columns adjacent the inner perforated walls 70. As the heated air continues on its path across the columns, a certain amount of heat is lost to the grain in the columns and the air picks up and retains moisture from the grain. By the time the air reaches the grain adjacent the outermost perforate walls 26, a significant portion of the heat has been lost to the grain and the same flow of air is also somewhat moisture laden and not able to dry the grain as effectively.
  • the drying of the grain is somewhat uneven across the column, the grain adjacent the inner perforate walls 70 becoming drier as it flows down the columns than the grain flowing down the columns adjacent the outer perforate walls 26.
  • the faster drying grain adjacent wall 70 is more quickly removed from the columns and the slower drying grain adjacent wall 26 is retained in the columns for a longer period of time and is exposed to the drying air for a longer period of time to promote more uniform drying across the column.
  • each of the partitions 78 is provided with an adjustable or pivotable section or divider 79.
  • the adjustable or pivotable sections 79 may be adjusted depending upon the initial moisture content and type of grain being dried to change the relative proportions of the grain entering the channels 78 and 80 in order to further improve the uniformity of the drying across the columns. For example, when drying corn with a very high initial moisture content, it may be desirable to adjust the pivotable sections 79 to provide for a smaller portion of the grain flowing into channels 80 than is flowing into channels 78. In this manner, more of the corn is retained in the drying columns 68 for a longer time period.
  • the uniformly dried grain discharged from each of the channels 78 and 80 of the outer drying columns 68 is received and collected in the receiving hopper 86.
  • a tube member 88 which extends vertically upwardly into the dryer housing 12.
  • a conveyor means for example, a grain carrying auger 90 which is driven to rotation by means of a suitable drive pulley 92 extending outwardly from the bottom of the receiving hopper 86.
  • the drive pulley 92 may be driven by any suitable means, for example, an electric motor or the power takeoff from a tractor or other vehicle (not shown).
  • the lower end of the tube member 88 contains a plurality of openings 94 which allow the partially dried grain from the outer columns 68 which has accumulated within the receiving hopper 86 to pass into the tube member 88.
  • the grain passing into the tube member 88 is conveyed or transported upwardly by the rotating grain auger 90 and is discharged from the tube member 88 into a substantially enclosed inner chamber 96.
  • the rotation of the grain auger 90 is sufficient to evenly distribute the grain discharged from the tube member 88 over the inner chamber 96.
  • cross- augers or other suitable means may be employed to provide an even distribution of the grain across the length and width of the inner chamber 96.
  • the inner chamber 96 serves as a steeping or tempering chamber for the grain.
  • the sloping lower walls 98 of the steeping chamber 96 are at an angle of not less than 45° in order to provide for an acceptable flow of the moist grain downwardly through the steeping chamber.
  • the sloping lower walls 98 of the steeping chamber include suitable insulation 102 to prevent the grain flowing through the steeping chamber adjacent the lower walls 98 from becoming overheated due to its proximity to the incoming heated air passing through the hot air ducts 62.
  • the upper walls 74 of the steeping chamber 96 are also sloped at an angle of not less than 45° to assure an acceptable flow of the incoming moist grain from the wet grain inlet 32 into the outer drying columns 68.
  • the upper steeping chamber walls 74 include means, for example, a plurality of slots 106 extending therethrough which allow some of the incoming moist grain to pass directly into the steeping chamber 96, in order to make up for any shrinkage of the grain which may have occurred as a result of the drying of the grain as it passed through the outer drying columns 68.
  • the slots 106 may also be employed to control the moisture content of the grain in the steeping chamber in a manner which will hereinafter become apparent. In the steeping chamber, the moisture in the grain tends to be uniformly distributed amongst all the grain in the chamber.
  • the roof 28 may also contain a level control means 104 positioned slightly above the slots 106.
  • the level control means 104 functions to actuate an elevator bucket or infeed auger (not shown) to maintain the grain in the wet grain hopper 72 at a level above the slots 106 in order to ensure that there is sufficient moist grain available for adding to the steeping chamber 96 to make up for any shrinkage which may have occurred.
  • the grain in the steeping chamber 96 flows downwardly at a controlled rate and passes into a pair of inner drying columns 100 which are also comprised of first and second perforate walls 108 and 110, respectively.
