• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    PROCESS OF THERMAL MODIFICATION IN HIGH TEMPERATURE OF WOOD IN A VACUUM AUTOCLAVE A process for the treatment of thermochemical modification of wood is described, in which such modification is obtained through multiple chemical reactions of the substances comprising the wood structure generated exposing the wood to temperatures at which the pyrolysis phenomenon begins, that is, in the range of 180 ° C to 240 ° C, in a vacuum autoclave cell while always keeping the internal pressure lower than the atmospheric pressure, in a range of values of 7 to 35 kPa (70 to 350 mBar) of absolute pressure, consisting of the preheating steps, real heat treatment and cooling of the wood mass.
    公开号:BR112013030700B1
    申请号:R112013030700-5
    申请日:2012-06-15
    公开日:2020-12-22
    发明作者:Ernesto Pagnozzi
    申请人:Wde Maspell S.R.L；
    IPC主号:
    专利说明:

    Technical field
    [001] The present disclosure refers to a process of thermal treatment at high temperature of the wood in a vacuum autoclave, suitable to produce the modification of the wood structure through multiple chemophysical reactions of the substances comprising it, generated by the exposure of the wood. wood at temperatures at which the pyrolysis phenomenon begins (180 ° C to 240 ° C), in any case while preventing its combustion. Prior art
    [002] In this paragraph, the current state of the art is described. In this regard, it is important to state that the heat treatment processes of wood currently used in industry consist substantially of the sequence of the following three steps: 1. Pre-heating of pre-dried wood to humidity values close to zero within a cell until when its temperature reaches the temperature at which pyrolysis begins, from approximately 180 to 230 ° C, with measures to prevent its combustion, 2 .real heat treatment, consisting of keeping the wood at the pre-established temperature for a pre-established period of time, while in any case and always preventing its combustion, 3 .cooling the wood to bring it to temperatures in any case below 100 ° C, in order to subsequently be able to expose the wood material to the external environment without danger of combustion and / or thermal shock problems.
    [003] Currently, three technologies are known to obtain heat-treated wood, which are described here below while highlighting their aspects. 1) Heat treatment at atmospheric pressure in cells with superheated steam heating (Finnish method).
    [004] The pile, composed of the wood predisposed in slats and dried in other devices, is loaded inside a cell that is adequately isolated and impermeable to steam, similar to a conventional wood drying cell, equipped with internal fans to generate the circulation of the heating fluid through the stack, in this case, superheated steam at a temperature of 150 to 230 ° C, supplied by an external steam generator and strictly maintained, for obvious safety reasons, at atmospheric pressure, by means of a safety duct and / or chimney open to the atmosphere, with which the cell must necessarily be equipped to prevent dangerous internal overpressures.
    [005] The wood is protected against the combustion trigger, since it is heated in the heat treatment temperature of 180 to 230 ° C in an environment that is inert, since the air initially existing in it (therefore, the oxygen contained in it) ) has been replaced by overheated steam.
    [006] Therefore, the first two steps, that is, preheating and treatment, are performed with the same method using the circulation of superheated steam.
    [007] The third step, that is, cooling, is carried out by interrupting the entry of superheated steam and injecting demineralized water into the cell by means of special sprayers that produce the “atomization” of the water jet, which, being instantly converted into steam, subtracts the heat for the treatment cell, in a ratio of approximately 540 Kcal per liter of evaporated water, thus executing the cooling of the wood contained in it; the steam thus generated is discharged into the atmosphere through the “chimney” mentioned above.
    [008] Of course, there are some variations in the method for producing heating steam, which will be omitted here for the sake of brevity, but which always find their origin in the use of superheated steam as a means of heating and inerting the cell .
    [009] The limits of this technique consist of the following points: drying: the wood to be treated has to be pre-dried in another device in order to decrease the humidity values, then cooled and finally fed into the treatment cell to be heated again, with a great waste of time, labor and, above all, thermal energy, heating: there is a need to install a steam generator equipped with all the safety measures that are required for its use, inertization: it is carried out by means of the injection of superheated steam, cooling: in order to decrease the temperature of the wood from 230 ° C to 100 ° C, a subtraction of the thermal energy is necessary, equal to approximately 45,000 Kcal / m3, which corresponds to a consumption of demineralized water of 70 to 80 liters per m3 of treated wood and the consequent production of approximately 150 m3 of steam per m3 of treated wood, pollution: the water vapor coming out of the cell chimney acts i nevitably as a vehicle for a significant set of gases and volatile chemical substances resulting from the chemical conversion of wood (resins, semi-cellulose, cellulose, etc.). Therefore, it is important to know that a heat treatment chamber with 10 m3 of wood storage produces 1,500 m3 of potentially polluting steam per treatment cycle, safety: it will be evident that, in the case of a lack of power supply due to an external failure and / or internal machinery, the internal temperature must be maintained in some way to prevent the heating vapor from condensing inside the cell, thereby drastically decreasing its volume and sucking in air from the external environment through the safety chimney , that way the wood mass could ignite instantly. 2) Heat treatment at atmospheric pressure in a cell saturated with inert gas (nitrogen)
    [010] The process is similar to the previous one, except for the variation that the interior of the cell is saturated with nitrogen which, being an inert gas, prevents the firing of the combustion of the wood material.
    [011] The limits of this technique consist of the following points: drying: see the previous case, heating: the system is equipped with electric heat exchangers and / or internal fluid of diathermic oil, as well as fans for the circulation of nitrogen through of the wood pile, inerting: it is carried out by means of nitrogen injection, so that the system has to be equipped with a nitrogen generator and / or an appropriately sized storage tank, since the gas consumption is significant; moreover, the system must be equipped with an expensive oxygen concentration analyzer to ensure that its concentration is always lower than the dangerous thresholds. cooling: see the previous case, pollution: see the previous case, safety: the occasional lack of tension is more easily handled than the previous method; however, special care must be taken to constantly monitor the oxygen concentration within the cell to prevent the risk of combustion. In addition, it is absolutely necessary to provide an accurate and safe disposal of nitrogen from inerting the cell at the end of the process to avoid, with the opening of the cell, the danger of suffocation due to nitrogen inhalation for technical personnel. 3) Treatment with superheated steam in a pressurized autoclave
    [012] This process differs completely from the two previous processes and consists of feeding the wood into an autoclave suitably isolated and suitable to withstand an internal pressure of up to 1.9 MPa (19 bar).
