US2732630A - Markowich - Google Patents
Markowich Download PDFInfo
- Publication number
- US2732630A US2732630A US2732630DA US2732630A US 2732630 A US2732630 A US 2732630A US 2732630D A US2732630D A US 2732630DA US 2732630 A US2732630 A US 2732630A
- Authority
- US
- United States
- Prior art keywords
- grain
- outer casing
- channels
- air
- end walls
- 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 - Lifetime
Links
- 238000001035 drying Methods 0.000 description 8
- 238000010276 construction Methods 0.000 description 4
- 229920002456 HOTAIR Polymers 0.000 description 2
- 210000002370 ICC Anatomy 0.000 description 2
- 230000001276 controlling effect Effects 0.000 description 2
- 230000000875 corresponding Effects 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000006011 modification reaction Methods 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
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
Definitions
- My invention relates to new and useful improvements in grain drying devices, an object of my invention being to provide a device of the character herewithin described whereby grain can be passed through the device continuously and dried during its passage therethrough.
- a further object of my invention is to provide a device of the character herewithin described whereby the speed of grain passing through the device can be controlled accurately thereby enabling the amount of moisture being removed from the grain, to be controlled.
- Still another object of my invention is to provide a device of the character herewithin described wherein the warm air used in drying passes to the centre of the device and then outwardly through the grain mass to be collected in an exhaust manifold, both the exhaust manifold and the intake being provided with separate air moving devices thereby ensuring continuous ilow of air through the machine.
- Yet another object of my invention is to provide a device of the character herewithin described which has been designed specifically for farm use and is extremely simple in construction, economical in operation, and otherwise Well suited to the purpose for which it is designed.
- Figure l is a side sectional elevation of my device.
- Figure 2 is a horizontal section of my device substantially along the lines 2 2 of Figure l.
- a rectangular inner casing 5 Situated within the outer casing 1 is a rectangular inner casing 5 and it will be seen from a perusal of Figure 2 that this inner casing comprises a pair of end walls 6 parallel with the end walls 7 of the outer casing, and a front wall 8 parallel with and spaced from the front wall 9 of the outer casing.
- the rear wall 10 of the outer casing is common to both casings.
- the end walls 6 are perforated as at 11 and ICC that they extend from the platform 2 to the roof 3 of the outer casing being joined thereto as indicated at 12.
- the areas 17 bounded by the partitions 13 and the end walls 6 of the inner casing form what I definedY as Vertical grain channels upon each side of the column 16 and these vertical channels are open at the upper ends thereof and communicate with the interior of the roof 3 of the outer casing.
- the areas 18 between the end walls 6 of the inner casing, the end wa1ls7 of the outer casing, and the front walls 8 and 9 of the casings form a communicating passageway which acts as an air exhaust manifold and bears the reference character 18.
- An air intake duct 19 extends from the exterior of the device inwardly through the outer casing to the aforementioned air distributor column 16 and is provided with a fan 20 and means to heat the air passing therethrough (not illustrated). Also associated with the air heating means are suitable control valves of a conventional nature (also not illustrated).
- An air exhaust duct 21 having a fan 22 therein communicates with the aforementioned manifold 18 and discharges air therefrom to the atmosphere.
- the aforementioned grain intake duct 4 diverges into the two ducts 4 and 4 so that grain passing therethrough can be directed into each of the grain channels 17 and a control ilap 23 enables the operator to control the quantity of grain flowing to either channel.
- Grain discharge means collectively designated 25 are provided at the base of each of the grain channels 17, said means including a pair of rollers 26 mounted for rotation Within the base of the channels, said rollers being parallel and provided with spiral striations 27 to facilitate the movement of grain thereby.
- Means are provided to rotate said rollers in the direction of arrows 28 but as said means are conventional they have not been illustrated in the drawings.
- a longitudinally extending shroud 29 is situated above each pair of rollers 26, said shroud being of an inverted V configuration when viewed in section. These shrouds direct the grain passing downwardly within the channels 17, through the outside portions 30 of the said rollers and ensure that the grain exits from the channels adjacent the partitions 13 and the end walls 6 into collecting chutes 11 situated therebelow.
- Means to control the volume of grain passed by the rollers is provided and takes the form of aps 32 hingedly depending from the lower edges of the partition 13 and the end wall 6.
