EP1232047B1 - Method and device for treating wood and similar materials - Google Patents
Method and device for treating wood and similar materials Download PDFInfo
- Publication number
- EP1232047B1 EP1232047B1 EP00981456A EP00981456A EP1232047B1 EP 1232047 B1 EP1232047 B1 EP 1232047B1 EP 00981456 A EP00981456 A EP 00981456A EP 00981456 A EP00981456 A EP 00981456A EP 1232047 B1 EP1232047 B1 EP 1232047B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- pieces
- bath
- heating
- wood
- cooling
- 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.)
- Expired - Lifetime
Links
- 239000002023 wood Substances 0.000 title claims abstract description 56
- 238000000034 method Methods 0.000 title claims abstract description 36
- 239000000463 material Substances 0.000 title abstract description 28
- 238000001816 cooling Methods 0.000 claims abstract description 40
- 238000010438 heat treatment Methods 0.000 claims abstract description 39
- 238000011282 treatment Methods 0.000 claims abstract description 32
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 27
- 239000003755 preservative agent Substances 0.000 claims abstract description 14
- 238000007654 immersion Methods 0.000 claims abstract description 13
- 239000007788 liquid Substances 0.000 claims abstract description 11
- 239000003921 oil Substances 0.000 claims description 29
- 235000019198 oils Nutrition 0.000 claims description 29
- 238000012546 transfer Methods 0.000 claims description 18
- 238000009835 boiling Methods 0.000 claims description 10
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- 238000006073 displacement reaction Methods 0.000 claims description 3
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- 241000894007 species Species 0.000 description 3
- 238000005507 spraying Methods 0.000 description 3
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 2
- 235000014466 Douglas bleu Nutrition 0.000 description 2
- 229920002488 Hemicellulose Polymers 0.000 description 2
- 241000238631 Hexapoda Species 0.000 description 2
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- 238000002791 soaking Methods 0.000 description 2
- 239000011269 tar Substances 0.000 description 2
- 239000010875 treated wood Substances 0.000 description 2
- 235000013311 vegetables Nutrition 0.000 description 2
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- RBTBFTRPCNLSDE-UHFFFAOYSA-N 3,7-bis(dimethylamino)phenothiazin-5-ium Chemical compound C1=CC(N(C)C)=CC2=[S+]C3=CC(N(C)C)=CC=C3N=C21 RBTBFTRPCNLSDE-UHFFFAOYSA-N 0.000 description 1
- 241000208140 Acer Species 0.000 description 1
- 240000001606 Adenanthera pavonina Species 0.000 description 1
- 235000001674 Agaricus brunnescens Nutrition 0.000 description 1
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- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 240000000731 Fagus sylvatica Species 0.000 description 1
- 235000010099 Fagus sylvatica Nutrition 0.000 description 1
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- 240000004460 Tanacetum coccineum Species 0.000 description 1
- VXSIXFKKSNGRRO-MXOVTSAMSA-N [(1s)-2-methyl-4-oxo-3-[(2z)-penta-2,4-dienyl]cyclopent-2-en-1-yl] (1r,3r)-2,2-dimethyl-3-(2-methylprop-1-enyl)cyclopropane-1-carboxylate;[(1s)-2-methyl-4-oxo-3-[(2z)-penta-2,4-dienyl]cyclopent-2-en-1-yl] (1r,3r)-3-[(e)-3-methoxy-2-methyl-3-oxoprop-1-enyl Chemical class CC1(C)[C@H](C=C(C)C)[C@H]1C(=O)O[C@@H]1C(C)=C(C\C=C/C=C)C(=O)C1.CC1(C)[C@H](/C=C(\C)C(=O)OC)[C@H]1C(=O)O[C@@H]1C(C)=C(C\C=C/C=C)C(=O)C1 VXSIXFKKSNGRRO-MXOVTSAMSA-N 0.000 description 1
- OUFJROAVKKYZEN-UHFFFAOYSA-N [Cr].[Cu].[As] Chemical compound [Cr].[Cu].[As] OUFJROAVKKYZEN-UHFFFAOYSA-N 0.000 description 1
- 238000007605 air drying Methods 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 239000010775 animal oil Substances 0.000 description 1
- 239000008346 aqueous phase Substances 0.000 description 1
- 229910052785 arsenic Inorganic materials 0.000 description 1
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 1
- JEMGLEPMXOIVNS-UHFFFAOYSA-N arsenic copper Chemical compound [Cu].[As] JEMGLEPMXOIVNS-UHFFFAOYSA-N 0.000 description 1
- 239000003124 biologic agent Substances 0.000 description 1
- VEMKTZHHVJILDY-UXHICEINSA-N bioresmethrin Chemical compound CC1(C)[C@H](C=C(C)C)[C@H]1C(=O)OCC1=COC(CC=2C=CC=CC=2)=C1 VEMKTZHHVJILDY-UXHICEINSA-N 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 235000021588 free fatty acids Nutrition 0.000 description 1
- 239000013529 heat transfer fluid Substances 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229960000907 methylthioninium chloride Drugs 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 210000000056 organ Anatomy 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000003209 petroleum derivative Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000002028 premature Effects 0.000 description 1
- HYJYGLGUBUDSLJ-UHFFFAOYSA-N pyrethrin Natural products CCC(=O)OC1CC(=C)C2CC3OC3(C)C2C2OC(=O)C(=C)C12 HYJYGLGUBUDSLJ-UHFFFAOYSA-N 0.000 description 1
- 229940070846 pyrethrins Drugs 0.000 description 1
- 239000002728 pyrethroid Substances 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
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- 235000019871 vegetable fat Nutrition 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B27—WORKING OR PRESERVING WOOD OR SIMILAR MATERIAL; NAILING OR STAPLING MACHINES IN GENERAL
- B27K—PROCESSES, APPARATUS OR SELECTION OF SUBSTANCES FOR IMPREGNATING, STAINING, DYEING, BLEACHING OF WOOD OR SIMILAR MATERIALS, OR TREATING OF WOOD OR SIMILAR MATERIALS WITH PERMEANT LIQUIDS, NOT OTHERWISE PROVIDED FOR; CHEMICAL OR PHYSICAL TREATMENT OF CORK, CANE, REED, STRAW OR SIMILAR MATERIALS
- B27K1/00—Damping wood
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B27—WORKING OR PRESERVING WOOD OR SIMILAR MATERIAL; NAILING OR STAPLING MACHINES IN GENERAL
- B27K—PROCESSES, APPARATUS OR SELECTION OF SUBSTANCES FOR IMPREGNATING, STAINING, DYEING, BLEACHING OF WOOD OR SIMILAR MATERIALS, OR TREATING OF WOOD OR SIMILAR MATERIALS WITH PERMEANT LIQUIDS, NOT OTHERWISE PROVIDED FOR; CHEMICAL OR PHYSICAL TREATMENT OF CORK, CANE, REED, STRAW OR SIMILAR MATERIALS
- B27K3/00—Impregnating wood, e.g. impregnation pretreatment, for example puncturing; Wood impregnation aids not directly involved in the impregnation process
- B27K3/02—Processes; Apparatus
- B27K3/0207—Pretreatment of wood before impregnation
- B27K3/0221—Pore opening
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B27—WORKING OR PRESERVING WOOD OR SIMILAR MATERIAL; NAILING OR STAPLING MACHINES IN GENERAL
- B27K—PROCESSES, APPARATUS OR SELECTION OF SUBSTANCES FOR IMPREGNATING, STAINING, DYEING, BLEACHING OF WOOD OR SIMILAR MATERIALS, OR TREATING OF WOOD OR SIMILAR MATERIALS WITH PERMEANT LIQUIDS, NOT OTHERWISE PROVIDED FOR; CHEMICAL OR PHYSICAL TREATMENT OF CORK, CANE, REED, STRAW OR SIMILAR MATERIALS
- B27K5/00—Treating of wood not provided for in groups B27K1/00, B27K3/00
- B27K5/001—Heating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B27—WORKING OR PRESERVING WOOD OR SIMILAR MATERIAL; NAILING OR STAPLING MACHINES IN GENERAL
- B27K—PROCESSES, APPARATUS OR SELECTION OF SUBSTANCES FOR IMPREGNATING, STAINING, DYEING, BLEACHING OF WOOD OR SIMILAR MATERIALS, OR TREATING OF WOOD OR SIMILAR MATERIALS WITH PERMEANT LIQUIDS, NOT OTHERWISE PROVIDED FOR; CHEMICAL OR PHYSICAL TREATMENT OF CORK, CANE, REED, STRAW OR SIMILAR MATERIALS
- B27K5/00—Treating of wood not provided for in groups B27K1/00, B27K3/00
- B27K5/003—Treating of wood not provided for in groups B27K1/00, B27K3/00 by using electromagnetic radiation or mechanical waves
- B27K5/0055—Radio-waves, e.g. microwaves
Definitions
- the present invention relates to a method and a device for heat treatment and impregnation, essentially by immersion, wood or similar woody materials.
- Patent application EP-A-956 934 describes a process impregnating wood with a termite preservative and arylpyrazole type mushrooms, in which the mixture is heated to 350 ° C. wood to remove moisture and oils, placing it in an oven under an inert gas atmosphere for 5 minutes; the wood is then cooled to 20 ° C and immersed in an aqueous solution containing the agent of preservation for one hour.
- the impregnation of wood in preservatives depends on the composition and structure of the latter.
- the impregnation capacity is very variable from one species to another; beech, maple and charm soak up completely while the heart of other species is difficult accessible and only the sapwood can be significantly impregnated with preserving substances.
- some species, such as fir, spruce or Douglas fir can be very difficult to impregnate.
- the effectiveness of an impregnation treatment can be assessed at once by the quantity and depth of penetration of the preservative absorbed in the piece of wood.
