JP2006035435A - Wood drying method and wood drying equipment - Google Patents

Wood drying method and wood drying equipment Download PDF

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JP2006035435A
JP2006035435A JP2004213980A JP2004213980A JP2006035435A JP 2006035435 A JP2006035435 A JP 2006035435A JP 2004213980 A JP2004213980 A JP 2004213980A JP 2004213980 A JP2004213980 A JP 2004213980A JP 2006035435 A JP2006035435 A JP 2006035435A
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drying
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coating film
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Kunita Arai
國太 荒井
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a wood drying method adaptable to the drying of wood represented, for example, by a floor heating flooring material, achieving high quality and low in cost, and wood drying equipment capable of performing this method. <P>SOLUTION: Wood, which is processed into a required dimension and has a heat-resistant coating film formed on its surface, is heated to a drying temperature or above in a drying process to evaporate and diffuse the moisture in the wood. The heat-resistant coating film is preferably a coating film made of a polyurethane resin or a coating film made of ceramic. Further, in the drying process, a drying means using a heating medium oil, which is constituted of at least one kind of oils and fats such as mineral oil, vegetable oil, animal oil and used waste oil, is desirably employed. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、木材の乾燥方法および乾燥設備に関し、特に、使用環境の変化に対して高い耐久性と安定性を発揮する木材を得ることが可能な乾燥方法とこれを実施するための乾燥設備に関するものである。   The present invention relates to a method for drying wood and a drying facility, and more particularly, to a drying method capable of obtaining wood exhibiting high durability and stability against changes in the use environment, and a drying facility for carrying out the method. Is.

通常、木材の乾燥方法として採用されている種々の人工乾燥方式は、建材などに使用される前の木材中の水分除去が主たる目的である。例えば、最近流行の床材(フローリング材)の場合、所要サイズに加工した板材を乾燥工程にて含水率10〜20%程度以下にまで乾燥させてから、表面を適宜の木材用塗料にて塗装し塗膜を形成させて製品として出荷している。
家庭用などの比較的狭い場所での使用では問題はないが、体育館等の広い面積での床材の使用に際しては、床材の使用枚数が多いことから、温度や湿度の環境変化に対して木材の収縮と膨張が問題となる。例えば、乾燥期には床材が収縮して床材相互間に隙間が生じ、また高湿度の時期には床材が膨張して浮き上がってしまう事態が発生する。また近年、冬期の暖房手段として床暖房方式が徐々に増える傾向にあるが、この床暖房に使用するフローリング材についても、上記の同様の事態が生じる。特に、含水率10%程度以上のものでは、高温時における幅方向の収縮が問題となり、実際には使用に供し得なかった。
Usually, various artificial drying methods employed as a method for drying wood are mainly intended to remove moisture in the wood before it is used as a building material. For example, in the case of a recently popular flooring material (flooring material), the board material processed to the required size is dried to a moisture content of about 10 to 20% or less in the drying process, and then the surface is painted with an appropriate wood paint. A coating film is formed and shipped as a product.
There is no problem in using it in a relatively small place such as home use, but when using flooring in a large area such as a gymnasium, the number of flooring used is large, so it is resistant to environmental changes in temperature and humidity. The shrinkage and expansion of wood is a problem. For example, the floor material contracts during the dry season, creating a gap between the floor materials, and the floor material expands and floats during high humidity. Further, in recent years, floor heating systems tend to gradually increase as winter heating means, but the same situation as described above also occurs in the flooring material used for this floor heating. In particular, when the water content is about 10% or more, shrinkage in the width direction at a high temperature becomes a problem, and it cannot be actually used.

床暖房用のフローリング材は、含水率で言えば大体7%以下にすることが望ましいが、現状の乾燥方式ではこの含水率以下にまで乾燥してこの含水率のまま維持することは、かなり困難であり、実現したとしてもコスト的に高価とならざるを得ない。従って、所望の含水率まで下げかつこの含水率を維持することが可能であると共に、コスト的にも安価な床材を供給できる乾燥方法の開発が強く要望されているのが実情であった。   Flooring materials for floor heating are preferably about 7% or less in terms of moisture content, but with the current drying method, it is quite difficult to dry to below this moisture content and maintain this moisture content. Even if it is realized, it must be expensive. Accordingly, there has been a strong demand for the development of a drying method that can reduce the moisture content to a desired level and maintain the moisture content and supply a floor material that is inexpensive in terms of cost.