  • the perforate walls 108 cooperate with perforate walls 70 and with the housing end walls 14 and 16 to form a pair of substantially enclosed plenum chambers 112.
  • the plenum chambers 112 receive the heated airfrom the hot air ducts 62 and distribute the heated air so that it passes outwardly through the outer drying columns 68 and inwardly through the inner drying columns 100 along the entire length of the columns.
  • the plenum chambers 112 may include suitable adjustable damper means 114 extending across the plenum chambers 112 between the end walls 14 and 16 to further control the distribution of the heated air to the inner and outer drying columns 68 and 100.
  • the damper means 114 limits the amount of air which passes into the lower portion of the plenum chamber 112 to force more air through the upper section of the columns 68 and 100.
  • the openings of the adjustable damper means 114 are tapered extending across the plenum chambers with the larger openings being adjacent end wall 14 or in close communication with the hot air ducts 62 to provide a generally uniform distribution of drying air into the lower portion of each plenum chamber.
  • Figs. 1, 4 and 6 show a slightly different structural arrangement for evenly distributing the heated air within the plenum chambers 112.
  • a pair of tapered perforate tubes 116 (116' in Fig. 6) extend across the plenum chambers 112 between the end walls 14 and 16.
  • the larger end of the tapered tubes 116 re connected to and communicate with the hot air ducts 62 to receive the flow of heated air therefrom. Because the tubes 116 are tapered, the amount of heated air that passes along the length of the tube is restricted, thereby providing a uniform static pressure distribution along the length of the tube to ensure a uniform airflow out of the perforations therein.
  • the uniform air flow from the tapered tubes 116 provides a generally uniform distribution of the heated air along the tubes and throughout the plenum chamber 112, thereby providing a more uniform flow of the heated air through the columns 68 and 100 along their entire length.
  • the tapered tubes 116 may be replaced with constant diameter tubes. (not shown) having perforations varying in size and percentage of total opening along the length of the tubes, (the end of the tubes connected to the hot air ducts 62 having the larger diameter perforations and greater percentage of openings) to provide the desired generally uniform static pressure distribution along the length of the tubes into the plenum chamber.
  • the inner drying columns 100 also have a generally vertical partition 118, which divides each column into inner and outer channels 120 and 122 in a manner corresponding to the partitions 76 for the outer drying columns 68.
  • Discharge means in the form of metering rolls 124 and 126 are also provided for discharging grain from the inner and outer channels 120 and 122, respectively.
  • the metering rolls 124 and 126 also turn at different predetermined rates for discharging the grain from the channels 120 and 122 at different rates.
  • the metering rolls 126 adjacent the first perforate walls 108 discharge the material at a rate faster than the metering rolls 124.
  • a pair of distribution ducts 127 having triangular cross-sections extend across the plenum chambers 112 between the end walls 14 and 16.
  • One end of the distribution ducts 127 is connected to the cool air ducts 56 for receiving the cooling air flow.
  • the ducts 127 have one wall provided by the perforated walls 108, which provide for the passage of cooling air into the lower portion of the inner drying columns 100. Adjacent each of the ducts 127 are small access or clean-out doors 129 to provide for the removal of debris which may accumulate within the plenum chambers 112.
  • the inner drying columns 100 may also be wider at the bottoms than at the tops in a manner similar to that of the outer drying column 68 for substantially the same reasons as discussed above. Grain from the channels 120 and 122 of the inner drying columns 100 is discharged into a second or inner receiving hopper 130. Grain from the second receiving hopper 130 may be removed from the dryer by means of a discharge tube 132 and may thereafter be transported to a suitable storage facility (not shown).
  • the dryer 10 also includes a central inner chamber 134 surrounding the vertical tube member 88 and formed on opposite sides by the innermost perforate walls 110.
  • the central chamber 134 extends the entire length of the dryer between end walls 14 and 16 (shown on Fig. 1) and provides the conduit between the hot air fan 44 and the second air inlet opening 49 for the movement of ambient air into the inlet of the hot air fan 44.
  • the central chamber 134 also receives and collects both the heating and cooling air exhausted from the inner drying columns 100 and recycles or recirculates this exhausted air back to the hot air fan 44.
  • Figs. 7, 8 and 9 show additional details of the lower portion of the dryer, including the grain discharge means.