    [013] Heating is performed by directly injecting superheated steam into the autoclave, therefore, it does not provide the provision of ventilation devices and / or internal exchangers.
    [014] The process takes place according to the following steps: 4. preheating: after performing a pre-vacuum with a residual pressure of 20 kPa (200 mBar), the superheated steam produced by a special generator is fed in. of the cell, even when the wood reaches the treatment temperature of 180 to 230 ° C, 5 .treatment: the temperature is maintained at the desired value by means of an appropriate steam supply, 6 .cooling: it is carried out with water spray, as in previous methods and ends with a final vacuum, followed by an external air supply.
    [015] The limits of this technique consist of the following points: drying: see previous cases, heating: there is a need to install a steam generator equipped with all the safety measures that are required for its use, inerting: it is performed with the injection of superheated steam, cooling: see previous cases, pollution: see previous cases, safety: the cell, since it is a pressurized autoclave, must be subjected to the periodic inspections indicated by the laws in force. Brief description of the invention
    [016] The process that is the objective of the present patent application aims to overcome most or all of the limitations described above with reference to the prior art and is characterized in that the treatment of wood in order to prevent its combustion is performed by completely eliminating the oxygen contained in the cell, in the first place, by dramatically reducing the initial amount thanks to the partial vacuum created in the cell that makes the air extremely rarefied, since it is brought to an absolute pressure of 7 to 35 kPa (70 to 350 mBar) and subsequently for completely consuming the small residual amount of oxygen, inducing a micro-combustion of an infinitesimal portion of the wood mass submitted to the treatment. This phenomenon is defined by the author as “wood self-inerting”, since it is the wood itself that generates its own inerting, sacrificing an insignificant part of its matter.
    [017] Such thermochemical reactions induce the following macroscopic changes in the characteristics of the wood: 1) COLOR: change (darkening) and color homogenization across the entire thickness of the wood, the intensity of which can be controlled by appropriate adjustments of the process parameters, ie ie, temperature, pressure and time of exposure, 2) DURABILITY: improvement of its durability, in the sense that the treated wood becomes more resistant to attacks by fungi and other xylophagic microorganisms; therefore, “softwood” species classified with class 5 durability, such as conifers (such as fir, pine and larch) easily available and having a low economic value, can reach class 1, which is typical of “hardwoods”. law ”, known as very durable (such as oak, chestnut and teak), whose economic value can be 3 to 10 times higher than that of conifers, 3) HIGROSCOPICITY: reduction of its hygroscopicity, that is, of its ability to capture or absorb the humidity of the surrounding environment, thus making it almost insensitive to variations in time (temperature and air humidity), 4) DIMENSIONAL STABILITY: as a consequence of decreased hygroscopicity, wood acquires a high dimensional stability against variations in environmental humidity, which results in an improvement in the quality of the finished products (furniture, wooden floors, accessories, musical instruments, etc.) that become virtually insensitive to variations in the time, 5) MECHANICAL CHARACTERISTICS: a 10 to 15% worsening of some mechanical characteristics (tensile, compressive and shear strength), but an important improvement in its hardness was detected; in other words, heat-treated wood becomes slightly more fragile, but harder. This phenomenon, which could be partially limiting in relation to the implementation of structural beams for the construction sector, is absolutely advantageous in any other applications, since the increase in hardness facilitates not only some of the operations of processing the wood material, such as polishing and painting, but allows to obtain manufactured articles that are more resistant to accidental scratches, which is a fundamental result for the final quality of the finished products, such as floors, furniture and window and door frames, etc.
    [018] It is necessary to show that the wood, even before being subjected to heat treatment temperatures, needs to be dried, however, to final humidity values close to zero, to prevent the residual water contained in the cell walls of the material from wood, brought to temperatures of 180 to 230 ° C, generates such pressures in order to produce its collapse, resulting in irreparable damage.
    [019] Additional features and advantages of the invention will become evident from the following detailed description, given by way of non-limiting example only, with reference to the accompanying drawings, in which: Figures 1a-1c show schematically sectional views of a first modality of an apparatus for the heat treatment of wood, Figures 2a-2c schematically show sectional views of a second embodiment of an apparatus for the heat treatment of wood, Figures 3a-3c show schematically sectional views of a third embodiment of an apparatus for heat treatment the heat treatment of the wood, Figure 4 shows a perspective view of the apparatus of figure 1. Detailed Description
    [020] The process described here aims to overcome all, or most, of the negative implications of currently existing processes, while maintaining a much higher quality of the final product and more precisely: drying: performed in an impermeable cell, preferably planned in order to perform the double function of vacuum dryer and heat treatment device, in order to avoid the transposition of the wood pile from one machine to another, with great time savings, labor force and, above all, thermal energy . heating: carried out in a partial vacuum through the forced circulation of rarefied air (closed circuit) through the wood pile and special heat exchangers that use any source of thermal energy (electricity, diathermic oil, superheated water) without the need for any injection steam and / or nitrogen and / or other gas. inertization: according to a process of "AUTOINERTIZATION" of the wood, thus not needing any injection of steam and / or nitrogen and / or other gas to render the interior of the cell inert.
    [021] In order to understand the dynamics of the self-inerting phenomenon, first consider that the interior of the autoclave cell (isolated and perfectly impermeable) is a virtually adiabatic system, that is, it does not allow energy exchanges with the outside.
    [022] This means that, after the wood has been loaded into the cell, the system appears to be completely isolated and contains only the following elements: the wood to be heat treated and the air that fills the remaining internal free volume.