従来の乾燥方式は多種多様提案されているが、コストや乾燥時間、および目標とする含水率などを考慮した場合、本件出願人が開発した特許文献1に開示した乾燥方法が非常に有利といえる。該特許文献1に示す乾燥方法は、水分と親和性のない熱媒体オイル中に木材を浸漬して、加熱工程、平衡工程およびオイル乾燥工程を経ることによって、含水率20%以下まで乾燥させることを内容とする。
特許第3044039号掲載公報
A wide variety of conventional drying methods have been proposed, but the drying method disclosed in Patent Document 1 developed by the present applicant can be said to be extremely advantageous in consideration of cost, drying time, target moisture content, and the like. . In the drying method shown in Patent Document 1, wood is immersed in a heat medium oil having no affinity for moisture and dried to a moisture content of 20% or less through a heating step, an equilibrium step, and an oil drying step. Is the content.
Patent No. 3044039 publication

しかしながら、上記した特許文献1による乾燥方法によれば、目標とする含水率に従前の乾燥方式に比較して極めて短時間で到達し得る利点はあるが、直接熱媒体オイルに浸漬することから、乾燥後の木材表面に僅かではあるがオイルが浸透するため、木材の使用目的によっては表面層の清浄化処理が必要とされる場合があった。例えば、このオイル乾燥方式を前記した床暖房用フローリング材の乾燥に適用した場合、最終的には含水率を7%以下にすること、乾燥後この含水率を維持し得ること、コスト面で安価なこと、の点での有利性は認められるが、上記した表面の清浄性に関しては問題を残していた。
本発明は、以上の点を考慮してなされたもので、例えば床暖房用フローリング材に代表されるような木材製品に適用でき、高品質を達成しかつ安価なコストで済む木材の乾燥方法およびこの方法を効果的に実施し得る乾燥設備を提供することを課題とする。特に、熱媒体オイルによる乾燥方式を採用する場合には、その利点を最大限に生かしつつ効率良く高品質の木材を得ることができる乾燥方法を提供すること目的とする。
However, according to the drying method according to Patent Document 1 described above, there is an advantage that it can be reached in a very short time compared to the previous drying method according to the target moisture content, but because it is directly immersed in the heat medium oil, Since oil permeates the surface of the wood after drying to a small extent, depending on the purpose of use of the wood, a cleaning treatment of the surface layer may be required. For example, when this oil drying method is applied to drying flooring materials for floor heating as described above, the moisture content should be finally reduced to 7% or less, the moisture content can be maintained after drying, and it is inexpensive in terms of cost. However, although the advantage in this respect is recognized, the above-mentioned surface cleanliness still has a problem.
The present invention has been made in consideration of the above points, and can be applied to, for example, a wood product represented by a flooring flooring material, achieves a high quality and can be produced at a low cost, and a method for drying wood. It is an object to provide a drying facility that can effectively carry out this method. In particular, when a drying method using a heat medium oil is employed, an object is to provide a drying method capable of efficiently obtaining high-quality wood while making the most of its advantages.

