WO1991002778A1 - Treated bark product - Google Patents

Treated bark product Download PDF

Info

Publication number
WO1991002778A1
WO1991002778A1 PCT/AU1990/000369 AU9000369W WO9102778A1 WO 1991002778 A1 WO1991002778 A1 WO 1991002778A1 AU 9000369 W AU9000369 W AU 9000369W WO 9102778 A1 WO9102778 A1 WO 9102778A1
Authority
WO
WIPO (PCT)
Prior art keywords
bark
granules
heating
exogenous
granulated
Prior art date
Application number
PCT/AU1990/000369
Other languages
French (fr)
Inventor
Lea Charles Rampton
Original Assignee
Polwood Pty Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Polwood Pty Ltd filed Critical Polwood Pty Ltd
Publication of WO1991002778A1 publication Critical patent/WO1991002778A1/en

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K17/00—Soil-conditioning materials or soil-stabilising materials
    • C09K17/40—Soil-conditioning materials or soil-stabilising materials containing mixtures of inorganic and organic compounds
    • C09K17/48—Organic compounds mixed with inorganic active ingredients, e.g. polymerisation catalysts
    • C09K17/50—Organic compounds mixed with inorganic active ingredients, e.g. polymerisation catalysts the organic compound being of natural origin, e.g. cellulose derivatives
    • C—CHEMISTRY; METALLURGY
    • C05—FERTILISERS; MANUFACTURE THEREOF
    • C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F11/00—Other organic fertilisers