    [023] When the wood reaches the pyrolysis temperature (180 ° C to 230 ° C) at a pressure of 7 to 35 kPa (70 to 350 mBar), the internal atmosphere of the cell is formed by air that is very thin, as seen, by the combined effect of vacuum and temperature, still having an oxygen content that, although not very low, could induce the firing of wood combustion.
    [024] Therefore, in order to assess the extent, therefore, of the potential risk of the aforementioned combustion phenomenon, it is desirable to know the amount of wood mass that could be induced to burn by the oxygen existing in the residual air contained within the autoclave cell, after the operative point of treatment has been reached.
    [025] Due to the constructive causes of geometry, mechanics and aerodynamics, whatever the internal dimensions of the autoclave cell, the relationship between the free volume of internal air and the net volume of the stored wood is approximately 3: 1 = 3. This means that for each m3 of wood actually stored, an amount of oxygen approximately equal to that contained in 3 m3 of air at an ambient temperature of 25 ° C and an atmospheric pressure of 101.3 kPa (1013 mbar) is available.
    [026] Physics teaches that air density varies when temperature and pressure vary, and in particular it decreases when temperature increases and pressure decreases. Some significant figures for the present discussion are presented in table 1 below:
    [027] Table 1: Air density reduction coefficient.

    [028] From the table, it appears that the reduction in air density during the process is drastic and varies between 77% and 95% compared to density at normal temperature and pressure.
    [029] Applying such an observation in the ratio of volume of indoor air to the volume of wood stored (which was initially 3: 1 = 3), it is as if the amount of available air could be reduced by a value equal to the coefficient of the reduction of density, that is, according to table 2:
    [030] Table 2: Relationship between the volume of indoor air and the volume of wood stored.

    [031] From the analysis of the different values of the air volume / wood volume ratio at various operating points, it is observed that by increasing the temperature and reducing the pressure, the amount of available air is dramatically reduced along with the amount of oxygen available for possible combustion.
    [032] Chemistry teaches that the amount of oxygen needed to generate the combustion of 1 kg of wood mass under standard conditions (that is, atmospheric pressure and a temperature of 25 ° C) is approximately equal to that contained in 5 m3 of air, than the amount of wood mass “that can be burned” per m3 of wood stored inside the autoclave cell depending on the temperature and pressure parameters used during the treatment can be easily obtained:
    [033] Table 3: Amount of fuel wood.


    [034] Given that the specific gravity of dry wood varies, for the European species, from 400 to 650 kg / m3, it is evident that the amount of wood mass possibly sacrificed in the combustion phenomenon due to residual oxygen is infinitesimal and it can be calculated as follows:
    [035] Table 4: Silver fir wood (400 kg / m3):% of mass loss by combustion.

    [036] Table 5: Oak wood (650 kg / m3):% of mass loss by combustion.

    [037] In order to assess the dangers inherent in the combustion of the aforementioned tiny wood masses, it is necessary to know the amount of thermal energy released by the exothermic chemical process during its combustion.
    [038] Given that the calorific value of wood is at most 4200 kcal / kg, the thermal energy released by the combustion process can be easily calculated:
    [039] Table 6: Specific thermal energy released by the combustion of wood during the process.


    [040] This energy, even if it were released instantly, is not capable of producing any significant temperature variation in the internal environment of the cell and, therefore, it cannot create any danger to the mechanical structure, nor to the wood, nor for control personnel.
    [041] In reality, the oxygen OR has not "disappeared", but it is combined with the carbon C of the wood during the exothermic chemical reaction of combustion: C + O2 = CO2 + thermal energy being converted into carbon dioxide which, being a inert gas, prevents each additional combustion: from this, the initial definition derives according to which the described process is a process of “AUTOINERTIZATION” of the wood.
    [042] It is evident that this percentage of wood that can be burned being absolutely insignificant, the reduction-oxidation phenomenon that is the basis of the combustion of this small quantity makes the internal atmosphere of the cell totally inert, since the small percentage of oxygen is still present in the residual air before combustion, combining with the carbon contained in the wood, is converted to carbon dioxide CO2, totally eliminating the number of oxygen molecules present in the cell and rendering the final mixture of gases contained in the autoclave cell totally inert.
    [043] It is important to analyze the different compositions of the gas mixture inside the cell before reaching the temperature of the pyrolysis and during the process of autoinerting the wood caused by the described process:
    [044] BEFORE: 78% nitrogen, 21% oxygen, 0.9% argon, 0.04% carbon dioxide, 0.06% others.
    [045] DURING: 78% nitrogen, 0.9% argon, 21.04% carbon dioxide, 0.06% others.
    [046] cooling: using a new and original method, for example, heat exchangers allow the heat of the wood to be transferred from inside the cell (which is constantly kept in a partial vacuum and in a self-inert environment) to the external atmosphere without supplying water and / or other gases and without the production of polluting steam.
    [047] pollution: the device does not produce any pollution to the external environment, since no gas and / or vapor can escape from its autoclave cell, which is always at a pressure lower than atmospheric. The small possible amount of residual water vapor and / or gases generated during the heat treatment are transported, before being sucked by the vacuum pump, through a suitable condenser that allows them to be converted to the liquid phase, allowing their easy recovery. in a special reservoir, so that they can subsequently be disposed of according to the laws in force.
    [048] safety: the only real danger that occurs when heating the wood in temperatures above 160 ° C is to trigger the combustion of the wood when air enters the treatment cell due to accidental causes.
    [049] Such an event may occur due to causes that are external to the device (temporary interruption due to failure of the power supply) or due to causes intrinsic to the machinery itself (defect or poor operation of a component of the machinery).
    [050] Possible external and internal failures and an example of a technique practiced by the described procedure are analyzed here below.