- the processes ensuring low penetration depth let us quote in particular: the external application of the preservative using a brush, by sprinkling or spraying, by direct immersion in the treatment solution containing the preservation.
- Increasing penetration depth and impregnated quantities is generally obtained from a treatment in autoclave such as the process described in the document "Guide to the wood preservation ”, Michel RAYZAL, March 1998, Center technique du wood and furniture (CTBA) - 75012 PARIS, pages 62-67.
- CTBA Center technique du wood and furniture
- the autoclave treatment times are also long (several hours) and require long equipment downtimes.
- the object of the present invention is to provide an improved method wood treatment and a device for its implementation.
- the present invention also aims to remedy, in part at least, to the disadvantages of known methods.
- said part is heated in order to obtain an intense vaporization of a part water contained in the material.
- said part is suddenly cooled by placing contact with a "cold" liquid medium (the temperature of which is very below the boiling temperature of water at working pressure) containing the preservative (s).
- a "cold" liquid medium the temperature of which is very below the boiling temperature of water at working pressure
- This last step is carried out preferably by immersion in a (liquid) bath of the solution of which seeks to permeate the room.
- the invention is based on the generation of a strong pressure drop in wood fabrics (induced by intense vaporization) in the presence of high heat flux densities and a temperature of the material greater than or equal to the boiling point of water at the working pressure.
- This first step is followed by contacting the as fast as possible with the treatment solution at a very high temperature below the boiling point of water.
- To the internal overpressure of the first stage follows a depression during the second stage which is used for the impregnation of the pores and vessels of the piece of wood by capillary flow of the treatment solution in contact with its surface exterior.
- this transfer must be made in less than 30 seconds, especially in less than 10 seconds, for example in less than 3 or 5 seconds.
- This effect can, if necessary, be limited or even avoided by waterproofing or covering the ends of the part to be treated where the longitudinal fibers of the wood are exposed and which offer low pressure losses with gases and liquids; this further promotes the implementation internal removal of the piece of wood by heating.
- the maintaining the temperature of the atmosphere traversed by the material, during its transfer, at a temperature higher than the boiling point of water (at working pressure) by spraying liquid, hot air from steam or by additional heating (by infrared, high frequencies, microwave) will prevent early condensation of the vapor trapped in the porous matrix.
- the latter can finally be prevented by a transfer of the material with the atmosphere used during the first stage by means of a nacelle, a lock or any other adapted device.
- the parts to be treated are not dry; it is essential that the parts to be treated have humidity greater than 25%, in particular of the order of 40% to 80% (mass / mass dry); for this purpose the parts can if necessary be re-humidified before treatment by prolonged immersion in a tank of liquid water at ambient temperature.
- the latter is carried out in liquid medium in the treatment solution at a very less than the surface of the heated piece of wood.
- the gap between these last two temperatures are generally chosen above 40 ° C, in particular above 60 ° C.
- we maintain the bath temperature thanks to a cooling unit, a temperature generally below 90 ° C at atmospheric pressure, plus precisely located in the range of 10 ° C to 70 ° C.
- the treatment bath in which the cooling is carried out quick immersed parts to be treated, can essentially consist an aqueous phase containing hydrophilic preservatives (such as than Copper - Chromium-Arsenic), by creosotes diluted in petroleum, by an emulsion or a dispersion of these same agents in phases aqueous or hydrophobic, by one or a mixture of organic solvents.
- hydrophilic preservatives such as than Copper - Chromium-Arsenic
- creosotes diluted in petroleum by an emulsion or a dispersion of these same agents in phases aqueous or hydrophobic, by one or a mixture of organic solvents.
- an oil bath s
- preservatives hydrophobic for example pyrethrins and pyrethroids.
- the cooling in an oil bath can greatly reduce costs of the treatment solution and ensuring rapid cooling, about fifty degrees in less than 30 minutes, especially less than 10 minutes, under natural convection conditions (the oils are very thermodilatable fluids).
- we induce a tangential movement of the cold medium treating by relation to the parts is achieved, either by moving the parts, or by flow of the bath, either by a combination of these means (displacement pieces of wood on rails or carpets combined with a recirculation of the treatment solution in the cooling tank).
- the total duration of the treatment does not exceed four hours; for example the duration is of the order of 30 minutes at 1 hour (depending on the dimensions and the initial water content of the parts to be treated.
- the desired quality objective quantitative impregnated and / or penetration depth
- the heating is carried out in the presence of high flux densities and must lead to a boiling of the water in the material (ie vaporization of the water at the heart of the material under the effect of strong heat flux) ;
- the flux densities are generally at least equal to 10 kW / m 2 or 2 MW / m 3 , and in particular situated in the range from 10 kW / m 2 to 300 kW / m 2 (power related to the external surface of the parts treated), and / or in the range from 2 MW / m 3 to 20 MW / m 3 (power based on the volume of parts treated).
- Heating can be obtained by various processes which can be combined if necessary: radiation (infrared, high frequencies, ultra high frequencies), exposure to very hot air (eg combustion gas) or superheated steam , immersion in a fluid at high temperature (between 110 and 300 ° C at atmospheric pressure) whose boiling temperature is much higher than that of liquid water; in the latter case, the parts are preferably immersed in a bath of a similar nature to that used for cooling, in particular an oil bath maintained at a temperature between 110 and 250 ° C. at atmospheric pressure.
- radiation infrared, high frequencies, ultra high frequencies
- very hot air eg combustion gas
- superheated steam immersion in a fluid at high temperature (between 110 and 300 ° C at atmospheric pressure) whose boiling temperature is much higher than that of liquid water; in the latter case, the parts are preferably immersed in a bath of a similar nature to that used for cooling, in particular an oil bath maintained at a temperature between 110 and 250 ° C. at atmospheric pressure.
- an oil or a mixture of oils of animal, vegetable or mineral origin, in particular used vegetable oils, by-products of the food industry such as used frying oils.
- These inexpensive products are thermodegraded and therefore rich in surfactants (free fatty acids); they allow the use of preservatives hydrophilic or hydrophobic in the cooling bath.
- the use, for the cooling step, of an oil or of a treatment solution having the same hydrophobic character allows significantly reduce the costs of the impregnation solution and protect wood treated with a subsequent rewetting and its effects during a outdoor use (drying-rewetting cycles). These effects are responsible for the appearance and propagation of cracks in the periphery of the treated wood and constitute preferential routes of penetration of agents biological degradation of wood.
- the oil is used for its excellent fluid properties coolant in a two-phase medium (i.e. in the presence of steam) during the first stage.
- this first step can be accompanied by the strong fixation of fatty acids from the bath on celluloses and wood hemicelluloses, a very favorable reaction to the preservation of wood.
- the impregnation of the material in thermodegraded substances such as frying oils reduces very strongly the biological availability of the wood substrate for microorganisms and insects.
- the use of oils offers outlets for low-valued agro-food industry by-products and allows the material to be impregnated with biodegradable substances which will allow better compatibility of the materials produced with the environment during their use or recycling.
- each container receiving the bath includes means for holding pieces of wood in immersion total (the buoyancy of the material depending on the composition of the material and in particular its water content).
- immersion total the buoyancy of the material depending on the composition of the material and in particular its water content.
- These devices can be fixed or mobile, in the latter case they are also used for moving pieces in the bath.
- the two containers (or bins) must be contiguous preference; they can be obtained by equipping a tank with a partition wall physically and thermally insulating the bath heating the cooling bath. This separation can be total or partial.
- the transfer of parts from the first to second bath can be obtained without contact with the gas atmosphere present above the baths; for this purpose, the device may include a airlock (or "lock") fitted with devices for holding parts in immersion during their transfer.
- the bins are preferably covered, at least in part, by a cover making it possible to reproduce an enclosure of confinement under slight overpressure.
- the invention consists of a piece of wood, which is likely to be obtained, directly or indirectly, by a process according to the invention, part of which (or peripheral layer) at less is impregnated with a preservative; said part or layer is impregnated with an impregnation vector chosen from mineral oils, animal oils, vegetable oils, solvents (creosotes, tars, mineral oils from the fractionation of petroleum products, extracts vegetable in mineral solvents or not); in addition, a part (layer) can be roasted (partial charring), as a result of surface heating, especially in a high oil bath temperature (between 110 and 250 ° C at atmospheric pressure).
- the average water content of the part (in particular of said layer in peripheral part) will be less than 0.3 kg or 0.4 kg of water per kg of non-oily dry matter, in particular less than 0.1 kg / kg.
- Content average in impregnation solution (in particular oil) of said impregnated layer will generally be of the order of 0.05 to 2 kg of oil per kg non-oily dry matter.
- the thickness of the impregnated layer is in the order of 1 to 100 mm depending on the direction in which the pieces of wood are cut by relation to the orientation of the cellular elements of the wood, in particular of around 5 to 50 mm for a log 200 mm in diameter.
- the thickness mean of the roasted surface layer characterized by alteration hemicellulose and amorphous cellulose molecules (decrease significant of the number of hydroxyl groups associated with a partial crosslinking) and the appearance of pyrolysis products, may be about 0.5 to 2 cm (it depends very much on time and temperature treatment).
- FIG. 7 presents a schematic cross section of a piece of wood treated according to the invention.
- Each of the devices 1 comprises a tank 2 containing the bath 3 of heating of pieces 4 of wood, and a tank 5 containing the bath 6 of cooling and processing these same parts.
- the tank 2 is equipped with a connected heat exchanger 7 by conduits 50 to a heating device (not shown) of a heat transfer fluid circulating in the exchanger 7 and the conduits 50.
- the tank 5 is equipped with a heat exchanger 8 connected by conduits 51 to a cooling unit (not shown) of a coolant circulating in the exchanger 8 and the conduits 51.
