GB2262536A - Combustible wood product - Google Patents
Combustible wood product Download PDFInfo
- Publication number
- GB2262536A GB2262536A GB9220907A GB9220907A GB2262536A GB 2262536 A GB2262536 A GB 2262536A GB 9220907 A GB9220907 A GB 9220907A GB 9220907 A GB9220907 A GB 9220907A GB 2262536 A GB2262536 A GB 2262536A
- Authority
- GB
- United Kingdom
- Prior art keywords
- sticks
- distillation
- product
- oils
- softwood
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS 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
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/44—Solid fuels essentially based on materials of non-mineral origin on vegetable substances
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Fats And Perfumes (AREA)
- Chemical And Physical Treatments For Wood And The Like (AREA)
Abstract
Controlled distillation of softwood timber sticks in the presence of a restricted supply of oxygen removes water, alcohol and other volatiles boiling at less than about 110 DEG C at ambient temperature, and is terminated while the sticks remain intact with a substantially cellulosic molecular structure. The processed sticks are resistant to crumbling and gold yellow to pale brown in colour, and contain at least 4% by weight of oils and resins boiling at at least 120 DEG C at ambient pressure. As exemplified the distillation involves raising the temperature of a distillation vessel slowly from 40 - 110 DEG C over fifteen hours and thereafter increasing the temperature to about 120 DEG C over thirty minutes.
Description
wood Product
The present invention is concerned with wood products and in particular, wood distillation products.
The controlled pyrolysis of wood to charcoal has been knout since time immemorial. The charcoal process involves expulsion and combustion of volatiles, and conversion of cellulose to substantially pure ( > 99%) carbon, under conditions of restricted access to oxygen to avoid combustion of the carbon. Also known since ancient times are processes of wood distillation in which the object is to produce valuable chemicals, such as methanol, acetic acid, turpentine, rosin and the like.
Gums and resins like turpentine and rosin are typically present in softwoods (coniferous woods) in amounts up to 6 to 10 < c, whereas in hardu-ood (deciduous or broadleafed woods the proportion of gums and resins is typically only 1 to 3%. Charcoal is therefore normally made commercially from hardwoods in order to avoid the protracted processing needed for producing charcoal from softwoods.
Softwoods are also commonly destructively distilled to extract products such as turpentine, rosin, rosin oil, pine oil, pine tar and pitch, the residue being charcoal.
FR 2512053 is concerned with roasting of ligneous materials wherein fragmented ligneous starting materials are roasted at a temperature of 200 to 280t'C to produce a product with a substantially intact cellulosic structure and increased exothermic value. The product is distinguishable from both wood and charcoal.
The process disclosed by FR 2512053 may be used for roasting an extremely wide range of ligneous starting materials. The specification teaches that wood, bark, sa xdust, rice balls. nut shells, kernels, straw and flax are all suitable starting materials.
There is no clear statement of preferred ligneous starting material; the only starting materials exemplified are oak (a hardwood) and saudust. There is no hint or suggestion tat the use ot softwood might be advantageous, or of a lox: temperature distillation process.
I have now developed a method of low temperature distillation which utilises softwoods as a starting material, and have found that it is desirable for some purposes to stop the distillation of softwoods at an early stage, when substantially all the water has been removed .
According to a first aspect of the invention therefore, there is provided a method of distillation of a plurality of sticks (typically logs, split wood or planks) of softwood timber, which comprises controlled distillation of said sticks in the presence of a restricted supply of oxygen so as to substantially remove water, alcohols and other volatiles boiling at less than about 110 C at ambient pressure, and terminating said distillation such that the processed sticks remain intact with a molecular structure substantially in cellulose form such that the bulk of said processed sticks is resistant to crumbling and gold yellow to pale brown in colour, said processed sticks containing at least 4% based on the weight of the sticks, of oils and resins boiling at at least 1200C at ambient pressure.
A method according to the present invention is a relatively slow distillation process which allows an equilibrium to be established within a distillation vessel and thereby produces a substantially homogeneous product which differs from that obtained a roasting process as described by FR-2512053.
If the distillation according to the present invention is taken further, there arises a product of higher calorific value, but the cellulosic molecular structure is impaired and the loss of the natural oils impairs the flammability of the processed sticks.
The product of the method just described is highly combustible and burns with a smokeless yellow flame in a manner similar to charcoal soaked in turpentine (although, of course, the product according to the invention retains its structural integrity, which is, of course, a significant difference relative to turpentine-soaked charcoal).
It is further preferred that the method involves splitting of the processed timber sticks, such that the resultant product comprising a plurality of sticks each having a maximum thickness of less than about 2cm, and preferably of thickness of about 0.5cm.
The softwood sticks used as starting material in a method according to the present invention are typically logs, planks or split wood having diameters of up to about locum and lengths in the range of 150 to 200cm. Such softwood sticks would not be suitable to be used in a method as disclosed by FR 2512053, as such a method uses a preferred starting material comprising a fragmented ligneous material.
The present invention therefore further comprises a combustible product conaprising, a plurality of sticks of softwood, said softwood of said product retaining its structural integrity and comprising a cellulosic molecular structure, being substantially free of moisture, alcohol and other volatiles boiling at less than about 110"C at ambient pressures, and containing at least 4% of oils and resins boiling at at least 1200C at ambient pressure.
The oils and resins generally comprise turpentine or rosin (a principal constituent of which is abietic acid and its anhydride) as well as rosin oils, pine oils dipentenes, and the like natural oils and resins.
The plurality of sticks of the combustible product according to the invention each typically have a maximum thickness of less than about 2cm, preferably about 0.5cm, and are preferably provided in sealed, substantially waterproof packaging comprising sheet or tilt material (such as plastics bags or sacks!. The product, which has an appreciably higher calorific value than the air-dried wood, is useful as a firelighter material because it is easily ignitable ard sustains a regular flame.