    [051] According to a modality, in order to eliminate this disadvantage, by which all organs and sensors of the device would be apprehended, the device was equipped with a security system comprising the following elements: a UPS continuity unit, capable of intervene continuously at the time of the general power failure and supply the control (PLC) and device safety devices described here below for a continuous period of at least 6 hours, a telephone dialer that immediately alerts managers (up to 4 people) of the lack of voltage occurred by voicemail and SMS alert, a vacuum vacuum pump, having a relatively small capacity, adequate to keep the existing vacuum in the cell at the correct value, preventing the pressure in the cell from rising, ensuring that the oxygen concentration remains insignificant.
    [052] Since the safety vacuum pump certainly does not operate continuously, but thanks to the perfect sealing of the autoclave, it will have short periods of operation alternating with long periods of standstill, the supply capacity of the UPS continuity unit will allow the device is in a standby stage for a time even above 24 hours and, in some cases, in the case of continuous operation, for a period of time not less than 6 hours.
    [053] This solution provides the great advantage of preserving the wood material, keeping it under current conditions, in order to allow the device to automatically restart the heat treatment cycle from the point of interruption, without losing any information about the current state of the appliance and the wood and with maximum safety.
    [054] To overcome the problem of a possible defect in one of the electrical components of the device (motors, valves, sensors, etc.), according to a modality, each component is supervised by a device (for example: magnetothermal protections, probes auxiliary, etc.) that immediately alerts the PLC controller of the defect that has occurred, so that the PLC can take the appropriate measures: immediate stop of all components, activation of the UPS continuity unit, sending telephone alerts to operators through the disk of the telephone, activation of the safety vacuum pump to maintain the pressure in the cell at the desired value.
    [055] In this case again, the system reacts immediately, ensuring the preservation of the wood and allowing technicians to intervene in order to eliminate the disadvantage and restart the system.
    [056] According to a modality, in any case, the device can be equipped with an emergency system against the possibility of fire from the wood contained in the cell: such a system provides for the inertization of the interior of the cell through the entry of nitrogen or Water.
    [057] If the remote event of a fire ignition within the cell occurs, for a cause such as, for example, a loss of the impermeable seal that causes ambient air to enter the cell, resulting in a higher concentration of oxygen, therefore, the initiation of a combustion, special pressure and temperature sensors alert the PLC controller, which allows to activate the FAST INERTIZATION process, substantially consisting of the following operations: immediate stop of all components, activation of the UPS continuity unit, sending of telephone alerts for operators via a telephone dialer, nitrogen supply or water spray into the cell via a special electric valve, in order to saturate the cell's internal volume with a gas or vapor, even when the cell's internal pressure is equal to or slightly above atmospheric pressure, thus preventing ambient air from entering the cell and in any case stifling wood combustion , activation of the cooling system, in order to quickly lower the cell temperature to values below 100 ° C, which are well below the combustion temperature (160 ° C).
    [058] From the foregoing, it will be evident that the apparatus described is capable of implementing a suitable process to execute in sequence and / or separately the two physical processes: a. Drying, preferably in a vacuum, of wood at temperatures ranging from 50 ° C to 100 ° C, depending on whether it is hardwood or softwood, with a pressure ranging between 50 to 35 kPa (50 to 350 mbar), for example example, ranging between 12.5 and 25.0 kPa (125 and 250 mbar), b. the heat treatment of wood in a vacuum with absolute pressures ranging from 7 to 35 kPa (70 to 350 mBar) and with temperatures ranging from 160 to 240 ° C and comprising the three stages of: preheating, until the operating temperature has been achieved, real heat treatment, cooling of the wood mass through a new method that does not allow the use of water evaporation to cool the wood.
    [059] With reference to the attached figures, according to one embodiment, the apparatus 100 comprises the following elements: 1) a vacuum-sealed treatment chamber (internal chamber of the autoclave cell 1) suitable for containing the wood, that is, the wood mass 3 to be treated, provided with an impermeable door 4 for feeding and removing the wood, 2) a car 2 supporting the wood pile that has to be treated, 3) a heating system inside the cell autoclave 1, which may comprise electric batteries 5A, 5B or radiators with ribbed tubes for heating by means of steam and / or diathermic oil or a diathermic oil jacket external to the drying cell, 4) a ventilation system comprising a series of fans 6A, 6B suitable for transferring the thermal energy from the heating system to the wood material by circulating the gas inside the cell, 5) a 13-15 vacuum pump unit, comprising a vacuum pump, and a condenser 14 that is placed between the pump and the treatment chamber of the autoclave cell 1, in order to compensate for any vapors and / or gases that come out of the wood, in order to be able to provide its storage in a suitable reservoir , in order to be able to provide its disposal according to the requirements of the law, 6) a wood cooling system that can vary in its implementation according to the type of the heating method, but that does not yet use the spray of water inside the cell, 7) a security and alarm system that allows to manage situations of potential danger.
    [060] Three possible non-limiting modes of device 100 will be described here below: CONFIGURATION 1: as shown in figures 1a-1b, with direct electric resistor heating and cooling with an air jacket, CONFIGURATION 2: as shown in figures 2a-2b , with heating and cooling using oil-air heat exchangers, CONFIGURATION 3: as shown in figures 3a-3b, with heating with diathermic oil jacket and cooling with oil-air heat exchanger.
    [061] After introducing the three possible configurations, we will consider the descriptive analysis in more detail for each individual planned application: CONFIGURATION 1: device with heating by electric batteries and cooling of intermediate space with air Device description:
    [062] With reference to figures 1a-1b, in the illustrated example, the apparatus 100 comprises the following elements: a vacuum-sealed treatment cell 1 (also called an “autoclave cell”) comprising a cylinder 6, preferably made of stainless steel , defining a suitable treatment chamber to house the wood mass, a loading trolley 2 in which the wood pile to be thermochemically treated 3 is arranged, formed by layers of wooden planks and / or semi-finished articles separated from each other by spacer strips to allow the heating fluid to pass, a vacuum-tight door 4, a heating system comprising electric resistor batteries 5A and 5B, a ventilation system comprising, for example, two fans 6A and 6B that provide, through the internal air circulation, the transfer of thermal energy from the heating batteries to the wood, a box, preferably made of steel 7, concentric with the treatment cell 1 and form I walk an intermediate space 8 with it: such an intermediate space communicates with the atmosphere inferiorly through a hole 9 that extends through the entire length of the intermediate space, and superiorly through the suction distribution tube 10, the shut-off valve air 17 and fan 11, a vacuum pump unit, consisting of the suction tube 12, the condenser 14, a condensed steam collection and storage reservoir 15 and the vacuum pump 13. The cell is thermally isolated from the environment external through insulation 16.
