WO2004078892A1 - Coir pith - Google Patents

Coir pith Download PDF

Info

Publication number
WO2004078892A1
WO2004078892A1 PCT/GB2004/000962 GB2004000962W WO2004078892A1 WO 2004078892 A1 WO2004078892 A1 WO 2004078892A1 GB 2004000962 W GB2004000962 W GB 2004000962W WO 2004078892 A1 WO2004078892 A1 WO 2004078892A1
Authority
WO
WIPO (PCT)
Prior art keywords
coir
coir pith
dust
pith
pellets
Prior art date
Application number
PCT/GB2004/000962
Other languages
French (fr)
Inventor
Geoffrey Nutland
Original Assignee
Dainton Limited
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 Dainton Limited filed Critical Dainton Limited
Priority to EP04718343A priority Critical patent/EP1608724A1/en
Publication of WO2004078892A1 publication Critical patent/WO2004078892A1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L5/00Solid fuels
    • C10L5/02Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
    • C10L5/34Other details of the shaped fuels, e.g. briquettes
    • C10L5/36Shape
    • C10L5/363Pellets or granulates
    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01KANIMAL HUSBANDRY; AVICULTURE; APICULTURE; PISCICULTURE; FISHING; REARING OR BREEDING ANIMALS, NOT OTHERWISE PROVIDED FOR; NEW BREEDS OF ANIMALS
    • A01K1/00Housing animals; Equipment therefor
    • A01K1/015Floor coverings, e.g. bedding-down sheets ; Stable floors
    • A01K1/0152Litter
    • A01K1/0155Litter comprising organic material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/24Naturally occurring macromolecular compounds, e.g. humic acids or their derivatives
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28014Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
    • B01J20/2803Sorbents comprising a binder, e.g. for forming aggregated, agglomerated or granulated products
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L5/00Solid fuels
    • C10L5/40Solid fuels essentially based on materials of non-mineral origin
    • C10L5/44Solid fuels essentially based on materials of non-mineral origin on vegetable substances
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2220/00Aspects relating to sorbent materials
    • B01J2220/40Aspects relating to the composition of sorbent or filter aid materials
    • B01J2220/48Sorbents characterised by the starting material used for their preparation
    • B01J2220/4812Sorbents characterised by the starting material used for their preparation the starting material being of organic character
    • B01J2220/4825Polysaccharides or cellulose materials, e.g. starch, chitin, sawdust, wood, straw, cotton
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2220/00Aspects relating to sorbent materials
    • B01J2220/40Aspects relating to the composition of sorbent or filter aid materials
    • B01J2220/48Sorbents characterised by the starting material used for their preparation
    • B01J2220/4812Sorbents characterised by the starting material used for their preparation the starting material being of organic character
    • B01J2220/485Plants or land vegetals, e.g. cereals, wheat, corn, rice, sphagnum, peat moss
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Definitions