Definitions

  • TREATED BARK PRODUCT This invention is concerned with a method and apparatus for treatment of timber bark waste and a treated bark product produced thereby.
  • Timber logs may be debarked by a labour intensive stripping process prior to saw milling or, more commonly, shallow surface cuts may be made to remove a thin flitch of timber with a layer of bark adhering thereto.
  • waste barks from logging operations may be used as a culture and/or growth medium for delicate aerophytes such as orchids or the like. It is a requirement of culture or growth media for aerophytes or like plants such as orchids that the medium comprises a particulate material having a substantially neutral pH and otherwise to be free of plant pathogens such as viruses, bacteria and/or fungal spores. In addition, the medium should be resistant to attack by fungus as fungi harbored by the medium can be detrimental to plant health.
  • barks of the species pinus Although the invention is exemplified by reference to barks of the species pinus, it is considered that barks of many other commonly occurring species such as eucalyptus, acacia, grevillea and the like may be suitable for use with the method and apparatus of the invention with appropriate modifications if required.
  • a method for the manufacture of plant growth media from tree barks comprising the ⁇ tep ⁇ of:- treating granules of bark at an elevated temperature for a predetermined period of time to kill heat labile plant pathogens; chemically treating said granulated bark with an alkali material to form at least an outer pH neutral layer on said bark granules; immersing said heated, bark granule ⁇ in water at ambient temperature or lower to cau ⁇ e ⁇ eparation of sapwood and exogenous portions of said granules of bark; and, collecting and drying said exogenous portions.
  • Preferably ⁇ aid granulated bark is of a particle size in the range 3mm to 30mm.
  • alkaline material which may be selected from any suitable inexpensive and readily obtainable material such as sodium or calcium hydroxide or hypo ⁇ hlorite, quicklime, soda ash or the like.
  • the alkali material comprises crushed or powdered limestone or dolomite or a mixture thereof.
  • the chemical treatment proces ⁇ may also include impregnation of said particulate bark with trace elements, nutrients, fungicides, pe ⁇ ti ⁇ ide ⁇ and the like, either singularly or in a preselected combination.
  • Heating of the particulate bark to kill heat labile plant pathogens may be carried out by any suitable means such as a hot air oven, a steam oven, radiant heaters, microwave heating radiation.
  • heating is effected by heating the bark granules in water at atmospheric or elevated pressures in a pressure ves ⁇ el.
  • the chemical treatment step i ⁇ carried out simultaneously with the heating step although the treating and chemical treatment steps may be carried out independently.
  • Chemical treatment is suitably carried out within the temperature range 50°C - 105°C, preferably 95 - 103°C.
  • an apparatus for manufacture of treated bark products comprising:- a chemical treatment vessel including means to heat a volume of liquid contained therein; conveyor means adapted to move particulate bark through ⁇ aid chemical treatment vessel at a predetermined rate; a separation ve ⁇ el containing, in use, a volume of unheated water; transfer means to transfer treated particulate bark from said chemical treatment ves ⁇ el to said separation ves ⁇ el; and, collection mean ⁇ to collect particles of chemically treated exogenous bark from said separation vessel.
  • said chemical treatment vessel comprises a rectangular chamber with an inlet region and outlet region respectively at opposed ends of ⁇ aid chamber.
  • said conveyor means is adapted to move particulate bark material between said inlet region and said outlet region at a predetermined rate.
  • the conveyor means may be adapted to agitate said particulate bark material a ⁇ it moves between said inlet region and said outlet region.
  • an apparatus for manufacture of treated bark products comprising:- heating means adapted to heat particulate bark for a predetermined period of time to kill heat labile plant pathogens associated therewith; a chemical treatment ves ⁇ el to receive heat treated particulate bark, said chemical treatment vessel including conveyor means to move particulate bark through said chemical treatment vessel at a predetermined rate; a separation vessel containing in use a volume of unheated water; transfer means adapted to transfer chemically treated bark from " ⁇ aid chemical treatment vessel to said separation ves ⁇ el; and, collection means to collect chemically treated exogenous bark from said separation vessel.
  • Fig 3 show ⁇ a schematic, view of an alternative form of an apparatus according to the invention.
  • Fig 1 saw mill waste such as pine bark i ⁇ granulated in a hammer mill 1 and is then graded into selected particle size ranges by passing through a series of graded ⁇ creen ⁇ 2.
  • a ⁇ uitable range of particle ⁇ ize ⁇ may be between ⁇ ay 6mm and 30mm in 6mm step ⁇ .
  • the particle size ranges the particulate bark with attached sapwood is fed into a reaction vessel 3 containing an aqueous suspension of pulverized limestone or a mixture of pulverized limestone and dolomite.
  • the particulate bark i ⁇ maintained in the reaction ve ⁇ el 3 with gentle agitation to allow neutralization of at lea ⁇ t the surface layer of the bark which is acidic due to the presence of tannins, etc.
  • one or more trace elements 4 may be added to the reaction ves ⁇ el 3.
  • the trace elements are selected according to the intended purpose of the treated bark material. For example with bark particles of smaller size these may be employed as a propagation medium in seed germination and early seedling stage ⁇ and thus the nature and quantity of trace elements will be selected according to known criteria. Bark particle ⁇ of larger ⁇ ize may be employed in later growth stages and will also be treated according to known criteria.
  • the neutralized bark, impregnated with trace elements is fed into a container 5 of clean unheated water.
  • the sapwood separates from the exogenous bark and settle ⁇ to the bottom of container 5. This is believed to occur due to differentials in thermal expansion and water absorption between the sapwood and exogenou ⁇ bark.
  • the ⁇ apwood and the neutralization waste, a heavy red-brown liquid containing unspent limestone, and some wood chips are combined and, if required, may be utilized as a mulch for crops or other plants.