- Conventional screw threaded rods 33 engageable within brackets 34 provide means whereby the position of the iaps from the vertical may be controlled thereby controlling the gap between the fiaps and the perimeter of the rollers so that the speed at which the grain is discharged can be controlled. In other words the speed with which the grain passes through my dryer is controlled solely by these aps 32 in conjunction with the rollers 26.
- grain is fed through the duct i and passes downwardly through the vertical grain channels l? at a speed determined by the percentage moisture therewithin.
- Hot air is passed through duct 24 and into the central air distributor column 16 whereupon it passes through the grain within the channels l? and is thence exhausted as hereinbefore described.
- a device for removing moisture from grain or the like comprising in combination a substantially rectangular, vertical outer casing, an inner casing spaced from three of the walls of said outer casing the fourth wall of said outer casing being common to both casings, and a pair of vertical perforate partitions within said inner casing and parallel with the end walls thereof, said partitions constituting a central air distributor column being closed at both ends thereof, said partitions and said end Walls constituting vertical grain channels on each side of said column, said end walls also being perforate, said end walls and the end walls of said outer casing constituting an air discharge manifold, an air intake duct communicating with the interior of said column, and an air exhaust duct communicating with the interior of said manifold, grain intake means situated at the upper end of said outer casing, and grain discharge means Situated at the base of each of said grain channels, and means associated with the bases of said channels to control the volume of grain discharging therefrom, said grain intake means comprising a substantially vertical duct extending through the upper side of said outer casing and substantially
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Drying Of Solid Materials (AREA)
Description
Jan. 3l, v 1956 A. MARKOWICH GRAIN DRYER Filed May 27, 1955 miss: EL 2 United States Patent() GRAIN DRYER Andrew Markowich, Clairmont, Alberta, Canada Application May 27, 1953, Serial No. 357,857 1 Claim. (Cl. 34-174) My invention relates to new and useful improvements in grain drying devices, an object of my invention being to provide a device of the character herewithin described whereby grain can be passed through the device continuously and dried during its passage therethrough.
A further object of my invention is to provide a device of the character herewithin described whereby the speed of grain passing through the device can be controlled accurately thereby enabling the amount of moisture being removed from the grain, to be controlled.
Still another object of my invention is to provide a device of the character herewithin described wherein the warm air used in drying passes to the centre of the device and then outwardly through the grain mass to be collected in an exhaust manifold, both the exhaust manifold and the intake being provided with separate air moving devices thereby ensuring continuous ilow of air through the machine.
Yet another object of my invention is to provide a device of the character herewithin described which has been designed specifically for farm use and is extremely simple in construction, economical in operation, and otherwise Well suited to the purpose for which it is designed.
With the foregoing objects in view, and such other objects and advantages as will become apparent to those skilled in the art to which this invention relates as this speciiication proceeds, my invention consists essentially in the arrangement and construction of parts all as hereinafter more particularly described, reference being had to the accompanying drawings in which:
Figure l is a side sectional elevation of my device.
Figure 2 is a horizontal section of my device substantially along the lines 2 2 of Figure l.
In the drawings like characters of reference indicate corresponding parts in the diiferent figures.
Due to the relatively high cost of conventional commercial grain drying apparatus, it is normally not possible for the average farmer to possess equipment for the drying of grain. Consequently I have designed a grain dryer of high efliciency yet relatively low cost and which furthermore operates extremely economically. This dryer, hereinafter to be described, is particularly suitable for individual farmers as well as for elevator operators and the like.
Proceeding now to describe my invention in detail, it will be seen from the accompanying drawings that I have provided a substantially rectangular outer casing 1 supported upon a platform 2. This outer casing is provided with a conical roof 3 through the apex of which extends a grain intake conduit 4.
Situated within the outer casing 1 is a rectangular inner casing 5 and it will be seen from a perusal of Figure 2 that this inner casing comprises a pair of end walls 6 parallel with the end walls 7 of the outer casing, and a front wall 8 parallel with and spaced from the front wall 9 of the outer casing. In other words, the rear wall 10 of the outer casing is common to both casings. It will also be observed that the end walls 6 are perforated as at 11 and ICC that they extend from the platform 2 to the roof 3 of the outer casing being joined thereto as indicated at 12.