  • the invention relates to coir pith which is the residue from coconut husk after the fibrous material is removed for rope manufacture and the like.
  • Coir pith is normally dried and compressed into briquettes, blocks or bales (hereinafter collectively referred to as "briquettes") for export to a country such as the United Kingdom by the producers.
  • briquettes blocks or bales
  • the briquettes are reconstituted by the addition of large volumes of water to produce a product for use as a peat substitute, in GB-A-2 308 538 there is disclosed a process for reconstituting the briquettes back into the original dry form from the briquettes, this process is carried out by converting the coir pith dust by a milling, cutting, chopping, hammering or flailing process without the use of water as the reconstituting agent.
  • a process for the production of a coir pith product comprising forming the coir pith into a dust with a desired particle size range and forming said dust into granules.
  • the starting point for the process is coir pith which may be utilised as the untreated residue from coconut husks.
  • the coir pith may be a compressed material.
  • it may be a material formed by drying and compressing the coconut husk residue into briquettes, blocks or bales or other bulk form.
  • the coir pith can be processed in a wet or dry state using mechanical methods to reduce the material down to the required size prior to granule forming. These methods include any one or more of milling, grinding, liquidising, pulverising and effecting changes of temperature.
  • the coir pith is in a milled form.
  • the coir pith has a particle size of up to 5mm.
  • the coir pith is in a mixture including at least one of wood sawdust and chopped straw. More preferably the amount of wood sawdust and/or chopped straw present is up to 20% by volume.
  • the coir pith dust having the required particle size range is then converted into granules.
  • Various methods may be used examples of which are as follows:-
  • the coir pith dust is mixed to a paste with or without addition of agents. It is then extruded through a screen to produce a desired granule size.
  • the density of the granule will depend, at least partially on the pressure in the extrusion device as well as the liquid content. Air can be incorporated into the coir pith dust to alter the density and structure of the granules, or to assist in the extrusion process.
  • the extruded paste is subjected to a drying process to produce a finished product with absorbent properties.
  • the coir pith dust is pressed within a chamber or series of rollers to form a compressed material having the appropriate integrity for granule maintenance.
  • Liquids of various compositions and/or assisting agents may be incorporated for specific purposes.
  • the coir pith dust is pressed through a forming die to produce the required granule size.
  • This method can utilise heat generated by friction when pushing the material through the die. It may be dried from heat generated internally or externally. Drying can be achieved in the context of a cooling process as well as by the use of heat.
  • use may be made of heat in the form of, for instance, a cooking process, in order to assist in the formation of the granules.
  • the present invention also provides a granular coir pith product formed from coir pith dust having a desired particle size range.
  • the present invention provides a method of fluid absorption comprising contacting together a fluid and the granular coir product of the invention (or formed by the method of the present invention).
  • the highly effective absorption properties of the granular coir pith may be utilised in many different situations including the following:-
  • the present invention also provides a coir granule formed from coir pith dust.
  • the coir granule comprises a mixture of coir and at least one of wood sawdust and chopped straw. More preferably the wood sawdust and/or chopped straw is present in an amount up to 20% by volume.
  • granules is intended to cover granules and granular-like materials such as grains and pellets.
  • coir pith dust Although coir pith dust has a very high absorbency capability, it is a dust and this imposes certain restrictions on its use as loose absorbent material.
