AU2003204523B2 - Treatment of crops and fibrous materials - Google Patents
Treatment of crops and fibrous materials Download PDFInfo
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- AU2003204523B2 AU2003204523B2 AU2003204523A AU2003204523A AU2003204523B2 AU 2003204523 B2 AU2003204523 B2 AU 2003204523B2 AU 2003204523 A AU2003204523 A AU 2003204523A AU 2003204523 A AU2003204523 A AU 2003204523A AU 2003204523 B2 AU2003204523 B2 AU 2003204523B2
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- moisture content
- temperature
- crop
- compressed
- harvested
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- 239000002657 fibrous material Substances 0.000 title claims description 13
- 238000005056 compaction Methods 0.000 claims description 41
- 239000000463 material Substances 0.000 claims description 33
- 238000000034 method Methods 0.000 claims description 24
- 238000010438 heat treatment Methods 0.000 claims description 22
- 230000006835 compression Effects 0.000 claims description 13
- 238000007906 compression Methods 0.000 claims description 13
- 210000002268 wool Anatomy 0.000 claims description 10
- 239000010902 straw Substances 0.000 claims description 4
- 241000609240 Ambelania acida Species 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 3
- 244000060011 Cocos nucifera Species 0.000 claims description 2
- 240000000491 Corchorus aestuans Species 0.000 claims description 2
- 235000011777 Corchorus aestuans Nutrition 0.000 claims description 2
- 235000010862 Corchorus capsularis Nutrition 0.000 claims description 2
- 229920000742 Cotton Polymers 0.000 claims description 2
- 239000010905 bagasse Substances 0.000 claims description 2
- 239000003595 mist Substances 0.000 claims description 2
- 238000002203 pretreatment Methods 0.000 claims description 2
- 235000013162 Cocos nucifera Nutrition 0.000 claims 1
- 240000006240 Linum usitatissimum Species 0.000 claims 1
- 235000004431 Linum usitatissimum Nutrition 0.000 claims 1
- 239000000835 fiber Substances 0.000 description 36
- 238000003306 harvesting Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 4
- 230000007774 longterm Effects 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- 238000012545 processing Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000004463 hay Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 238000007781 pre-processing Methods 0.000 description 1
- 239000000523 sample Substances 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
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Description
Regulation 3.2 Revised 2/98
AUSTRALIA
Patents Act, 1990
ORIGINAL
COMPLETE SPECIFICATION TO BE COMPLETED BY THE APPLICANT NAME OF APPLICANT: ACTUAL INVENTORS: ADDRESS FOR SERVICE: INVENTION TITLE: DETAILS OF ASSOCIATED APPLICATION NO(S): Riyate Pty Limited ACN 002 675 416 Kim Antony Campbell Paul Thomas McCardell Peter Maxwell Associates Level 6 Pitt Street SYDNEY NSW 2000 TREATMENT OF CROPS AND FIBROUS MATERIALS Divisional of Australian Patent Application No. 69,650/00 filed on October 2000 which is a divisional of Australian Patent Application No.
77,296/98 filed on 17 July 1998, which is a divisional of Australian Patent Application No. 66,406/94 filed on 6 May 1994 The following statement is a full description of this invention including the best method of performing it known to us:m:\docs\941316\035774.doc The present invention relates to a method and apparatus for the compaction of crops and certain other materials of a fibrous nature.
The apparatus of the invention can be utilised as either a mobile or stationary apparatus.
In the area of crop transport and storage, a particular problem of the prior art is concerned with compaction of the crop to the optimum density. A specific example occurs in the matter of filling containers which are of fixed volume and shape and designated for a fixed maximum payload. In this situation, there will be a given crop density for a crop which will exactly fill the volume of the container at the maximum allowable weight. A crop which is more dense than this predetermined density will reach the maximum allowable payload weight before entirely filling the volume of the container. Equally, a crop of less density will entirely fill the volume of the container but will not reach the maximum allowable payload. In the overdense case, unnecessary energy has been expended on compacting the crop for no gain. In the underdense situation, the container is being under utilised and therefore transport of the crop is inefficient leading to additional expense.