- each tray 2, 5 is respectively equipped with a member 10, 12 ensuring immersion.
- This member 10, 12 can be fixed and be in the form of a rail flush with or immersed in the surface of the bath; alternately this member can be mobile and can be in the form of a conveyor belt, chain or cable; in this case, it can be equipped with organs protrusions forming fingers capable of moving parts 4 in motion in the baths, as schematically represented by the arrows 11, 13.
- One or two conveyor (s) 14a, 14b, 14c (figures 1 and 3) of structure similar can be used to quickly transfer parts 4 from bath 3 to bath 6: each of these conveyors has a cable 52 fitted of fingers 53 for driving parts 4; conventionally, each cable shaped in a closed loop, extends between two pulleys or rollers rotated by an actuator along perpendicular axes in terms of figures.
- such a conveyor 14a partially immersed in bath 3 is used to move (arrow 55) the pieces 4 along an inclined wall 54 of the tank 2, so as to cause them to fall (arrow 56) into the bath 6.
- two conveyors 14b, 14c similarly transfer the pieces 4 from tray 2 to tray 5 by sliding and / or rolling on the inclined walls 54, 57 (respectively up and down) of these 2 tanks; the bins are joined by the edge common superior of the two walls 54, 57.
- a single conveyor 14 the central part of the longitudinal profile is curved to extend substantially parallel to the inclined walls 54, 57 through which the trays are connected, fulfills both the function of drive in motion parts 4 in the baths 3, 6, for keeping these parts immersed in these baths, and transfer of the parts from the first to the second bath.
- one or more pumps and / or agitators can contribute to the relative movement of the pieces of wood with the treatment solution.
- a cover 16 equipped with a nozzle 18 for injection (arrow 58) of a hot gas covers zone 9 of transfer between the tanks.
- the heating of rooms 4 can be obtained and / or supplemented by the action of a device as marked 17 which diffuses into the enclosure 59 of processing delimited by the cover 16 and the tanks 2, 5, microwaves or infrared radiation.
- the transfer from one bin to the other is obtained by pivoting 60 along the axis 61 (perpendicular to the plane of the figure), of a basket 62 mounted at the end of an arm 63.
- this transfer is obtained by a similar pivoting of a partially submerged airlock with four flaps 64 whose transverse profiles form a cross; the extremities of the two flaps located in the lower part slide, during the pivoting of the airlock, along a wall 65 in the form of a cylinder portion with a horizontal axis, which wall extends at the upper end of a partition 66 separating the trays 2, 5; the space 67 delimited by the two lower flaps and the wall 65 is adapted to receive one or more pieces 4; flap rotation of the airlock according to the arrow (anti-clockwise) causes the transfer of the parts of the bath 3 to bath 6 without emersion.
- the device illustrated in FIG. 6 has two structures similar to that of Figure 3, which are arranged end to end and connected by a additional transfer device capped with a structure 16, 18 of protection; this device allows a treatment comprising successively a first heating, a first cooling, a second heating and a second cooling.
- FIG. 7 The cross section of a treated axis 4b post which is illustrated Figure 7 shows the impregnated layer 4c of thickness 4d, the part of which 4th roasted device of thickness 4f.
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- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Wood Science & Technology (AREA)
- Forests & Forestry (AREA)
- Physics & Mathematics (AREA)
- Electromagnetism (AREA)
- Mechanical Engineering (AREA)
- Chemical And Physical Treatments For Wood And The Like (AREA)
Abstract
Description
La présente invention est relative à un procédé et à un dispositif pour le traitement thermique et l'imprégnation, essentiellement par immersion, du bois ou des matériaux ligneux similaires.The present invention relates to a method and a device for heat treatment and impregnation, essentially by immersion, wood or similar woody materials.
Il existe de nombreux procédés de préservation du bois en vue d'améliorer sa résistance aux attaques par des agents biologiques tels que les termites ou autres insectes xylophages et les pourritures (cubiques, fibreuses ou molles). Ils se distinguent d'une part par l'agent ou la solution d'imprégnation utilisé(e), et d'autre part par le procédé permettant d'introduire et de fixer cet agent (ou la solution à imprégner) à l'intérieur des pièces ou structures de bois à traiter.There are many wood preservation processes in sight to improve its resistance to attack by biological agents such as termites or other wood-eating insects and rot (cubic, fibrous or soft). They are distinguished on the one hand by the agent or the solution impregnation used, and on the other hand by the process allowing to introduce and fix this agent (or the solution to be impregnated) inside pieces or structures of wood to be treated.
La demande de brevet EP-A-956 934 décrit un procédé d'imprégnation de bois par un agent de préservation contre les termites et les champignons de type arylpyrazole, dans lequel on chauffe à 350°C le bois pour en enlever l'humidité et les huiles, en le plaçant dans un four sous atmosphère gazeuse inerte pendant 5 minutes ; le bois est ensuite refroidi jusqu'à 20°C et plongé dans une solution aqueuse contenant l'agent de préservation pendant une heure.Patent application EP-A-956 934 describes a process impregnating wood with a termite preservative and arylpyrazole type mushrooms, in which the mixture is heated to 350 ° C. wood to remove moisture and oils, placing it in an oven under an inert gas atmosphere for 5 minutes; the wood is then cooled to 20 ° C and immersed in an aqueous solution containing the agent of preservation for one hour.
Un autre procédé d'imprégnation de bois est mentionné dans la demande de brevet CA-A-976 813.Another wood impregnation process is mentioned in patent application CA-A-976 813.
L'imprégnation du bois en produits de préservation dépend de la composition et de la structure de ce dernier. La capacité d'imprégnation est très variable d'une essence à l'autre ; le hêtre, l'érable et le charme s'imprègnent en totalité alors que le coeur d'autres essences est difficilement accessible et seul l'aubier peut être significativement imprégné en substances de préservation. Enfin, certaines essences, telles que le sapin, l'épicéa ou le douglas, peuvent être très difficilement imprégnés.The impregnation of wood in preservatives depends on the composition and structure of the latter. The impregnation capacity is very variable from one species to another; beech, maple and charm soak up completely while the heart of other species is difficult accessible and only the sapwood can be significantly impregnated with preserving substances. Finally, some species, such as fir, spruce or Douglas fir can be very difficult to impregnate.
L'efficacité d'un traitement d'imprégnation peut être évaluée à la fois par la quantité et la profondeur de pénétration de l'agent de préservation absorbé dans la pièce de bois. Parmi les procédés assurant une faible profondeur de pénétration, citons en particulier : l'application externe de l'agent conservateur à l'aide d'un pinceau, par aspersion ou pulvérisation, par immersion directe dans la solution de traitement contenant l'agent de préservation. L'augmentation de la profondeur de pénétration et des quantités imprégnées est généralement obtenue à partir d'un traitement en autoclave tel que le procédé décrit par le document « Guide de la préservation du bois », Michel RAYZAL, Mars 1998, Centre technique du bois et de l'ameublement (CTBA) - 75012 PARIS, pages 62-67.The effectiveness of an impregnation treatment can be assessed at once by the quantity and depth of penetration of the preservative absorbed in the piece of wood. Among the processes ensuring low penetration depth, let us quote in particular: the external application of the preservative using a brush, by sprinkling or spraying, by direct immersion in the treatment solution containing the preservation. Increasing penetration depth and impregnated quantities is generally obtained from a treatment in autoclave such as the process described in the document "Guide to the wood preservation ”, Michel RAYZAL, March 1998, Center technique du wood and furniture (CTBA) - 75012 PARIS, pages 62-67.
L'inconvénient majeur de ces traitements réside dans l'utilisation d'enceinte et de pompes permettant la réalisation de cycles vide - pression dont les coûts d'investissement et de fonctionnement (énergie essentiellement) sont élevés. De plus, la réalisation d'une qualité d'imprégnation donnée requiert un séchage préalable du bois - coûteux énergétiquement et long - ainsi qu'un pilotage et un contrôle délicats des cycles de pression et de vide.The major drawback of these treatments is the use enclosure and pumps allowing the realization of vacuum - pressure cycles including investment and operating costs (energy essentially) are high. In addition, achieving quality given impregnation requires pre-drying the wood - expensive energetically and long - as well as delicate steering and control of pressure and vacuum cycles.
Les temps de traitement en autoclave sont en outre longs (plusieurs heures) et nécessitent de longues immobilisations des équipements.The autoclave treatment times are also long (several hours) and require long equipment downtimes.
La présente invention a pour objet de proposer un procédé amélioré de traitement du bois et un dispositif permettant sa mise en oeuvre.The object of the present invention is to provide an improved method wood treatment and a device for its implementation.
La présente invention a également pour objet de remédier, en partie au moins, aux inconvénients des procédés connus.The present invention also aims to remedy, in part at least, to the disadvantages of known methods.
Dans un procédé de traitement d'une pièce de bois selon l'invention, on chauffe ladite pièce afin d'obtenir une vaporisation intense d'une partie de l'eau contenue dans le matériau. Avant que la teneur en eau au coeur de la pièce soit inférieure au point de saturation des fibres (c'est-à-dire soit située dans une plage allant de 20 % à 60 %, en particulier entre 30% et 40% masse/masse sèche), on refroidit brutalement ladite pièce par mise en contact avec un milieu liquide "froid" (dont la température est très inférieure à la température d'ébullition de l'eau à la pression de travail) contenant le ou les agents de préservation. Cette dernière étape est réalisée de préférence par l'immersion dans un bain (liquide) de la solution dont on cherche à imprégner la pièce.In a method of treating a piece of wood according to the invention, said part is heated in order to obtain an intense vaporization of a part water contained in the material. Before the water content at the heart of the part is below the fiber saturation point (i.e. either located in a range from 20% to 60%, in particular between 30% and 40% mass / dry mass), said part is suddenly cooled by placing contact with a "cold" liquid medium (the temperature of which is very below the boiling temperature of water at working pressure) containing the preservative (s). This last step is carried out preferably by immersion in a (liquid) bath of the solution of which seeks to permeate the room.