  • the granular product produced by the process of the invention is dust free and therefore usable in environments where the use of dust is not permitted or advisable. It is found that the granules produced by the process of the present invention are, as with coir pith dust, highly absorbent.
  • granules of different sizes and properties may be produced for various uses and applications, the parameters including the following:
  • Tests were carried out to establish the required die sizes for successful absorbent pellet manufacture using a combination of compressed organic materials.
  • the coir/sawdust combination was then treated by the addition of a natural material (code A001 Clumping agent) to promulgate clumping of the pellets when in use.
  • a natural material code A001 Clumping agent
  • pellets produced were of good and consistent diameter and were of a sufficiently firm texture and build to withstand moderate pressure. Colouration was slightly random mottled dark to mid-brown.
  • Pellets of pure coir were produced on a flat bed die, having pre-conditioned milled material with steam prior to the pressing process.
  • the coir/chopped straw combination comprised 33.32 litres coir (83.3% by volume) and 6.68 litres straw (16.7% by volume), a ratio of coir to straw of 5:1 and a total volume of 40 litres.
  • the coir/sawdust combination comprised 32 litres of coir (79.6% by volume) and 8 litres sawdust (19.9% by volume), the ratio of coir to sawdust being 4:1.
  • a clumping agent (code A001) was added in the amount of 0.2 litres (0.5% by volume). The total volume of the mixture was 40 litres.
  • the coir/straw mixture had a moisture content of 18.7% and the coir/wood sawdust mixture had a moisture content of 16%.
  • the moisture level of the coir was between 30 and 35%.
  • pellets were of a dark brown colour, highly polished and were rather brittle, having a length up to 8 cm.
  • pellets were prepared using the flat bed die. The pelleting process required less pressure and generated less heat than that for the pure coir product.
  • the pellets were of a mottled mid-brown appearance with a polished outer surface. The average length was from 2 to 3 cm. The pellets could be broken with moderate force and pellet cross-section observations suggested a fairly even material mix.
  • Pellets were subjected to absorbency testing using the method of a leading pellet manufacturer according to which pellets are placed in a glass container and twice the volume of clean water is added. In the original tests one litre of pellets were added to two litres of water but in these tests smaller quantities were used because of the limited volume of pellets available.
  • the pellets had all expanded to the same degree, with no unexpanded pallets present.
  • the resultant material resembled a magnified version of the original pellet mass, a mottled mousse of sawdust and coir mixture that was quite moist to the touch but not "sopping wet". No free water was present although water could be released from the mousse by application of pressure (squeezing by hand).
  • the results were very similar. However, the absorption process was quicker with all the water being absorbed in 55 seconds.
  • the test was applied to pure sawdust pellets.
  • One measure of pellets was added to two measures of water in a large open bowl. The pellets began to expand in 20 seconds and the rate of expansion increased slightly as the body of the pellets expanded.
  • the pellets had all expanded to create a mousse of sawdust that was extremely wet to the touch and, although no free water was evident, it required very little pressure to squeeze out water. It was unlikely that the pellets could have absorbed any more water.
  • coir to sawdust increases the speed of absorption, compared to sawdust pellets, by a factor of at least three.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Environmental Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Animal Husbandry (AREA)
  • Zoology (AREA)
  • Environmental & Geological Engineering (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Geology (AREA)
  • Housing For Livestock And Birds (AREA)

