1. Field of the Invention
The present invention relates generally to methods and apparatus for treating a commodity. More specifically, to a method and apparatus for treating wood products for the purpose of preserving the wood without the use of chemicals.
2. Description of Background Art
Heat treated wood and lumber is a relatively new, environmentally-friendly product. Wood that has been heat treated does not contain chemicals or compounds typically present in chemically treated lumber. Thus, the heat treated wood can be used in a wider variety of applications and with less concern for contact with humans, pets and other animals, ground water, plants and other elements of the environment.
When wood is exposed to high temperatures (i.e., 200 degrees centigrade or more), the properties of the wood change in relatively significant ways. Saps inside the wood are changed into a form not digestible by insects. By heating the wood to a high temperature, the moisture in the wood is reduced to 4% which will not support fungus, mold or bacteria. All types of woods can be heat treated. The stability of heat treated wood is enhanced, as compared to untreated forms, and the wood is naturally darkened so that painting and/or staining is, in many instances, unnecessary.
It is an object of an embodiment of the present invention to provide a method and apparatus for treating a commodity, such as lumber or wood products, by pulling heated air through and/or around a stack of commodity that may be stacked on pallets or carts.
Another object of the present invention is to provide a method and apparatus for treating a commodity, such as lumber or wood products, by circulating heated air through and/or around layers of the commodity so as to evenly and efficiently heat treat the commodity.
It is a further object of an embodiment of the present invention to provide a plurality of pallets or layered stacks of the commodity that are positioned in two rows with a space formed therebetween. A cover is positioned over at least a top surface and an exposed end surface of the commodities or an exposed surface of an air handler to form a plenum. The air handler is positioned to pull air from between the plurality of pallets and through the ventilation layers formed adjacent to the adjoining commodities and along the length of the space formed between the two rows for achieving an even flow of air for treating the commodity positioned on the pallets or in the layered stacks.
Other objects of an embodiment of the present invention are achieved by providing a method and apparatus for treating a commodity, such as lumber or wood products, by positioning the lumber or wood in a plurality of layers spaced apart so as to provide ventilation spaces therebetween. The commodity may be positioned in at least two rows with a space formed therebetween. A cover is positioned over at least a top surface and an exposed end surface of the row or an exposed surface of the air handler so as to provide a seal along the top surface and the end surface or an exposed surface of the air handler. The air handler is positioned in communication with the space between the rows so as to move air along the space and through the ventilation areas between the layers of the commodity. A source of heat is provided to allow for elevation of the temperature of the air circulated by the air handler. Unburnt fuel and oxygen are depleted from the heated air circulated by the air handler by use of a catalytic heater/converter so as to prevent combustion of the wood.
Further scope of applicability of the present invention will become apparent from the detailed description given hereinafter. However, it should be understood that the detailed description and specific examples, while indicating preferred embodiments of the invention, are given by way of illustration only, since various changes and modifications within the spirit and scope of the invention will become apparent to those skilled in the art from this detailed description.
The present invention will become more fully understood from the detailed description given hereinbelow and the accompanying drawings which are given by way of illustration only, and thus are not limitative of the present invention, and wherein:
As illustrated in
In the embodiment illustrated in
In addition, a reduction in physical mass and mechanical strength as a function of hydrolysis caused by acetic and formic acids being liberated during the heating process also occurs.
Further, dimensional stability is also of key importance. As wood or lumber is heated non-uniformly, stress risers result. The stresses cause surface and internal checking and cracking. The use of a high velocity, turbulent air flow is provided between the boards stacked in the heating unit 100 to evenly distribute the heat.
An electric heater or a boiler is operatively connected to provide heat to the heating unit 100. The boiler may be heated by using propane gas or oil, raw wood products or electricity. The present invention provides for a maximum utilization of various ways to provide heat to the heating unit 100 to enable a user to use various sources of fuel. The heating unit 100 is equipped with a steam boiler for developing raw steam or pressurized steam to raise the temperature up to 105 degrees C.
As illustrated in
A catalytic heater/converter 400 is used to burn unburnt fuel and for depleting oxygen from the sealed environment of the heating unit 100. As the wood or lumber is heated to the critical processing temperature of approximately 175 to 235 degrees C. (depending upon the wood species and the application), the commodity looses mass due to the pyrolysis reactions and exothermic oxidation reactions. By reducing the oxygen, the pyrolysis and the exothermic oxidation reactions are minimized. By reducing these reactions the present invention maintains more of the mechanical properties of the wood or lumber. The use of the catalytic heater/converter also reacts to burn any combustible gases which are liberated from the wood being processed in the heating unit 100. As illustrated in
The present invention utilizes a turbulent flow of air that is produced by the air handler 704 which is a high velocity fan system to circulate air within the heating unit 100 to produce turbulent air flow between the boards stacked in the heating unit 100. This reduces the mechanical stress in the wood to minimize physical warping, cracking, checking, etc. A system for drawing air to the center of the heating unit 100 and recirculating the air to a space 802 between an enclosure 702 and the stacks of commodities is used.
An integrated control system 600 is included for measuring the temperature of the heating unit 100, product temperature, product moisture content, oxygen levels in the heating unit 100, internal pressure in the heating unit 100, relative humidity in the heating unit 100, CO content in the heating unit 100, boiler conditions, safety conditions, etc. Adjustments to the heating unit 100 and operating variables will be carried out by the control system 600.