Currently, compaction of crop or fibre is performed by a system known as "double dumping" or "triple dumping" wherein the crop is either teased apart and then recompacted or simply compacted to a high degree using mechanical force upon crop that has previously been cured to an appropriate moisture content.
A subsidiary problem is control or management of moisture content of the crop of fibre immediately before, during and immediately after compaction.
In particular, moisture content for storage under compressed conditions may not be the desired moisture content for harvesting. Treatment of crops in order to alter or control their moisture content at the time of harvesting and so 27/10/00 as to provide better or optimum harvest moisture content conditions for a crop is addressed in Australian Patent No. 561,014 (see also U.S. Patent No.
4,254,605 and U.S. Patent No. 4,604,857).
These prior art patents do not address compaction efficiency problems and/or humidity control problems consequent or in relation to compaction processes.
In the description to follow, the terms "fibre", "fibrous" and "crop" are to be taken in a broad sense and are to include that which is harvested whether from plants or animals, and which will be referred to hereinafter collectively as "crop or fibre".
Also, in the description which follows, the term "fibrous" or "fibre" refers to organic materials which are made up of elongate strands such as harvested hay, bagasse, straw, shorn wool, cotton, jute or kenaff.
In the description which follows the term "ambient" or "base reference" applied to the temperature and/or moisture content or humidity of a crop or fibre is to be taken as that temperature and/or moisture content at which the crop or fibre presents itself for processing by the method or apparatus of the invention described and claimed in this specification.
In references to elevation of temperature and/or moisture content above ambient in relation to crops or fibres it should be understood that such references do not extend to an elevation of temperature or moisture content to a level where the crop or fibre will be permanently adversely affected either immediately or in terms of its medium to long term storage characteristics.
It is an object of the present invention to provide enhanced or improved means and a method of compacting crop or fibre so as to overcome or ameliorate one or more of the above mentioned disadvantages and/or to 27/10/00 provide cost advantages in relation to storage, handling and transport of harvested crops.
According to one aspect of the invention, there is provided a method of forming a compacted bale of harvested fibrous material in its harvested form, said method comprising applying a mechanical compacting force to said material at the same time as or immediately after subjecting said material to an elevated temperature above a base reference temperature and adjusting moisture content condition of the material to above a base reference moisture content condition whereby said material is compressed to a compressed state of density from about 300 kg/cm[PMA1 ]33 to about 640 kg/m 3 using less compacting force than would otherwise be the case if compression were applied at said base reference temperature and said base reference moisture content condition.
In a preferred form of the invention, said steps of subjecting said crop or fibre to an elevated temperature and/or an elevated moisture content condition are performed by applying steam to said crop or fibre.
In an alternative preferred form of the invention, said steps of subjecting said crop or fibre to an elevated temperature and/or an elevated moisture content condition are performed respectively by the application of microwave energy and the application of steam or micro sprays.
The moisture is removed from said crop after compaction by subjecting said material to superheated steam.
Alternatively, moisture can be removed by application of a hot air blast preferably in conjunction with the application of heat by other means (for example, microwave heating).
According to another aspect of the invention, there is provided apparatus for forming a compacted bale of harvested fibrous material in its 27/10/00 harvested form, said apparatus including mechanical compacting means adapted to compact said material, said apparatus further including heating means and moisture content altering means; said heating means adapted to heat said material to an elevated temperature above a base reference temperature; said moisture content altering means adapted to apply to said material an elevated moisture condition above a base reference moisture content condition during compaction of said material whereby said material is compressed to a compressed state of density from about 300 kg/m 3 to about 640 kg/m 3 using less compacting force that would otherwise be the case.
In a preferred form of the invention, said mechanical compacting means comprises a combination of groups of generally opposed planar plates.
Preferably said groups act through different axes more preferably, said groups act through mutually orthogonally opposed axes.
Preferably said heating means comprises microwave generation means which heats only said crop or fibre and not said mechanical compacting means.
27/10/00 Preferably said moisture content altering means comprises a source of steam or of superheated steam or of a fine mist spray of water.
In an alternative preferred form, steam generating means (either ordinary steam where moisture content of the crop is to be increased or superheated steam where the moisture content of the crop or fibre is to be decreased) is utilised both as said heating means and as said moisture content altering means.