  • the treated exogenous bark particles are then placed on a mesh conveyor 6 to allow initial drainage before being dried in a rotary kiln 7. After drying the particulate bark is hermetically sealed in plastic bags or the like to prevent ingress of contaminants, particularly of the bacterial or fungal " kind.
  • the product according to the process comprises a graded particulate exogenous bark product which i ⁇ ⁇ ubstantially pH neutral at least on the surface layer of the particles and is packaged in a clean sterile form. If required the product may be impregnated with trace elements or other plant nutrients.
  • Fig 2 illustrate ⁇ one embodiment of an apparatu ⁇ for substantially continuous production of treated bark.
  • Feed rate may be controlled or varied by any suitable means such as a rotary feeder 13 on hopper 10 or adjusting the speed of conveyor 11 or both.
  • a further hopper 14 contains a mixture of pulverized limestone and magnesium silicate and this powdered material is metered onto the conveyor belt 11 by mean ⁇ of a vibratory feeder 15.
  • a walking beam conveyor 23 which momentarily elevates a layer of bark above the water surface as the layer progresse ⁇ forwardly toward ⁇ the outlet end of the ve ⁇ el 12.
  • Conveyor 23 compri ⁇ e ⁇ a plurality of rotating cranks 24 connected via link arms 25 to a bed 26 in the form of a wire mesh rack, timber platform or the like.
  • the oscillatory motion of the walking beam conveyor 23 not only serves to control the duration of treatment of the bark in reaction ves ⁇ el 12, it al ⁇ o ⁇ erve ⁇ to continuously agitate the bark particles to ensure complete and even chemical treatment.
  • a chain ⁇ craper 17 compri ⁇ ing ⁇ paced ⁇ lat ⁇ 18 extending between chain and sprocket drives 16 on each side of ve ⁇ el 12.
  • a chain ⁇ craper 17 compri ⁇ ing ⁇ paced ⁇ lat ⁇ 18 extending between chain and sprocket drives 16 on each side of ve ⁇ el 12.
  • the reaction product of the limestone and the soluble acidic components of the bark settles to the floor of vessel 12 as a viscous red-brown liquid containing at least some unreacted limestone.
  • Reaction time in the reaction vessel is dependent upon surface area of the bark particles. ? finer grades having an average particle size around 6mm, e. asidence time of about 10 minutes is sufficient to neutralize the acidic bark residues, impregnate with trace elements and to sterilize the bark. For larger particles sizes of say, 30mm, a residence time of up to one hour may be required to fully treat the bark.
  • walking beam conveyor 23 and chain scraper 17 transfer the treated bark particle ⁇ and the reaction ve ⁇ el residues, under the influence of gravity, to a separation vessel 19 containing clean, unheated water at ambient temperature.
  • a separation vessel 19 containing clean, unheated water at ambient temperature.
  • a perforated belt conveyor 20 removes from one end of vessel 19 the exogenou ⁇ bark particle ⁇ , impregnated with one cr more selected trace elements or other plant nutrient media, while sedimentary residues are removed by a chain scraper 21 or the like.
  • the exogenous bark particle ⁇ are then dried in a suitable drying apparatus such as a rotary kiln, grain dryer or the like prior to bagging.
  • a suitable drying apparatus such as a rotary kiln, grain dryer or the like prior to bagging.
  • the drying and bagging operations are carried out immediately after the ⁇ eparation ⁇ tep to remove the sapwood to maintain the sterility of the treated bark product.
  • Fig 3 shows an alternative embodiment of the apparatus of the invention wherein the heating of the bark and chemical treatment are carried out as separate step ⁇ .
  • the apparatus i ⁇ substantially identical to that illustrated in Fig 2 except that the bark and pulverized limestone/magne ⁇ ium- ⁇ ilicate on conveyor belt 11 travel through a heating chamber 30 before entering reaction ve ⁇ el
  • the heating chamber 30 may include radiant heater ⁇ , a ⁇ ource of heated air or superheated steam or microwave radiation (or a combination of heating methods) to elevate the temperature of the bark particles to a degree and for a period sufficient to kill heat labile plant pathogens as ⁇ o ⁇ iated with the bark.
  • radiant heater ⁇ a ⁇ ource of heated air or superheated steam or microwave radiation (or a combination of heating methods) to elevate the temperature of the bark particles to a degree and for a period sufficient to kill heat labile plant pathogens as ⁇ o ⁇ iated with the bark.
  • a re ⁇ iden ⁇ e time of from 15 min to 1 hour in an atmosphere of heated air or superheated ⁇ team will be sufficient to kill most unwanted pathogen ⁇ , however thi ⁇ re ⁇ idence time may be ⁇ ub ⁇ tantially reduced where heating i ⁇ effected by microwave radiation, particularly if the bark i ⁇ sprayed with water before entering the heating chamber.
  • the reaction ves ⁇ el 12 need not be heated in this embodiment as residual heat from the heated bark particles is ⁇ ufficient to elevate the temperature of the aqueou ⁇ neutralization/impregnation liquor to assist in the rate of reaction of the neutralization and impregnation proces ⁇ e ⁇ .
  • a microwave heater is employed to dry the treated exogenous bark is ⁇ uing from ⁇ eparation vessel 19, the period of the drying cycle may be reduced and any residual heat labile pathogen ⁇ are killed. Thi ⁇ may permit reduction of the period of the initial heating cycle.
  • the treated bark product produced according to the invention is a particularly suitable growing/propagation medium for delicate aerophytes such as orchids and the like.
  • the particulate bark material is pH neutral and is free of any bacteria or fungi which could adver ⁇ ely affect plant growth.
  • the treatment process according to the invention removes soil particles and other contaminants which could harbour plant pathogen ⁇ and the removal of the highly water absorbent sapwood component largely alleviate ⁇ subsequent fungal attach from airborne fungus spores.
  • selected trace elements or other plant nutrients may be incorporated to suit the particular requirements of different plants at different growth stages. It will be clear to a skilled addres ⁇ ee that many modification ⁇ and variation ⁇ may be made to the invention without departing from the ⁇ pirit and scope thereof.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Soil Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Cultivation Of Plants (AREA)

