Abstract: A grain dryer unload system is presented that facilitates operation of a discharge system independent of a metering system. A motor connects to an axle that connects to the discharge system, which may be a drag chain, a belt or an auger. The axle also connects to a metering system. A clutch mechanism is connected to an end of the axle and is positioned between the discharge system and the metering system. When the clutch mechanism is in an engaged position, the motor simultaneously operates the metering system and the discharge system. However, when the clutch mechanism is in a disengaged position, the motor operates the discharge system while the metering system does not operate. This arrangement facilitates easier cleaning of the grain dryer without introducing the fines into the grain or a connected grain storage device.

Abstract: Grain dryer of the type comprising a vertical main structure consisting of a central body through which the grain to be dried passes, a front hot air intake chamber and a rear used air outlet chamber, being that the main body has in its upper part an entrance from where wet grains are loaded, underneath which there is a loading hopper that communicates with the central body, wherein the grain descends along the central body within which it is dried during its fall by a flow of hot air that passes through the mass of grain, finally exiting through a discharge hopper arranged at the lower end of the dryer, the dryer of the invention being characterized in that it allows to significantly reduce the energy consumption in order to obtain a better quality of grain and a process much faster than conventional ones due to the arrangement of one or more preheating chambers without extraction of moisture from the grain.

Abstract: A food heating device includes a conveying unit, a heating unit, and a suction unit. The conveying unit has an endless belt member which allows hot air to pass therethrough. The belt member has an outgoing side on which the food is placed, and a return side, wherein the outgoing side passes through a space between the heating unit and the suction unit, and the return side is disposed to face the outgoing side and avoid the space between the heating unit and the suction unit.

Abstract: A dividing-wall rotary kiln device comprises a rotary kiln, an exhaust gas residual-heat power generation device, a gas recovery processing device, a cooler, a combustion fan, a feeding system and an exhaust emission system. A refractory brick unit of a kiln body is a hollow structure formed by a refractory inner cylinder and a refractory outer cylinder. A center of the refractory inner cylinder is a kiln chamber. A material channel is between the refractory inner cylinder and the refractory outer cylinder. The feeding system is connected to a feeding device via a raw material preheating compartment or a dividing-wall preheater. The feeding device is provided with a decomposition gas outlet connected to the gas recovery processing device via the raw material preheating compartment or the dividing-wall preheater. The kiln chamber is connected to the exhaust gas residual-heat power generation device via a kiln tail hood.

Abstract: A retrofit turner and sensor unit includes, on its upper portion, a grain turner for moving grain from a central portion in the grain pathway to a defined outer space for measurement. On its lower portion, the retrofit unit includes a moisture sensor and a temperature sensor provided in a plate configuration in line with the outer wall of the grain dryer for sensing moisture and temperature of grain in the defined space. In the preferred configuration, the plate sensor includes redundancies, and is mounted on a hinged door. The retrofit unit is easily installed into an existing grain dryer with columns and continuous flow capabilities, and electrically connected with a controller/processor and a motor for metering rolls which determine grain speed through the dryer.

Abstract: A system and method for at least partially drying seeds treated with a liquid. A supply of heated air is continuously fed to a drying chamber. Treated seeds enter one opening of the drying chamber and are forced around at least a portion of the internal perimeter of the drying chamber before exiting out a second opening. Another embodiment can treat the seeds during and/or after the seeds entering the drying chamber.

Abstract: Methods and apparatuses are provided for separating a slurry mixture into its constituent melted liquid form and solid frozen form. This involves forcing the slurry mixture through an inlet into a vessel and through the vessel to an opening, wherein the vessel comprises a plurality of perforations dimensioned to receive a liquid flow from the slurry mixture to dry the slurry mixture; vibrating the vessel and the slurry mixture within the vessel to shake the material in the melted liquid form out through the plurality of perforations to dry the slurry mixture; and, extracting the dried slurry mixture from the opening.

Abstract: The present application discloses an apparatus for manufacturing high-quality coal products. In certain embodiments, the apparatus comprises a housing and a heat conducting mechanism disposed within the housing. The heat conducting mechanism is provided with a heat conducting medium inlet proximate a material outlet end and a thermal conduction medium outlet proximate a material inlet end. The heat conducting mechanism comprises multiple groups of heat conducting units and the heating conducting unit comprises a plurality of heat conducting tubes. The heat conducting tubes are in communication with the heat conducting medium inlet and outlet. A plurality of fins inclining downward relative to the vertical direction are arranged along the longitudinal direction between adjacent heat conducting tubes.