Within this inner casing I have provided a pair of vertical partitions 13 also perforated as at 14 and situated parallel to the end walls 6 and extending between the rear wall 10 and the front wall 5. These partitions do not extend upwardly the full height of the outer casing but terminate in an inverted V cap 15 which thus seals off the space 16 between the partitions. These partitions together with the cap 15 constitute what I dene as a central air distributor column bearing the reference character 16 and having perforated walls as hereinbefore described.
The areas 17 bounded by the partitions 13 and the end walls 6 of the inner casing form what I definedY as Vertical grain channels upon each side of the column 16 and these vertical channels are open at the upper ends thereof and communicate with the interior of the roof 3 of the outer casing. The areas 18 between the end walls 6 of the inner casing, the end wa1ls7 of the outer casing, and the front walls 8 and 9 of the casings form a communicating passageway which acts as an air exhaust manifold and bears the reference character 18.
An air intake duct 19 extends from the exterior of the device inwardly through the outer casing to the aforementioned air distributor column 16 and is provided with a fan 20 and means to heat the air passing therethrough (not illustrated). Also associated with the air heating means are suitable control valves of a conventional nature (also not illustrated).
An air exhaust duct 21 having a fan 22 therein communicates with the aforementioned manifold 18 and discharges air therefrom to the atmosphere.
The aforementioned grain intake duct 4 diverges into the two ducts 4 and 4 so that grain passing therethrough can be directed into each of the grain channels 17 and a control ilap 23 enables the operator to control the quantity of grain flowing to either channel.
From the foregoing it will be appreciated that grain can flow downwardly into the channels 17 and that warmed air enters the central column 16 in the direction of arrows 24 whereupon the air passes through the perforations 14, through the grain contained in the grain channels 17 and thence through the perforations 11 into the air exhaust manifold 18 whereupon it is exhausted through the duct 21 to the atmosphere carrying with it moisture picked up from the grain within the channels.
Grain discharge means collectively designated 25 are provided at the base of each of the grain channels 17, said means including a pair of rollers 26 mounted for rotation Within the base of the channels, said rollers being parallel and provided with spiral striations 27 to facilitate the movement of grain thereby. Means are provided to rotate said rollers in the direction of arrows 28 but as said means are conventional they have not been illustrated in the drawings.
A longitudinally extending shroud 29 is situated above each pair of rollers 26, said shroud being of an inverted V configuration when viewed in section. These shrouds direct the grain passing downwardly within the channels 17, through the outside portions 30 of the said rollers and ensure that the grain exits from the channels adjacent the partitions 13 and the end walls 6 into collecting chutes 11 situated therebelow.
Means to control the volume of grain passed by the rollers is provided and takes the form of aps 32 hingedly depending from the lower edges of the partition 13 and the end wall 6. Conventional screw threaded rods 33 engageable within brackets 34 provide means whereby the position of the iaps from the vertical may be controlled thereby controlling the gap between the fiaps and the perimeter of the rollers so that the speed at which the grain is discharged can be controlled. In other words the speed with which the grain passes through my dryer is controlled solely by these aps 32 in conjunction with the rollers 26.
In operation, grain is fed through the duct i and passe downwardly through the vertical grain channels l? at a speed determined by the percentage moisture therewithin. Hot air is passed through duct 24 and into the central air distributor column 16 whereupon it passes through the grain within the channels l? and is thence exhausted as hereinbefore described.
In conclusion Irwish to stress the ease with which my device is controlled to suit all conditions as both the speed of grain passing therethrough and also the volume and temperature there utilized may readily be controlled.
Since various modifications can be made in my invention as hereinabove described, and many apparently widely different embodiments of same made within the spirit and scope of the claim without departing from such spirit and scope, it is intended that all matter contained in the accompanying specification shall be interpreted as illustrative only and not in a limiting sense.