Abstract

A process for the production of a coir pith product comprises forming the coir pith into a dust with the desired particle size range and forming the dust into granules. The invention also provides a coir granule formed from a coir pith dust. Preferably the coir is in admixture with at least one of wood sawdust and chopped straw.

Description

COIR PITH
Field of Invention
The invention relates to coir pith which is the residue from coconut husk after the fibrous material is removed for rope manufacture and the like.
Background to the Invention
Coir pith is normally dried and compressed into briquettes, blocks or bales (hereinafter collectively referred to as "briquettes") for export to a country such as the United Kingdom by the producers.
The briquettes are reconstituted by the addition of large volumes of water to produce a product for use as a peat substitute, in GB-A-2 308 538 there is disclosed a process for reconstituting the briquettes back into the original dry form from the briquettes, this process is carried out by converting the coir pith dust by a milling, cutting, chopping, hammering or flailing process without the use of water as the reconstituting agent.
Statements of the Invention
According to the present invention there is provided a process for the production of a coir pith product, the process comprising forming the coir pith into a dust with a desired particle size range and forming said dust into granules.
The starting point for the process is coir pith which may be utilised as the untreated residue from coconut husks. As an alternative the coir pith may be a compressed material. For instance it may be a material formed by drying and compressing the coconut husk residue into briquettes, blocks or bales or other bulk form. In the process of the present invention the coir pith can be processed in a wet or dry state using mechanical methods to reduce the material down to the required size prior to granule forming. These methods include any one or more of milling, grinding, liquidising, pulverising and effecting changes of temperature.
Preferably the coir pith is in a milled form.
Preferably the coir pith has a particle size of up to 5mm.
Preferably the coir pith is in a mixture including at least one of wood sawdust and chopped straw. More preferably the amount of wood sawdust and/or chopped straw present is up to 20% by volume.
The coir pith dust having the required particle size range is then converted into granules. Various methods may be used examples of which are as follows:-
1. The coir pith dust is mixed to a paste with or without addition of agents. It is then extruded through a screen to produce a desired granule size. The density of the granule will depend, at least partially on the pressure in the extrusion device as well as the liquid content. Air can be incorporated into the coir pith dust to alter the density and structure of the granules, or to assist in the extrusion process. The extruded paste is subjected to a drying process to produce a finished product with absorbent properties.
2. The coir pith dust is pressed within a chamber or series of rollers to form a compressed material having the appropriate integrity for granule maintenance. Liquids of various compositions and/or assisting agents may be incorporated for specific purposes.
3. The coir pith dust, optionally mixed with agents and liquids, is pressed through a forming die to produce the required granule size. This method can utilise heat generated by friction when pushing the material through the die. It may be dried from heat generated internally or externally. Drying can be achieved in the context of a cooling process as well as by the use of heat.
In any of the above methods, use may be made of heat in the form of, for instance, a cooking process, in order to assist in the formation of the granules.
The present invention also provides a granular coir pith product formed from coir pith dust having a desired particle size range.
In addition the present invention provides a method of fluid absorption comprising contacting together a fluid and the granular coir product of the invention (or formed by the method of the present invention).
The highly effective absorption properties of the granular coir pith may be utilised in many different situations including the following:-
(a) cat litter and other types of pet bedding and litters;
(b) an absorbent cleaning agent for use in, for instance, workshops, kitchens, highways and public areas;
(c) in the absorption and fixing of various chemical materials;
(d) as a carrying agent for use in a variety of situations including the holding of enhancing agents, repellents and binders for various uses including agricultural, industrial and domestic;
(e) to form masking and odour control agents for dealing with both natural and non-natural (or chemical) odours and fumes. The present invention also provides a coir granule formed from coir pith dust.
Preferably the coir granule comprises a mixture of coir and at least one of wood sawdust and chopped straw. More preferably the wood sawdust and/or chopped straw is present in an amount up to 20% by volume.
Further Details of the Invention
The term "granules", as used herein, is intended to cover granules and granular-like materials such as grains and pellets.
Although coir pith dust has a very high absorbency capability, it is a dust and this imposes certain restrictions on its use as loose absorbent material. By contrast the granular product produced by the process of the invention is dust free and therefore usable in environments where the use of dust is not permitted or advisable. It is found that the granules produced by the process of the present invention are, as with coir pith dust, highly absorbent.
In a process in accordance with the present invention, granules of different sizes and properties may be produced for various uses and applications, the parameters including the following:
(a) size;
(b) degree of compaction and density;
(c) surface area;
(d) incorporation of agents for particular purposes, including binders, digesters and surfactants;
(e) incorporation of fillers and colorants to change appearance and weight; (f) texture including texture of the whole granule and also that of the surface of the granule.
Examples of the Invention
The invention will now be further described, by way of examples only: Example 1
Tests were carried out to establish the required die sizes for successful absorbent pellet manufacture using a combination of compressed organic materials.