The present invention therefore further comprises a method of ignition of carbonaceous material (such as charcoal, coal or the likei which comprises igniting the product according to the invention with discrete sticks of said product arranged around said carbonaceous material.
The softood used in the method according to the invention mav be European larch Noruetian spruce, Scots pine or the like. The distillation may be effected in distillation vessels such as charcoal kilns. distillation units, or oil baths. in the latter case direct contact between the timber and oil is substantially obviated. Heating is gradual during the distillation, with restricted access to air so as to preclude flame generation. degradation or des+rilctive distillation of the soft!ood.
During a first distillation stage of the method according to the present invention, the operating temperature of the distillation vessel is slowly raised from 40 to 110"C over a period of about fifteen hours in order to drive off water and softwood volatiles boiling at less than 110"C at ambient pressure.
Following the first distillation stage, the operating temperature is further raised for about thirty minutes until a temperature of about 1200C is attained, when a yellow distillate characteristic of a product according to the present invention is observed. The distillation is terminated on observation of the yellow distillate to ensure that the resultant product contains at least 4% by weight of the natural oils and resins boiling at at least 1200C at ambient pressure.
Claims (14)
1.A method of distillation of a starting material comprising a plurality of sticks of softwood timber, which comprises controlled distillation of said sticks in the presence
of a restricted supply of oxygen so as to substantially remove water, alcohols and
other volatiles boiling at less than about 110 C at ambient pressure, and terminating
said distillation such that the processed sticks remain intact with a molecular structure
substantially in the form of cellulose and that the bulk of said processed sticks is
resistant to crumbling and gold yellow to pale brown in colour, said processed sticks
containing at least 4%, based on the weight of the sticks, of oils and resins boiling
at at least 120"C at ambient pressure.
2. A method according to claim 1, wherein said starting material comprises a plurality
of softwood timber sticks, each having a diameter of up to 10cm and a length in the
range of 150 to 200cm.
3. A method according to claim 1 or 2. which comprises splitting of the processed
sticks, such that the split product comprises a plurality of sticks. each having a
maximum thickness of less than about 2cm.
A. A method according to claim 3, wherein said split product comprises a plurality of
sticks each having a maximum thickness of about 0.5cm.
5. A method according to any of claims 1 to A, which comprises a first distillation stage wherein the temperature of a distillation vessel is raised from about 40 C to 110 C over a period of about fifteen hours.
6. A method according to claim 5, wherein the temperature of said distillation vessel is
further raised to about 120 C over a period of about thirty minutes, following said
first distillation stage.
7. A method according to any of claims 1 to 6, wherein said distillation is terminated
on observation of a yellow distillate.
8. A method according to any of claims 1 to 7, wherein said softwood comprises
European larch, Norwegian spruce or Scots pine.
9. A combustible product comprising a plurality of sticks of softwood, said softwood of
said product retaining its structural integrity and comprising a cellulosic molecular
structure, being substantially free of moisture, alcohols and other volatiles boiling at
less than about 110 C at ambient pressures, and containing at least 4% of oils and
resins boiling at at least 1200C at ambient pressure.
10. A product according to claim 9, wherein said oils and resins comprise one or more
of turpentine, rosin, rosin oils, pine oils and dipentenes.
11. A product according to claim 9 or 10, wherein said plurality of sticks each have a
maximum thickness of less than about 2cm.
12. A product according to claim 11, wherein said plurality of sticks each have a
maximum thickness of about 0.5cm.
13. A sealed pack comprising substantially waterproof sheet or film material containing
therein a product according to any of claims 9 to 12.
14. A method of ignition of carbonaceous material which comprises igniting a product
according to any of claims 9 to 12 with discrete sticks of said product arranged
around said carbonaceous material.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB919126676A GB9126676D0 (en) | 1991-12-16 | 1991-12-16 | Wood product |
Publications (3)
Publication Number | Publication Date |
---|---|
GB9220907D0 GB9220907D0 (en) | 1992-11-18 |
GB2262536A true GB2262536A (en) | 1993-06-23 |
GB2262536B GB2262536B (en) | 1995-05-31 |
Family
ID=10706342
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB919126676A Pending GB9126676D0 (en) | 1991-12-16 | 1991-12-16 | Wood product |
GB9220907A Expired - Fee Related GB2262536B (en) | 1991-12-16 | 1992-10-05 | Wood product |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB919126676A Pending GB9126676D0 (en) | 1991-12-16 | 1991-12-16 | Wood product |
Country Status (1)
Country | Link |
---|---|
GB (2) | GB9126676D0 (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4553978A (en) * | 1981-08-28 | 1985-11-19 | Association Pour La Recherche Et Le Developpement Des Methodes Et Processus Industriels | Process for converting ligneous matter of vegetable origin by torrefaction, and product obtained thereby |
-
1991
- 1991-12-16 GB GB919126676A patent/GB9126676D0/en active Pending
-
1992
- 1992-10-05 GB GB9220907A patent/GB2262536B/en not_active Expired - Fee Related
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4553978A (en) * | 1981-08-28 | 1985-11-19 | Association Pour La Recherche Et Le Developpement Des Methodes Et Processus Industriels | Process for converting ligneous matter of vegetable origin by torrefaction, and product obtained thereby |
Also Published As
Publication number | Publication date |
---|---|
GB2262536B (en) | 1995-05-31 |
GB9126676D0 (en) | 1992-02-12 |
GB9220907D0 (en) | 1992-11-18 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PCNP | Patent ceased through non-payment of renewal fee |
Effective date: 20071005 |