  • metering roll 82 is retained within a plurality of aligned spaced-apart tubular members 136. Adjacent to and above the tubular members 136 are a plurality of inverted V-shaped members 138, which serve as deflectors to direct the downward flow of grain into spaces 140 between the tubular members 136.
  • the metering roll 82 further comprises a horizontal rotating grain auger 142 disposed within the tubular members 136.
  • the grain auger is supported by, for example, a suitable bearing 144 and is driven, for example, by means of a suitable drive pulley of the type hereinbefore described.
  • Grain flowing downwardly in each of the channels of the drying columns is deflected by the inverted V-shaped members 138 into the spaces 140 between the tubular members 136 where it is received and carried by the rotating grain auger 142 as shown by the flow arrows. Thereafter, the grain is discharged from the grain auger 142 through a plurality of openings 146 located between the lower portions of each of the tubular members 136 and the grain enters the receiving hopper 86, as shown in Fig. 3.
  • Each of the spaces 140 between the tubular members 136 is enclosed and includes a removable bottom panel 148, which is retained in place as shown by means of a pair of supporting side flanges 150 and a pair of suitably sized U-shaped clamps 152.
  • the bottom panels 148 may be conveniently removed for cleaning out the spaces 140 and the grain auger 142.
  • the combination of the metering rolls and the inverted V-shaped members 138 provide for a uniform withdrawal of grain across each of columns of the dryer. Additional details concerning the structure and operation of the grain discharge means may be obtained from US-A-4152841.
  • the other metering rolls 84,124 and 126 operate and are constructed similarly to metering rolls 82.
  • cross flow dryers of the type shown it is desirable to use the same dryer to dry particulate materials or grains of widely varying dimensions. For example, it may be desirable to dry either corn or rice in the same dryer. In order to be able to dry such different types of grains in the same dryer without any considerable loss of product or drying efficiency, it is necessary to have the ability to conveniently vary the size of the openings in the dryer's perforate walls forming the drying columns.
  • each module is complete in itself and comprises four generally parallel perforate side panels 110', 108', 70' and 26', which are fixed to a plurality of generally vertical support members or cross braces 172.
  • primes are used to designate component parts of the module 160, the primes being dropped when the module 160 is installed in the dryer 10 as shown on Fig. 4 (Fig. 3 does not show the modular construction features of the dryer 10).
  • the perforate panels 110', 108', 70' and 26' may all be of one piece construction or may be made up of a plurality of individual smaller panels which are attached to the cross braces 172.
  • the perforate panels 110', 108', 70' and 26' cooperate to form a pair of drying columns 100' and 68' with a plenum chamber 112' therebetween.
  • a tapered perforate tube 116', a generally triangularly-shaped distribution duct 127' in cross-section having a perforated side wall 108' as a part thereof, and a clean-out door 129' are also included as part of the module 160 as shown.
  • a pair of complementary modules 160 When a pair of complementary modules 160 are placed in position in the dryer housing 12 as shown in Fig. 4, they form the drying columns 68 and 100.
  • the upper and lower portions of the modules 160 are suitably contoured to enable the modules to be appropriately positioned within the dryer housing 12 as shown in Fig. 4.
  • the tapered perforate tubes 116 are connected to and cooperate with the hot air ducts 62 (shown in Fig. 1) for the distribution of hot air within the plenum chamber 112.
  • the triangular-shaped air ducts 127 are connected to and cooperate with the cooing air ducts 56 (shown in Fig. 1) to provide a flow of cooling air when the modules 160 are in place within the dryer housing 12.
  • Suitable sealing means may be provided to prevent air leakage from around the connection of the perforate tubes 116 and the triangular-shaped ducts 127 with the hot air ducts 62 and cooling air ducts 56.
  • a number of small flanges 178 on the corners of the modules 160 engage suitable complementary flanges 180 on the dryer housing 12 in order to properly position and retain the modules 160 in place within the housing 12.
  • a plurality of sealing means, for example, neoprene flaps 182 are employed to close any gaps or openings which may occur along the joint lines where the modules 160 meet the dryer housing 12 and to prevent the leakage of any grain through any such gaps or openings.
  • each dryer 10 has one or more pairs of such modules 160.
  • Each pair of such modules 160 has perforate side panels 110', 108', 70' and 26' with perforations of a different size than the other pairs of modules.
  • one pair of modules have perforations ideally suited for drying rice, whereas another pair of modules will have perforations ideally suited for drying corn. In this manner, greater flexibility and drying efficiency may be achieved with a single basic dryer structure.