Abstract

A plant growth medium is formed by granulating tree barks, heating the granular bark so formed to kill heat labile plant pathogens, chemically treating the granular bark with an aqueous solution of an alkali material to form at least a pH neutral outer layer on the granules and optionally impregnating the granules with trace elements, plant nutrients and fungicides. The heated, chemically treated bark granules are then immersed in cold water to cause separation of sapwood from the exogenous bark portion. The separated exogenous bark portion is then dried and bagged as a sterile plant growth medium particularly suited to aerophytes.

Description

TREATED BARK PRODUCT This invention is concerned with a method and apparatus for treatment of timber bark waste and a treated bark product produced thereby. Timber logs may be debarked by a labour intensive stripping process prior to saw milling or, more commonly, shallow surface cuts may be made to remove a thin flitch of timber with a layer of bark adhering thereto.
Traditionally, these bark offcuts were disposed of by burning as until recently there has been no use for waste bark. It has now been discovered that, with appropriate treatment, waste barks from logging operations may be used as a culture and/or growth medium for delicate aerophytes such as orchids or the like. It is a requirement of culture or growth media for aerophytes or like plants such as orchids that the medium comprises a particulate material having a substantially neutral pH and otherwise to be free of plant pathogens such as viruses, bacteria and/or fungal spores. In addition, the medium should be resistant to attack by fungus as fungi harbored by the medium can be detrimental to plant health.
While granulated barks of the pinus species have been found to be at least partially suitable as growth media in the short term, considerable care must be taken to avoid fungal infection of the medium from airborne sources. It has now been discovered that the major cause of fungal infections in granulated pine bark growth medium is the presence of a layer of porous sapwood usually adhering to the exogenous bark layer. The sapwood layer absorbs a relatively large quantity of moisture and, over a period of time, iε likely to undergo fungal degradation often with disastrous results for the plant being supported by the medium.
Although the invention is exemplified by reference to barks of the species pinus, it is considered that barks of many other commonly occurring species such as eucalyptus, acacia, grevillea and the like may be suitable for use with the method and apparatus of the invention with appropriate modifications if required.
According to one aspect of the invention there iε provided a method for the manufacture of plant growth media from tree barks, said method compriεing the εtepε of:- treating granules of bark at an elevated temperature for a predetermined period of time to kill heat labile plant pathogens; chemically treating said granulated bark with an alkali material to form at least an outer pH neutral layer on said bark granules; immersing said heated, bark granuleε in water at ambient temperature or lower to cauεe εeparation of sapwood and exogenous portions of said granules of bark; and, collecting and drying said exogenous portions.
Preferably εaid granulated bark is of a particle size in the range 3mm to 30mm.
Chemical treatment to effect εubstantial pH neutralization is suitably carried out with an alkaline material which may be selected from any suitable inexpensive and readily obtainable material such as sodium or calcium hydroxide or hypoσhlorite, quicklime, soda ash or the like.
Preferably the alkali material comprises crushed or powdered limestone or dolomite or a mixture thereof.
The chemical treatment procesε may also include impregnation of said particulate bark with trace elements, nutrients, fungicides, peεtiσideε and the like, either singularly or in a preselected combination.
Heating of the particulate bark to kill heat labile plant pathogens may be carried out by any suitable means such as a hot air oven, a steam oven, radiant heaters, microwave heating radiation. Preferably heating is effected by heating the bark granules in water at atmospheric or elevated pressures in a pressure vesεel.
Suitably the chemical treatment step iε carried out simultaneously with the heating step although the treating and chemical treatment steps may be carried out independently.
Chemical treatment is suitably carried out within the temperature range 50°C - 105°C, preferably 95 - 103°C. According to another aspect of the invention there is provided an apparatus for manufacture of treated bark products, said apparatus comprising:- a chemical treatment vessel including means to heat a volume of liquid contained therein; conveyor means adapted to move particulate bark through εaid chemical treatment vessel at a predetermined rate; a separation veεεel containing, in use, a volume of unheated water; transfer means to transfer treated particulate bark from said chemical treatment vesεel to said separation vesεel; and, collection meanε to collect particles of chemically treated exogenous bark from said separation vessel. Preferably said chemical treatment vessel comprises a rectangular chamber with an inlet region and outlet region respectively at opposed ends of εaid chamber.