Abstract: Methods and systems are provided for drying wet biosolids to produce a class A biosolids. Generally described, the method of treating biosolids includes drying a wet biosolids in an indirect dryer to produce a partially dried biosolids and drying the partially dried biosolids in a direct dryer in series with and downstream of the indirect dryer to produce a class A biosolids. The indirect dryer and direct dryer may be operated at an average temperature of greater than about 100° C. and may have a total combined residence time of less than about 60 minutes. Also provided are systems for drying wet biosolids including an indirect biosolids dryer and a direct biosolids dryer in series. The methods and systems are particularly effective at reducing the moisture content of the biosolids from greater than 85% to less than 10% by weight.

Abstract: A heat treatment apparatus for heat-treating powder particles each containing a binder resin and a colorant includes: a powder particle supply unit (3); a hot air supply unit (2); a cold air supply unit (4); a regulating unit (6); and a collection unit (5). The apparatus is characterized in that: a protrusion with a height of 2 mm or more and 50 mm or less is provided in a region on a downstream side of the powder particle supply unit and on an upstream side of the cold air supply unit in an inner wall surface of the treatment chamber; and the heat treatment apparatus has a cross-section plane, which is perpendicular to a center axis of the treatment chamber and situated at the region where the protrusion is provided, and Dmin and Dmax satisfy the following relation 0.50?Dmin/Dmax<1.

Abstract: Biosolids in the nature of sewage sludge is processed in a controlled environment to produce a dried sludge product of relatively high dry solid content with the elimination of or reduced levels of pathogens. The water containing sewage sludge is dried while cascading within a processing chamber using heated air at a temperature below the ignition or smoldering temperature of the sewage sludge to prevent the formation of embers. The sewage sludge before discharge is retained within the processing chamber for a sufficient time and temperature as mandated by the Environment Protection Agency rules and guidelines.

Abstract: Solids drying equipment via an axial flow process can include a plenum, a product to dry distributor feeder, drying air distribution pipe, one or more upper diffusion modules(s), one or more drying chamber(s), lower air diffusion module, with four to sixteen discharge bases with a hollow pyramidal format, discharge hopper, with a sluice, with a drying air feeding pipe and with a vertical output air tube provided with air output extensions. Such equipment may obtain better productivity and may allow for uniform insufflation of a large volume of air in a reduced space, for example, in addition to allowing seeds temperature to be maintained in safe levels due to the greater height of the drying layer, and allowing a progressive rest of seeds which, during motion by gravity, go towards the drying air at the bottom of the chamber.

Abstract: The present invention provides an improved continuous vertical feed pistachio nut dryer that has an inner compartment defined by bulkhead walls formed of smooth and seamless outer walls of perforated sheet stock, and has an infeed chamber with a batch hopper used in conjunction with an auger to provide a structure configured to operate in a batch fill mode wherein the inner compartment is filled evenly along the length of the dryer.

Abstract: A radial rotary dryer improves drying efficiency for sludge and other substances, prevents clogging phenomenon, and is realized in a simple structure. The radial rotary dryer includes spaces formed by inner and outer drums and partitioned by a plurality of radial plates. The substances, which have been introduced through a drum inlet together with hot blowing air, sequentially move throughout all spaces and are dried during drum rotation. The substances are discharged through an opposite side of the inner drum. A lift plate is attached at one surface of each radial plate to improve the drying efficiency. Hammers are attached to an opposite surface of the radial plate to free-fall according to the rotation of the drum, thereby crushing the substances. The radial rotary dryer is useful to dry sewage sludge, food waste, or other industrial substances with the best drying efficiency, the minimum installation space, and a crushing function.

Abstract: A grain turner for turning grain in a drying tower includes opposed generally vertical side walls and a generally vertical dividing plate (which is shorter than the side walls) extending between the side walls; the dividing plate defining inner and an outer vertical channels in a portion of the turner. An inner inclined plate is pivotally connected to one side wall to be within the inner channel and an outer inclined plate is connected to the other side wall to be within the outer channel. The inclined plates are pivotal between a first position in which they are inclined downwardly in a opposite widthwise directions and a second position in which they are generally adjacent their respective side walls. The inclined plates have a length such that when they are in the first position, their lower edges are proximate a bottom of the divider plate.

