GB2355058A - Dryer having rotary base and stationary cylindrical walls for drying coated small particles - Google Patents
Dryer having rotary base and stationary cylindrical walls for drying coated small particles Download PDFInfo
- Publication number
- GB2355058A GB2355058A GB9922698A GB9922698A GB2355058A GB 2355058 A GB2355058 A GB 2355058A GB 9922698 A GB9922698 A GB 9922698A GB 9922698 A GB9922698 A GB 9922698A GB 2355058 A GB2355058 A GB 2355058A
- Authority
- GB
- United Kingdom
- Prior art keywords
- dryer
- stator
- wall
- particles
- rotor
- 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.)
- Withdrawn
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B11/00—Machines or apparatus for drying solid materials or objects with movement which is non-progressive
- F26B11/12—Machines or apparatus for drying solid materials or objects with movement which is non-progressive in stationary drums or other mainly-closed receptacles with moving stirring devices
- F26B11/14—Machines or apparatus for drying solid materials or objects with movement which is non-progressive in stationary drums or other mainly-closed receptacles with moving stirring devices the stirring device moving in a horizontal or slightly-inclined plane
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Drying Of Solid Materials (AREA)
Abstract
A dryer for drying seed (16) and other small particles has a cylindrical stator (11) with a coaxial rotor (12) having a flat base (13) and outwardly-sloping sides (14). Seed (16) is thrown upwardly and outwardly as the rotor (12) rotates, climbing the sides (14) of the rotor (12) and the wall (15) of the stator (11) before falling back down onto the rotor (12). As the seed (16) falls, fluid (19) is sprayed onto the moving seed (16) from a central spray head (18). Drying of the sprayed seed (16) takes place <I>in situ</I> by passing air through apertures (107) in the walls (15) just above the upper edge of the rotor (12). The drying means preferably includes a circular stub (110) with a fishtail connector (108), a flange (109) connected to the outside of the wall (15), a vertical slot (107), and a strip (105, 106) directing the air into the chamber.
Description
2355058 Dryer This invention is concerned with a dryer, and relates more
specifically to apparatus for drying a flowable collection of a myriad of small objects, as typified by batches of a particulate material such as plant seeds.
In various different fields there is often a need in some way to treat material in the form of large quantities of small particles. One such particulate material is plant seeds - grains such as wheat or barley, or the seeds of linseed (flax) or oil-seed rape, f or example - and f or these the treatment might be the application of a fungicide or the provision or a coating of some sort. Indeed, coatings of a waterimpermeable but cold-breakable polymer are of value in allowing seed to be sown early in the warm Autumn of one year yet not germinate until the warmth of the Spring of the next (by when the ground is still not dry enough to drill seed). This is especially useful in northern Countries, with very cold winters, such as Canada, where it is desirable to sow early in Autumn, while the ground is still soft enough to drill, and yet not have the seed germinate until the Spring of the next year, when it is warm enough for the young plant to survive.
One advantageous way to effect this type of treatment is to use a rotary coating machine of the kind available under the Mark ROTOGARD (RTM) from J E Elsworth Ltd, of King's Lynn, England. In this class of machine the seed - or whatever the particulate matter is - is contained within a cylindrical, 2 drum-like, stator the bottom of which is a co-axial, cup-like rotor, having a flat base and outwardly- sloping sides, so that seed therein is thrown outwardly and upwardly as the rotor rotates (at about 300rpm), climbing up the inside of the rotor wall and eventually reaching the wall of the stator where, after travelling further up and round across that wall, it slows down to the point at which it falls back down into/onto the rotor, so forming a roughly tubular body of seed co-axial with the stator, and as it falls so the treatment fluid is sprayed laterally onto the inner surface of the tubular moving mass from a spray head located generally centrally and axially thereof.
When using such a rotary coating machine to spray-coat seed with some substance that will form on the seed a water- impermeable polymer coating (so as to allow the seed safely to overwinter in the ground without it germinating and then dying), the substance the polymer precursor - is commonly sprayed on as a solution or slurry, typically an aqueous one containing around 50wt% polymer solids, and all the solvent/water has to be evaporated off to get the treated seed "dry" enough for storage and then subsequent use. Of course, this drying of the seed can be done in any conventional drying machine, but it would be convenient if each batch of treated seed could be dried in situ within the rotary treatment machine rather than having to be extracted therefrom and then subjected to a further processing/drying stage in a different machine in a different place.