Suitably said conveyor means is adapted to move particulate bark material between said inlet region and said outlet region at a predetermined rate.
The conveyor means may be adapted to agitate said particulate bark material aε it moves between said inlet region and said outlet region.
According to yet another aspect of the invention there is provided an apparatus for manufacture of treated bark products, said apparatus comprising:- heating means adapted to heat particulate bark for a predetermined period of time to kill heat labile plant pathogens associated therewith; a chemical treatment vesεel to receive heat treated particulate bark, said chemical treatment vessel including conveyor means to move particulate bark through said chemical treatment vessel at a predetermined rate; a separation vessel containing in use a volume of unheated water; transfer means adapted to transfer chemically treated bark from " εaid chemical treatment vessel to said separation vesεel; and, collection means to collect chemically treated exogenous bark from said separation vessel. In order that the invention may be more readily understood, reference will now be made to preferred embodiments illustrated in the accompanying drawings in which Fig 1 shows a flow chart illustrating the method according to the invention, Fig 2 shows a schematic view of an apparatus according to the invention,
Fig 3 showε a schematic, view of an alternative form of an apparatus according to the invention.
In Fig 1, saw mill waste such as pine bark iε granulated in a hammer mill 1 and is then graded into selected particle size ranges by passing through a series of graded εcreenε 2. A εuitable range of particle εizeε may be between εay 6mm and 30mm in 6mm stepε.
After grading into suitable particle εize ranges the particle size ranges the particulate bark with attached sapwood is fed into a reaction vessel 3 containing an aqueous suspension of pulverized limestone or a mixture of pulverized limestone and dolomite. The particulate bark iε maintained in the reaction veεεel 3 with gentle agitation to allow neutralization of at leaεt the surface layer of the bark which is acidic due to the presence of tannins, etc.
During the neutralization process one or more trace elements 4 may be added to the reaction vesεel 3. The trace elements are selected according to the intended purpose of the treated bark material. For example with bark particles of smaller size these may be employed as a propagation medium in seed germination and early seedling stageε and thus the nature and quantity of trace elements will be selected according to known criteria. Bark particleε of larger εize may be employed in later growth stages and will also be treated according to known criteria.
After a suitable reaction time in vesεel 3, the neutralized bark, impregnated with trace elements is fed into a container 5 of clean unheated water. As the hot particulate bark starts to cool, the sapwood separates from the exogenous bark and settleε to the bottom of container 5. This is believed to occur due to differentials in thermal expansion and water absorption between the sapwood and exogenouε bark. The εapwood and the neutralization waste, a heavy red-brown liquid containing unspent limestone, and some wood chips are combined and, if required, may be utilized as a mulch for crops or other plants.
The treated exogenous bark particles are then placed on a mesh conveyor 6 to allow initial drainage before being dried in a rotary kiln 7. After drying the particulate bark is hermetically sealed in plastic bags or the like to prevent ingress of contaminants, particularly of the bacterial or fungal" kind.
The product according to the process comprises a graded particulate exogenous bark product which iε εubstantially pH neutral at least on the surface layer of the particles and is packaged in a clean sterile form. If required the product may be impregnated with trace elements or other plant nutrients.
Fig 2 illustrateε one embodiment of an apparatuε for substantially continuous production of treated bark. Graded pulverized bark mill waste iε fed via hopper
10 onto a conveyor belt 11 for tranεfer to reaction veεsel 12 at a predetermined feed rate. Feed rate may be controlled or varied by any suitable means such as a rotary feeder 13 on hopper 10 or adjusting the speed of conveyor 11 or both. A further hopper 14 contains a mixture of pulverized limestone and magnesium silicate and this powdered material is metered onto the conveyor belt 11 by meanε of a vibratory feeder 15.
Reaction veεεel 12 iε εubεtantially filled with water which is maintained at or near lOO^C by a fuel fed boiler (not shown) .