  • the dryer 10 may be operated as a batch-type dryer or as a continuous flow-type dryer. In either type of dryer operation, an operator makes a determination as to what type of grain is to be dried and the initial moisture content of the grain. The operator then selects the appropriate pair of modules 160 for the grain to be dried and installs the modules in the dryer housing 12 as shown in Fig. 4. The operator also adjusts the adjustable air flow dampers 66 (shown in Fig. 1) to the proper setting to provide the desired air flow to provide optimum drying for the particular grain being dried. Likewise, the operator adjusts the pivotable sections 79 on the partitions 76 and 118 (shown in Fig. 1) to determine the relative portion of the grain which will be rapidly discharged from the grain columns 68 and 100 as described in detail above.
  • the dryer is then activated and the grain to be dried is fed into the wet grain inlet 32.
  • the grain from the wet grain inlet 32 flows downwardly into the wet grain hopper 72 and is introduced into the top of the outer drying columns 68.
  • heated air from the plenum chamber 112 flows outwardly through the grain to heat the grain and remove moisture therefrom.
  • the drying air passes outwardly through the outer perforate wall 26 to the atmosphere. As the grain flows downwardly through the column, it becomes increasingly drier due to its continued contact with the heated air.
  • the grain flowing down the columns adjacent to perforate walls 70 is dried more rapidly than the grain flowing down the column adjacent outer walls 26. Accordingly, as also discussed in detail above relative to Fig. 3, the grain flowing through the columns 68 adjacent perforate walls 70 is discharged from the columns 68 at a faster rate than the grain flowing down the column adjacent the perforate walls 26.
  • All of the grain discharged from the outer columns 68 is received and collected in the first receiving hopper 86.
  • the collected grain flows downwardly within the hopper 86 and enters the vertical tube member 88 through the openings 94.
  • the rotating grain auger 90 within the vertical tube member 88 transports the grain upwardly to the top of the tube member 88 where it is discharged into the steeping chamber 96.
  • the steeping chamber 96 is generally filled with partially dried grain. Due to the relatively large size of the steeping chamber 96 with respect to the inner drying columns 100 which receive the grain discharged from the steeping chamber, the grain introduced to the top of the steeping chamber 96 moves slowly down from the steeping chamber 96 at a predetermined uniform rate. It is anticipated that the grain remains in the steeping chamber for at least a one hour period. While within the steeping chamber, the grain is steeped or sweats in a manner well known in the art.
  • the grain After passing out of the steeping chamber 96, the grain enters the inner drying columns 100 and passes downwardly therethrough. At the top of the inner drying columns 100, the grain is again exposed to a flow of heated drying air, which passes inwardly from the plenum chambers 112, through the columns 100 and into the central chamber 134, as shown in Fig. 3. As the grain moves further down the inner columns 100, it is exposed to the cooling air which passes inwardly from the cooling air distribution ducts 127, through the columns 100 and into the central chamber 134. The dried and cooled grain is then discharged into the second or inner receiving hopper 130. The grain may then be removed from the dryer by means of the discharge tube 132 for subsequent storage and/or use.
  • the slots 106 may be employed in conjunction with the metering rolls 124 and 126 at the bottom of the inner drying columns 100 to further control the moisture content of the grain discharged from the dryer 10. More specifically, by putting the metering rolls 124 and 126 on a separate drive (not shown), the amount of wet grain which enters the steeping chamber 96 through the slots 106 may be accurately controlled.
  • the dryer 10 is better able to dry various types of grains having various initial moisture contents to a specified final moisture content.
  • the heated air passing through the inner drying columns 100 enters the central chamber 134 and is recycled back to the hot air fan 44 for reuse.
  • the cooling air which has passed through the inner columns 100 and has picked up heat from the heated grain within the columns is recycled back to the hot air fan 44 in the same manner.
  • the heated air passing through the outer columns 68 is too saturated with moisture which has been removed from the grain, to be of desired use in recycling, and, thus, is exhausted to the atmosphere through the outer perforate walls 26.
  • the present invention comprises a multi-stage gravity flow dryer for particulate material in which the particulate material is discharged in a channelized manner in order to provide improved uniformity of drying, as well as prevents overheating and cracking of the particulate material being dried.