    [063] The description of the operation of the apparatus 100 as a vacuum dryer will be omitted since it is already known, since it has been the objective of several patents granted in the past to the applicant and being a part of the knowledge licensed by the applicant for several companies, both in Italy and abroad (for example, US patent 4,223,451, Italian patent 1187959). Operation of the device according to configuration 1
    [064] After loading the wood pile 3, that is, the wood mass to be treated, in the special car 2 and feeding the car into the treatment cell (autoclave) 1 through port 4, it is hermetically closed through special devices.
    [065] At that point, the actual treatment cycle can be started which consists, as noted in the introduction, following the following 3 steps: STEP 1: preheating the wood, STEP 2: real treatment STEP 3: cooling the mass of wood Step 1: preheating the wood
    [066] During this stage, fans 6A and 6B (according to the teachings of Italian patent 1187959 by the applicant related to the longitudinal-lateral “LO-LA” type ventilation system) provide the internal air circulation through the batteries heating elements 5A and 5B and the wood pile, in order to transfer the thermal energy produced by them to the wood itself (of course, it is possible to arrange batteries and fans differently, as long as the fluid circulation is equally efficient).
    [067] Preferably, a system of at least two temperature probes 18 immersed in the air flow makes it possible to measure the temperatures upstream and downstream of the wood pile and consequently carry out their adjustment according to the program defined by the operator.
    [068] At the same time, the vacuum pump system provides to suck air out of cell 1 until the desired value of absolute pressure is reached and maintained.
    [069] According to the need, this value can vary between 7 kPa (70 mBar) and the atmospheric pressure 102.3 kPa (1023 mBar) until when the internal temperature of the treatment chamber is lower than 180 ° C, this that is, the temperature at which the start of combustion can be fired at the wood; subsequently, the apparatus 100 proceeds to decrease the pressure to a value varying between 7 and 35 kPa (70 and 350 mBar), in order to guarantee that, once the pyrolysis start temperature has been reached, the internal atmosphere is already extremely low on oxygen so that, as noted, the amount of wood material “that can be burned” due to the phenomenon of oxidation reduction between residual oxygen and carbon in the wood is infinitesimal and produces the desired “self-inerting” phenomenon.
    [070] A temperature probe 18, located in a hole drilled in the middle of a wooden plank that was selected as a sample, allows to measure and adjust the temperature of the thermochemical treatment, generally varying between 180 ° C and 230 ° C, the which can be achieved in several successive stages and / or with a desired slope according to the type of wood, its thickness, etc. Step 2: real thermochemical treatment
    [071] Once it has been evaluated by means of a special wood core probe 18, that the wood mass has reached the desired treatment temperature, the device provides to maintain such temperature constant for the period of time defined by the operator, whose duration depends on the result of changes in the characteristics of the wood to be obtained (color, durability, hygroscopicity, etc.) in the thickness of the wood, its type, etc.
    [072] In this stage, the fans and, when necessary, also the heating batteries, as well as the vacuum pump unit that provides to maintain the pressure in the cell at the operating value, also varying according to the needs between 7 and 35 kPa (70 and 350 mBar) absolute, are active.
    [073] Vapors and gases possibly produced by the wood mass during the treatment are sucked by the vacuum pump 13, which provides for transporting them through the tube 12, through the condenser 14, where they are cooled to the condensation temperature and then converted to the liquid phase, collected in storage reservoir 15, from where they can be extracted at the end of the cycle and sent, if necessary, for disposal according to the requirements of the law. Step 3: cooling the wood mass
    [074] At the completion of the treatment step, the wood is at a temperature of 180 230 ° C, so it cannot be extracted from the cell unless after being cooled in an inert atmosphere until it is below 80 ° C , to avoid its exposure to ambient air when it is still at a temperature that is dangerous for combustion, not to subject it to harmful thermal shocks and, finally, to allow its handling without risk of burns for the operator.
    [075] The method used to cool the wood is new and original and consists of subjecting the entire outer surface of the autoclave cell 1 to a forced circulation of fresh ambient air, in order to create, through the wall of the cell itself, a large temperature differential between the interior (180 ° to 230 ° C) and the exterior (25 ° C), thus generating a corresponding thermal energy circulation according to known laws of thermodynamics, where the amount of heat transferred to the external environment is equal to: Q = k S (Ti Te) where: K = heat exchange coefficient of AISI 304S steel = outer surface of the autoclave cell Ti = internal temperature of the cell = 180 to 230 ° C Te = average temperature of the outside air = 25 ° C than we understand the high efficiency of the autoclave cell when considered as an air heat exchanger for total surface air.
    [076] The cooling operations consist of opening the air interruption door 17, activating the fan 11 which, through the upper distribution pipe 10, allows the removal of fresh ambient air from the lower hole 9 and passing it into the space intermediate 8 with such speed in order to generate a turbulent flow that, touching the wall of the treatment cell 1 externally, produces a quick cooling of it, thus establishing, as observed, a highly efficient thermal exchange between the interior of the cell (with all its wood content) and the ambient air, without direct mutual contact: thanks to this thermodynamic measure, the cell wall is converted into a highly efficient total surface gas air heat exchanger.
    [077] The internal fans 6A and 6B that produce, as noted, the circulation of the internal air, allow to remove the stored heat from the wood and send it to the internal surface of the treatment cell wall, through which the thermal exchange and the transfer of thermal energy to the circulating fresh air stream to the intermediate space 8 takes place.