Two samples were prepared using coir milled as described in GB-A-2308538 to a mixed particulate size varying from fines up to a fibre length of about 4 to 5 mm. This milled coir was then mixed with alternative materials (straw and wood sawdust) both of which are prepared to broadly similar dimensions.
The coir/sawdust combination was then treated by the addition of a natural material (code A001 Clumping agent) to promulgate clumping of the pellets when in use.
The mixtures were then pelleted using an industrial pellet mill (model CL3) with the addition of further moisture as necessary. It was found that, using a die with a 4.8mm hole diameter a pellet length of 13mm resulted in successful pellet manufacture whereas a pellet length of 19mm blocked the die.
The pellets produced were of good and consistent diameter and were of a sufficiently firm texture and build to withstand moderate pressure. Colouration was slightly random mottled dark to mid-brown.
In absorbency tests, a measured amount of pellets were placed on a shallow container to which twice the volume of water was added. Comparison control samples were used having an identical volume of similar pellets manufactured solely from wood sawdust, again placed on a shallow container with twice their volume of water.
Observations were then made to determine the speed and completion of absorbency. These were the same for the two coir-based products, both of which were noticeably quicker and more effective than the pure wood sawdust pellets.
Accordingly it was concluded that successful pellet manufacture of coir-based materials could be achieved using standard industrial pellet presses. Furthermore it was possible to compute the likely die specifications for ongoing production.
Example 2
Pellets of pure coir were produced on a flat bed die, having pre-conditioned milled material with steam prior to the pressing process.
The coir/chopped straw combination comprised 33.32 litres coir (83.3% by volume) and 6.68 litres straw (16.7% by volume), a ratio of coir to straw of 5:1 and a total volume of 40 litres.
The coir/sawdust combination comprised 32 litres of coir (79.6% by volume) and 8 litres sawdust (19.9% by volume), the ratio of coir to sawdust being 4:1. A clumping agent (code A001) was added in the amount of 0.2 litres (0.5% by volume). The total volume of the mixture was 40 litres.
The coir/straw mixture had a moisture content of 18.7% and the coir/wood sawdust mixture had a moisture content of 16%. The moisture level of the coir was between 30 and 35%.
Relatively high pressures were required to get the material through the die, as compared with those for a coir/sawdust mix. The resultant pellets were of a dark brown colour, highly polished and were rather brittle, having a length up to 8 cm. Using a mixture of coir pith and pine sawdust in a ratio of 50%/50% and with the sawdust moisture level at approximately 16%, pellets were prepared using the flat bed die. The pelleting process required less pressure and generated less heat than that for the pure coir product. The pellets were of a mottled mid-brown appearance with a polished outer surface. The average length was from 2 to 3 cm. The pellets could be broken with moderate force and pellet cross-section observations suggested a fairly even material mix.
Pellets were subjected to absorbency testing using the method of a leading pellet manufacturer according to which pellets are placed in a glass container and twice the volume of clean water is added. In the original tests one litre of pellets were added to two litres of water but in these tests smaller quantities were used because of the limited volume of pellets available.
Where the pellets were made of pure coir the uptake of water was quite slow over a period of some 30 minutes, with very little expansion of the pellet. Even after 30 minutes the pellets still retained their original shape, albeit slightly enlarged, and free water was still present in the container.
With a 50/50 coir/sawdust mix formed from one measure of pelletes and two measures of water, the pellets started to expand in 10 seconds and the rate of expansion increased as the pellets expanded. After 25 seconds the expansion was progressing rapidly and the level of free water was dropping rapidly. All free water was absorbed after one minute 25 seconds.
The pellets had all expanded to the same degree, with no unexpanded pallets present. The resultant material resembled a magnified version of the original pellet mass, a mottled mousse of sawdust and coir mixture that was quite moist to the touch but not "sopping wet". No free water was present although water could be released from the mousse by application of pressure (squeezing by hand). Where tests were carried out on a similar 50%/50% coir/sawdust mixture but using larger quantities (one litre of pellets and two litres of water) the results were very similar. However, the absorption process was quicker with all the water being absorbed in 55 seconds. For comparison purposes, the test was applied to pure sawdust pellets. One measure of pellets was added to two measures of water in a large open bowl. The pellets began to expand in 20 seconds and the rate of expansion increased slightly as the body of the pellets expanded.
At 50 seconds, the expansion was continuing steadily, this rate being maintained for three minutes. After this time a little free water, judged to be between 5 and 10% of the original volume, was observed in the base of the container.
It was apparent that the pellets near the upper surface of the bowl had not expanded at the same rate as those below, suggesting that they need to be in contact with free water for a period of time in order to commence absorption, as opposed to drawing moisture from contiguous pellets. All free water was absorbed after four minutes.
The pellets had all expanded to create a mousse of sawdust that was extremely wet to the touch and, although no free water was evident, it required very little pressure to squeeze out water. It was unlikely that the pellets could have absorbed any more water.
The addition of coir to sawdust increases the speed of absorption, compared to sawdust pellets, by a factor of at least three.
Although, in the examples above, pure coir pellets seem less effective than those made of a mixture of coir and sawdust, different results may be obtained by, for instance, reducing die depth, increasing or decreasing bore diameter, increasing or decreasing bore count (per die) and increasing or decreasing moisture level within the coir.