It is this drying of a particulate material in this case, seed - that the present invention is concerned with. In particular, the invention relates to a modified version of the rotary coating machine that 3 allows the treated particulate material (such as seed) to be dried in situ during or after the treatment. This can be advantageous not only to allow the preparation of dried particles after a single treatment but also to facilitate the preparation in a single machine of multi-layer- coated particles by a series of sequential coating treatment /drying stages.
More specifically, then, the invention is a modified rotary treatment machine having means on or in the stator wall - and most conveniently the means is a simple aperture, most preferably formed as a vertical slot, in the stator wall - just above the upper edge of the rotor and through which in operation hot, and preferably dry, air can be blown into the alreadytreated/coated seed as it travels past, so speeding up the evaporation of the treatment solvent/water and thus improving the drying of the seed.
In one aspect, therefore, the invention provides a dryer based on a particulate-matter rotary treatment machine of the type having a cylindrical, drum-like, stator within which in operation the batch of matter particles is contained, within the bottom of which stator is a cuplike rotor, having a flat base and outwardly-sloping si ' des, so that in operation particles therein are thrown outwardly and upwardly as the rotor rotates, eventually reaching the wall of the stator where, after travelling up and round across the wall, they fall back down into/onto the rotor, the machine including treatment-fluid spray means having a statoraxially-located spray head central thereof from which treatment fluid can be sprayed laterally onto the moving mass of particles, 4 and wherein there is means, on or in the stator wall adjacent the edge of the rotor, through which in operation drying air can be blown into the mass of particles as they travel past.
The dryer of the invention can be utilised to dry any sort of particulate matter that has just been spray treated therein, and while its primary use is envisaged as drying seeds (such as grains like wheat or barley, or oil-producing seeds such as rape and flax, or even larger ones such as palm nuts) nevertheless it can also be employed for treating and then drying a myriad of other particulate materials. Examples of such treatment include: pelleting seed (either to provide a biologically active or useful coating or simply to make them "bigger" so as to increase their ease of handling), as is done, say, to sugar beet seed; treating pelleted animal feed products to provide them with a vitamin coating; treating particles, or small items, of food for humans with spices, colouring, flavouring and the like (coating peanuts with salt and sugar, and breadcrumbs with colour); giving granules of plastics a layer of pigment or dye; and coating ceramic powders with slippery, "parting" agents to assist removal from the mould of some object moulded therefrom without it being damaged.
While the rotary treatment machine is most conveniently one of the aforementioned ROTOGARD (RTM) machines, nevertheless it can be any machine having a drum-like stator at the bottom of which is a cup-like rotor. Typical rotor speeds are around 300rpm, although the smaller machines run a little faster than that.
In the rotary treatment machine some treatment fluid is sprayed onto the moving mass of particles from a spray head located within the stator and generally centrally of the tube-like body of particles (the spray is preferably disk-like, the treatment liquid being projected radially outwards in all 3600 at once into the surrounding body of particles). The treatment, and thus the nature of the fluid, can be of any appropriate sort.
The invention is a modification of the rotary treatment machine by adding the improvement of means on or in the stator wall adjacent the rotor edge - just above the upper edge of the rotor - through which in operation drying air can be blown into the mass of particles as they travel past. There may, of course, be more than one such means, but usually a single means is sufficient.
While the drying air input means might be a pipe leading down the stator wall to the appropriate point adjacent the upper edge of the rotor, the preferred form the means takes is as an aperture - and especially a vertical elongate but narrow (ie, slot-like) aperture created in the stator wall and through which the hot air can be blown from outside. For strengthening purposes the slot can if thought desirable have a central strut across it.
Typical dimensions for the stator used in the ROTOGARD rotary treatment machines are 15-100cm (6-40in) internal diameter, and with an internal height of about 50-70% of that diameter. For such machines typical dimensions for the air input means aperture slot are 20-40mm (and especially 30mm) wide and 200-400mm (especially 300mm) long.
On the outside of the stator wall the aperture most advantageously has connector means to which may be attached a pipe (or similar) to a source of hot air. In the case of a slotted aperture, this connector means is 6 preferably a fish-tail connector, which may be angled up or down, or left or right, as required to f it most appropriately with the other elements of the machine and its environment. Preferably the angle is such as to return to the inside of the stator any particles that come out through the slot - ie, the bottom of the fishtail is steeply down in the airflow direction.