上記課題を達成するための本発明に係る木材の乾燥方法は、所要の寸法に加工され、表面に耐熱性の塗膜を形成した木材を乾燥工程にて乾燥温度以上に加熱し、木材中の水分を蒸発拡散させることを特徴とする。
上記の方法において、前記耐熱性の塗膜は、ポリウレタン樹脂製塗膜或いはセラミック製塗膜であることが好ましく、これらの塗膜は、木材の乾燥温度(大体100℃〜130℃)以上であっても変質せず、その塗膜としての形態を維持し得る。
また、上記の乾燥工程は、鉱物油、植物油、動物油もしくは使用済みの廃油の1種又は2種以上の油脂類で構成される熱媒体オイル中に木材を浸漬することにより乾燥を行うことが望ましい。
一方、本発明に係る乾燥設備は、所要の寸法に加工され、表面に耐熱性の塗膜を形成した木材間に桟木を挟んで外部から締付固定した複数の木材ブロックを、熱媒体オイル槽中に浸漬して木材を乾燥温度以上に加熱することを特徴とする。
上記の乾燥設備において、熱媒体オイル槽としては、木材ブロックを連続的に移動し得る乾燥槽、木材ブロックを浸漬する油槽、もしくは熱媒体オイルの注入と排出を可能とする筒状槽のいずれかを選択すればよい。
A method for drying wood according to the present invention for achieving the above-mentioned object is the method of heating a wood having a heat-resistant coating film formed on a surface thereof to a drying temperature or higher in a drying process, and processing the required dimensions. It is characterized by evaporating and diffusing moisture.
In the above method, the heat-resistant coating film is preferably a polyurethane resin coating film or a ceramic coating film, and these coating films have a drying temperature of wood (approximately 100 ° C. to 130 ° C.) or higher. Even if it does not change in quality, the form as the coating film can be maintained.
In the drying step, it is desirable to perform drying by immersing wood in a heat medium oil composed of one or more oils such as mineral oil, vegetable oil, animal oil, or used waste oil. .
On the other hand, the drying equipment according to the present invention comprises a plurality of wood blocks, which are processed to a required size and are clamped and fixed from the outside by sandwiching a pierced piece between woods having a heat-resistant coating film formed on the surface. It is characterized by heating the wood above the drying temperature by dipping in it.
In the above drying equipment, the heat medium oil tank is any one of a drying tank that can continuously move the wood block, an oil tank that immerses the wood block, or a cylindrical tank that enables the injection and discharge of the heat medium oil. Should be selected.

本発明に係る木材の乾燥方法によれば、極めて含水率の低い木材を容易にかつ低コストで得ることができると共に、特別な含水率維持処理を行うことなく低い含水率のままで木材を使用することが可能となる。このため本発明により、従前では無理とされていた、変形(特に、幅方向の伸縮)の小さいかつローコストの床暖房用フローリング材を提供することができる。
また、本発明に係る乾燥設備によれば、上記した方法を効果的に実施することが可能であり、効率的に目標とする含水率の木材を得ることができる。
According to the method for drying wood according to the present invention, it is possible to easily obtain low-moisture wood at low cost, and to use wood with low moisture content without performing special moisture content maintenance treatment. It becomes possible to do. Therefore, according to the present invention, it is possible to provide a floor heating flooring material with low deformation (especially expansion and contraction in the width direction) and low cost, which has been impossible in the past.
Moreover, according to the drying equipment which concerns on this invention, it is possible to implement the above-mentioned method effectively and to obtain the wood of the target moisture content efficiently.

以下、本発明の実施の形態を図面に基づいて説明するが、図示の例では床材の乾燥を具体例として示す。
図1は、本発明に係る乾燥方法の基本的な工程を示すもので、まず、床材加工工程Aとして、原木から所要のサイズの断面および長さに加工し、表面仕上を施した所望の床材用原板を得る。このとき原木は所要の加工が可能な含水率に予め公知の乾燥方式(自然乾燥もしくは蒸気乾燥などの適宜の人工乾燥方式)により乾燥しておく。この事前の含水率としては、例えば、柱材では25%、内装材では20%、特殊な床暖房用フローリング材では10%という値であり、これらをそれぞれ20%以下、15%以下、7%以下という含水率まで乾燥するのが本発明の目標である。なお、目標の含水率に達した場合の木材の収縮を考慮して、最終寸法に加工するときに、原板幅を1%程度、収縮代をとっておくこともできる。
Hereinafter, embodiments of the present invention will be described with reference to the drawings. In the illustrated example, drying of a flooring material is shown as a specific example.
FIG. 1 shows the basic steps of a drying method according to the present invention. First, as a flooring processing step A, a desired cross-section and length of a required size are processed from a raw wood and subjected to surface finishing. Get the flooring master. At this time, the log is dried in advance by a known drying method (appropriate artificial drying method such as natural drying or steam drying) to a moisture content that allows the required processing. The moisture content in advance is, for example, 25% for pillar materials, 20% for interior materials, and 10% for flooring materials for special floor heating. These are 20% or less, 15% or less, and 7%, respectively. It is a goal of the present invention to dry to a moisture content of: In consideration of the shrinkage of the wood when the target moisture content is reached, the width of the original plate can be reduced by about 1% when processing into the final dimensions.