Il a été constaté expérimentalement que, lors de ce refroidissement, le liquide de traitement pénètre jusqu'à une profondeur significative dans la pièce de bois. Cette pénétration résulte de la forte dépression crée par la condensation brutale de la vapeur résiduelle précédemment créé. Le pouvoir de succion (ou aspiration), ainsi généré, permet l'imprégnation importante des vides initiaux ou laissés par le départ de l'eau lors de la première étape.It has been found experimentally that, during this cooling, the treatment liquid penetrates to a significant depth in the piece of wood. This penetration results from the strong depression created by the brutal condensation of the residual vapor previously created. The power of suction (or aspiration), thus generated, allows impregnation significant of the initial voids or those left by the departure of the water during the first stage.
En d'autres termes, l'invention repose sur la génération d'une forte perte de charge dans les tissus du bois (induite par la vaporisation intense) en présence de fortes densités de flux de chaleur et d'une température du matériau supérieure ou égale à la température d'ébullition de l'eau à la pression de travail. Cette première étape est suivie d'une mise en contact la plus rapide possible avec la solution de traitement à une température très inférieure à la température d'ébullition de l'eau. A la surpression interne de la première étape succède une dépression lors de la seconde étape qui est utilisée pour l'imprégnation des pores et vaisseaux de la pièce de bois par écoulement capillaire de la solution de traitement en contact avec sa surface extérieure.In other words, the invention is based on the generation of a strong pressure drop in wood fabrics (induced by intense vaporization) in the presence of high heat flux densities and a temperature of the material greater than or equal to the boiling point of water at the working pressure. This first step is followed by contacting the as fast as possible with the treatment solution at a very high temperature below the boiling point of water. To the internal overpressure of the first stage follows a depression during the second stage which is used for the impregnation of the pores and vessels of the piece of wood by capillary flow of the treatment solution in contact with its surface exterior.
A cet effet, il est essentiel d'éviter la mise en contact prolongée de la pièce chauffée, lors de son transfert vers le bain de refroidissement contenant le ou les agents de préservation, avec une phase intermédiaire non traitante (gazeuse, en particulier avec l'air ambiant), qui serait susceptible de "remplir" les vaisseaux du bois aux lieux et place du produit de traitement. De préférence, ce transfert doit être effectué en moins de 30 secondes, en particulier en moins de 10 secondes, par exemple en moins de 3 ou 5 secondes. Cet effet, pourra, si nécessaire, être limité voire évité par l'imperméabilisation ou le recouvrement des extrémités de la pièce à traiter où affleurent les fibres longitudinales du bois et qui offrent de faibles pertes de charge aux gaz et liquides ; ceci favorise en outre la mise en suppression interne de la pièce de bois par le chauffage. De même, le maintien de la température de l'ambiance traversée par le matériau, lors de son transfert, à une température supérieure à la température d'ébullition de l'eau (à la pression de travail) par pulvérisation de liquide, d'air chaud de vapeur ou par un chauffage complémentaire (par infra-rouges, hautes fréquences, micro-ondes) permettra d'éviter une condensation anticipée de la vapeur piégée dans la matrice poreuse. Cette dernière pourra enfin être prévenue par un transfert du matériau avec l'ambiance utilisée lors de la première étape au moyen d'une nacelle, d'une écluse ou de tout autre dispositif adapté.To this end, it is essential to avoid prolonged contact of the heated room, when transferred to the cooling bath containing the preservative (s), with an intermediate phase non-treating (gaseous, in particular with ambient air), which would likely to "fill" the wood vessels in places and place of the product treatment. Preferably, this transfer must be made in less than 30 seconds, especially in less than 10 seconds, for example in less than 3 or 5 seconds. This effect can, if necessary, be limited or even avoided by waterproofing or covering the ends of the part to be treated where the longitudinal fibers of the wood are exposed and which offer low pressure losses with gases and liquids; this further promotes the implementation internal removal of the piece of wood by heating. Likewise, the maintaining the temperature of the atmosphere traversed by the material, during its transfer, at a temperature higher than the boiling point of water (at working pressure) by spraying liquid, hot air from steam or by additional heating (by infrared, high frequencies, microwave) will prevent early condensation of the vapor trapped in the porous matrix. The latter can finally be prevented by a transfer of the material with the atmosphere used during the first stage by means of a nacelle, a lock or any other adapted device.
Contrairement aux procédés en autoclave qui utilisent, lors des cycles vide-pression, la variation de volume spécifique des gaz initialement présents dans le matériau, et donc un séchage préalable, il est essentiel, dans un procédé selon l'invention, que les pièces à traiter ne soient pas sèches ; il est indispensable que les pièces à traiter aient une humidité supérieure à 25 %, en particulier de l'ordre de 40 % à 80 % (masse/masse sèche) ; à cet effet les pièces peuvent le cas échéant être ré-humidifiées avant traitement par immersion prolongée dans un bac d'eau liquide à température ambiante.Unlike autoclave processes which use, during cycles vacuum-pressure, the variation of specific volume of gases initially present in the material, and therefore prior drying, it is essential, in a process according to the invention, that the parts to be treated are not dry; it is essential that the parts to be treated have humidity greater than 25%, in particular of the order of 40% to 80% (mass / mass dry); for this purpose the parts can if necessary be re-humidified before treatment by prolonged immersion in a tank of liquid water at ambient temperature.
Afin d'obtenir un refroidissement rapide, ce dernier est réalisé en milieu liquide dans la solution de traitement à une température très inférieure à celle de la surface de la pièce de bois chauffée. L'écart entre ces deux dernières températures est généralement choisi supérieur à 40°C, en particulier supérieur à 60°C. Dans la première étape, on chauffe à cet effet la pièce de bois jusqu'à une température supérieure à la température d'ébullition de l'eau en surface (de l'ordre de 110 à 180°C si l'opération est effectuée à pression atmosphérique) et à une température à coeur voisine de la température d'ébullition de l'eau (qui dépend de la pression de travail et de la surpression interne).Dans la deuxième étape, on maintient la température du bain, grâce à une unité de refroidissement, à une température généralement inférieure à 90°C à pression atmosphérique, plus précisément située dans la plage de 10°C à 70°C. Ces opérations, en particulier celle de refroidissement, sont de préférence effectuées à pression atmosphérique ou à une pression voisine de celle-ci. Dans le cas particulier où le chauffage est réalisé dans une enceinte fermée, la vapeur d'eau sortant de la pièce de bois peut être utilisée pour induire une élévation de la pression de travail dans l'enceinte et ainsi augmenter l'échauffement dans la pièce à traiter ; la condensation de la vapeur lors de la deuxième étape résultera alors de l'action simultanée du refroidissement et de la remise à pression atmosphérique (condensation isenthalphique de la vapeur dans ce dernier cas). In order to obtain rapid cooling, the latter is carried out in liquid medium in the treatment solution at a very less than the surface of the heated piece of wood. The gap between these last two temperatures are generally chosen above 40 ° C, in particular above 60 ° C. In the first step, we heat to this effect the piece of wood up to a temperature higher than the temperature boiling water on the surface (around 110 to 180 ° C if the operation is performed at atmospheric pressure) and at a core temperature close to the boiling point of water (which depends on the working pressure and internal pressure). In the second step, we maintain the bath temperature, thanks to a cooling unit, a temperature generally below 90 ° C at atmospheric pressure, plus precisely located in the range of 10 ° C to 70 ° C. These operations, in particularly that of cooling, are preferably carried out at atmospheric pressure or at a pressure close to it. In the case particular where the heating is carried out in a closed enclosure, the steam of water coming out of the piece of wood can be used to induce a increase in working pressure in the enclosure and thus increase overheating in the room to be treated; vapor condensation during the second step will then result from the simultaneous action of cooling and return to atmospheric pressure (isenthalphic condensation of the steam in the latter case).
Le bain de traitement, dans lequel est réalisé le refroidissement rapide des pièces à traiter immergées, peut être essentiellement constitué d'une phase aqueuse additionnée d'agents de préservation hydrophiles (tel que Cuivre - Chrome -Arsenic), par des créosotes diluées dans du pétrole, par une émulsion ou une dispersion de ces mêmes agents dans des phases aqueuses ou hydrophobes, par un ou un mélange de solvants organiques. Toutefois, l'utilisation d'un bain d'huile(s) (huiles minérales, huiles végétales ou graisses animales) additionné d'agents de préservation hydrophobes est privilégié (par exemple pyrèthres et pyrèthrinoïdes). Le refroidissement dans un bain d'huile(s) permet de réduire fortement les coûts de la solution de traitement et d'assurer un refroidissement rapide, d'une cinquantaine de degrés en moins de 30 minutes, en particulier en moins de 10 minutes, en conditions de convection naturelle (les huiles sont des fluides très thermodilatables). Afin de faciliter la circulation de la solution et d'homogénéiser le traitement entre les pièces de bois (traitement par lot), on induit un mouvement tangentiel du milieu froid traitant par rapport aux pièces est réalisé, soit par déplacement des pièces, soit par écoulement du bain, soit par une combinaison de ces moyens (déplacement des pièces de bois sur rails ou tapis combinés à une re-circulation de la solution de traitement dans le bac de refroidissement).The treatment bath, in which the cooling is carried out quick immersed parts to be treated, can essentially consist an aqueous phase containing hydrophilic preservatives (such as than Copper - Chromium-Arsenic), by creosotes diluted in petroleum, by an emulsion or a dispersion of these same agents in phases aqueous or hydrophobic, by one or a mixture of organic solvents. However, the use of an oil bath (s) (mineral oils, oils vegetable or animal fat) added with preservatives hydrophobic is preferred (for example pyrethrins and pyrethroids). The cooling in an oil bath can greatly reduce costs of the treatment solution and ensuring rapid cooling, about fifty degrees in less than 30 minutes, especially less than 10 minutes, under natural convection conditions (the oils are very thermodilatable fluids). In order to facilitate the circulation of solution and homogenize the treatment between the pieces of wood (treatment by batch), we induce a tangential movement of the cold medium treating by relation to the parts is achieved, either by moving the parts, or by flow of the bath, either by a combination of these means (displacement pieces of wood on rails or carpets combined with a recirculation of the treatment solution in the cooling tank).