What I claim as my invention is:
A device for removing moisture from grain or the like comprising in combination a substantially rectangular, vertical outer casing, an inner casing spaced from three of the walls of said outer casing the fourth wall of said outer casing being common to both casings, and a pair of vertical perforate partitions within said inner casing and parallel with the end walls thereof, said partitions constituting a central air distributor column being closed at both ends thereof, said partitions and said end Walls constituting vertical grain channels on each side of said column, said end walls also being perforate, said end walls and the end walls of said outer casing constituting an air discharge manifold, an air intake duct communicating with the interior of said column, and an air exhaust duct communicating with the interior of said manifold, grain intake means situated at the upper end of said outer casing, and grain discharge means Situated at the base of each of said grain channels, and means associated with the bases of said channels to control the volume of grain discharging therefrom, said grain intake means comprising a substantially vertical duct extending through the upper side of said outer casing and substantially in the centre thereof, the lower end of said duct being of an inverted Y configuration, and baie means within said duct to control the direction of ow of grain therethrough.
References Cited in the tile of this patent UNITED STATES PATENTS 618,508 Hess Jan. 3l, i899 1,308,942 French July 8, 1919 1,482,812 Roberts Feb. 5, 1924 2,552,093 Gollbach et al May 8, 1951 2,660,809 Morrison Dec. l, 1953
Publications (1)
Publication Number | Publication Date |
---|---|
US2732630A true US2732630A (en) | 1956-01-31 |
Family
ID=3442288
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US2732630D Expired - Lifetime US2732630A (en) | Markowich |
Country Status (1)
Country | Link |
---|---|
US (1) | US2732630A (en) |
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3040443A (en) * | 1959-06-10 | 1962-06-26 | Deere & Co | Crop dryer |
US3092472A (en) * | 1959-11-23 | 1963-06-04 | Charles D Figley | Grain drier |
US3097934A (en) * | 1958-08-07 | 1963-07-16 | Robert D Applegate | Portable continuous drier |
US3107160A (en) * | 1960-05-31 | 1963-10-15 | Jay L Mcclaren | Grain dryer |
US3152873A (en) * | 1960-04-15 | 1964-10-13 | Gen Precision Inc | Grain drying |
US3238640A (en) * | 1962-09-04 | 1966-03-08 | Hart Carter Co | Grain dryer |
US3426442A (en) * | 1967-06-01 | 1969-02-11 | Toshihiko Satake | Drying apparatus for cereals |
US3514861A (en) * | 1968-05-09 | 1970-06-02 | Toshihiko Satake | Circulating-grain drying apparatus |
US3739493A (en) * | 1971-05-04 | 1973-06-19 | E Nivon | Grain drying apparatus |
US4149844A (en) * | 1977-09-08 | 1979-04-17 | Beard Industries, Inc. | Optimum continuous flow grain drying and conditioning method and apparatus |
US4249891A (en) * | 1978-09-14 | 1981-02-10 | Beard Industries, Inc. | Advanced optimum continuous crossflow grain drying and conditioning method and apparatus |
EP0068734A2 (en) * | 1981-06-19 | 1983-01-05 | Christianus Marinus Theresia Westelaken | Multi-stage particulate material dryer having channelized discharge |
US4398356A (en) * | 1981-06-19 | 1983-08-16 | Westelaken C | Multi-stage dryer for particulate material |
US4402302A (en) * | 1981-06-19 | 1983-09-06 | Westelaken C | Air heating apparatus |
CN107238272A (en) * | 2017-07-25 | 2017-10-10 | 陈群 | A kind of paddy delays the implementation method that drop formula is dried |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US618508A (en) * | 1899-01-31 | Apparatus for drying and cooling grain | ||
US1308942A (en) * | 1919-07-08 | Method of and apparatus for drying- stone or other material | ||
US1482812A (en) * | 1921-12-14 | 1924-02-05 | William E Roberts | Apparatus for drying divided materials |
US2552093A (en) * | 1946-06-28 | 1951-05-08 | H M Shanzer Co | Rotary discharge mechanism for driers |
US2660809A (en) * | 1951-06-23 | 1953-12-01 | Union Stock Yards & Transit Co | Apparatus for composting animal manure |