次の塗装工程Bは、所要寸法に加工された原板表面を均一に塗装する工程である。本発明においてこの塗装工程にて用いる塗料としては、後述の乾燥工程における加熱温度で変質しない性質(耐熱性および耐久性)を有するものが要求される。乾燥温度は、100℃〜130℃程度となるので、塗料の耐熱温度はそれ以上の温度に耐えるものでなければならない。この条件を満たせばいかなる塗料でも良いが、通常、床材用の塗料として広く使用されている耐摩耗性や耐薬品性に優れたポリウレタン樹脂塗料が最も好ましく、他にはセラミック塗料でも使用可能である。なお、ポリウレタン樹脂塗料の塗装後に、UV(Ultra Violet)処理を施すことが望ましい。UV処理は、紫外線を照射することで塗膜を硬化させ、より優れた耐摩耗性、可とう性、美装性等を発揮させるものである。
塗装は木材の全面にむらなく均等に塗料を塗布することが必要であるが、塗装手段としては、スプレー、ロールコータ、刷毛塗りなど公知の方式のなかから適宜選択すればよい。塗装終了後は、塗料の熱風乾燥など後処理を行って木材表面に所望の塗膜を形成してから次の乾燥工程に送る。
The next painting step B is a step of uniformly painting the surface of the original plate that has been processed to the required dimensions. In the present invention, the paint used in this coating step is required to have a property (heat resistance and durability) that does not change at the heating temperature in the drying step described later. Since the drying temperature is about 100 ° C. to 130 ° C., the heat resistance temperature of the paint must withstand higher temperatures. Any paint is acceptable as long as this condition is met, but polyurethane resin paints with excellent wear resistance and chemical resistance, which are widely used as paints for flooring, are most preferred, and ceramic paints can also be used. is there. In addition, it is desirable to perform UV (Ultra Violet) processing after the application of the polyurethane resin paint. In the UV treatment, the coating film is cured by irradiating with ultraviolet rays, and more excellent wear resistance, flexibility, beauty, etc. are exhibited.
The coating needs to be applied evenly over the entire surface of the wood, but the coating means may be appropriately selected from known methods such as spraying, roll coater, and brush coating. After the coating is finished, the coating film is subjected to post-treatment such as hot air drying to form a desired coating film on the surface of the wood, and then sent to the next drying step.