Selon une caractéristique de l'invention, la durée totale du traitement n'excède pas quatre heures ; par exemple la durée est de l'ordre de 30 mn à 1 heure (en fonction des dimensions et de la teneur en eau initiale des pièces à traiter. Toutefois, selon l'objectif de qualité désiré (quantité imprégnée et/ou profondeur de pénétration), il est possible de réitérer plusieurs fois la séquence de chauffage-refroidissement. On pourra également, suivant l'anisotropie du bois traité et l'objectif recherché (une imprégnation par une ou les extrémités, imprégnation seulement superficielle), éventuellement recourir à une imperméabilisation partielle ou totale des extrémités de la pièce de bois (par voie chimique, physique ou mécanique).According to one characteristic of the invention, the total duration of the treatment does not exceed four hours; for example the duration is of the order of 30 minutes at 1 hour (depending on the dimensions and the initial water content of the parts to be treated. However, depending on the desired quality objective (quantity impregnated and / or penetration depth), it is possible to repeat several times the heating-cooling sequence. We will be able to also, depending on the anisotropy of the treated wood and the objective sought (a impregnation by one or the ends, impregnation only surface), possibly use partial waterproofing or total of the ends of the piece of wood (chemical, physical or mechanical).
Selon une autre caractéristique de l'invention, le chauffage est réalisé en présence de densités de flux élevés et doit conduire à une ébullition de l'eau dans le matériau (i.e. vaporisation de l'eau à coeur du matériau sous l'effet de fort flux de chaleur) ; les densités de flux sont généralement au moins égales à 10 kW/m2 ou à 2 MW/m3, et en particulier situées dans la gamme de 10 kW/m2 à 300 kW/m2 (puissance rapportée à la surface externe des pièces traitées), et/ou dans la gamme de 2 MW/m3 à 20 MW/m3 (puissance rapportée au volume des pièces traitées). Le chauffage peut être obtenu par différents procédés pouvant être le cas échéant combinés : rayonnement (infrarouge, hautes fréquences, ultra hautes fréquences), exposition à de l'air très chaud (ex. gaz de combustion) ou de la vapeur d'eau surchauffée, immersion dans un fluide à haute température (entre 110 et 300°C à pression atmosphérique) dont la température d'ébullition est très supérieure à celle de l'eau liquide ; dans ce dernier cas les pièces sont de préférence plongées dans un bain de nature similaire à celui utilisé pour le refroidissement, en particulier un bain d'huile maintenu à une température comprise entre 110 et 250°C à pression atmosphérique.According to another characteristic of the invention, the heating is carried out in the presence of high flux densities and must lead to a boiling of the water in the material (ie vaporization of the water at the heart of the material under the effect of strong heat flux) ; the flux densities are generally at least equal to 10 kW / m 2 or 2 MW / m 3 , and in particular situated in the range from 10 kW / m 2 to 300 kW / m 2 (power related to the external surface of the parts treated), and / or in the range from 2 MW / m 3 to 20 MW / m 3 (power based on the volume of parts treated). Heating can be obtained by various processes which can be combined if necessary: radiation (infrared, high frequencies, ultra high frequencies), exposure to very hot air (eg combustion gas) or superheated steam , immersion in a fluid at high temperature (between 110 and 300 ° C at atmospheric pressure) whose boiling temperature is much higher than that of liquid water; in the latter case, the parts are preferably immersed in a bath of a similar nature to that used for cooling, in particular an oil bath maintained at a temperature between 110 and 250 ° C. at atmospheric pressure.
Pour le bain d'huile chauffant, on peut utiliser une huile (ou un mélange d'huiles) d'origine animale, végétale, ou minérale, en particulier des huiles végétales usagées, sous-produits de l'industrie agroalimentaire telle que les huiles de friture usagées. Ces produits bon marché sont thermodégradés et donc riches en tensio-actifs (acides gras libres) ; ils permettent d'utiliser indifféremment des produits de préservation hydrophiles ou hydrophobes dans le bain de refroidissement.For the heating oil bath, an oil (or a mixture of oils) of animal, vegetable or mineral origin, in particular used vegetable oils, by-products of the food industry such as used frying oils. These inexpensive products are thermodegraded and therefore rich in surfactants (free fatty acids); they allow the use of preservatives hydrophilic or hydrophobic in the cooling bath.
De même l'utilisation, pour l'étape de refroidissement, d'une huile ou d'une solution de traitement ayant le même caractère hydrophobe, permet de réduire fortement les coûts de la solution d'imprégnation et de protéger le bois traité d'une réhumidification ultérieure et de ses effets lors d'une utilisation en extérieur (cycles de séchage-réhumidification). Ces effets sont responsables de l'apparition et de la propagation de fentes en périphérie du bois traité et constituent des voies préférentielles de pénétration des agents biologiques de dégradation du bois.Likewise the use, for the cooling step, of an oil or of a treatment solution having the same hydrophobic character, allows significantly reduce the costs of the impregnation solution and protect wood treated with a subsequent rewetting and its effects during a outdoor use (drying-rewetting cycles). These effects are responsible for the appearance and propagation of cracks in the periphery of the treated wood and constitute preferential routes of penetration of agents biological degradation of wood.
L'huile est utilisée pour ses excellentes propriétés de fluide caloporteur en milieu diphasique (i.e. en présence de vapeur) lors de la première étape. A haute température, cette première étape peut être accompagnée par la fixation forte des acides gras du bain sur les celluloses et hémicelluloses du bois, réaction très favorable à la préservation du bois. Lors de l'étape de refroidissement, l'imprégnation du matériau en substances thermodégradées telles que les huiles de friture réduit très fortement la disponibilité biologique du substrat bois pour les micro-organismes et insectes. Par ailleurs, l'utilisation d'huiles offre des débouchés à des sous-produits de l'industrie agro-alimentaire peu valorisés et permet d'imprégner le matériau en substances biodégradables qui permettront une meilleure compatibilité des matériaux produits avec l'environnement lors de leur utilisation ou recyclage.The oil is used for its excellent fluid properties coolant in a two-phase medium (i.e. in the presence of steam) during the first stage. At high temperature, this first step can be accompanied by the strong fixation of fatty acids from the bath on celluloses and wood hemicelluloses, a very favorable reaction to the preservation of wood. During the cooling step, the impregnation of the material in thermodegraded substances such as frying oils reduces very strongly the biological availability of the wood substrate for microorganisms and insects. In addition, the use of oils offers outlets for low-valued agro-food industry by-products and allows the material to be impregnated with biodegradable substances which will allow better compatibility of the materials produced with the environment during their use or recycling.
L'utilisation d'une étape de "friture" du bois (nommée ainsi par analogie avec l'utilisation des huiles dans le domaine alimentaire) suivie rapidement d'une immersion dans le milieu (la solution) dont on cherche à imprégner le matériau (bois) permet de réaliser à la fois :
- un ressuyage, voire un séchage complémentaire du matériau,
- un léger traitement thermique conduisant à une relaxation des contraintes mécaniques dans le matériau et à une légère torréfaction du bois (permettant d'obtenir une réduction partielle des réserves alimentaires que recherche les organismes responsables de la dégradation du matériau ligneux),
- une imprégnation en profondeur ne nécessitant pas l'usage d'un cycle de variation de pression du milieu entourant la pièce à traiter, comme c'est le cas dans un autoclave.
- drying, or even additional drying of the material,
- a slight heat treatment leading to a relaxation of the mechanical stresses in the material and to a slight roasting of the wood (making it possible to obtain a partial reduction of the food reserves that the organisms responsible for the degradation of the woody material are looking for),
- deep impregnation not requiring the use of a pressure variation cycle of the medium surrounding the part to be treated, as is the case in an autoclave.
Comparé aux autres modes de chauffage surfaciques (infrarouges, vapeur d'eau surchauffée) ou volumiques (micro-ondes, hautes fréquences), l'étape d'immersion dans un bain porté à une température au-dessus de la température d'ébullition de l'eau est intéressante pour le procédé d'imprégnation proposé par ce qu'elle permet :
- de forts flux de chaleur absorbés par le matériau, (qui permettent des débits évaporatoires élevés et d'une forte surpression (transitoire) dans le matériau,
- un traitement rapide (quelques minutes à dizaines de minutes),
- une mise en oeuvre aisée,
- le traitement direct de bois verts (i.e. humides et non imprégnables en l'état par les procédés précédemment décrits),
- le traitement thermique et les contraintes générées sont susceptibles d'améliorer l'imprégnabilité du matériau par l'ouverture continue du réseau cellulaire (ouverture d'opercules...),
- de faibles coûts d'investissement et de fonctionnement.
- strong heat fluxes absorbed by the material, (which allow high evaporative flows and a strong (transient) overpressure in the material,
- rapid processing (a few minutes to tens of minutes),
- easy implementation,
- direct treatment of green woods (ie moist and not impregnable in the state by the methods described above),
- the heat treatment and the stresses generated are likely to improve the impregnability of the material by the continuous opening of the cellular network (opening of lids ...),
- low investment and operating costs.