    [078] All of this happens in absolute respect for the environment, since there is no contact and / or mixture between the internal fluid (mixture of air, vapors and gases from the wood) and the cooling air. Naturally, the hot air coming out of the fan 11 can be recovered during the winter months and used to heat industrial buildings.
    [079] After the wood has been cooled to the desired temperature, it is possible to open the waterproof door 4 and remove the car. Configuration 2: device with heating and cooling by means of heat exchangers
    [080] The process is substantially the same as that previously described with reference to figures 1a 1c, with the following technological variations (see figures 2a 2c): the heating of the wood is achieved by means of internal radiators 15A and 15B in which the diathermic oil , heated by a special boiler 27 is circulated; in the example, these internal radiators are supplied combined with the corresponding fans 6A, 6B, the wood cooling is achieved by diverting, through the 3-way valve 18, the flow of the boiler diathermic oil to the external cooling radiator 20, in the example associated with a 6C fan, in order to establish a circulation of thermal energy from radiators 5A and 5B arranged in the cell (at high temperature) to the ambient air.
    [081] In the illustrated example, a pump 19 is provided for forced circulation of the diathermic oil.
    [082] For drying and actual treatment, all measures described with reference to figures 1a 1c can be applied. Configuration 3: device with diathermic oil jacket heating and cooling by air-oil heat exchanger
    [083] The physical process is substantially similar to that described with reference to 1a 1c, with the following technological variations (see figures 3a 3c): heating is obtained through an intermediate space 8 external to the wood heat treatment cell 8 in the which, through a pump 19, the diathermic oil heated by a special boiler 27 is circulated, so that the entire cell wall becomes a total surface heat exchanger, since it absorbs the heat from the diathermic oil externally and internally transports it to the air inside the cell, whose air is circulated by fans 6A and 6B tangentially to the same wall, then deflected while passing through the wood pile 3, cooling is obtained by circulating the diathermic oil through an oil heat exchanger -external air 20 capable of cooling the oil and then, through a thermal exchange of the internal surface, the wood contained in the treatment cell 1.
    [084] For drying and actual treatment, see what has already been described with reference to figures 1a 1c.
    [085] As will be evident from what has been described above and as confirmed by the field tests, a process and an apparatus of the type described above allow to fully achieve the planned objectives.
    权利要求:
    Claims (10)
    [0001]
    1. Process for the treatment of thermochemical modification of wood, CHARACTERIZED by the fact that such modification is obtained through multiple chemical reactions of the substances comprising the wood structure generated by exposing the wood to temperatures at which the pyrolysis phenomenon begins, that is, in the range of 180 ° C to 240 ° C, in a vacuum autoclave cell (1) while always keeping the internal pressure lower than the atmospheric pressure, in a range of values from 7 to 35 kPa (70 350 mBar) absolute pressure, consisting of the preheating steps, real heat treatment and cooling of a wood mass, in which the preheating step is carried out in order to dry the wood first at a temperature ranging from 50 ° C to 100 ° C, and a pressure range of 50 to 35 kPa (50 to 350 mbar), the wood cooling step at the end of the heat treatment is achieved by means of heat exchange systems between the internal atmosphere of the autoclave cell vacuum (1) and external atmosphere, without these never coming into direct contact with each other.
    [0002]
    2. Process for heat treatment of wood at a high temperature in a vacuum autoclave cell (1), according to claim 1, CHARACTERIZED by the fact that, in the said step of real thermal treatment, the heating of the wood, in order to prevent combustion, it is performed by completely eliminating the oxygen contained in the cell (1) by first “reducing” the initial quantity thanks to the partial vacuum created in the cell that makes the air extremely rarefied and, subsequently, “consuming” it totally the small residual amount, inducing a micro-combustion of an infinitesimal portion of the wood mass submitted to the treatment.
    [0003]
    3. Process for the high temperature heat treatment of wood in a vacuum autoclave cell (1), according to claim 2, CHARACTERIZED by the fact that the atmosphere inside said vacuum autoclave cell (1) undergoes inertization , thanks to the phenomenon of oxide reduction, supporting the micro-combustion of the limited amount of residual oxygen still present in the rarefied air, in which the oxygen, combined with the carbon contained in the wood, is converted into carbon dioxide, totally eliminating the number of molecules of free oxygen existing in the cell and thus rendering the final mixture of gases contained in the autoclave cell totally inert.
    [0004]
    4. Process for the high temperature heat treatment of wood in a vacuum autoclave cell (1), according to any of the preceding claims, CHARACTERIZED by the fact that said vacuum autoclave cell (1) is suitable for perform the dual function of a vacuum dryer and a heat treatment device in order to first dry the wood in a temperature range of 50 to 100 ° C and a pressure range of 5 to 35 kPa (50 to 350 mBar), to avoid damaging the wood even when decreasing its humidity to values close to zero and subsequently being able to expose it to “brutal” temperatures of the thermochemical modification treatment, in a temperature range of 180 to 240 ° C and a pressure range of 7 to 35 kPa (70 to 350 mBar), always using the same cell (1).
    [0005]
    5. Process for the high temperature heat treatment of wood in a vacuum autoclave cell (1), according to any one of claims 1 to 3, CHARACTERIZED by the fact that said vacuum autoclave cell (1) is this in order to perform only one of the functions, that is, a vacuum dryer and a thermal treatment device.
    [0006]
    6. Process for high temperature heat treatment of wood in a vacuum autoclave cell (1), according to any one of the preceding claims, CHARACTERIZED by a particular heating method, which is carried out in a partial vacuum through a forced circulation of a mixture of inert gases in a closed circuit through a pile of wood (3) and special heat exchangers, the cell being able to use any source of thermal energy selected from the following: electricity, diathermic oil, superheated water.
    [0007]
    7. Process for high temperature heat treatment of wood in a vacuum autoclave cell (1), according to any of the preceding claims, CHARACTERIZED by the fact that the partial vacuum maintained in the autoclave cell during treatment is used both to prevent the escape of vapors and / or gases from the cell and to decrease the evaporation temperature and, as a consequence of the dew point, so that the same vapors and / or gases during the cycle can be converted into the liquid phase transporting them through a condenser, therefore, allowing them to be recovered for proper disposal.