Abstract: A method and apparatus for indirect-heat thermal processing of material, such as a dryer or evaporator for treatment of particulate material, is provided. In one embodiment, a dryer for drying particulate material comprises a plurality of heat transfer plates arranged in spaced relationship for the flow of the material to be dried therebetween. Each heat transfer plate is provided with an inlet and an outlet for the flow of the heating fluid through the plates. A purge fluid delivery system provides a flow of purge fluid, such as air, gas or steam between the plates in a direction across the direction of flow of the material to be dried. The purge fluid delivery system provides a flow path for the purge fluid which is isolated from the flow of the heating fluid through the plates. A method for the indirect-heat processing of particulate material is also provided.

Abstract: The inner space of a drying tank 4 is made up of a mixing and drying zone MZ to mix and dry supplied material 3 by swirling the material 3 upward onto rotor blades 5 and pressing the material centrifugally against a heated cylindrical inner surface of the tank wall 2, and a drying zone DZ beneath the mixing and drying zone MZ. An upper screw conveyer 15, connected to the upper part of the mixing and drying zone MZ transfers material 3 out of the drying tank 4. A lower screw conveyer 13, connected to the bottom of the mixing and drying zone MZ transfers material received from the upper conveyor 15 through a vertical transfer pipe 17 back into the drying tank 4 along with new material to be dried. A discharge screw conveyer 21 is connected to the drying zone DZ to discharge out dried material continuously.

Abstract: A retrofit turner and sensor unit includes, on its upper portion, a grain turner for moving grain from a central portion in the grain pathway to a defined outer space for measurement. On its lower portion, the retrofit unit includes a moisture sensor and a temperature sensor provided in a plate configuration in line with the outer wall of the grain dryer for sensing moisture and temperature of grain in the defined space. In the preferred configuration, the plate sensor includes redundancies, and is mounted on a hinged door. The retrofit unit is easily installed into an existing grain dryer with columns and continuous flow capabilities, and electrically connected with a controller/processor and a motor for metering rolls which determine grain speed through the dryer.

Abstract: A continuous flow grain dryer includes airflow paths such that air passes through a grain column twice prior to exiting the grain dryer or being recirculated. The dual pass airflow defines a preheat zone in an upper portion of the grain flow paths adjacent an exhaust plenum. A heat zone is defined in the grain flow paths adjacent a high heat plenum and below the preheat zone. The dual pass airflow defines a temper zone in the grain flow paths adjacent a return plenum and below the heat zone. A cooling zone can be defined below the temper zone and adjacent the return plenum. A recirculating airflow path can provide fluid communication from the return plenum to the fan and back to the heat plenum. The burner is positioned outside the airflow path to feed ambient air into the recirculating airflow path, without recirculating airflow passing through the burner.

Abstract: A rotatable grain tower mounted on a stationary base. The base includes an opening for the removal of grain from a grain plenum in the tower. As the tower is rotated, a metering device adjacent the opening meters the rate of grain exiting the plenum. The rotating tower alleviates uneven drying due to sun, wind and other conditions to more evenly dry grain in the plenum. A cleaning device may be positioned adjacent the tower to clean the plenum as the tower rotates, thereby eliminating catwalks and other expensive equipment and devices used for cleaning stationary towers.

Abstract: The invention provides a dryer for drying particulate material, comprising at least one substantially vertical elongate container having: an upper inlet for receiving a charge of moisture containing particulate material; a lower outlet for discharging dried particulate material, whereby the particulate material travels under the influence of gravity from the inlet to the outlet; at least one substantially vertical gas permeable wall through which a drying gas can pass to contact the particulate material; the dryer also comprising at least one plenum on an exterior surface of the at least one gas permeable wall, covering ingress and egress openings within the at least one gas permeable wall.

Abstract: The inner space of a drying tank 4 is made up of a mixing and drying zone MZ to mix and dry supplied material 3 by swirling the material 3 upward onto rotor blades 5 and pressing the material centrifugally against a heated cylindrical inner surface of the tank wall 2, and a drying zone DZ beneath the mixing and drying zone MZ. An upper screw conveyer 15, connected to the upper part of the mixing and drying zone MZ transfers material 3 out of the drying tank 4. A lower screw conveyer 13, connected to the bottom of the mixing and drying zone MZ transfers material received from the upper conveyor 15 through a vertical transfer pipe 17 back into the drying tank 4 along with new material to be dried. A discharge screw conveyer 21 is connected to the drying zone DZ to discharge out dried material continuously.