-
0
- US US2732630D patent/US2732630A/en not_active Expired - Lifetime
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US618508A (en) * | 1899-01-31 | Apparatus for drying and cooling grain | ||
US1308942A (en) * | 1919-07-08 | Method of and apparatus for drying- stone or other material | ||
US1482812A (en) * | 1921-12-14 | 1924-02-05 | William E Roberts | Apparatus for drying divided materials |
US2552093A (en) * | 1946-06-28 | 1951-05-08 | H M Shanzer Co | Rotary discharge mechanism for driers |
US2660809A (en) * | 1951-06-23 | 1953-12-01 | Union Stock Yards & Transit Co | Apparatus for composting animal manure |
Cited By (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3097934A (en) * | 1958-08-07 | 1963-07-16 | Robert D Applegate | Portable continuous drier |
US3040443A (en) * | 1959-06-10 | 1962-06-26 | Deere & Co | Crop dryer |
US3092472A (en) * | 1959-11-23 | 1963-06-04 | Charles D Figley | Grain drier |
US3152873A (en) * | 1960-04-15 | 1964-10-13 | Gen Precision Inc | Grain drying |
US3107160A (en) * | 1960-05-31 | 1963-10-15 | Jay L Mcclaren | Grain dryer |
US3238640A (en) * | 1962-09-04 | 1966-03-08 | Hart Carter Co | Grain dryer |
US3426442A (en) * | 1967-06-01 | 1969-02-11 | Toshihiko Satake | Drying apparatus for cereals |
US3514861A (en) * | 1968-05-09 | 1970-06-02 | Toshihiko Satake | Circulating-grain drying apparatus |
US3739493A (en) * | 1971-05-04 | 1973-06-19 | E Nivon | Grain drying apparatus |
US4149844A (en) * | 1977-09-08 | 1979-04-17 | Beard Industries, Inc. | Optimum continuous flow grain drying and conditioning method and apparatus |
US4249891A (en) * | 1978-09-14 | 1981-02-10 | Beard Industries, Inc. | Advanced optimum continuous crossflow grain drying and conditioning method and apparatus |
EP0068734A2 (en) * | 1981-06-19 | 1983-01-05 | Christianus Marinus Theresia Westelaken | Multi-stage particulate material dryer having channelized discharge |
US4398356A (en) * | 1981-06-19 | 1983-08-16 | Westelaken C | Multi-stage dryer for particulate material |
US4402302A (en) * | 1981-06-19 | 1983-09-06 | Westelaken C | Air heating apparatus |
EP0068734A3 (en) * | 1981-06-19 | 1984-09-12 | Christianus Marinus Theresia Westelaken | Multi-stage particulate material dryer having channelized discharge |
EP0206069A2 (en) * | 1981-06-19 | 1986-12-30 | Christianus Marinus Theresia Westelaken | Multi-stage particulate material dryer having channelized discharge |
EP0206069A3 (en) * | 1981-06-19 | 1987-02-25 | Christianus Marinus Theresia Westelaken | Multi-stage particulate material dryer having channelized discharge |
CN107238272A (en) * | 2017-07-25 | 2017-10-10 | 陈群 | A kind of paddy delays the implementation method that drop formula is dried |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2732630A (en) | Markowich | |
RU187214U1 (en) | Zernosushilka mine louvre | |
US4020561A (en) | Method and apparatus for drying grain | |
US2538888A (en) | Drier for lumber and the like | |
US3279094A (en) | Apparatus for controlling flow of gases | |
US1892319A (en) | Device for the conditioning and drying of cereals | |
US2415738A (en) | Endless conveyor drier structure | |
US2187799A (en) | Drier | |
US1966405A (en) | Drying machine | |
US2857684A (en) | Rotary cooler and dryer | |
DK2719983T3 (en) | Drying system for bulk material with an air inlet | |
US2610412A (en) | Plant for drying of solid materials | |
CN205843303U (en) | A kind of novel circulation-type foodstuff drying device complete machine device | |
US2921382A (en) | Shrimp preparing machine | |
SE508395C2 (en) | Drying at asphalt plant | |
US3303577A (en) | Air agitated laundry drier | |
US1496473A (en) | Grain drying and cooling apparatus | |
US3604126A (en) | Grain treatment apparatus | |
US1172575A (en) | Dehydrating apparatus. | |
US3553846A (en) | Grain dryer | |
US128707A (en) | Improvement in grain-driers | |
US2603882A (en) | Cooling system for industrial ovens of the conveyer type | |
US1054765A (en) | Dehydrating apparatus. | |
US2444406A (en) | Apparatus for drying and conditioning sulfate of ammonia and other granular and crystalline products | |
US1319605A (en) | morton |