As the particulate bark is added to the reaction veεsel it floats on the surface of the aqueouε limeεtone suspenεion within the tank. The floating layer of bark iε conveyed from one end of the vessel to the other at a predetermined rate by a walking beam conveyor 23 which momentarily elevates a layer of bark above the water surface as the layer progresseε forwardly towardε the outlet end of the veεεel 12. Conveyor 23 compriεeε a plurality of rotating cranks 24 connected via link arms 25 to a bed 26 in the form of a wire mesh rack, timber platform or the like.
The oscillatory motion of the walking beam conveyor 23 not only serves to control the duration of treatment of the bark in reaction vesεel 12, it alεo εerveε to continuously agitate the bark particles to ensure complete and even chemical treatment.
Located in the base of vesεel 12 iε a chain εcraper 17 compriεing εpaced εlatε 18 extending between chain and sprocket drives 16 on each side of veεεel 12. As the bark particles progresε along the surface of the water in veεsel 12, particles of sapwood, dirt and other contaminantε εink to the floor of veεsel 12. The reaction product of the limestone and the soluble acidic components of the bark settles to the floor of vessel 12 as a viscous red-brown liquid containing at least some unreacted limestone.
Reaction time in the reaction vessel is dependent upon surface area of the bark particles. ? finer grades having an average particle size around 6mm, e. asidence time of about 10 minutes is sufficient to neutralize the acidic bark residues, impregnate with trace elements and to sterilize the bark. For larger particles sizes of say, 30mm, a residence time of up to one hour may be required to fully treat the bark.
The combined effects of walking beam conveyor 23 and chain scraper 17 transfer the treated bark particleε and the reaction veεεel residues, under the influence of gravity, to a separation vessel 19 containing clean, unheated water at ambient temperature. As the hot treated bark particleε come into contact with the cold water the exogenous bark portion separates from the sap wood portion and the latter sinkε to the floor of veεεel 19 while the exogenouε bark portion σontinueε to float.
A perforated belt conveyor 20 removes from one end of vessel 19 the exogenouε bark particleε, impregnated with one cr more selected trace elements or other plant nutrient media, while sedimentary residues are removed by a chain scraper 21 or the like.
The exogenous bark particleε are then dried in a suitable drying apparatus such as a rotary kiln, grain dryer or the like prior to bagging. The drying and bagging operations are carried out immediately after the εeparation εtep to remove the sapwood to maintain the sterility of the treated bark product.
Fig 3 shows an alternative embodiment of the apparatus of the invention wherein the heating of the bark and chemical treatment are carried out as separate stepε.
The apparatus iε substantially identical to that illustrated in Fig 2 except that the bark and pulverized limestone/magneεium- εilicate on conveyor belt 11 travel through a heating chamber 30 before entering reaction veεεel
12.
The heating chamber 30 may include radiant heaterε, a εource of heated air or superheated steam or microwave radiation (or a combination of heating methods) to elevate the temperature of the bark particles to a degree and for a period sufficient to kill heat labile plant pathogens asεoσiated with the bark. Depending on the εize of the bark particleε, a reεidenσe time of from 15 min to 1 hour in an atmosphere of heated air or superheated εteam will be sufficient to kill most unwanted pathogenε, however thiε reεidence time may be εubεtantially reduced where heating iε effected by microwave radiation, particularly if the bark iε sprayed with water before entering the heating chamber.
The reaction vesεel 12 need not be heated in this embodiment as residual heat from the heated bark particles is εufficient to elevate the temperature of the aqueouε neutralization/impregnation liquor to assist in the rate of reaction of the neutralization and impregnation procesεeε. Similarly, if a microwave heater is employed to dry the treated exogenous bark isεuing from εeparation vessel 19, the period of the drying cycle may be reduced and any residual heat labile pathogenε are killed. Thiε may permit reduction of the period of the initial heating cycle. The treated bark product produced according to the invention is a particularly suitable growing/propagation medium for delicate aerophytes such as orchids and the like. The particulate bark material is pH neutral and is free of any bacteria or fungi which could adverεely affect plant growth. The treatment process according to the invention removes soil particles and other contaminants which could harbour plant pathogenε and the removal of the highly water absorbent sapwood component largely alleviateε subsequent fungal attach from airborne fungus spores. Depending upon the nature of the plant to be grown in the product according to the invention, selected trace elements or other plant nutrients may be incorporated to suit the particular requirements of different plants at different growth stages. It will be clear to a skilled addresεee that many modificationε and variationε may be made to the invention without departing from the εpirit and scope thereof.