Abstract: A method for dehumidifying and drying resin pellets that can efficiently dry both non-crystallized resin pellets and crystallized resin pellets, the apparatus being adapted to downsizing. A control means 67 adapts to operate in a first drying mode of controlling the heating operation of the first heating member 25 for heating longitudinally divided regions of the first cylinder 5 section to produce differentiated respective heating effects and that of the second heating member 31 for uniformly heating the second cylinder 7 section so as to crystallize the supplied non-crystallized resin pellets NCRP and subsequently drying them and in a second drying mode of controlling the heating operation of the first heating member 25 and that of the second heating member 31 for uniformly heating the first and second cylinder 5,7 sections so as to drying the supplied crystallized resin pellets CRP.

Abstract: The invention relates to a spray-drying device (1) having a vertical drying chamber (2), material-atomization means (4) and drying-gas feed (6) means. Filter elements (11) are present in order to filter the fine particles out of the flow of drying gas (7). The fine particles are periodically removed from the filter elements (11) and collected in fine-particle collection means (10) in such a manner that they remain separate from the main flow of spray-dried material. In this way, it is possible to successfully control the properties of the spray-dried (main) material without it being undesirably influenced by the fine particles.

Abstract: A two-deck apparatus, one deck above the other, is provided for enabling drying of approximately twice as much material with very little increase in heat used to dry the material, when compared to a single deck dryer. The fan usually provided with dryers of this type requires only a small incremental size increase over prior art. The second or upper deck, in operation, experiences a greater pressure below that deck than the pressure above the deck. Solid material flows into the top of the apparatus from above, and then from the upper deck to the lower deck through what is essentially a one-way valve, with air flow moving from below the lower deck through the upper deck, without impeding the material flow downwardly in the apparatus. The same apparatus, but with the use of cold air to cool the product, rather than hot air to heat and dry a product, is also within the teachings of the present invention.

Abstract: A method and an apparatus for reducing the moisture content bound by capillary action in fiber cells. To include fine material economically and easily in the process, coarse material is sandwiched on top of fine material and then pressed and dried. The material prepared by grinding and screening is transferred as coarse material to a first spreader hopper, and the screened fine material is transferred over a chute and conveyor belt to a second spreader hopper. The fine material is spread in a thin layer through a vertically adjustable gate from the second spreader hopper onto a spreading, loading and filtering belt, and the coarse material is withdrawn on a transfer conveyor belt running below the first spreader hopper and then is spread through a vertically adjustable gate onto the fine layer, to form a sandwich-like mat.

Abstract: An apparatus for controlling grain flow within a column of a grain dryer is disclosed. The grain dryer includes a metering roll positioned to contact grain advancing out of a discharge opening of the column. The grain dryer further includes a regulator member which is movable between a flow regulating position and a trash escape position. The regulator member contacts either the metering roll, or grain supported by the metering roll when the regulator member is positioned in the flow regulating position. The regulator member is spaced from the metering roll by a distance sufficient to enable a trash object to advance between the regulator member and the metering roll when the regulator is positioned in the trash escape position. A method of controlling grain flow within a column of a grain dryer is also disclosed.

Abstract: A spreader apparatus (10) designed to evenly spread pellets or the like across an inlet deck (20) of a dryer or cooler is provided which includes a plurality of elongated, telescoping, pivotally supported delivery tubes (12) arranged in side-by-side relationship to form an array (14) extending across the deck (20). A drive assembly (16) is coupled with the tube array (14) so as to sequentially move the array (14) fore and aft to spread product thereon. A distributor (18, 152) is positioned above the array (14) in order to deliver product thereto. The distributor (18) includes a stationary, annular, multiple-pocket tray (76) as well as a spout (98) mounted for 360° rotation about an upright axis. As the spout (98) rotates, successive quantities of product are delivered to each pocket (84) of the tray (76). A ducting assembly (86) is provided between the tray (76) and the upper ends of the tubes (12).

Abstract: The grain dryer of the present invention has upper and lower heat plenums, with first and second grain conduits, with each conduit having an upper section and a lower section, and a central crossover section between the upper and lower sections. The upper section of each conduit is on one side of the upper heat plenum, while the lower section of each conduit is on the opposite side of the lower heat plenum. The crossover sections of each conduit extend the respective conduits from one side of the upper heat plenum to the opposite side of the lower heat plenum.