In a further particular preferred form said apparatus further includes crop pre-treatment means for altering the moisture content of said crop or fibre prior to treatment by said mechanical compacting means.
In yet a further preferred form, said apparatus further includes post treatment means for altering the moisture content of said crop or fibre after compaction by said mechanical compacting means.
In order that the invention may be more readily understood and put into practical effect, reference will now be made to the drawings in which:- Fig. 1 is a perspective view of a compaction apparatus according to a first embodiment of the invention, Fig. 2 is a perspective view of a compaction apparatus according to a second embodiment of the invention, Fig. 3 is a graph of temperature against moisture content graphing lines of constant compaction energy, Fig. 4 is a graph of compaction energy against temperature showing lines of constant moisture content, Fig. 5 is a graph of compaction energy against moisture content showing lines of constant temperature.
Fig. 6 is a diagrammatic view of a compaction apparatus according to a third embodiment of the invention for processing of 27/10/00 crop or fibre at the point of harvesting, and Fig. 7 is a diagrammatic view of compaction apparatus according to a fourth embodiment of the invention incorporating pre and/or post processing of compacted cropor fibre.
With reference to Fig. 1 the compaction apparatus 10 of a first embodiment comprises two opposed planar plates 11, 12 actuated by pistons 13, 14 which, in turn, are driven by mechanical means such as hydraulic or pneumatic actuators (not shown).
The assembly 10 further includes a sensor 15 having a probe 16 which extends into the volume defined between the plates 11, 12. The sensor 15 is adapted to sense both temperature and moisture content of material located within the volume between the plates 11, 12.
Both plates 11, 12 include one or more steam orifices 17 adapted to conduct steam or heated air by means of pipes 18 into the volume defined between the plates 11, 12.
In addition, heating elements 19 can be embedded in the plates 11, 12 for the purpose of preheating the plates to a predetermined temperature. The heating elements 19 can be of the electrical resistance type or can be steam conduction tubes.
In use a crop or fibre 20 such as hay or wool is placed in the volume defined between the plates 11, 12 whilst the plates are in a spaced apart position (as shown in Fig. The crop or fibre may have been pre-heated including pre-steaming and/or pre-heating immediately prior to being placed between the plates.
Also, the crop may have been pre-treated to alter its moisture content (see for example Example 4 later).
27/10/00 8 Sensor 15 communicates the precompression temperature and moisture content of the crop or fibre 20 to control means (not shown). On the basis of this information, the control means causes plates 11 and 12 to be urged towards each other so as to compact the crop or fibre 20 located therebetween whilst, at the same time, injecting either heated air, steam or superheated steam by means of orifices 17 into the volume between the plates 11 and 12 so as to adjust the moisture content of the crop under compaction to an elevated humidity condition above a base reference humidity condition and the temperature of the crop under compression to an elevated temperature above a base reference temperature.
As shown in Fig. 3 it has been determined experimentally that the compaction energy per kilogram of crop required toa compact the crop reduces as both the temperature and moisture content of the crop under compaction is increased.
To support this, Fig. 3 graphs temperature versus moisture content for a set of three different constant compaction energy lines. Fig. 4 graphs compaction energy versus temperature for a series of three different constant moisture content lines whilst Fig. 5 graphs compaction energy versus moisture content or a series of three different constant temperature lines.
In the first embodiment, the plates 11, 12 are preheated to a predetermined temperature to aid in controlling the environment of the volume between the plates 11, 12.
Referring to Fig. 2, a second embodiment is shown wherein the plates 11, 12 are not themselves heated. Instead, a source of microwave energy 21 is applied directly to the crop or fibre 20 for the purpose of providing uniform elevation of crop temperature.
27/10/00 9 In all other respects, the structure and operation of the second embodiment is the same as that described in respect of the first embodiment.
If the cropor fibre moisture content as sensed by sensor 15 is below the desired elevated humidity condition above the base reference humidity condition, then the control means will utilise steam or a fine water spray (in combination with heating) to elevate the moisture content of the crop injected through orifices 17 so as to elevate the moisture content of the crop or fibre to the desired elevated humidity condition.
If the crop or fibre is determined by sensor 15 to be above the elevated humidity condition, then the control means will utilise superheated steam or heated air injected through orifices 17 to reduce the humidity condition of the crop or fibre down to the desired elevated humidity condition above a base reference humidity condition.