Claims

1. A method for the manufacture of plant growth media from tree barks, said method comprising the stepε of:- heating granuleε of bark at an elevated temperature for a predetermined period of time to kill heat labile plant pathogens; chemically treating said granulated bark with an alkali material to form at least an outer pH neutral layer on said granules; immersing said heated bark granules in water at ambient temperature or lower to cauεe separation of sapwood and exogenous portions of said granules, and; collecting and drying said exogenous portions.
2. A method as claimed in claim 1 wherein said stepε of heating the granuleε and chemically treating the granuleε are carried out εimultaneouεly.
3. A method aε claimed in claim 1 wherein said stepε of heating the granuleε and chemically treating the granules are carried out as separate steps.
4. A method as claimed in any preceding claim wherein the bark granules have a particle size in the range 3mm to 30mm.
5. A method as claimed in any preceding claim wherein the alkali material compriseε powdered limeεtone, powdered dolomite or a mixture thereof.
6. A method aε claimed in any preceding claim wherein the chemical treatment εtep alεo includes impregnation of said bark granules with trace elements, plant nutrients, fungicides, pesticides or any combination thereof.
7. A method as claimed in any preceding claim wherein the chemical treatment εtep iε carried out in the temperature range of from 50^C - 105^C.
8. An apparatus for the manufacture of plant growth media from tree barks, said apparatus comprising:- heating means to heat granulated bark at an elevated temperature for a predetermined period of time to kill heat labile plant pathogens; a reaction vessel to chemically treat said granulated bark; conveyor means adapted to move granulated bark through said reaction vessel at a predetermined rate; a separation vessel containing, in use, a quantity of water at ambient temperature or lower; transfer meanε to tranεfer chemically treated granules of bark from said reaction vesεel to εaid εeparation veεsel; and, collection means to collect exogenous bark separated from sapwood in said separation vessel.
9. An apparatus as claimed in claim 8 wherein said heating means comprises a heated aqueous solution in said reaction vesεel.
10. An apparatuε as claimed in claim 8 wherein εaid heating meanε compriεeε a heating chamber upstream of said reaction vessel.
11. An apparatus as claimed in any one of claims 8-10 wherein said conveyor meanε iε adapted to agitate said granulated bark in said reaction vessel.
12. An apparatus as claimed in any one of claims 8-11 wherein said collection means compriseε a perforated conveyor.
PCT/AU1990/000369 1989-08-25 1990-08-24 Treated bark product WO1991002778A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
AUPJ595589 1989-08-25
AUPJ5955 1989-08-25

Publications (1)

Publication Number Publication Date
WO1991002778A1 true WO1991002778A1 (en) 1991-03-07

Family

ID=3774134

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/AU1990/000369 WO1991002778A1 (en) 1989-08-25 1990-08-24 Treated bark product

Country Status (1)

Country Link
WO (1) WO1991002778A1 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5709729A (en) * 1993-09-28 1998-01-20 Environmental And Resource Technology Holdings Pty. Ltd. Formulation and production of growing media from green organic material
WO2000025569A1 (en) * 1998-11-02 2000-05-11 Superlawn Cc A hydroponic grass growing system
GB2376028A (en) * 2001-11-02 2002-12-04 Unigro Ltd Growing room, growing medium and environmental control
WO2004009732A1 (en) * 2002-07-22 2004-01-29 Polwood Aussie Bark Pty Ltd Plant growth medium
FR2874618A1 (en) * 2004-08-27 2006-03-03 Philippe Morin Degreasing product, useful e.g. for cleaning kitchens and workshops, comprises powdered natural, non-corrosive and non-polluting materials

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU6094580A (en) * 1980-07-30 1980-11-06 N.Z. Forest Products Limited Plant growing medium
EP0104355A1 (en) * 1982-09-24 1984-04-04 Chemie Linz Aktiengesellschaft Process for the preparation of a complete humus carrier and fertilizer based on tree-bark
DE3334540A1 (en) * 1983-09-23 1985-04-11 ebs Holzkraft GmbH & Co KG, 8464 Wackersdorf Method of producing a soil improver or soil auxiliary, from the bark of trees, in which the bark is cleaned, comminuted and subjected to heat treatment and drying in the course of the process
CA1203991A (en) * 1981-07-29 1986-05-06 Gilbert Guidat Process for making an inert material for soils or gardens
US4804401A (en) * 1985-04-17 1989-02-14 Wahlberg Arvo Method of producing a phosphorus fertilizer soil conditioner
EP0360447A2 (en) * 1988-09-19 1990-03-28 Camland Products Limited Bark treatment