Landscapes

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

Claims (9)

1. Séchoir (10) à écoulement par gravité pour matière granuleuse, comprenant une première colonne de séchage (68) généralement verticale comportant une première et une seconde parois perforées (70, 26) opposées et écartées, des premiers moyens d'entrée (32) pour introduire la matière granuleuse humide dans une partie supérieure de la première colonne de séchage (68), des premiers moyens d'évacuation (82, 84) pour extraire la matière granuleuse partiellement séchée d'une partie inférieure de la première colonne de séchage (68), une deuxième colonne de séchage (100) généralement verticale comportant une première et une seconde parois perforées (108, 110) opposées et écartées, les première et deuxième colonnes de séchage étant écartées l'une de l'autre, un collecteur d'air (112) délimité par les premières parois perforées (70, 108) de chaque colonne de séchage, des seconds moyens d'entrée (90, 96) pour introduire la matière granuleuse partiellement séchée dans une partie supérieure de la deuxième colonne de séchage (100), des seconds moyens d'évacuation (124,126) pour extraire la matière granuleuse séchée d'une partie inférieure de la deuxième colonne de séchage (100), des moyens (40) pour fournir de l'air de séchage au collecteur d'air (112) par lesquels l'air de séchage passe dans les première et deuxième colonnes de séchage (68, 100) à travers les premières parois perforées (70, 108) pour sécher la matière granuleuse, l'air de séchage étant rejeté des colonnes de séchage (68, 100) à travers les secondes parois perforées (26, 110), et des moyens (42, 56,127) pour diriger un courant d'air de refroidissement à travers une partie de la deuxième colonne de séchage (100) pour refroidir la matière granuleuse séchée avant sa sortie de la deuxième colonne de séchage (100), caractérisé en ce qu'il est prévu des moyens de transport (88, 90) pour recevoir la matière granuleuse partiellement séchée provenant des premiers moyens d'évacuation (82, 84) et pour transporter la matière granuleuse partiellement séchée jusqu'aux seconds moyens d'entrée (90, 96), en ce que le collecteur d'air (112) est prévu entre les première et deuxième colonnes de séchage et en ce que les seconds moyens d'entrée comprennent une chambre de trempage (96) recevant un premier courant de la matière granuleuse partiellement séchée provenant des moyens de transport pour tremper la matière granuleuse partiellement séchée avant son introduction dans la duxième colonne de séchage (100).
2. Séchoir suivant la revendication 1, caractérisé par des moyens de conduit (134) pour recevoir l'air de séchage rejeté de la deuxième colonne de séchage (100) et pour renvoyer l'air rejeté de la deuxième colonne de séchage (100) vers les moyens (40) pour fournir de l'air de séchage.
3. Séchoir suivant la revendication 1 ou la revendication 2, caractérisé en ce que la chambre de trempage (96) comprend des moyens (106) pour introduire un second courant de matière granuleuse humide dans celle-ci afin de maintenir la chambre de trempage (96) à un niveau prédéterminé de remplissage.
4. Séchoir suivant la revendication 3, caractérisé en ce que les seconds moyens d'évacuation (124, 126) sont agencés de façon à coopérer avec les moyens (106) pour introduire le second courant de matière dans la chambre de trempage (96) afin de régler la quantité de matière granuleuse dans la chambre de trempage (96).