The process of varying the moisture content of the crop or fibre necessarily increases the temperature of the crop or fibre 20. If additional heating is required to achieve the desired elevated temperature above a base reference temperature, then this can be achieved by use of convection heating of the plates 11, 12 (refer Fig. 1) or microwave heating (refer Fig. 2).
In one particular variation of the second embodiment, the plates 11, 12 can be made from non-porous material whereby the microwave sources 21 can be placed on the outside of the plates and arranged so as to inject microwaves through the plates 11, 12 and into the volume defined between the plates so as to heat the crop or fibre 20 uniformly without heating the plates, 11, 12 directly.
In addition, the crop can be constrained on the sides of the plates.
In certain circumstances, the crop or fibre to be treated by the compaction apparatus 10 can be treated prior to placement between the plates 11, 12. This can be achieved by steam treatment methods and the like as, for 27/10/00 example, described in Australian Patent 606,317 and Australian Patent Application 61,915/80.
In some circumstances, it may be desirable to alter the moisture content of the crop or fibre, when at ambient temperature, following compaction so as to provide an ideal moisture content for long term storage purposes. Again, this can be achieved by additional heating or steam treatment following the previously described compaction process.
Use of the above described embodiments allows on the one hand compaction of crops or fibres using less compaction energy than has previously bee required for the same task and on the other hand, allows greater control of the density achieved whereby optimum crop-fibre densities for packing into particular volumes can be achieved. For example, hay or wool an optimum compaction density of about 640Kg/m3 allows the compacted hay or wool to fill a 20' container so that the filled container is at maximum allowable payload.
Example 1 One specific example is the compaction of hay (where "hay" is stored fodder made from a variety of crops).
Hay would normally be pressed into bales at ambient temperatures, at a moisture content of 18% mc+2%, and a density of 160Kg/ 3 to 200 Kg/m 3 Conventionally, hay is compacted ("Double-Dumped") to reduce its bulk for export and thereby reduce the cost of ocean freight when it is packed into containers at a final density of around 320 Kg/m 3 Practice has shown that to reduce the change of mould growth the hay needs to be packed at a moisture content of less than 12% preferably less than 10% mc. However, hay cannot be successfully made at this low moisture content as it will suffer "leaf shatter" and hence suffer a loss of nutritional value and a reduction of crop yield in 27/10/00 Tonnes/Ha. Therefore, the current industry practice is to make hay conventionally at 18% mc+2%mc (ideal conditions) and then store it to dry out naturally over a period of one month to four months. Once dry, it is then unstacked, unbound, teased apart and fed into a compression chamber to be recompressed to "double dumped" stage. The double dumping machinery is expensive (approximately $250,000.00 for a machine with a daily average capacity of 30 to 40 tonnes or 3-4 tonnes/hour).
By the application of moisture and temperature together, according to embodiments of the present invention, naturally dry hay (<12%mc) can be baled and compacted to "double dumped" densities of 320 Kg/m 3 or higher with less than half the force compared to conventional means (ambient temperature and <120 mc). A means for applying moisture and temperature together is to apply steam to the hay immediately prior to baling in the field. An alternative is to bring hay to a stationary compression machine where heat and temperature are applied to the hay (by steam) immediately prior to compaction.
Our experience has shown that the application of steam in raising the temperature of the hay to at least 700C and adjusting the moisture to 18% to can reduce the compression force for double dumping to between a third and a quarter of the force required otherwise. If the stream is superheated it may also dehydrate a moist crop down to an ideal moisture content of The application of steam (temperature) ensures that the hay dries rapidly (within hours) so that its final state is dry (<12%mc) and dense.
Example 2 Conventionally, wool is pressed into bales in the shearing shed. It is then transported as a bulky commodity to major collection points, usually at a port, where it is later double or triple dumped to fit into 20' containers to reduce ocean freight charges. By the application of embodiments of the present 27/10/00 12 invention, through steam or microwaves, wool can be pressed more densely on-farm. This will reduce domestic freight and storage costs.