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU6094580A (en) * 1980-07-30 1980-11-06 N.Z. Forest Products Limited Plant growing medium
CA1203991A (en) * 1981-07-29 1986-05-06 Gilbert Guidat Process for making an inert material for soils or gardens
EP0104355A1 (en) * 1982-09-24 1984-04-04 Chemie Linz Aktiengesellschaft Process for the preparation of a complete humus carrier and fertilizer based on tree-bark
DE3334540A1 (en) * 1983-09-23 1985-04-11 ebs Holzkraft GmbH & Co KG, 8464 Wackersdorf Method of producing a soil improver or soil auxiliary, from the bark of trees, in which the bark is cleaned, comminuted and subjected to heat treatment and drying in the course of the process
US4804401A (en) * 1985-04-17 1989-02-14 Wahlberg Arvo Method of producing a phosphorus fertilizer soil conditioner
EP0360447A2 (en) * 1988-09-19 1990-03-28 Camland Products Limited Bark treatment

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5709729A (en) * 1993-09-28 1998-01-20 Environmental And Resource Technology Holdings Pty. Ltd. Formulation and production of growing media from green organic material
WO2000025569A1 (en) * 1998-11-02 2000-05-11 Superlawn Cc A hydroponic grass growing system
GB2376028A (en) * 2001-11-02 2002-12-04 Unigro Ltd Growing room, growing medium and environmental control
GB2376028B (en) * 2001-11-02 2005-11-23 Unigro Ltd Growing system
WO2004009732A1 (en) * 2002-07-22 2004-01-29 Polwood Aussie Bark Pty Ltd Plant growth medium
FR2874618A1 (en) * 2004-08-27 2006-03-03 Philippe Morin Degreasing product, useful e.g. for cleaning kitchens and workshops, comprises powdered natural, non-corrosive and non-polluting materials

Similar Documents

Publication Publication Date Title
AU2010227018B2 (en) Plant growth medium
US5352780A (en) Absorbent material and litter from ground cellulose
US5397499A (en) Alkali-ionization and oxidation inhibiting composition
US5413618A (en) Method for the production of a peat substitute, installation for implementing said method, drying device, application of said method, and peat substitute produced according to said method
US5195465A (en) Flaked cellulose litter material which can be reused as food or fertilizer
US5951947A (en) Vacuumized microwave decontamination of waste materials
NL8502618A (en) CONTINUOUS PROCESS FOR THE PARTIAL STERILIZATION OF MUSHROOM COVER MATERIALS.
AU634573B2 (en) Treated bark product
WO1991002778A1 (en) Treated bark product
AU2013399657B2 (en) Organic composition for use with plants
WO1995003371A1 (en) Peat moss alternative
US5047255A (en) Activating material composed mainly of animal bone, flocculating agent composed mainly of the material and processes for preparation thereof
AU682200B2 (en) Peat moss alternative
Morel et al. Assessment of the possible phytotoxicity of a substrate using an easy and representative biotest
GB2224022A (en) Bark treatment
RU1783957C (en) Method for selecting viable seeds of sugar beet
EP1257177B1 (en) Method for producing feed pieces from sewage sludge
Van Wambeke Bromide residues in lettuce after soil fumigation with methyl bromide, and some factors involved
US20050211401A1 (en) Process for the production of cellulose fiber pulp
RU2051552C1 (en) Seed treatment method and device
RU2048173C1 (en) Method of cleaning gases from formaldehyde
JP2684924B2 (en) Cutting device and cutting method for coconut peel
EP0626190B1 (en) Sheet type and sheet-filter type methyl bromide removing material, and methyl bromide removing method using the same materials
CA2521786C (en) Method of destroying seeds
WO1988006148A1 (en) Method and plant for composting

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): AU CA JP US

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): AT BE CH DE DK ES FR GB IT LU NL SE

NENP Non-entry into the national phase

Ref country code: CA