5. Séchoir suivant l'une ou l'autre des revendications précédentes, caractérisé en ce qu'il comprend en outre une troisième et une quatrième colonnes de séchage (68, 100) généralement verticales, substantiellement les mêmes que les première et deuxième colonnes de séchage (68, 100), les troisième et quatrième colonnes de séchage étant disposées dans le séchoir (10) pour former un séchoir à quatre colonnes, les premiers moyens d'entrée (32) introduisant également la matière granuleuse humide dans une partie supérieure de la troisième colonne de séchage (68) et les seconds moyens d'entrée (90, 96) introduisant également la matière granuleuse partiellement séchée dans une partie supérieure de la quatrième colonne de séchage (100), les troisième et quatrième colonnes formant entre elles un second collecteur d'air (112), les moyens (40) pour fournir de l'air de séchage fournissant également de l'air de séchage au second collecteur d'air (112), et en ce que l'air de séchage pénètre dans les troisième et quatrième colonnes de séchage (68, 100) à travers des premières parois perforées correspondantes (70, 108) pour sécher la matière granuleuse, l'air de séchage étant rejeté des troisième et quatrième colonnes de séchage (68, 100) à travers des secondes parois perforées (26, 110), les deuxièe et quatrième colonnes de séchage (100) formant entre elles une chambre centrale (134) pour recevoir l'air de séchage rejeté de celles-ci, qui est renvoyé vers les moyens (40) pour fournir de l'air de séchage.
6. Séchoir suivant l'une ou l'autre des revendications précédentes, caractérisé par des moyens de paroi de division (76, 79) s'étendant entre les parois perforées (70, 26) de la première colonne de séchage pour diviser au moins une partie de la colonne (68) en au moins deux canaux (78, 80), lesdits premiers moyens d'évacuation (82, 84) comprenant des premiers moyens (84) d'évacuation d'un canal associés à un premier des canaux (80) et des seconds moyens (82) d'évacuation d'un canal associés à un second des canaux (78), le premier canal (80) étant adjacent à la première paroi perforée (70) et les premiers moyens (84) d'évacuation d'un canal étant agencés pour évacuer la matière granuleuse à une vitesse plus élevée que les seconds moyens d'évacuation (82).
7. Séchoir suivant la revendication 6, caractérisé en ce que des seconds moyens de paroi de division (118) s'étendent entre les parois perforées (108, 110) de la deuxième colonne de séchage (100) pour diviser au moins une partie de la deuxième colonne (100) en au moins deux canaux, lesdits seconds moyens d'évacuation (124, 126) comprenant des troisièmes moyens (126) d'évacuation d'un canal associés à un des canaux (122) de la deuxième colonne (100) et des quatrièmes moyens (124) d'évacuation d'un canal associés à un canal (120) de la deuxième colonne (100) différent de celui des troisièmes moyens (126) d'évacuation d'un canal, les troisièmes moyens (126) d'évacuation d'un canal étant adjacents à la première paroi perforée (108) de la deuxième colonne (100) et étant agencés pour évacuer la matière granuleuse à une vitesse plus élevée que les quatrièmes moyens (124) d'évacuation d'un canal.
8. Séchoir suivant l'une ou l'autre des revendications précédentes, caractérisé en ce que la ou chaque colonne de séchage (68) présente une section transversale substantiellement rectangulaire et a une plus grande largeur au pied qu'au sommet.
9. Séchoir suivant la revendication 6, caractérisé en ce que les moyens de paroi de division (76, 79) sont situés à la partie inférieure de la première colonne de séchage (68), les premiers et seconds moyens (82, 84) d'évacuation d'un canal servant de premiers moyens d'évacuation pour extraire la matière granuleuse zéchée hors de la colonne (68), au moins une partie (79) des moyens de paroi de division (76, 79) étant réglable pour faire varier les grandeurs relatives des canaux (78, 80).
EP19820303149 1981-06-19 1982-06-17 Séchoir à étages multiples pour matière granuleuse comportant un dispositif d'évacuation canalisé Expired EP0068734B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT82303149T ATE33306T1 (de) 1981-06-19 1982-06-17 Mehrstufentrockner fuer koerniges material mit kanalisierter abfuehrung.