L'étape d'immersion dans la solution à traiter après vaporisation partielle de l'eau contenue dans le matériau permet :
- l'utilisation d'une dépression dynamique du fait de la modification de l'équilibre liquide-vapeur lors du refroidissement,
- une imprégnation profonde en présence de forts gradients de pression difficiles à générer par les procédés classiques,
- une réduction de la durée de traitement,
- un investissement réduit, une mise en oeuvre aisée,
- l'utilisation d'une grande variété de solutions d'imprégnation (aqueuses ou hydrophobes) dont les huiles et les alcools qui peuvent être difficilement utilisés dans les procédés classiques de vide-pression en autoclave (dans le cas de l'utilisation d'alcool additionné de substances de préservation, le solvant vecteur peut être secondairement éliminé par séchage à l'air).
- the use of a dynamic vacuum due to the modification of the liquid-vapor balance during cooling,
- a deep impregnation in the presence of strong pressure gradients difficult to generate by conventional methods,
- a reduction in the duration of treatment,
- reduced investment, easy implementation,
- the use of a wide variety of impregnating solutions (aqueous or hydrophobic) including oils and alcohols which can be difficult to use in conventional vacuum-pressure processes in an autoclave (in the case of the use of alcohol added with preserving substances, the carrier solvent can be secondarily removed by air drying).
Selon un autre aspect, l'invention consiste en un dispositif de traitement de bois qui comporte :
- des moyens de chauffage de pièces de bois en présence de fortes densités de flux de chaleur, dans une première enceinte ou conteneur,
- des moyens de refroidissement rapide de pièces de bois réalisé dans une (deuxième) enceinte ou conteneur, de préférence distincte de la première enceinte ou conteneur,
- des moyens de transfert (déplacement) rapide des pièces de bois de l'enceinte (ou du conteneur) où est réalisé chauffage vers le l'enceinte (ou le conteneur) où est réalisé le refroidissement.
- means for heating pieces of wood in the presence of high densities of heat flow, in a first enclosure or container,
- means for rapidly cooling pieces of wood produced in a (second) enclosure or container, preferably separate from the first enclosure or container,
- means for rapid transfer (movement) of the wooden pieces of the enclosure (or of the container) where heating is carried out towards the enclosure (or the container) where cooling is carried out.
Dans le cas où le chauffage et/ou le refroidissement sont obtenus par trempage des pièces de bois dans un bain, chaque conteneur recevant le bain comporte des moyens de maintien des pièces de bois en immersion totale (la flottabilité du matériau dépendant de la composition du matériau et notamment de sa teneur en eau). Ces dispositifs peuvent être fixes ou mobiles, dans ce dernier cas ils servent également au déplacement des pièces dans le bain. Les deux conteneurs (ou bacs) doivent être de préférence contigus ; ils peuvent être obtenus en équipant un bac d'une cloison de séparation isolant physiquement et thermiquement le bain chauffant du bain de refroidissement. Cette séparation peut être totale ou partielle. Dans ce dernier cas, le transfert des pièces du premier au deuxième bain peut être obtenu sans contact avec l'atmosphère gazeuse présente au-dessus des bains ; à cet effet, le dispositif peut comporter un sas (ou "écluse") muni(e) de dispositifs pour le maintien des pièces en immersion pendant leur transfert. Les bacs sont de préférence recouverts, en partie au moins, par un capot permettant de reproduire une enceinte de confinement en légère surpression. Celle-ci permet i) de maximiser l'imprégnation lors de l'étape de refroidissement, ii) de limiter les risques de projection, iii) d'augmenter la température de l'atmosphère traversée par le matériau lors de son transfert (s'il a lieu en phase gazeuse) et de limiter la circulation d'air qui pourraient induire une condensation prématurée de la vapeur contenue dans le matériau, iv) de réaliser une aspersion éventuelle du matériau par de la vapeur d'eau surchauffée, de l'air très chaud, de l'huile à haute température. Dans tous les cas les dispositifs et leur conduite doivent permettre le maintien de la surpression dans le matériau bois et ainsi limiter le remplissage des vaisseaux par une phase gazeuse lors du transfert..In the case where the heating and / or cooling are obtained by soaking the pieces of wood in a bath, each container receiving the bath includes means for holding pieces of wood in immersion total (the buoyancy of the material depending on the composition of the material and in particular its water content). These devices can be fixed or mobile, in the latter case they are also used for moving pieces in the bath. The two containers (or bins) must be contiguous preference; they can be obtained by equipping a tank with a partition wall physically and thermally insulating the bath heating the cooling bath. This separation can be total or partial. In the latter case, the transfer of parts from the first to second bath can be obtained without contact with the gas atmosphere present above the baths; for this purpose, the device may include a airlock (or "lock") fitted with devices for holding parts in immersion during their transfer. The bins are preferably covered, at least in part, by a cover making it possible to reproduce an enclosure of confinement under slight overpressure. This allows i) to maximize impregnation during the cooling step, ii) limit the risks of projection, iii) to increase the temperature of the atmosphere traversed by the material during its transfer (if it takes place in the gas phase) and to limit air circulation that could induce premature condensation of the vapor contained in the material, iv) to carry out a possible spraying material by superheated steam, very hot air, oil at high temperature. In all cases the devices and their conduct must allow the overpressure in the wood material to be maintained and thus limit the filling of the vessels with a gas phase during the transfer..
Selon un autre aspect, l'invention consiste en une pièce de bois, qui est susceptible d'être obtenue, directement ou indirectement, par un procédé selon l'invention, dont une partie (ou couche périphérique) au moins est imprégnée d'un agent conservateur ; ladite partie ou couche est imprégnée d'un vecteur d'imprégnation choisi parmi les huiles minérales, les huiles animales, les huiles végétales, les solvants (créosotes, goudrons, huiles minérales issues du fractionnement de produits pétroliers, extraits végétaux dans des solvants minéraux ou non) ; en outre, une partie (couche) superficielle peut être torréfiée (carbonisation partielle), par suite d'un chauffage surfacique, en particulier dans un bain d'huile à haute température (entre 110 et 250°C à pression atmosphérique). Généralement, la teneur moyenne en eau de la pièce (en particulier de ladite couche en partie périphérique) sera inférieure à 0,3 kg ou 0,4 kg d'eau par kg de matière sèche non huileuse, en particulier inférieure à 0,1 kg/kg. La teneur moyenne en solution d'imprégnation (en particulier d'huile) de ladite couche imprégnée sera généralement de l'ordre de 0,05 à 2 kg d'huile par kg de matière sèche non huileuse. L'épaisseur de la couche imprégnée est de l'ordre de 1 à 100 mm suivant la direction coupe des pièces de bois par rapport à l'orientation des éléments cellulaires du bois, en particulier de l'ordre de 5 à 50 mm pour un rondin de 200 mm de diamètre. L'épaisseur moyenne de la couche superficielle torréfiée, caractérisée par une altération des molécules d'hemicellulose et cellulose amorphe (diminution significative du nombre de groupement hydroxyles associée à une réticulation partielle) et l'apparition de produits de pyrolyse, peut être de l'ordre de 0,5 à 2 cm (elle dépend très fortement des temps et températures de traitement).According to another aspect, the invention consists of a piece of wood, which is likely to be obtained, directly or indirectly, by a process according to the invention, part of which (or peripheral layer) at less is impregnated with a preservative; said part or layer is impregnated with an impregnation vector chosen from mineral oils, animal oils, vegetable oils, solvents (creosotes, tars, mineral oils from the fractionation of petroleum products, extracts vegetable in mineral solvents or not); in addition, a part (layer) can be roasted (partial charring), as a result of surface heating, especially in a high oil bath temperature (between 110 and 250 ° C at atmospheric pressure). Usually, the average water content of the part (in particular of said layer in peripheral part) will be less than 0.3 kg or 0.4 kg of water per kg of non-oily dry matter, in particular less than 0.1 kg / kg. Content average in impregnation solution (in particular oil) of said impregnated layer will generally be of the order of 0.05 to 2 kg of oil per kg non-oily dry matter. The thickness of the impregnated layer is in the order of 1 to 100 mm depending on the direction in which the pieces of wood are cut by relation to the orientation of the cellular elements of the wood, in particular of around 5 to 50 mm for a log 200 mm in diameter. The thickness mean of the roasted surface layer, characterized by alteration hemicellulose and amorphous cellulose molecules (decrease significant of the number of hydroxyl groups associated with a partial crosslinking) and the appearance of pyrolysis products, may be about 0.5 to 2 cm (it depends very much on time and temperature treatment).
D'autres avantages et caractéristiques de l'invention seront compris au travers de la description suivante qui se réfère aux dessins annexés, qui illustrent sans aucun caractère limitatif des modes préférentiels de réalisation de l'invention.Other advantages and characteristics of the invention will be understood through the following description which refers to the accompanying drawings, which illustrate without any limiting character preferential modes of realization of the invention.
Les figures de 1 à 6 présentent schématiquement 6 exemples de réalisations du procédé selon l'invention proposée, la figure 7 présente une coupe transversale schématique d'une pièce de bois traitée selon l'invention.Figures 1 to 6 schematically show 6 examples of embodiments of the method according to the proposed invention, FIG. 7 presents a schematic cross section of a piece of wood treated according to the invention.