    [0008]
    8. Apparatus (100) for the treatment of thermochemical modification of wood, said modification originating from multiple chemical reactions of substances comprising the wood structure generated by exposing the wood to temperatures at which the pyrolysis phenomenon begins, that is, in the range of 180 ° C to 240 ° C, the apparatus (100) being specially adapted to carry out the process as defined in claim 1, CHARACTERIZED by the fact that it comprises: a vacuum autoclave cell (1) comprising a treatment chamber, the pressure of which during treatment is suitable to be kept lower than atmospheric pressure, in a range of values from 7 to 35 kPa (70 to 350 mBar) of absolute pressure, suitable device and configured to obtain the above mentioned internal pressure and to preheat, to perform the actual heat treatment, and to cool a mass of wood inside the autoclave cell (1), a condenser (14) in fluid communication with said heating chamber treatment and suitable to be crossed by gases and / or vapors produced during the treatment to be converted to the liquid phase by the condenser (14); wherein the apparatus (100) still comprises: an external cylinder (7) concentric to the autoclave cell (1), in which an intermediate space (8) is defined between said cylinder (7) and said autoclave cell (1 ), suitable for containing a fluid suitable for cooling said wood mass; and / or a heat exchanger (20) outside the autoclave cell (1) in communication with said intermediate space (8), wherein said fluid is an oil forced to circulate in said intermediate space (8) and in said exchanger (20); a vacuum pump (13) and wherein said condenser (14) is operatively placed between said vacuum pump (13) and said treatment chamber.
    [0009]
    9. Apparatus (100), according to claim 8, CHARACTERIZED by the fact that the apparatus comprises said external cylinder (7) and said fluid is the air sucked from the external environment and forced to circulate in said intermediate space (8 ).
    [0010]
    Apparatus (100) according to claim 8, CHARACTERIZED by the fact that the apparatus comprises said external cylinder (7) and said fluid is an oil.
    类似技术:
    公开号 | 公开日 | 专利标题
    BR112013030700B1|2020-12-22|process and apparatus for the treatment of thermochemical modification of wood
    KR101434472B1|2014-08-27|Method and apparatus for drying conifer wood using superheated steam and wood dried thereby for a korean-style house
    JP2010018032A|2010-01-28|Method for treating stacked wood by high-temperature heat treatment
    JP2007263409A|2007-10-11|Method and device for heat treating and drying wood
    WO2010098698A2|2010-09-02|Method for drying wood and an apparatus for the implementation thereof
    KR100948625B1|2010-03-24|Heat-treating apparatus for drying wood
    JP3844124B2|2006-11-08|Wood drying method
    JP2008106959A|2008-05-08|Wood drying apparatus and wood drying method
    JP5744721B2|2015-07-08|Carbonization method and apparatus
    CN101497799A|2009-08-05|Superhigh temperature wood carbonization method
    JP3989432B2|2007-10-10|Vacuum drying equipment
    FR2861009A1|2005-04-22|Lingo-cellulosic material e.g. wood, drying and treating method, involves drying material at vaporization temperature of water, and gradually heating material to stabilized temperature by controlling pressure inside enclosure
    CN104890084A|2015-09-09|Energy-saving type wood heat treatment kiln and wood heat treatment method thereof
    KR101174335B1|2012-08-16|Apparatus for drying and high heat-treating wood
    TW201502441A|2015-01-16|Flow treatments in evaporative desorption processes
    RU2304747C1|2007-08-20|Method for wood drying
    RU2694109C1|2019-07-09|Device for heat treatment of wood
    JP2006044135A|2006-02-16|Timber drier and timber drying method
    RU180306U1|2018-06-08|CHAMBER FOR HEAT TREATMENT OF WOOD
    RU2724421C2|2020-06-23|Method and device for preparation and high-temperature treatment of wood
    FR3067607B1|2019-07-05|METHOD FOR FUNGICIDAL AND / OR INSECTICIDAL TREATMENT OF AN ELEMENT CONTAINED IN AN ENCLOSURE AND DEVICE FOR IMPLEMENTING SAID METHOD
    GB2178149A|1987-02-04|Method and apparatus for drying timber
    JP3149743U|2009-04-09|Oga powder dryer
    RU2336475C1|2008-10-20|Method of wood drying and impregnation
    RU2621436C1|2017-06-06|Way of wood heating and flame hardening
    同族专利:
    公开号 | 公开日
    US20140124354A1|2014-05-08|
    WO2012172585A2|2012-12-20|
    EP2535156B1|2014-10-29|
    KR101980924B1|2019-05-21|
    CN103608155B|2016-10-26|
    EA201400025A1|2014-04-30|
    CN103608155A|2014-02-26|
    US10344218B2|2019-07-09|
    EA027892B1|2017-09-29|
    PT2535156E|2015-02-06|
    EP2535156A1|2012-12-19|
    SI2535156T1|2015-03-31|
    CA2838568C|2021-03-02|
    KR20140059171A|2014-05-15|
    DK2535156T3|2015-02-02|
    WO2012172585A3|2013-04-11|
    EP2720839A2|2014-04-23|
    PL2535156T3|2015-04-30|
    ITRM20110314A1|2012-12-17|
    CA2838568A1|2012-12-20|
    ES2528903T3|2015-02-13|
    BR112013030700A2|2018-06-12|