Abstract: Free-flowing solid particles are dried in a moving bed dryer by passing the particles adjacent to a heat exchanger plate containing a heated fluid while passing a dehumidified gas into the solid particles from a gas flow manifold in the heat exchanger plate.

Abstract: An apparatus for the drying of particulate material in superheated steam in a closed vessel (1) has a number of upwardly open, elongated and substantially vertical processing cells (2) which are placed around a central part with a heat exchanger (3). The last of these processing cells (2) has a closed bottom and is the discharge cell (4), while the remainder (2) have bottoms (5) through which steam can permeate. The processing cells (2), which lie at the side of one another, stand in mutual connection through openings (11) at the lowermost ends of the cells, so that the particulate material which is dried by the superheated steam which is blown up from the heat exchanger (3) through the steam-permeable bottoms (5) can pass from one processing cell (2) to the next through the openings (11). The discharge cell (4) and/or the last of the processing cells (2) are provided with one or more substantially vertical plates for restraining and/or controlling the flow of particulate material.

Abstract: A method and apparatus for drying grain in which a plurality of conveyors are mounted one above the other. The discharge end of one conveyor feeds the input end of the next lower conveyor. The conveyors have a porous top surface and are vibrated to move the grain. Warm air is conveyed beneath the top conveyor and every other conveyor thereafter. Cool air is conveyed beneath the conveyor beneath the top conveyor and every other conveyor thereafter. The warm and cool air passes through the porous top surfaces of the conveyors. Thus the conveyors alternately heat and cool the grain to remove moisture to the desired level. The apparatus can be free standing or mounted as part of a combine or harvester.

Abstract: This invention is a new, energy efficient, environmentally clean grain drying system which consists of two main parts: a hot drying air generator and a modular, portable drying bin. One novel aspect of the air generator is the introduction of a heat pipe design which enhances the efficiency of a dehumidifier heat pump, making its use economically feasible, especially for humid climates. Another novel aspect is the use of advanced burners incorporating antipollution devices. The hot air generator can operate on many sources of energy such as electricity; gasoline; diesel; biomass such as wood, charcoal, or rice husks; or even solar energy. The modular bin is made of several modules which can be disassembled, transported, and reassembled with great ease. The bin design also creates a very low air pressure drop, allowing substantial savings on blower energy. The complete system will offer great benefits for developing countries that are producers of rice, especially for those with humid climates.

Abstract: An apparatus for controlling grain flow within a column of a grain dryer is disclosed. The grain dryer includes a metering roll positioned to contact grain advancing out of a discharge opening of the column. The grain dryer further includes a regulator member which is movable between a flow regulating position and a trash escape position. The regulator member contacts either the metering roll, or grain supported by the metering roll when the regulator member is positioned in the flow regulating position. The regulator member is spaced from the metering roll by a distance sufficient to enable a trash object to advance between the regulator member and the metering roll when the regulator is positioned in the trash escape position. A method of controlling grain flow within a column of a grain dryer is also disclosed.

Abstract: A grain dryer has three levels of modulated air chambers; a multi-perforated chamber holding grains which surround all three levels of the modulated air chambers; an intermediate air passage; partition walls and a set of central fans to direct airflow cross-upwardly in an S-shape inside the grain dryer; and an external chamber to exhaust air out to the ambient, minimizing heat loss, and thereby increasing the effiency of moisture exhange between grains and air.

Abstract: Method and apparatus for the removal of liquid from particulate material by evaporation through the supply of heat, said heat being transferred substantially by superheated vapours or steam of the liquids existing in the particulate material, and where said method is executed in a substantially closed system. The particulate material is supplied continuously to a process chamber which is configured as an annual or partly annular chamber (1) which lies in a substantially horizontal manner, where the superheated vapours are introduced from below and up through openings (11) in a bottom (10) in the annular chamber, so that the particulate material is brought into movement by the superheated vapours, and such that a transport of the particulate material takes place through the annular chamber (1).

Abstract: A heat treatment furnace and conveyor with multi-conveyance, wherein the top of the furnace has a feeder and the bottom of which has a disposal. The inside of the furnace has a number of conveying units, each unit is in circular status lined up and move with the feeder at the top of the first pallet, and the end of each pallet is connected to the beginning of the next pallet, and the end of the last pallet is connected to the disposal. This reduces the width of the furnace and extend the length of conveying which enhances the heat treatment processing time. The furnace is also divided into several sections, as a heating section and a cooling section. The heating section is equipped with electric heating elements while the cooling section is not. The pallet belt is in a flat surface with some ribs to prevent objects from sticking or sliding off.