Chacun des dispositifs 1 comporte un bac 2 contenant le bain 3 de
chauffage des pièces 4 de bois, et un bac 5 contenant le bain 6 de
refroidissement et de traitement de ces mêmes pièces.Each of the
A cet effet le bac 2 est équipé d'un échangeur thermique 7 raccordé
par des conduits 50 à un dispositif de chauffage (non représenté) d'un
fluide caloporteur circulant dans l'échangeur 7 et les conduits 50.For this purpose the
Dc façon similaire le bac 5 est équipé d'un échangeur thermique 8
raccordé par des conduits 51 à une unité de refroidissement (non
représentée) d'un fluide frigoporteur circulant dans l'échangeur 8 et les
conduits 51.Similarly, the
Afin de maintenir les pièces de bois (telles que planches, poutres,
piquets ou poteaux) immergées dans chaque bain 3, 6, chaque bac 2, 5 est
respectivement équipé d'un organe 10, 12 assurant l'immersion.In order to hold the pieces of wood (such as planks, beams,
stakes or posts) immersed in each
Cet organe 10, 12 peut être fixe et se présenter sous forme d'un rail
affleurant à la surface du bain ou immergé dans celui-ci ; alternativement
cet organe peut être mobile et peut se présenter sous forme d'un convoyeur
à bande, à chaíne ou à câble ; dans ce cas, il peut être équipé d'organes
saillants formant des doigts aptes à entraíner en mouvement les pièces 4
dans les bains, tel que schématiquement représenté par les flèches 11, 13.This
Un ou deux convoyeur(s) 14a, 14b, 14c (figures 1 et 3) de structure
similaire peu(ven)t être utilisé(s) pour transférer rapidement les pièces 4 du
bain 3 au bain 6 : chacun de ces convoyeurs comporte un câble 52 équipé
de doigts 53 d'entraínement des pièces 4 ; de façon classique, chaque câble
conformé en boucle fermée, s'étend entre deux poulies ou rouleaux
entraíné(es) en rotation par un actionneur selon des axes perpendiculaires
au plan des figures.One or two conveyor (s) 14a, 14b, 14c (figures 1 and 3) of structure
similar can be used to quickly transfer parts 4 from
bath 3 to bath 6: each of these conveyors has a
Dans le mode de réalisation illustré figure 1, un tel convoyeur 14a
partiellement immergé dans le bain 3, est utilisé pour déplacer (flèche 55)
les pièces 4 le long d'une paroi 54 inclinée du bac 2, de manière à
provoquer leur chute (flèche 56) dans le bain 6.In the embodiment illustrated in FIG. 1, such a
Dans le mode de réalisation illustré figure 3, deux convoyeurs 14b,
14c transfèrent manière similaire les pièces 4 du bac 2 au bac 5 par
glissement et/ou roulement sur les parois inclinées 54, 57 (respectivement
montantes et descendantes) de ces 2 bacs ; les bacs sont accolés par le bord
supérieur commun des deux parois 54, 57.In the embodiment illustrated in FIG. 3, two
Dans la variante illustrée figure 4, un convoyeur unique 14, dont la
partie centrale du profil longitudinal est incurvée pour s'étendre
sensiblement parallèlement aux parois inclinées 54, 57 par lesquelles les
bacs sont reliés, remplit à la fois la fonction d'entraínement en mouvement
des pièces 4 dans les bains 3, 6, de maintien de ces pièces immergées dans
ces bains, et de transfert des pièces du premier au deuxième bain. In the variant illustrated in Figure 4, a single conveyor 14, the
central part of the longitudinal profile is curved to extend
substantially parallel to the
Selon une variante non représentée une ou plusieurs pompes et/ou des agitateurs peuvent contribuer au déplacement relatif des pièces de bois avec la solution de traitement.According to a variant not shown, one or more pumps and / or agitators can contribute to the relative movement of the pieces of wood with the treatment solution.
Comme illustré figures 1 à 4 notamment, un capot 16 équipé d'une
buse 18 d'injection (flèche 58) d'un gaz chaud, recouvre la zone 9 de
transfert entre les bacs.As illustrated in FIGS. 1 to 4 in particular, a
Le chauffage des pièces 4 peut être obtenu et/ou complété par
l'action d'un dispositif tel que repéré 17 qui diffuse dans l'enceinte 59 de
traitement délimité par le capot 16 et les bacs 2, 5, des micro-ondes ou des
rayonnements infrarouges.The heating of rooms 4 can be obtained and / or supplemented by
the action of a device as marked 17 which diffuses into the
Dans la variante illustrée figure 2, le transfert d'un bac à l'autre est
obtenu par pivotement 60 selon l'axe 61 (perpendiculaire au plan de la
figure), d'un panier 62 monté à l'extrémité d'un bras 63.In the variant illustrated in Figure 2, the transfer from one bin to the other is
obtained by pivoting 60 along the axis 61 (perpendicular to the plane of the
figure), of a
Dans la variante illustrée figure 5, ce transfert est obtenu par un
pivotement similaire d'un sas partiellement immergé comportant quatre
volets 64 dont les profils transversaux forment une croix ; les extrémités
des deux volets situés en partie inférieure glissent, lors du pivotement du
sas, le long d'une paroi 65 en forme de portion de cylindre d'axe horizontal,
laquelle paroi s'étend à l'extrémité supérieure d'une cloison 66 séparant les
bacs 2, 5 ; l'espace 67 délimité par les deux volets inférieurs et la paroi 65
est adapté pour recevoir une ou plusieurs pièces 4 ; la rotation des volets
du sas selon la flèche (sens anti-horaire) provoque le transfert des pièces du
bain 3 au bain 6 sans émersion.In the variant illustrated in FIG. 5, this transfer is obtained by a
similar pivoting of a partially submerged airlock with four
Le dispositif illustré figure 6 comporte deux structures similaires à
celle de la figure 3, qui sont disposées bout à bout et reliées par un
dispositif supplémentaire de transfert coiffé d'une structure 16, 18 de
protection ; ce dispositif permet un traitement comportant successivement
un premier chauffage, un premier refroidissement, un deuxième chauffage
et un deuxième refroidissement.The device illustrated in FIG. 6 has two structures similar to
that of Figure 3, which are arranged end to end and connected by a
additional transfer device capped with a
La section transversale d'un poteau d'axe 4b traité qui est illustrée
figure 7 montre la couche 4c imprégnée d'épaisseur 4d, dont la partie
périphérique torréfiée 4e d'épaisseur 4f.The cross section of a treated axis 4b post which is illustrated
Figure 7 shows the impregnated layer 4c of thickness 4d, the part of which
4th roasted device of
Pour traiter un lot de 3 piquets de Douglas écorcé de 0,15 m de diamètre et 1.5 m de long dont la teneur en eau initiale était proche de 100% (kg/kg de masse sèche), on a utilisé deux bains d'huile de colza maintenus respectivement à 180°C et 35°C à pression atmosphérique. On a immergé les piquets, dont les extrémités avaient été préalablement imperméabilisées par trempage dans du goudron, dans le bain de chauffage pendant 60 minutes en prenant soin de permettre une circulation aisée de l'huile entre les poteaux par convection naturelle et d'assurer une compensation efficace de la chute de température du bain. Les piquets enserrés en leurs extrémités par des cadres métalliques ont été maintenus immergés dans le bain au moyen de chaínes et retirés du bain par le même dispositif. Le transfert dans le bain de refroidissement a été réalisé avec un passage dans l'air de l'ordre de 5 secondes. Le matériau est resté immergé dans la solution de traitement une trentaine de minutes en prenant soin de limiter l'échauffement du bain de refroidissement en deçà de 50°C. Ce bain coloré en rouge au rouge Soudan contenait des pyrèthres comme agent de préservation.To treat a batch of 3 stakes of debarked Douglas-fir 0.15 m diameter and 1.5 m long with an initial water content close to 100% (kg / kg dry mass), two rapeseed oil baths were used maintained respectively at 180 ° C and 35 ° C at atmospheric pressure. We have submerged the stakes, the ends of which had been previously waterproofed by soaking in tar, in the heating bath for 60 minutes taking care to allow easy circulation of the oil between the posts by natural convection and ensuring a effective compensation for the drop in bath temperature. The stakes clamped at their ends by metal frames have been kept immersed in the bath by chains and removed from the bath by the same device. Transfer to the cooling bath was carried out with a passage in the air of the order of 5 seconds. The material remained submerged in the treatment solution for about 30 minutes, taking care to limit the heating of the cooling bath below 50 ° C. This bath colored red to red Sudan contained pyrethrums as a preservation.
Après sortie du bain et égouttage (sans ressuyage), on a constaté, dans une coupe transversale du piquet, une imprégnation du bois par l'huile colorée et l'agent de préservation sur une profondeur de 3 à 6 cm (dans tous les cas l'aubier est entièrement imbibé d'huile colorée) suivant l'état de la surface extérieure et une légère torréfaction sur une profondeur de 5 mm maximum.After leaving the bath and draining (without drying), it was found, in a cross section of the stake, an impregnation of the wood with oil colored and the preservative to a depth of 3 to 6 cm (in in all cases the sapwood is completely soaked in colored oil) depending on the state of the outer surface and a light roast to a depth of 5 mm maximum.
On a répété l'exemple 1 avec les différences suivantes :
- un bain de refroidissement contenant une solution aqueuse de chrome, cuivre arsenic colorée au bleu de méthylène,
- un bain de refroidissement maintenu à 20°C.
- a cooling bath containing an aqueous solution of chromium, arsenic copper colored with methylene blue,
- a cooling bath maintained at 20 ° C.
On a dans ce cas constaté une profondeur d'imprégnation en solution de préservation de l'ordre de 2 à 6 cm, et une torréfaction superficielle sur une épaisseur de même importance.In this case, a depth of impregnation in solution has been observed. of preservation of the order of 2 to 6 cm, and a superficial roasting on a thickness of the same importance.