Typically wool is double dumped to bale densities of the order of 300 Kg/m 3 requiring compaction pressures of the order of 0.1 to 0.3 MPa. Typical moisture content is less than Utilisation of the apparatus of either Fig. 1 or Fig. 2 so as to raise temperature of the wool to at least 60C during compression will allow densities of up to 640 Kg/m 3 to be achieved for a compression pressure of the order of half to one third otherwise required.
Increase of moisture content by around 5% also enhances the reduction in pressure required to achieve a given density.
Example 3 With reference to Fig. 6 a particular example of the process of the invention applied in the field is illustrated.
A harvested crop 30 is transported on input conveyor 31 to compactor 32. Compactor 32 can take the form of the compactor of Fig. 1 or the compactor of Fig. 2 wherein the temperature and/or humidity of crop 30 is raised a predetermined amount above its base temperature and humidity (that is the conditions pertained to the crop on conveyor 31) and then compacting the crop for discharge onto discharge conveyor 33. Discharge conveyor 33 conveys the compressed crop to transporter 34. Examples of particular crops which can be processed according to the apparatus illustrated in Fig. 6 include the following: Hay/Straw Hay/Straw is harvested at a base temperature of ambient and a base moisture content of less than 40% as presented on conveyor 30. Within compactor 32 the base temperature is elevated by a minimum of 200C and the 27/10/00 base moisture content is elevated by about 5% mc at which time compression takes place at a pressure of approximately 0.35 MPa for a density of 300 Kg/m 3 The resulting bale is discharged onto conveyor 33.
This is to be compared with a pressure of 0.7 MPa if the hay/straw is compacted at ambient temperature and moisture content.
Wool Wool is harvested at a base temperature of ambient and a base moisture content of about 15% mc as presented on conveyor 30. Within compactor 32 the base temperature is elevated by at least 200C and the base humidity is elevated by about 5% mc at which time compression takes place at a pressure of approximately 0.25 MPa for a density of 300 Kg/m 3 The resulting bale is discharged onto conveyor 33.
This is to be compared with a pressure of 0.3 Mpa if the wool is compacted at ambient temperature and mc.
Cotton Cotton is harvested at a base temperature of ambient and a typical base moisture content of 5-20% mc as presented on conveyor 30. Within compactor 32 the base temperature is elevated by about a minimum of 200C at which time compression takes place at a pressure of approximately 0.3-1 MPa depending on fibre type. The resulting bale is discharged onto conveyor 33.
If moisture content is elevated prior to or during compaction then improved compaction for a given pressure is noted.
Copra Copra is harvested at a base temperature of ambient and a typical base moisture content of 5-20% mc as presented on conveyor 30. Within compactor 32 the base temperature is elevated by about a minimum of 200C at which time 27/10/00 compression takes place at a pressure of approximately 0.25-1 MPa depending on fibre type. The resulting bale is discharged onto conveyor 33.
If moisture content is elevated prior to or during compaction then improved compaction for a given pressure is noted.
Bagasse Bagasse is harvested at a base temperature of ambient and a typical base moisture content of 5-20% mc as presented on conveyor 30. Within compactor 32 the base temperature is elevated by about a minimum of 200C at which time compression takes place at a pressure of approximately 0.25-1 MPa depending on fibre type. The resulting bale is discharged-onto conveyor 33.
If moisture content is elevated prior to or during compaction then improved compaction for a given pressure is noted.
Example 4 With reference to Fig. 7 an assembly of generally similar configuration to that illustrated in Fig. 6 is shown comprising input conveyor 31, compactor 32 and discharge conveyor 33. In this example a pre-processor unit 35 treats crop 30 as it moves on conveyor 31.
A post processor unit 36 treats crop in baled form on conveyor 33.
Pre-processor 35 and post processor 36 can take substantially the form of the devices illustrated and described in respect of either Fig. 1 or Fig. 2. The degree to which the capabilities of these devices are utilised can be varied in order to on the one hand allow compactor 32 to compact the crop 30 at a lower compaction pressure than would otherwise be the case and also to ensure that the moisture content of the baled product 37 leaving discharge conveyor 33 is at or will relatively soon achieve a predetermined moisture content which is 27/10/00 appropriate for medium to long-term storage purposes of the crop in compressed form.