Abstract: A method and apparatus for drying grain which includes a method and apparatus for unloading the grain from a grain dryer of a type including spaced apart first and second walls for defining a passageway or grain column for directing grain flowing downwardly by gravity between the first and second walls. A substantially horizontal shelf is disposed below the outlet port of the grain confinement walls for receiving grain thereon from the grain column. A channel is disposed below the shelf for receiving grain which is pushed off of the shelf. A discharge port is disposed in the channel. A strip of material is disposed for moving along above the shelf for metering grain from the shelf to the channel as the strip moves along the shelf. A paddle is disposed for movement in the channel for pushing grain from the channel into the discharge port. The dryer also has a central air passage from top to bottom, which lends itself to being used for three mode drying, if desired.

Abstract: Apparatus for the drying of particulate material in superheated steam in a closed vessel (1). The vessel consists of a number of upwardly open, elongated and substantially vertical processing cells (2) which are placed around a central part with a heat exchanger (3). The last of these processing cells (2) has a closed bottom and is the discharge cell (4), while the remainder (2) have bottoms (5) through which steam can permeate. The processing cells (2), which lie at the side of one another, stand in mutual connection through openings (11) at the lowermost ends of the cells, so that the particulate material which is dried by the superheated steam which is blown up from the heat exchanger (3) through the steam-permeable bottoms (5) can pass from one processing cell (2) to the next through said openings (11).

Abstract: An apparatus and method for controlling grain flow within a column of a grain dryer is disclosed. The grain dryer includes a metering roll positioned to contact grain advancing out of a discharge opening of the column. The grain dryer further includes a regulator member which is movable between a flow regulating position and a trash escape position. The regulator member contacts either the metering roll, or grain supported by the metering roll when the regulator member is positioned in the flow regulating position. The regulator member is spaced from the metering roll by a distance sufficient to enable a trash object to advance between the regulator member and the metering roll when the regulator is positioned in the trash escape position. A method of controlling grain flow within a column of a grain dryer is also disclosed.

Abstract: A grain dryer which includes a grain column through which grain may flow is disclosed. The grain column has a discharge opening. The grain dryer further includes a metering roll positioned to contact grain advancing out of the discharge opening of the grain column and a grain support member interposed between the metering roll and the discharge opening. The grain support member being movable between a grain support position and a cleaning position. The grain dryer yet further includes a transport bin positioned below the metering roll. The grain support member directs grain flowing out of the discharge opening to the metering roll when the grain support member is positioned in the grain support position. The grain support member directs grain positioned on the grain support member to advance under the metering roll and into the transport bin when the grain support member is positioned in the cleaning position.

Abstract: A grain dryer which includes a grain column through which grain may flow is disclosed. The grain column includes a left lateral discharge sidewall, a right lateral discharge sidewall, a lower discharge surface and an upper discharge surface which collectively define a discharge opening. The lower discharge surface is spaced apart from the upper discharge surface by a distance equal to D1. The distance D1 is greater to or equal to 5.0 inches. The grain dryer further includes a metering roll positioned to contact grain advancing out of the discharge opening of the grain column. The metering roll has a vane diameter equal to VD. The vane diameter VD is greater to or equal to 6.0 inches.

Abstract: A grain turner (101)of the present invention is adapted for use with a grain dryer having an inner dryer wall (7) and an outer dryer wall (9) spaced therefrom and defining a vertically extending grain path (11) therebetween. A grain turner (101) of the present invention is disposed within the grain path for exchanging (turning) grain from the inner portion of the grain path to the outer portion of the grain path and vice versa and for exchanging grain widthwise within the grain path. The grain turner comprises a vertical wall (109) disposed between the inner and outer dryer walls. The grain turner further has at least one pair inclined plates (119, 125) with one of the plates (119) being on the inside of the vertical wall and with the other of the inclined plates (125) being on the outside of the vertical wall. Plate (119) is inclined downwardly in a first widthwise direction and the other of the inclined plates is inclined downwardly in the opposite widthwise direction.