Claims (18)
- A method of treating pieces (4) of wood such as planks, beams, stakes, or posts by means of a hydrophobic wood-preserving agent, the method comprising a step of heating said pieces by immersing them in a bath of oil, followed by a step of cooling the pieces by putting them into contact with a bath of oil (6) containing said agent, in which method the pieces for treatment present a moisture content of more than 25% by weight, and for this purpose the pieces (4) are moistened, where appropriate, prior to being heated, the method being characterized in that:the intensity of the heating of said bath of heating oil is not less than 10 kW/m2 of outside surface of the treated pieces or 2 MW/m3 of volume of the treated pieces, so as to cause the water contained in the pieces to vaporize suddenly;the pieces are transferred into a said bath of cooling oil where they are confined in an enclosure (16, 59) so as to maintain the pieces at raised pressure, while avoiding prolonged contact between the heated pieces and a non-treating medium such as ambient air; andin that said heating and cooling baths are of a composition based on vegetable oil.
- A method according to claim 1, in which the temperature of the environment through which the pieces pass on being transferred into said bath is maintained at a temperature above the boiling temperature of water, by applying additional heating.
- A method according to claim 1 or claim 2, in which the pieces are transferred with the environment used during the heating step by means of a boat, a lock, or any other suitable device.
- A method according to any one of claims 1 to 3, in which the pieces (4) of wood that are treated have a moisture content of about 40% to 80% by weight (relative to dry weight).
- A method according to any one of claims 1 to 4, in which the heating and the cooling are obtained by successive immersion in two baths (3, 6) of oil, the pieces (4) being transferred from the first bath to the second bath in less than 30 seconds.
- A method according to claim 5, in which the first bath is maintained at a temperature lying in the range 110°C to 250°C, and in which the second bath is maintained at a temperature below 90°C.
- A method according to any one of claims 1 to 6, in which prior to heating, the ends of the pieces (4) where the longitudinal fibers of the wood are flush with the surface are made liquid-proof or are covered so as to enhance the rise in pressure inside the pieces (4) by the heating operation, and so as to limit the contact between the pieces and a non-treating substance.
- A method according to any one of claims 1 to 7, in which the duration of the treatment is of the order of 30 minutes to 4 hours, and in which the duration of the cooling is longer than the duration of the heating.
- A method according to any one of claims 1 to 8, in which the heating power is delivered per unit area with flux densities lying in the range 30 kW/m2 to 300 kW/m2 by making contact with a hot liquid, by infrared radiation, by making contact with superheated steam (at 140°C to 300°C) or with air at high temperature (150°C to 300°C), or in bulk by high frequency or very high frequency radiation at flux densities lying in the range 2 MW/m3 to 20 MW/m3.
- A method according to any one of claims 1 to 9, in which the changeover from heating to cooling is made when the ratio of the weight of water contained in the pieces over the dry weight thereof lies in the range 60% to 30%.
- Apparatus for treating pieces (4) of wood, the apparatus comprising:which treatment apparatus is characterized in that:a heater device (7) for heating the pieces (4); anda cooler device (8) for cooling the pieces (4) by contact with a bath of liquid (6) containing a wood preservation agent,said heater device (7) is suitable for delivering a flux of not less than 10 kW/m2 of outside area of the treated pieces or of 2 MW/m3 of volume of the treated pieces, so as to obtain sudden vaporization of the water contained in a piece; andin that it includes a device (9) for moving the pieces (4) relative to the heater and cooler devices (7, 8), and a confinement enclosure (16, 59) enabling the pieces (4) to be maintained at high pressure and prevent prolonged contact between the heated pieces and a non-treating medium such as ambient air.
- Apparatus according to claim 11, which comprises:and which further comprises:a vessel (2) suitable for receiving a bath (3);a member (7) for heating the bath (3), such as a heat exchanger;a member (10) for keeping the pieces (4) immersed in the bath; anda member (11) for moving the pieces (4) relative to the bath (3), such as a pump for circulating the bath or a conveyor for moving the pieces;and in which the displacement device (9) comprises a conveyor (14) or a transfer device (15) of the airlock type.a vessel (5) suitable for receiving a bath (6);a cooling member (8) for cooling the bath (6), such as a heat exchanger;a member (12) for keeping the pieces (4) immersed in the bath (6); anda member (13) for moving the pieces (4) relative to the bath (6), such as a pump and/or a conveyor;
- Apparatus according to claim 11 or claim 12, which further comprises:a cover (16) for at least partially confining the treatment enclosure (2, 5) and the displacement device (9);a member (17) for heating the pieces (4) without contact, such as a microwave generator or an infrared radiation generator; anda member (18) for introducing a hot gas into the treatment enclosure (2, 5, 16).
- Apparatus according to claim 12 or claim 13, the apparatus comprising at least two heater vessels (2) and at least two cooling vessels (5) disposed in alternation, each pair of contiguous vessels (2, 5) being provided.with means for transferring pieces (4) from one vessel to the other.
- A piece (4) of wood suitable for being obtained by a method according to any one of claims 1 to 11, in which at least a portion of the piece is impregnated with a preservative agent and with used vegetable oil.
- A piece (4) according to claim 15, in which the used oil content in the impregnated portion of the piece (4) is of the order of 0.05 to 2 kilograms of oil per kilogram of non-oily dry matter.
- A piece (4) according to claim 15 or claim 16, including a roasted surface layer of thickness of the order of 0.5 centimeters to 2 centimeters.
- A piece according to any one of claims 15 to 17, in which the thickness of the impregnated layer relative to the half-diameter (or equivalent diameter) of a cross-section of the piece is 10% to 100%, and in which the water content of said impregnated layer is less than 0.4 kilograms per kilogram of dry matter.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR9914672 | 1999-11-22 | ||
| FR9914672A FR2801241B1 (en) | 1999-11-22 | 1999-11-22 | PROCESS AND DEVICE FOR TREATING WOOD OR SIMILAR MATERIALS |
| PCT/FR2000/003245 WO2001038055A1 (en) | 1999-11-22 | 2000-11-22 | Method and device for treating wood and similar materials |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP1232047A1 EP1232047A1 (en) | 2002-08-21 |
| EP1232047B1 true EP1232047B1 (en) | 2004-07-28 |
Family
ID=9552392
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP00981456A Expired - Lifetime EP1232047B1 (en) | 1999-11-22 | 2000-11-22 | Method and device for treating wood and similar materials |
Country Status (8)
| Country | Link |
|---|---|
| EP (1) | EP1232047B1 (en) |
| AT (1) | ATE271959T1 (en) |
| AU (1) | AU1869801A (en) |
| CA (1) | CA2392159C (en) |
| DE (1) | DE60012564T2 (en) |
| ES (1) | ES2225274T3 (en) |
| FR (1) | FR2801241B1 (en) |
| WO (1) | WO2001038055A1 (en) |
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| US7300705B2 (en) * | 2003-06-23 | 2007-11-27 | Weyerhaeuser Company | Methods for esterifying hydroxyl groups in wood |
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| CN109746993B (en) * | 2018-12-29 | 2023-10-17 | 湖北宝源木业有限公司 | Impregnation device and impregnation method for wet flaking |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA976813A (en) * | 1972-10-19 | 1975-10-28 | Canadian Wood Council | Method of manufacturing fire retardant plywood employing a high frequency electromagnetic field |
| US3928677A (en) * | 1972-12-08 | 1975-12-23 | Firewood Inc | Process of treating wood |
| GB2099870B (en) * | 1981-06-08 | 1985-06-19 | Hager Bror Olof | Process for drying wood |
| JPS58219005A (en) * | 1982-06-15 | 1983-12-20 | 松下電工株式会社 | Method of impregnating treating liquid |
| ATA237789A (en) * | 1989-07-03 | 1992-06-15 | Robert Boho | METHOD FOR TREATING WET NEEDLE OR DECUMBER LUMBER |
| GB2244067B (en) * | 1990-05-16 | 1994-11-09 | Rajdvinder Singh Bains | The proposal of an oil based wood preservative |
| EP0956934A1 (en) * | 1998-05-12 | 1999-11-17 | Rhone Poulenc Agro | Protection of timber by arylpyrazoles |
-
1999
- 1999-11-22 FR FR9914672A patent/FR2801241B1/en not_active Expired - Fee Related
-
2000
- 2000-11-22 WO PCT/FR2000/003245 patent/WO2001038055A1/en not_active Ceased
- 2000-11-22 DE DE60012564T patent/DE60012564T2/en not_active Expired - Lifetime
- 2000-11-22 AT AT00981456T patent/ATE271959T1/en not_active IP Right Cessation
- 2000-11-22 ES ES00981456T patent/ES2225274T3/en not_active Expired - Lifetime
- 2000-11-22 AU AU18698/01A patent/AU1869801A/en not_active Abandoned
- 2000-11-22 EP EP00981456A patent/EP1232047B1/en not_active Expired - Lifetime
- 2000-11-22 CA CA002392159A patent/CA2392159C/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107030823A (en) * | 2017-04-18 | 2017-08-11 | 浙江永裕竹业股份有限公司 | A kind of modification cooling treatment method of section bar |
| CN107127846A (en) * | 2017-04-18 | 2017-09-05 | 浙江永裕竹业股份有限公司 | A kind of preparation method of bamboo recombined material |
Also Published As
| Publication number | Publication date |
|---|---|
| CA2392159C (en) | 2009-04-07 |
| DE60012564T2 (en) | 2005-08-04 |
| WO2001038055A1 (en) | 2001-05-31 |
| CA2392159A1 (en) | 2001-05-31 |
| FR2801241A1 (en) | 2001-05-25 |
| EP1232047A1 (en) | 2002-08-21 |
| AU1869801A (en) | 2001-06-04 |
| ES2225274T3 (en) | 2005-03-16 |
| FR2801241B1 (en) | 2002-02-08 |
| ATE271959T1 (en) | 2004-08-15 |
| DE60012564D1 (en) | 2004-09-02 |
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