For example a pre-processor 35 can be utilised only to alter the humidity or moisture content of the crop 30 prior to presentation to compactor 32.
Compactor 32 can then be utilised only to heat and compress or alternatively be used to alter the moisture content further as well as to heat and compress the crop.
Post processor 36 can be utilised to either further raise or lower the moisture content of the baled product 37 when it first appears on discharge conveyor 33. Heating can be performed in conjunction with this. For example post processor 36 can inject steam into the baled product 37 so as to further raise its moisture content whilst also further heating the baled product whereby ultimately the moisture content of the baled product will drop as the baled product 37 cools after discharge from conveyor 33. Alternatively super heated steam can be applied to post processor 36 to baled product 37 whereby the baled product is both heated and its moisture content is reduced whilst passing through post processor 36. Ultimately it can be expected that the moisture content will drop further as the baled product 37 cools after discharge from conveyor 33.
It will be observed that the selective combination and utilisation of preprocessor 35, compactor 32 and post processor 36 can provide relatively rigorous control of both the temperature and moisture content of harvested crop 30 and baled product 37.
The above describes only some embodiments of the present invention and modifications obvious to those skilled in the art can be made thereto without departing from the scope and spirit of the present invention.
27/10/00 Examples of the invention have particular applicability where it is desired to optimise containerised transport of crops and fibrous materials following harvesting thereof or otherwise to bale or pack harvested crop for storage or transport.
27/10/00
Claims (20)
1. A method of forming a compacted bale of harvested fibrous material in its harvested form, said method comprising applying a mechanical compacting force to said material at the same time as or immediately after subjecting said material to an elevated temperature above a base reference temperature and adjusting moisture content condition of the material to above a base reference moisture content condition whereby the material is compressed to a compressed state of density from about 300 kg/cm 3 to about 640 kg/m 3 using less compacting force than would otherwise be the case if compression were applied at said base reference temperature and said base reference moisture content condition, and then reducing the moisture content of the compressed material to the base reference moisture content.
2. The method claim of 1 wherein said steps of subjecting said material to and elevated temperature and an elevated moisture content condition are performed by applying steam to said material.
3. The method of claim 2 wherein said steps of subjecting said material to an elevated temperature and an elevated moisture content condition are performed respectively by the application of microwave energy and the application of steam.
4. The method of claim 1 wherein moisture content of the compressed material is reduced by subjecting the compressed material to superheated steam. 24/09/2007 The method of claim 1 wherein moisture content of the compressed material is reduced by the application of a hot air blast.
6. The method of claim 1 wherein moisture content of the compressed material is reduced by microwave heating.
7. The method of claim 1 wherein the fibrous material is hay or straw.
8. The method of claim 1 wherein the fibrous material is hay and the base reference temperature is ambient temperature and the base reference moisture content is less than 12%.
9. The method of claim 8 wherein the elevated temperature is at least 700C and the moisture content is adjusted to 18% to The method of claim 1 wherein the fibrous material is hay and the compacting force is between a third and a quarter of the force otherwise required.
11. The method of claim 1 wherein the fibrous material is any one of bagasse, flax, jute, kenaff, wool, cotton or copra.
12. Apparatus for forming a compacted bale of harvested fibrous material in its harvested form, said apparatus including mechanical compacting means adapted to compact said material, said apparatus further including heating means and moisture content altering means; said heating means adapted to heat said material to an elevated temperature above a base reference 24/09/2007 temperature; said moisture content altering means adapted to apply to said material an elevated moisture condition above a base reference moisture content condition during compaction of said material whereby said material is compressed to a compressed state of density from about 300 kg/m 3 to about 640 kg/m 3 using less compacting force that would otherwise be the case and wherein the heating means is adapted to reduce the moisture content of the compressed material to the base.
13. The apparatus of claim 12 wherein said mechanical compacting means comprises a combination of groups of generally opposed planar plates.
14. The apparatus of claim 13 wherein said groups of plates act through different axes. The apparatus of claim 14 wherein said groups of plates act through mutually orthogonally opposed axes.
16. The apparatus of claim 12 wherein said heating means comprises microwave generation means which heats only said material and not said mechanical compacting means.