Abstract: A grain dryer has a horizontal plenum connected to a source of heated forced air and has at least one generally perforated wall. A substantially enclosed grain conduit extends along the plenum and has one of its sidewalls being the perforated wall of the plenum. The grain conduit has upper and lower ends to receive and discharge, respectively, a quantity of grain to be dried by heat conveyed to the grain through the perforated wall of the plenum. The lower end of the grain conduit defines an opening generally dwelling in a substantially vertical plane and having upper and lower discharge ports, separated by a plate extending across the central portion thereof to close the flow of grain therethrough.

Abstract: There is provided an improved centrifugal dryer that includes a motor section or portion, a dryer section or portion disposed therebelow, and a reservoir section or portion disposed below the dryer portion, the dryer portion being hingedly attached to the reservoir portion. A product slurry is introduced into the dryer portion through a center inlet pipe and flows into the dryer section where the product is dried by forcing the fluid in the slurry through apertures in a perforated screen held in position between upper and lower screen positioning plates.

Abstract: A metering unloader (101) for unloading a fluent material from a flow path (11) is disclosed. The flow path has a fluent material outlet (27). The metering unloader comprises an unloader body (103) having an outer cylindric wall (105) and an inner cylindric wall (107) spaced radially inwardly from the outer wall with the walls defining a chamber (126) therebetween. Means (117) is provided for rotating the unloader body about a vertical axis. Outer wall (105) has a fluent material inlet opening (119) such that with the fluent material inlet opening (119) in register with the flow path fluent material outlet (27), the fluent material will flow by gravity through the fluent material inlet opening (119) in the outer wall into the chamber (126). The inner wall (107) has a fluent material outlet opening (127) therein such that the fluent material in the chamber (126) will flow by gravity from the chamber to a fluent material discharge outlet (15).

Abstract: Apparatus and a method for de-watering a bead suspension of fragile beads having a high water content suspended in a liquid includes a staging vat, a metering vat, and a de-watering vat. The application of pressurized gas to the staging vat causes the bead suspension to move up a central feed tube which extends from the staging vat to the metering vat. The bead suspension is gravity fed from the metering vat through a transfer pipe and into the de-watering vat. The bottom portion of the de-watering vat has both an inner wall and an outer wall wherein the upper portion of the inner wall has perforations and the bottom portion is solid. Upon entering the de-watering vat, the bead suspension pours a short distance onto an inverted spreader cone. The bead suspension flows down the spreader cone and pours over the edge of the cone toward the perforated upper portion of the inner wall.

Abstract: A counter flow cooler in which feed material is fed into the top inlet of the cooler and dispersed into a plurality of cooling chambers. At the bottom of each cooling chamber is a discharge grid which will discharge feed material uniformly over the area of the cooling chamber. The discharge rate of this discharge grid can be adjusted to the desired throughput of the cooler. Air is drawn through the bottom of the discharge grid and passes up through the feed material in a counter flow manner. That is, while the product is passing down through the cooler, the air is passing up through the feed material, carrying away heat and possibly. A feed controller is used to selectively direct feed material into the plurality of cooling chambers. When a second batch of feed material is to be introduced into the cooler, feed material to the first cooling chamber is stopped and all the feed material is directed into the second cooling chamber.

Abstract: The invention relates to a particulate conveying apparatus for evenly drying particulate material. The apparatus comprises a plurality of spatially separate, essentially parallel, vertically oriented proportioning plates, disposed between a first end and a discharge end of the conveying apparatus for flow of particulate material therebetween. An endless conveyor is positioned proximate to and below the bottom edge of the proportioning plates for receiving of particulate material flowing between the plates from the first end to the discharge end of the conveying apparatus. The plates each have side edges that vary a preset distance from one side edge to an opposing side edge of the plate.

Abstract: A centrifugal pellet dryer is provided which has a housing, a generally cylindrical mesh member vertically disposed within the housing and a rotor that is coaxial with the mesh member. The rotor has lifters which tend to move a slurry of pellets and water upwardly and outwardly relative to the cylindrical mesh member so that water moving radially through the mesh member is separated from the pellets which are retained by the mesh member. The rotor has a hollow interior portion that communicates with the bottom of the rotor so that the slurry of pellets of water are introduced into the dryer through the hollow interior of the rotating rotor. The slurry of pellets and water is distributed uniformly about the periphery of the mesh member by the rotating rotor and the rotation of the rotor enhances the centrifugal force of the slurry to initially dewater the slurry more effectively as the water moves radially outwardly through the mesh member.