    CL2013003600A1|2014-05-16|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US2296546A|1941-03-15|1942-09-22|Crossett Lumber Company|Method of artificially seasoning lumber|
    US2422557A|1942-11-27|1947-06-17|Kobiolke Adolf Martin|Process for seasoning timber|
    CH504661A|1967-07-20|1971-03-15|Pagnozzi Vincenzo|Process and system for vacuum drying wood in boards or strips|
    IT1071276B|1976-05-12|1985-04-02|Pagnozzi Ernesto Guglielmo|IMPROVEMENTS IN THE PROCESSES AND IN THE TIMBER DRYING SYSTEMS .. PARTICULARLY IN THE SYSTEMS THAT USE VACUUM|
    IT1083106B|1977-05-17|1985-05-21|Pagnozzi Vincenzo|EMPTY DRYER PARTICULARLY FOR TIMBER|
    IT1129420B|1980-03-12|1986-06-04|Vincenzo Pagnozzi|HIGH TEMPERATURE PROCESS FOR DRYING WOOD AND EQUIPMENT SUITABLE TO REALIZE THIS PROCEDURE|
    WO1987004779A1|1986-02-06|1987-08-13|Steen Ole Moldrup|Method for the drying of wood and wood-based products|
    IT1187959B|1986-02-28|1987-12-23|Vincenzo Pagnozzi|PROCEDURE FOR HEATING A STACK OF TIMBER INSIDE A VACUUM DRYING AND DRYING CHAMBER IN WHICH THE PROCEDURE IS CARRIED OUT|
    US5575083A|1993-07-05|1996-11-19|Goldstar Co., Ltd.|Vacuum dryer|
    FR2786424B1|1998-11-27|2002-01-25|Arimpex Sarl|PROCESS FOR THE HEAT TREATMENT OF A LIGNO-CELLULOSIC MATERIAL BY CONTAINING GASES, AND LIGNO-CELLULOSIC MATERIAL WHICH CAN BE OBTAINED BY THIS PROCESS|
    NL1015161C2|2000-05-11|2001-11-13|Npc Ind B V I O|Method for manufacturing sustainable products.|
    TW582400U|2001-10-04|2004-04-01|Univ Nat Cheng Kung|Device for synthesizing aluminum nitride|
    JP4206837B2|2003-06-18|2009-01-14|三菱瓦斯化学株式会社|Batch heating device|
    NL2000405C2|2006-12-22|2008-06-24|Willems Holding B V W|Method for making wood, wood product and its fixture sustainable.|
    CN101288963B|2008-06-11|2011-04-13|车炳雷|Wood electrothermal high-temperature processing device and heat treating device with combination drying function|
    DE102009031639A1|2009-07-03|2011-01-05|Herbert Hagensieker Sägewerk GmbH|Glulam|AT14770U1|2013-09-04|2016-05-15|Hedviga Group A S|Apparatus for the production of fuels for energy use|
    CZ304835B6|2013-09-04|2014-11-26|Hedviga Group, A.S.|Process for producing fuels for power engineering and fuel producing apparatus|
    CN103808121B|2014-03-05|2015-07-15|龙胜县宏胜木业有限公司|Castanopsis fagaceae drying process|
    US9470455B2|2014-08-11|2016-10-18|Weyerhaeuser Nr Company|Sorting green lumber|
    CN106573281B|2014-10-29|2020-06-16|宿州第威木构工程有限公司|Wood carbonization process and building material produced by same|
    GB201501073D0|2015-01-22|2015-03-11|Univ Dublin|A method and apparatus for thermochemically processing material|
    DK178526B1|2015-03-05|2016-05-23|Danish Wood Technology As|Method for Treatment of Wood|
    KR101655128B1|2015-04-01|2016-09-08|주식회사 티피에스|Multipurpose dry apparatus for wood amd method for drying|
    CN105563581B|2016-01-16|2017-04-26|南京林业大学|Hot and humid high-pressure wood heat treatment method|
    CN105773766B|2016-04-05|2017-09-26|中南林业科技大学|A kind of drying of wood and heat modification combination treatment method and device|
    SE540196C2|2016-06-15|2018-04-24|Stora Enso Oyj|Thermally modified wood product and a process for producing said product|
    DK179094B1|2016-07-15|2017-10-23|Wtt Holding Aps|Method and system for thermal modification of wood, as well as a control program for carrying out the improved method|
    CN106003321B|2016-07-15|2017-05-31|河南聆海整体家具有限公司|Suitable for log or the heat modification method of thick square bar|
    DE102018106806A1|2018-02-21|2019-08-22|Reinhard Brunner|Drying device for drying hygroscopic material to be dried|
    CN108507173A|2018-03-27|2018-09-07|陈洁|A kind of chemical raw material barrel heating device|
    RU2724421C2|2018-08-27|2020-06-23|Василий Юрьевич Чернов|Method and device for preparation and high-temperature treatment of wood|
    CN110715511A|2019-09-23|2020-01-21|吴江市松陵电器设备有限公司|Single-door microcirculation vacuum drying oven cooling system|
    CN111283840A|2020-02-14|2020-06-16|南京林业大学|Method for reducing chromatic aberration in wood board drying process|
    法律状态:
    2018-06-26| B06F| Objections, documents and/or translations needed after an examination request according [chapter 6.6 patent gazette]|
    2019-07-30| B06U| Preliminary requirement: requests with searches performed by other patent offices: procedure suspended [chapter 6.21 patent gazette]|
    2020-06-09| B06A| Patent application procedure suspended [chapter 6.1 patent gazette]|
    2020-10-06| B09A| Decision: intention to grant [chapter 9.1 patent gazette]|
    2020-12-22| B16A| Patent or certificate of addition of invention granted [chapter 16.1 patent gazette]|Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 15/06/2012, OBSERVADAS AS CONDICOES LEGAIS. |
    优先权:
    申请号 | 申请日 | 专利标题
    ITRM2011A000314|2011-06-16|
    ITRM20110314|ITRM20110314A1|2011-06-16|2011-06-16|PROCEDURE FOR THERMAL MODIFICATION OF HIGH-TEMPERATURE TIMBER WITHIN A VACUUM D AUTOCLAVE NOW FORWARD FOR A PATENTED DENOMINATION|
    PCT/IT2012/000180|WO2012172585A2|2011-06-16|2012-06-15|High temperature thermal modification process of wood in a vacuum autoclave|
    [返回顶部]