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US06/275,313 US4398356A (en) 1981-06-19 1981-06-19 Multi-stage dryer for particulate material
US275312 1981-06-19
US06/275,312 US4423557A (en) 1981-06-19 1981-06-19 Gravity flow dryer for particulate material having channelized discharge
US275313 1981-06-19

Related Child Applications (2)

Application Number Title Priority Date Filing Date
EP86107817A Division EP0206069A3 (fr) 1981-06-19 1982-06-17 Séchoir à étages multiples pour matière granuleuse comportant un dispositif d'évacuation canalisée
EP86107817.8 Division-Into 1982-06-17

Publications (3)

Publication Number Publication Date
EP0068734A2 EP0068734A2 (fr) 1983-01-05
EP0068734A3 EP0068734A3 (en) 1984-09-12
EP0068734B1 true EP0068734B1 (fr) 1988-03-30

Family

ID=26957361

Family Applications (2)

Application Number Title Priority Date Filing Date
EP19820303149 Expired EP0068734B1 (fr) 1981-06-19 1982-06-17 Séchoir à étages multiples pour matière granuleuse comportant un dispositif d'évacuation canalisé
EP86107817A Ceased EP0206069A3 (fr) 1981-06-19 1982-06-17 Séchoir à étages multiples pour matière granuleuse comportant un dispositif d'évacuation canalisée

Family Applications After (1)

Application Number Title Priority Date Filing Date
EP86107817A Ceased EP0206069A3 (fr) 1981-06-19 1982-06-17 Séchoir à étages multiples pour matière granuleuse comportant un dispositif d'évacuation canalisée

Country Status (10)

Country Link
EP (2) EP0068734B1 (fr)
AR (1) AR226984A1 (fr)
AU (2) AU565672B2 (fr)
BR (1) BR8203554A (fr)
CA (1) CA1176053A (fr)
DE (1) DE3278292D1 (fr)
DK (2) DK259682A (fr)
GR (1) GR76498B (fr)
HU (1) HU189147B (fr)
NZ (1) NZ200681A (fr)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NZ200681A (en) * 1981-06-19 1987-03-06 Westelaken C Gravity flow grain dryer with two stages of drying
US5992044A (en) * 1998-06-12 1999-11-30 Sukup Manufacturing Company Method and apparatus for drying grain
AU2004274520C1 (en) * 2003-09-25 2010-12-09 Ect Coldry Pty Ltd Dryer, drying method and drying plant
GB201007697D0 (en) 2010-05-06 2010-06-23 Ucl Business Plc A supra-threshold test for use in detecting sensitivity loss across the field of vision
CN106679393B (zh) * 2017-01-20 2022-04-22 中国科学院理化技术研究所 一种粮食烘干系统
CN109095017A (zh) * 2018-09-06 2018-12-28 云南中烟工业有限责任公司 一种新型打叶器进料流量控制装置
CN113280610B (zh) * 2021-05-31 2022-06-07 安徽华谷机械科技有限公司 一种梯度脱水的粮食烘干机
CN114963740B (zh) * 2022-04-29 2023-07-07 江苏经贸职业技术学院 一种食品加工烘干装置

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2732630A (en) * 1956-01-31 Markowich
GB190920758A (en) * 1909-09-10 1910-09-12 Diedrich Uhlhorn Shaft Drier for Corn with Automatically Regulated Discharge of the Dried Material.
GB213799A (en) * 1923-05-25 1924-04-10 George Richard Schueler Improvements in apparatus for cooling and drying nuts, cubes and similarly shaped pieces of compressed material for use as food for cattle and other animals, and grain, seed and other material in bulk
DE462031C (de) * 1925-11-07 1928-07-03 Otto Nordstroem Schachttrockner mit einem aus Siebmaenteln gebildeten Ringschacht
DE717052C (de) * 1939-01-12 1942-02-04 August Gronert Rieselschachttrockner fuer koerniges Gut
US3078590A (en) * 1960-06-27 1963-02-26 A F Meyer Mfg Co Grain dryer
US3238640A (en) * 1962-09-04 1966-03-08 Hart Carter Co Grain dryer
DE1604920B2 (de) * 1965-12-23 1973-01-18 Wilhelm Heine, Malzfabrik, 3150 Peine Vertikaltrockner fuer getreide bzw. zum schwelken und darren von malz
FR93262E (fr) * 1966-08-31 1969-03-07 Etablissements Rivierre Casali Séchoir pour produits granuleux.
US3426442A (en) * 1967-06-01 1969-02-11 Toshihiko Satake Drying apparatus for cereals
CH497768A (de) * 1968-10-10 1970-10-15 Sulzer Ag Bestrahlungsanlage, insbesondere für körniges Gut
US4223452A (en) * 1979-02-12 1980-09-23 Chambers John M Drying process and apparatus for accomplishing the same
NZ200681A (en) * 1981-06-19 1987-03-06 Westelaken C Gravity flow grain dryer with two stages of drying
US4423557A (en) * 1981-06-19 1984-01-03 Westelaken C Gravity flow dryer for particulate material having channelized discharge