17. The apparatus of claim 12 wherein said moisture content altering means comprises a source of steam.
18. The apparatus of claim 17 wherein said moisture content altering means comprises super heated steam. 24/09/2007
19. The apparatus of claim 17 wherein said moisture content altering means comprises a fine mist of water. The apparatus of claim 12 wherein steam generating means is utilised both as said heating means and as said moisture content altering means.
21. The apparatus of claim 12 further including pre-treatment means for altering the moisture content of said material prior to treatment by said mechanical compacting means.
22. The apparatus for claim 12 further including post treatment means for reducing the moisture content of said material after compaction by said mechanical compacting means.
23. A method of forming a compacted bale of harvested fibrous material in its harvested form substantially as hereinbefore described with reference to the accompanying drawings.
24. Apparatus for forming a compacted bale of harvested fibrous material in its harvested form substantially as hereinbefore described with reference to the accompanying drawings. Dated this 24th day of September 2007 Riyate Pty Limited Patent Attorneys for the Applicant PETER MAXWELL ASSOCIATES 24/09/2007
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AU2003204523A AU2003204523B2 (en) | 1993-05-06 | 2003-06-04 | Treatment of crops and fibrous materials |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AUPL8681 | 1993-05-06 | ||
| AU69650/00A AU6965000A (en) | 1993-05-06 | 2000-10-30 | Treatment of crops and fibrous materials |
| AU2003204523A AU2003204523B2 (en) | 1993-05-06 | 2003-06-04 | Treatment of crops and fibrous materials |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AU69650/00A Division AU6965000A (en) | 1993-05-06 | 2000-10-30 | Treatment of crops and fibrous materials |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| AU2003204523A1 AU2003204523A1 (en) | 2003-07-24 |
| AU2003204523B2 true AU2003204523B2 (en) | 2007-10-25 |
Family
ID=3753107
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AU69650/00A Abandoned AU6965000A (en) | 1993-05-06 | 2000-10-30 | Treatment of crops and fibrous materials |
| AU2003204523A Ceased AU2003204523B2 (en) | 1993-05-06 | 2003-06-04 | Treatment of crops and fibrous materials |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AU69650/00A Abandoned AU6965000A (en) | 1993-05-06 | 2000-10-30 | Treatment of crops and fibrous materials |
Country Status (1)
| Country | Link |
|---|---|
| AU (2) | AU6965000A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2023052792A1 (en) * | 2021-09-30 | 2023-04-06 | Haygain Ltd | Apparatus for and method of steam treating of plant fibres |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110972730B (en) * | 2019-12-31 | 2025-08-05 | 重庆市茂泽科技有限公司 | Semi-dried grass making equipment |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3163131A (en) * | 1962-08-31 | 1964-12-29 | Massey Ferguson Services Nv | Fluid supplying arrangement for wafering machines |
| AU6532886A (en) * | 1985-11-21 | 1987-05-28 | Riyate Pty Limited | treatment of crops |
| US5022317A (en) * | 1989-11-24 | 1991-06-11 | Williams Kenneth J | Fodder conditioning process |
-
2000
- 2000-10-30 AU AU69650/00A patent/AU6965000A/en not_active Abandoned
-
2003
- 2003-06-04 AU AU2003204523A patent/AU2003204523B2/en not_active Ceased
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3163131A (en) * | 1962-08-31 | 1964-12-29 | Massey Ferguson Services Nv | Fluid supplying arrangement for wafering machines |
| AU6532886A (en) * | 1985-11-21 | 1987-05-28 | Riyate Pty Limited | treatment of crops |
| US5022317A (en) * | 1989-11-24 | 1991-06-11 | Williams Kenneth J | Fodder conditioning process |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2023052792A1 (en) * | 2021-09-30 | 2023-04-06 | Haygain Ltd | Apparatus for and method of steam treating of plant fibres |
| GB2626283A (en) * | 2021-09-30 | 2024-07-17 | Farm & Stable Supplies Llp | Apparatus for and method of steam treating of plant fibres |
Also Published As
| Publication number | Publication date |
|---|---|
| AU6965000A (en) | 2001-02-01 |
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| FGA | Letters patent sealed or granted (standard patent) | ||
| MK14 | Patent ceased section 143(a) (annual fees not paid) or expired |