Claims

1. A process for the production of a coir pith product, the process comprising forming the coir pith into a dust with a desired particle size range and forming said dust into granules.
2. A process according to Claim 1, wherein the coir pith is in a milled form.
3. A process according to Claiml or Claim 2„ wherein the coir pith has a particle size of up to 5mm.
4. A process according to any of Claims 1 to 3, wherein the coir pith is in admixture with at least one of wood sawdust and chopped straw.
5. A process according to Claim 4, wherein the amount of wood sawdust and/or chopped straw present is up to 20% by volume.
6. A process according to any of the preceding claims, wherein the coir pith is mixed to a paste prior to granule formation.
7. A process according to Claim 6, wherein the paste is extruded through a screen to produce a desired granule size.
8. A process according to any of Claims 1 to 5, wherein the coir pith dust is pressed within a chamber or series of rollers to form a compressed material.
9. A process according to any of Claims 1 to 5, wherein the coir pith dust is pressed through a forming die to produce the required granule size.
10. A coir granule formed from coir pith dust.
11. A coir granule comprising a mixture of coir pith and at least one of wood sawdust and chopped straw.
12. A coir granule according to Claim 11, wherein the amount of wood sawdust and/or chopped straw present is up to 20% by volume.
PCT/GB2004/000962 2003-03-07 2004-03-08 Coir pith WO2004078892A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP04718343A EP1608724A1 (en) 2003-03-07 2004-03-08 Coir pith

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GBGB0305191.9A GB0305191D0 (en) 2003-03-07 2003-03-07 Coir pith
GB0305191.9 2003-03-07

Publications (1)

Publication Number Publication Date
WO2004078892A1 true WO2004078892A1 (en) 2004-09-16

Family

ID=9954276

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/GB2004/000962 WO2004078892A1 (en) 2003-03-07 2004-03-08 Coir pith

Country Status (3)

Country Link
EP (1) EP1608724A1 (en)
GB (1) GB0305191D0 (en)
WO (1) WO2004078892A1 (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008074310A2 (en) * 2006-12-21 2008-06-26 E & W Greenland Gmbh Material for the production of a molded body, and a molded body
EP2189573A1 (en) * 2005-07-21 2010-05-26 Italgreen S.p.A. Artificial turf structure and method of manufacturing thereof
ITUD20090186A1 (en) * 2009-10-20 2011-04-21 S I T T A S R L PROCEDURE FOR THE IMPLEMENTATION OF BALES MATERIAL FOR ANIMAL BEDDING AND BALES MATERIALS OBTAINED
US8316581B2 (en) 2004-11-19 2012-11-27 Rubin Patti D Compressed growing medium
US9756798B2 (en) 2004-11-19 2017-09-12 Patti D. Rubin Burrow filling compressed growing medium
WO2020106484A1 (en) * 2018-11-19 2020-05-28 Shoup David E Turf and lawn coir
US11737402B2 (en) 2018-11-19 2023-08-29 Genus Industries, Llc Turf and lawn coir

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2272903A (en) * 1992-11-20 1994-06-01 Puwakdandawe Narayan Nandadasa Organic material
GB2308538A (en) * 1995-12-29 1997-07-02 Organic & Absorbent Products L Coir dust
EP0867112A1 (en) * 1997-03-26 1998-09-30 Paolo Pellegatta Vegetable absorbent material for use as litter in zootechnical field
US6391120B1 (en) * 2000-02-28 2002-05-21 Tilak V. Silva Method of oil cleanup using coconut coir pith
US6408568B1 (en) * 2001-01-23 2002-06-25 Oms Investments, Inc. Compressed blends of coconut coir pith and a non-coir/non-peat materials, and processes for the production thereof

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2272903A (en) * 1992-11-20 1994-06-01 Puwakdandawe Narayan Nandadasa Organic material
GB2308538A (en) * 1995-12-29 1997-07-02 Organic & Absorbent Products L Coir dust
EP0867112A1 (en) * 1997-03-26 1998-09-30 Paolo Pellegatta Vegetable absorbent material for use as litter in zootechnical field
US6391120B1 (en) * 2000-02-28 2002-05-21 Tilak V. Silva Method of oil cleanup using coconut coir pith
US6408568B1 (en) * 2001-01-23 2002-06-25 Oms Investments, Inc. Compressed blends of coconut coir pith and a non-coir/non-peat materials, and processes for the production thereof