Also Published As

Publication number Publication date
EP0068734A3 (en) 1984-09-12
CA1176053A (fr) 1984-10-16
DK259682A (da) 1982-12-20
AU7055187A (en) 1987-07-09
DK468988D0 (da) 1988-08-19
NZ200681A (en) 1987-03-06
AR226984A1 (es) 1982-08-31
AU582301B2 (en) 1989-03-16
DE3278292D1 (en) 1988-05-05
EP0068734A2 (fr) 1983-01-05
EP0206069A3 (fr) 1987-02-25
HU189147B (en) 1986-06-30
BR8203554A (pt) 1983-06-07
EP0206069A2 (fr) 1986-12-30
GR76498B (fr) 1984-08-10
AU565672B2 (en) 1987-09-24
DK468988A (da) 1988-08-19
HUT35834A (en) 1985-07-29
AU8470282A (en) 1982-12-23

Similar Documents

Publication Publication Date Title
US4424634A (en) Modular column dryer for particulate material
US4423557A (en) Gravity flow dryer for particulate material having channelized discharge
US4125945A (en) Multiple stage grain dryer with intermediate steeping
US4398356A (en) Multi-stage dryer for particulate material
CA2868285C (fr) Sechoir multiproduit de courroie pour produits pateux et/ou pulverulents, en particulier pour boues de station d'epuration ou biomasse
US4477984A (en) Multi purpose three pass drum dryer
US20060123655A1 (en) Continuous flow grain dryer
JPS5833470B2 (ja) レンゾクセンタクドライヤ−
EP0068734B1 (fr) Séchoir à étages multiples pour matière granuleuse comportant un dispositif d'évacuation canalisé
US4402302A (en) Air heating apparatus
US4152841A (en) Flow control meters for gravity flow particle dryers
US6223454B1 (en) Method of drying moist organic material
KR101823598B1 (ko) 용량 가변형 열회수 건조기
US5443539A (en) Particulate dryer
US5233766A (en) Vertical grain dryer
US5467535A (en) Moisture equalizer for a continuous flow grain dryer
US5992044A (en) Method and apparatus for drying grain
US3869809A (en) Continuous flow grain drying apparatus
RU2082924C1 (ru) Циклическая сушилка для сыпучих материалов
NZ213520A (en) Gravity flow grain dryer:differential flow rates
US5940982A (en) Particulate material dryer
CA1195108A (fr) Sechoir a decharges dirigees pour les cereales
KR0135062B1 (ko) 열풍건조방법 및 그 장치
US3063159A (en) Dryer for tobacco or the like
US1751472A (en) Drying process and apparatus

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Designated state(s): AT BE CH DE FR GB IT LI NL SE

PUAL Search report despatched

Free format text: ORIGINAL CODE: 0009013

AK Designated contracting states

Designated state(s): AT BE CH DE FR GB IT LI NL SE

17P Request for examination filed

Effective date: 19850302

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE CH DE FR GB IT LI NL SE

REF Corresponds to:

Ref document number: 33306

Country of ref document: AT

Date of ref document: 19880415

Kind code of ref document: T

REF Corresponds to:

Ref document number: 3278292

Country of ref document: DE

Date of ref document: 19880505

ITF It: translation for a ep patent filed
ET Fr: translation filed
PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed
PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: SE

Payment date: 19890607

Year of fee payment: 8

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: CH

Payment date: 19890609

Year of fee payment: 8

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: AT

Payment date: 19890612

Year of fee payment: 8

ITTA It: last paid annual fee
PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 19890630

Year of fee payment: 8

Ref country code: GB

Payment date: 19890630

Year of fee payment: 8

Ref country code: FR

Payment date: 19890630

Year of fee payment: 8

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 19890809

Year of fee payment: 8

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 19890829

Year of fee payment: 8

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Effective date: 19900617

Ref country code: AT

Effective date: 19900617

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SE

Effective date: 19900618

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LI

Effective date: 19900630

Ref country code: CH

Effective date: 19900630

Ref country code: BE

Effective date: 19900630

BERE Be: lapsed

Owner name: WESTELAKEN CHRISTIANUS MARINUS THERESIA

Effective date: 19900630

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Effective date: 19910101

GBPC Gb: european patent ceased through non-payment of renewal fee
NLV4 Nl: lapsed or anulled due to non-payment of the annual fee
PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Effective date: 19910228

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DE

Effective date: 19910301

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

EUG Se: european patent has lapsed

Ref document number: 82303149.7

Effective date: 19910206