In a part i cular ly-pref erred form of rotary treatment machine the stator wall has a spoiler, or baffle, to introduce a mild turbulence into the particle flow around the wall, and so promote better mixing, and an advantageous form of such a baffle is an axiallyparallel elongate "bump" along the wall inside surface and disposed normal to the particle movement direction. Such a bump can be formed by a flat blade conveniently about Sin (12.5cm) wide and set at an acute angle to the stator wall to give a gap about 2in (5cm) across, but is preferably a section of "angle iron" (but at a flatter angle, such as around 1200, rather than 900). The baffle bump may be made of any suitable material (such as stainless steel), and may be secured to the wall in any appropriate manner. Where it is such a blade or angle piece then it is very much preferred that the slot be located behind this, the baffle's "trailing" edge then standing free (about 10mm or so) from the wall, to form a gap, so that the input hot air can emanate therefrom into and with the flowing seed. In one preferred form of treatment machine the baffle is "hingedly" mounted on the stator wall by a flexible hinge running its entire length, and by pushing the baffle back and forth so the trailing edge baffle gap is adjustable, right down to it being closed completely. The gap's length is also most conveniently adjustable so 7 that even with the stator only partially full of particulate material the drying air can be injected in only where it actually passes into that material, and thus not wastefully above the filling line. This is conveniently achieved by providing the gap with an integral sliding cover that moves down to reduce the height of the gap. Alternatively, the baffle may be formed in sections, which can be opened and closed independently so as to adjust the gap to correspond to the height of the load of the particulate matter.
In use, air - pref erably both dry and hot - is blown into the particles as they travel past (dry air absorbs more moisture than damp, and hot air more than cold). Obviously the temperature of the air, and the rate at which it is blown in, depends on many circumstances, including the nature of the particulate material being dried, and in general the air should be as hot as possible, and blown in at as high a rate as possible, without causing any damage to the particulate material. For seed, a suitable air temperature is around 40'-50C (any hotter might sterilise the seed), and an appropriate rate is around 300 to 500, especially 400, cubic feet per minute (this is around 8,000-13,000, especially 11,000, litres a minute).
8 An embodiment of the invention is now described, though by way of illustration only, with reference to the accompanying diagrammatic Drawings in which:
Figure 1 shows a cut-away perspective view of the stator and rotor assembly of a rotary treatment machine of the sort to which the invention relates; Figure 2 shows a sectional view of a rotary treatment machine much like that of Figure 1; Figure 3 shows a perspective view of an improved rotary treatment machine of the invention, with drying capability; Figure 4 shows a perspective view of the fishtail connector used on the improved rotary treatment machine of Figure 3; and Figure 5 shows a partial view f rom above of the fishtail connector in position on the improved rotary treatment machine of Figure 3.
Figures 1 and 2 show part of a conventional rotary treatment machine of the sort to which the invention relates. The machine has a drum-like stator (11) at the bottom of which is a co-axial cup-like rotor (12) driven from below. The rotor 12 has a floor-like base 9 portion (13) and an angled side wall (14) just reaching the lower part of the inside surface of the stator wall (15). As can be seen, in operation treating a mass of seed (16) the rotor 12 spins so as to fling the seed 16 out and then up the sloping part 14 into contact with the stator wall 15, up which the seed 16 f lows before falling back down nearer the middle of the rotor's base 13.
Centrally of the stator 11, and extending thereinto generally co-axially from the top, is one or more pipe (as 17: there may be several such pipes, for different materials) carrying treatment fluid. The pipe 17 leads to a spinning-disc spray head (18); in operation its spinning causes treatment fluid (19) falling thereon to be flung out laterally towards the inner surface of the body of seeds as they fall back down onto the rotor base 13, so coating the seeds.
Figure 3 shows an improved rotary treatment machine of the invention, with drying capability, and Figures 4 and 5 show details of the fishtail connector used thereon, and how it is connected.