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9756798B2 (en) 2004-11-19 2017-09-12 Patti D. Rubin Burrow filling compressed growing medium
US8316581B2 (en) 2004-11-19 2012-11-27 Rubin Patti D Compressed growing medium
US8544206B2 (en) 2004-11-19 2013-10-01 Patti D. Rubin Compressed growing medium
EP2189573A1 (en) * 2005-07-21 2010-05-26 Italgreen S.p.A. Artificial turf structure and method of manufacturing thereof
EP1907628B1 (en) * 2005-07-21 2013-01-02 Italgreen S.p.A. Artificial turf structure and production method therefore
US8563099B2 (en) 2005-07-21 2013-10-22 Italgreen S.P.A. Artificial turf structure and production method therefore
WO2008074310A3 (en) * 2006-12-21 2008-09-25 E & W Greenland Gmbh Material for the production of a molded body, and a molded body
WO2008074310A2 (en) * 2006-12-21 2008-06-26 E & W Greenland Gmbh Material for the production of a molded body, and a molded body
ITUD20090186A1 (en) * 2009-10-20 2011-04-21 S I T T A S R L PROCEDURE FOR THE IMPLEMENTATION OF BALES MATERIAL FOR ANIMAL BEDDING AND BALES MATERIALS OBTAINED
WO2020106484A1 (en) * 2018-11-19 2020-05-28 Shoup David E Turf and lawn coir
ES2841780A1 (en) * 2018-11-19 2021-07-09 Genus Ind Llc Dba Icoir Products Group Turf and lawn coir
US11737402B2 (en) 2018-11-19 2023-08-29 Genus Industries, Llc Turf and lawn coir
US11758855B2 (en) 2018-11-19 2023-09-19 Genus Industries, Llc Turf and lawn coir

Also Published As

Publication number Publication date
EP1608724A1 (en) 2005-12-28
GB0305191D0 (en) 2003-04-09

Similar Documents

Publication Publication Date Title
US5188064A (en) Clumping cat litter
US5230305A (en) Scoopable cat litter and method
CA1161020A (en) Aggregate composition and method for making same
US20080223302A1 (en) Animal Litter, Process for Preparing Animal Litter, and Method of Removal of Animal Waste
JP2004525211A (en) Compressed mixture of coconut coir pith and non-coir / non-peat material and method for producing the same
US5648306A (en) Process for producing sorbents based on smectites to absorb liquids
SK7532003A3 (en) Litter for cats and small animals
US6863027B1 (en) Method of making coconut coir pitch cat litter from powder created from crushed coconut husks
KR100912663B1 (en) Charcoal using coconut shells and method for manufacturing the same
EP1608724A1 (en) Coir pith
JP2010148444A (en) Toilet sand for pet and method for producing toilet sand for pet
WO1994021731A2 (en) Biodegradable films and molded products and process for their production
JPH0987646A (en) Production of solid fuel using organic waste
US20180007861A1 (en) Animal litter compositions
JPH0678643A (en) Material for treating excreta of pet
US20180263210A1 (en) Litter for use in animal keeping
JP3692352B2 (en) Animal manure treatment material
WO2013021406A1 (en) Biodegradable granular composition used as animal litter and disposable in toilets
JP2013244478A (en) Porous and solid water/odor adsorbent and method for producing the same
JP3150867B2 (en) Adsorption / deodorant and adsorption mat
CN101108332A (en) Drying agent for pet house and method of preparing the same and application thereof
JPH0690633A (en) Pet excreta treating material
JP3717468B2 (en) Animal excrement disposal material and method for producing the same
KR100701523B1 (en) Sound Absorption Materials
KR100420207B1 (en) Loess matt

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BW BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE EG ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NA NI NO NZ OM PG PH PL PT RO RU SC SD SE SG SK SL SY TJ TM TN TR TT TZ UA UG US UZ VC VN YU ZA ZM ZW

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): BW GH GM KE LS MW MZ SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IT LU MC NL PL PT RO SE SI SK TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG

121 Ep: the epo has been informed by wipo that ep was designated in this application
WWE Wipo information: entry into national phase

Ref document number: 2004718343

Country of ref document: EP

WWP Wipo information: published in national office

Ref document number: 2004718343

Country of ref document: EP

WWW Wipo information: withdrawn in national office

Ref document number: 2004718343

Country of ref document: EP