With further reference to
In an embodiment of the present invention, a plurality of stacks 701C and 701D of lumber may be arranged in two rows I and II with a space S formed therebetween. The air handler 704 may be positioned an end of the two rows with a cover positioned over the exposed surface of the air handler 704. In addition, the cover C would be positioned on the top surface and an exposed end surface of the stacks. The air handler 704 would pull heated air through ventilation areas between the layers of the lumber and exhaust the heated air into the space 802 provided between the enclosure 702 and the stacks 701C and 701D to ensure a flow of air around the stacks.
As illustrated in
In
A plenum P is formed between the two rows I and II, as illustrated in
Air handler 704 is positioned, in the embodiment of
The air handler 704 may exhaust air pulled through plenums P into the heating unit 100 for thermally treating the wood or lumber in the heating unit 100. Openings along the sides of the stacks are provided to allow the air to circulate, flowing from the sides of the stacks toward space S and through plenum P to air handler 704. In such embodiments, the environment inside the heating unit 100 is controlled, both in terms of temperature and the composition of the moisture, the unburnt gases and oxygen. The temperature of the air (or atmosphere) surrounding and circulating through enclosure 702 will vary between ambient or “room” temperature on the low side during the loading of the heating units to 175 to 235 degrees C. or more on the high side. At high temperatures, the percentage of oxygen in the heating unit 100 is reduced by use of the catalytic heater/converter 400 to burn unburnt fuel and to prevent combustion of the wood.
In other embodiments, the exhaust of air handler 704 is directed through passageways 802 formed on the sides of the stacks so as to form a closed air circulating system. In such embodiments, the temperature of the circulating air is controlled by heaters (not shown). The composition of the air (i.e., oxygen content, moisture content, etc.) may also be controlled to achieve proper heat treatment of the commodity.
The embodiment illustrated in
Another mechanism for assuring more even and uniform temperature control (i.e., heating and cooling) of the commodity is to control the rate of increase and decrease of the air temperature. Increasing or decreasing the air temperature incrementally (i.e., a few degrees at a time) affords time for the temperature of the commodity to increase or decrease in correspondence with the increases or decreases in air temperature. This facilitates, for example, relatively uniform treatment of a board located on an end of stacks 701A, 701B, 701C or 701D, as compared to a board in the same layer on an opposing end of the stack.
In a process of thermally treating wood or lumber, boards are stacked with a predetermined space between the boards. The boards are positioned on a trolley system for using the rails 500 for loading the boards into the heating unit 100.
At the beginning of the heating cycle, the heating unit 100 is heated by injecting raw saturated steam into the heating unit 100 with a turbulent air flow system. In addition, heaters connected to the heating unit 100 is actuated for providing additional heat. The steam injection provides a quick transfer of heat by condensing steam onto the wood surface as well as the moisture laden atmosphere helping to reduce the surface stress of wood. The catalytic heater/converter 400 is used to deplete the oxygen in the heating unit 100. The use of steam is not used for depleting the oxygen.
The temperature differential between the core of the commodity and the air is to be held constant at about 10 to 30 degrees C. This temperature differential will be programmable and will use multiple sensors arranged throughout the heating unit 100. There is a desire to raise the inner core temperature of the wood as rapidly as possible. However, the temperature differential between the air and the wood should not exceed the programmed value of 10 to 30 degrees C.
During the drying phase, the inner core temperature of the wood is raised to a first plateau of between 90 to 130 degrees C. Raw saturated steam initially injected into the heating unit 100 will be terminated and changed to a dry superheated steam. The drying phase is intended to permit the internal water in the wood to evaporate. The amount of time that the system is continued at the drying phase will depend on time, internal moisture content of the wood and relative humidity of the atmosphere in the heating unit 100. Venting to atmosphere through pressure controlling dampers will be provided.
During the treatment phase, after the drying phase has taken place, the temperature of the oven should be increased to the final treatment value. During this step, evacuation of the oxygen from the inside of the heating unit 100 should take place. At about 140 degrees C., the catalytic heater/converter 400 combination is turned on. This will burn unburnt fuel in the heating unit 100 to lower the oxygen level to 1 to 3 percent. The oxygen level is monitored and the catalytic heater/converter is turned off when the oxygen level is sufficiently low. The source of heat may be the boiler which can be switched from dumping raw steam into the heating unit 100 to a higher pressure boiler with a heat exchanger in the air stream. The source of the heat may be electric heating coils.
The pressure in the heating unit 100 should be maintained as slightly positive and above atmosphere to prevent any oxygen from entering the heating unit 100 through leaks.
The thermal treatment is continued for a predetermined time to permit the attainment of the final temperature by using the heating system for the duration of the treatment process. Oxygen depletion is maintained in this environment. The oxygen level should be monitored to assure the oxygen level does not rise. If the oxygen level rises, the catalytic heater/converter system is used to lower the oxygen level.
The temperature may be lowered by a combination of raw steam injection and water mist. Through the use of water mist and steam, the cooling ramp differential temperature is maintained between the wood product core and the turbulent air flow around the wood product. The set point differential temperature is a programmable value optimized on a per species basis to optimize product quality.
Although the present invention has been described with reference to particular means, materials and embodiments, from the foregoing description, one skilled in the art can easily ascertain the essential characteristics of the invention and various changes and modifications may be made to adapt the various uses and characteristics without departing from the spirit and scope of the invention.
The present application claims priority under 35 USC 119(e) to Provisional Patent Application No. 61/265,561 filed on Dec. 1, 2009 the entire contents of which are hereby incorporated by reference.
Number | Date | Country | |
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61265561 | Dec 2009 | US |