The general overall view of Figure 3 shows the stator drum (31) suitably mounted and associated with various control mechanisms (101), treatment fluid supply containers (102), and a particulate matter feed hopper (103); none of these are shown in detail. As best seen in Figure 5, the stator wall 15 has attached to it a baffle, or spoiler (104), in the form of a length of angle iron strip disposed parallel to the stator's axis (and thus across the line of motion of the seed). The strip is mounted to the wall by its leading edge (105), with its trailing edge (106) spaced slightly away from the inside wall surface to form a small gap. Aligned with (but shorter than) the baffle 104, a slot (107) is cut right through the stator wall, giving access from outside the stator to the inside thereof via the baffle and the gap along its spaced trailing edge 106.
On the outside of the stator wall 15, and aligned with, and covering, the slot 107, is a fishtail connector (generally 108: see also Figure 3). At the slot end this connector 108 is flanged (109) to allow it to be f ixed to the outside surface of the stator wall 15, and at the other end it is formed with a circular, tubular stub (110) onto which is in operation attached the pipe (not shown) bringing hot air from a source thereof (not shown). In this particular example the fishtail 108 is angled downwards and to the left (as viewed), to facilitate its connection to the hot air source.
The operation of the treatment and drying machine of Figure 3 will be self-evident. Seed 16 charged into the stator 11 is whirled around by the rotor 12, constantly moving both around and up and down as the machine operates. And as it does so, treatment fluid 19 is sprayed onto the inside surface of the mass of seeds (as they roll back down to the rotor). And either while this is actually happening or later, once the fluid treatment is finished, hot air is blown in through the slot 107 and out through the baffle gap into the seeds as they move past the trailing edge 106 of the baffle, warming them up, and speeding up the evaporation of the fluid treatment solvent/ carrier, and thus drying the seeds.
Claims (14)
- ClaimsA dryer, based on a part i cul ate -matter rotary treatment machine of the type having a cylindrical, drum-like, stator within which in operation the batch of matter particles is contained, within the bottom of which stator is a cup-like rotor, having a flat base and outwardly- sloping sides, so that in operation particles therein are thrown outwardly and upwardly as the rotor rotates, eventually reaching the wall of the stator where, after travelling up and round across the wall, they fall back down into/onto the rotor, the machine including treatment-fluid spray means having a statoraxially-located spray head central thereof from which treatment fluid can be sprayed laterally onto the moving mass of particles, and wherein there is means, on or in the stator wall adjacent the edge of the rotor, through which in operation drying air can be blown into the mass of particles as they travel past.
- 2. A dryer as claimed in Claim 1, wherein the rotor runs at 300rpm. or faster.
- 3. A dryer as claimed in either of the preceding Claims, wherein the spray head is disk-like, and in use sprays the treatment liquid radially outwards in all 3600 at once into the surrounding body of particles.
- 4. A dryer as claimed in any of the preceding Claims, wherein there is a single means through which in operation drying air is blown into the mass of particles.
- 5. A dryer as claimed in any of the preceding Claims, wherein the drying air input means is an aperture in the stator wall through which the hot air can be blown from outside.
- 6. A dryer as claimed in Claim 5, wherein the aperture is in the form of a vertical slot.
- 7. A dryer as claimed in Claim 6, wherein the slot has a central strut across it.
- 8. A dryer as claimed in any of Claims 5 to 7, wherein on the outside of the stator wall the aperture has connector means to which may be attached a pipe to a source of hot air.
- 9. A dryer as claimed in Claim 8, wherein the aperture is a slot, and the connector means is a fish-tail connector angled as required to fit with the other elements of the machine and its environment.
- 10. A dryer as claimed in Claim 9, wherein the f ishtail connector's angle is such as in use to return to the inside of the stator any particles that come out through the slot.
- 11. A dryer as claimed in any of the preceding Claims, wherein the stator wall has a spoiler, or baffle, to introduce turbulence into the particle flow around the wall, and so promote mixing.
- 12. A dryer as claimed in Claim 11, wherein the baffle is an axial lyparallel elongate bump along the wall inside surface and disposed normal to the particle movement direction, the bump being formed by a blade set at an angle to the stator wall to give a gap.
- 13. A dryer as claimed in Claim 12, wherein the slot is located behind the baffle blade, the blade's "trailing" edge then standing free from the wall to form a gap so that the input hot air can emanate therefrom into and with the flowing particles.i I i 14. A dryer as claimed in either of Claims 12 and 13, wherein the baffle blade is hingedly mounted on the stator wall by a flexible hinge running its entire length, whereby the gap may be adjustable by moving the blade.15. A dryer as claimed in Claim 14, wherein the gap's length is effectively adjustable, the baffle being formed in sections which can be opened and closed independently.16. A dryer as claimed in any of the preceding Claims and substantially as described hereinbefore.4 Amendments to the claims have been filed as follows 1. A dryer, based on a part i culate-matter rotary treatment machine of the type having a cylindrical, drum-like, stator within which in operation the batch of matter particles is contained, within the bottom of which stator is a cup-like rotor, having a flat base and outwardly-s loping sides, so that in operation particles therein are thrown outwardly and upwardly as the rotor rotates, eventually reaching the wall of the stator where, after travelling up and round across the wall, they fall back down into/onto the rotor, the machine including treatment-fluid spray means having a statoraxially-located spray head central thereof from which treatment fluid can be sprayed laterally onto the moving mass of particles, and wherein: there is means, on or in the stator wall adjacent the edge of the rotor, through which in operation drying air can be blown into the mass of particles as they travel past, and this means is an aperture slot in the stator wall through which the hot air can be blown from outside; and the stator wall has a spoiler, or baffle, to introduce turbulence into the particle flow around the wall, and so promote mixing.2. A dryer as claimed in Claim 1, wherein the rotor runs at 300rpm or faster. 3. A dryer as claimed in either of the preceding Claims, wherein the spray head is disk-like, and in use sprays the treatment liquid radially outwards in all 3600 at once into the surrounding body of particles.4. A dryer as claimed in any of the preceding Claims, wherein there is a single aperture slot. 5. A dryer as claimed in any of the preceding Claims, wherein the aperture slot is a vertical slot. 6. A dryer as claimed in any of the preceding Claims, wherein the slot has a central strut across it. 7. A dryer as claimed in any of the preceding Claims, wherein on the outside of the stator wall the aperture slot has connector means to which may be attached a pipe to a source of hot air. 8. A dryer as claimed in Claim 7, wherein the connector means is a fish-tail connector angled as required to fit with the other elements of the machine and its environment. 9. A dryer as claimed in Claim 8, wherein the f ishtail connector Is angle is such as in use to return to the inside of the stator any particles that come out through the slot. 10. A dryer as claimed in any of the preceding Claims, wherein the baf f le is an axially-parallel elongate bump along the wall inside surface and disposed normal to the particle movement direction, the bump being formed by a blade set at an angle to the stator wall to give a gap. 11. A dryer as claimed in Claim 10, wherein the aperture slot is located behind the baffle blade, the blade's "trailing" edge then standing free from the wall to form a gap so that the input hot air can emanate therefrom into and with the flowing particles. 12. A dryer as claimed in either of Claims 10 and 11, wherein the baffle blade is hingedly mounted on the stator wall by a flexible hinge running its entire length, whereby the gap may be adjustable by moving the blade. 13. A dryer as claimed in Claim 12, wherein the gap's length is effectively adjustable, the baffle being I G.formed in sections which can be opened and closed independently.
- 14. A dryer as claimed in any of the preceding Claims and substantially as described hereinbefore.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB9922698A GB2355058A (en) | 1999-09-25 | 1999-09-25 | Dryer having rotary base and stationary cylindrical walls for drying coated small particles |
PCT/GB2000/003674 WO2001023820A1 (en) | 1999-09-25 | 2000-09-25 | Dryer |
EP00962726A EP1214556A1 (en) | 1999-09-25 | 2000-09-25 | Dryer |
AU74370/00A AU7437000A (en) | 1999-09-25 | 2000-09-25 | Dryer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB9922698A GB2355058A (en) | 1999-09-25 | 1999-09-25 | Dryer having rotary base and stationary cylindrical walls for drying coated small particles |
Publications (2)
Publication Number | Publication Date |
---|---|
GB9922698D0 GB9922698D0 (en) | 1999-11-24 |
GB2355058A true GB2355058A (en) | 2001-04-11 |
Family
ID=10861590
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB9922698A Withdrawn GB2355058A (en) | 1999-09-25 | 1999-09-25 | Dryer having rotary base and stationary cylindrical walls for drying coated small particles |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP1214556A1 (en) |
AU (1) | AU7437000A (en) |
GB (1) | GB2355058A (en) |
WO (1) | WO2001023820A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1795842A1 (en) * | 2005-12-06 | 2007-06-13 | International Tobacco Machinery Poland Ltd | Apparatus for conditioning of organic materials |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9877424B2 (en) | 2010-12-08 | 2018-01-30 | Bayer Cropscience, Lp | Seed treatment facilities, methods and apparatus |
US9861027B2 (en) | 2010-12-08 | 2018-01-09 | Bayer Cropscience, Lp | Seed treatment systems and methods |
US9959511B2 (en) | 2010-12-08 | 2018-05-01 | Bayer Cropscience Lp | Retail point seed treatment systems and methods |
US10480857B2 (en) | 2017-05-24 | 2019-11-19 | Brett Edgerton | Seed drying system |
CN112984999B (en) * | 2021-02-28 | 2022-09-23 | 新疆禾旺农业科技有限公司 | Agricultural seed drying-machine |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4203228A (en) * | 1978-06-26 | 1980-05-20 | Mta Muszaki Kemiai Kutato Intezet | Contacting and drying of material in a spouted system |
WO1991010871A1 (en) * | 1990-01-11 | 1991-07-25 | Blaw-Knox Food And Chemical Equipment Company | Apparatus and process for conditioning particulate material |
DE4128258A1 (en) * | 1991-08-10 | 1993-02-11 | Saat & Erntetechnik Gmbh | Seed coating appts. - has controlled sprays and hot air feed to recirculating material in rotor for consistent coating and drying |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SE308892B (en) * | 1964-12-07 | 1969-02-24 | Atomenergi Ab | |
US3671296A (en) * | 1969-07-28 | 1972-06-20 | Takeda Chemical Industries Ltd | Process for coating granular materials |
FR2135494B1 (en) * | 1971-05-06 | 1973-05-11 | Vanniere Catherine | |
US4532155A (en) * | 1983-08-08 | 1985-07-30 | G. D. Searle & Co. | Apparatus and process for coating, granulating and/or drying particles |
DK161743C (en) * | 1989-07-03 | 1992-02-17 | Niro Atomizer As | PROCEDURE AND APPARATUS FOR AGGLOMERATION OF A POWDER-SHAPED MATERIAL |
US5105555A (en) * | 1990-01-11 | 1992-04-21 | Shoji Nakagomi | Plastic drying apparatus |
DK136595A (en) * | 1995-12-01 | 1997-03-17 | Aeromatic Fielder Ag | An apparatus and a method for treating particulate materials |
JP3839531B2 (en) * | 1996-11-05 | 2006-11-01 | フロイント産業株式会社 | Centrifugal rolling granulation coating apparatus, granulation method and coating method of granular material using the same |
DE19724055C2 (en) * | 1997-06-07 | 1999-07-29 | Glatt Systemtechnik Dresden | Device for drying pourable products and processes for use |
-
1999
- 1999-09-25 GB GB9922698A patent/GB2355058A/en not_active Withdrawn
-
2000
- 2000-09-25 WO PCT/GB2000/003674 patent/WO2001023820A1/en not_active Application Discontinuation
- 2000-09-25 AU AU74370/00A patent/AU7437000A/en not_active Abandoned
- 2000-09-25 EP EP00962726A patent/EP1214556A1/en not_active Withdrawn
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4203228A (en) * | 1978-06-26 | 1980-05-20 | Mta Muszaki Kemiai Kutato Intezet | Contacting and drying of material in a spouted system |
WO1991010871A1 (en) * | 1990-01-11 | 1991-07-25 | Blaw-Knox Food And Chemical Equipment Company | Apparatus and process for conditioning particulate material |
DE4128258A1 (en) * | 1991-08-10 | 1993-02-11 | Saat & Erntetechnik Gmbh | Seed coating appts. - has controlled sprays and hot air feed to recirculating material in rotor for consistent coating and drying |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1795842A1 (en) * | 2005-12-06 | 2007-06-13 | International Tobacco Machinery Poland Ltd | Apparatus for conditioning of organic materials |
Also Published As
Publication number | Publication date |
---|---|
WO2001023820A1 (en) | 2001-04-05 |
EP1214556A1 (en) | 2002-06-19 |
AU7437000A (en) | 2001-04-30 |
GB9922698D0 (en) | 1999-11-24 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
WAP | Application withdrawn, taken to be withdrawn or refused ** after publication under section 16(1) |