次の乾燥工程Cにおいては、塗装後の木材を100℃以上の温度に加熱し、木質中の水分を排出させ目標の含水率にするが、乾燥手段としては熱媒体オイル乾燥方式、蒸気乾燥方式、減圧(真空)乾燥方式、マイクロ波或いは高周波加熱乾燥方式等、公知のいずれかの方式を採用すればよい。本発明では操業およびコスト面で有利な熱媒体オイル浸漬方式による乾燥工程にて説明するがこれに限定されるものではない。
木材の100℃以上の加熱により木質中の水分は蒸気となって木材外部に排出され、更に木材表面を被覆する塗膜をも通過して外部に排出されるが、逆に熱媒体オイルはこの塗膜を通過して木材内部には侵入しない。塗膜は100℃以上でも変質せず、しかも気体分子である蒸気は通過させるが、液体である熱媒体オイルや水は通過させない。目標の含水率に到達したところで乾燥工程を終えるが、乾燥工程から取出された木材には全面に塗膜がそのまま維持されていることから、空気中の水分が木材中に侵入することなく、木材の変形が少ないし、含水率が変動することはない。
乾燥工程Cにおける加熱パターンの例としては、前記特許文献1にも開示しているように、木材を熱媒体オイル中に浸漬し、該熱媒体オイルを昇温して木材を乾燥温度以上に加熱する工程と、熱媒体オイルの昇温をいったん乾燥温度近辺で止め、この温度で一定時間保持する工程と、再度熱媒体オイルを昇温して木材中の水分を蒸気発散させる乾燥工程と、からなるパターンを採用できる。勿論、本発明ではこのような加熱パターンに限定されることはなく、目標とする含水率に短時間に達するものであれば他の任意の加熱パターンであっても差し支えないし、場合によっては単純な加熱パターンも採用可能である。木材の種類や断面サイズなどの条件に合わせた最適な加熱パターンを選択すればよい。
In the next drying step C, the painted wood is heated to a temperature of 100 ° C. or higher to discharge the moisture in the wood to the target moisture content. As a drying means, a heat medium oil drying method, a steam drying method, etc. Any known method such as a vacuum (vacuum) drying method, a microwave or high-frequency heating drying method, or the like may be employed. In the present invention, the drying process using a heat medium oil immersion method, which is advantageous in terms of operation and cost, will be described, but the present invention is not limited to this.
When the wood is heated to 100 ° C or higher, the moisture in the wood becomes vapor and is discharged outside the wood, and further passes through the coating film covering the wood surface and is discharged outside. It does not enter the wood through the coating. The coating film does not change even at a temperature of 100 ° C. or higher, and vapor that is a gas molecule is allowed to pass through, but heat medium oil and water that are liquids are not allowed to pass through. When the target moisture content is reached, the drying process is completed, but since the coating film is maintained on the entire surface of the wood removed from the drying process, moisture in the air does not enter the wood, and the wood There is little deformation and the moisture content does not fluctuate.
As an example of the heating pattern in the drying step C, as disclosed in Patent Document 1, wood is immersed in a heat medium oil, and the temperature of the heat medium oil is increased to heat the wood to a drying temperature or higher. A step of temporarily stopping the temperature increase of the heat transfer medium oil near the drying temperature and maintaining the temperature at this temperature for a certain period of time, and a drying step of increasing the temperature of the heat transfer medium oil again to vaporize moisture in the wood. The following pattern can be adopted. Of course, the present invention is not limited to such a heating pattern, and any other heating pattern may be used as long as the target moisture content can be reached in a short time. A heating pattern can also be employed. What is necessary is just to select the optimal heating pattern according to conditions, such as a kind of wood, and cross-sectional size.

乾燥工程Cにおいて用いる熱媒体オイルは、水との親和性のないものであって、発火点および引火点が高い(乾燥温度以上)油脂類が好ましい。また、毒性のないもの或いはあってもきわめて弱い性質のものが望ましい。これらの条件を前提として、鉱物油、植物油、動物油、使用済みの廃液などの中から選べばよく、場合によっては1種に限らず複数の油脂を混合してもよい。鉱物油では前記特許文献1にも示しているように潤滑油(例えば、出光興産(株)の「ダイナフレシア」W−8,W−32,P−32など)が適しており、また、使用済みの廃液としては使用済みのエンジンオイルが最適である。
乾燥工程Cを経て目標の含水率にまで乾燥された木材は、最終的には清浄工程Dにおいてその表面のオイルなどの汚れを洗浄或いは拭き取りによって清浄化してから製品として出荷する。
The heat medium oil used in the drying step C is preferably oil and fat having no affinity for water and having a high ignition point and flash point (above the drying temperature). Also, non-toxic or even very weak properties are desirable. On the premise of these conditions, the oil may be selected from mineral oil, vegetable oil, animal oil, used waste liquid, and the like. Depending on the case, a plurality of fats and oils may be mixed. As mineral oil, lubricating oil (for example, “Dyna Fresia” W-8, W-32, P-32, etc. of Idemitsu Kosan Co., Ltd.) is suitable and used as described in Patent Document 1. Used engine oil is the best waste liquid.
The wood dried to the target moisture content through the drying process C is finally cleaned in the cleaning process D by cleaning or wiping off dirt on its surface, and then shipped as a product.

次に、本発明の乾燥設備の具体例を説明するが、便宜上熱媒体オイル浸漬方式の乾燥設備を実施例としている。
図2は、乾燥設備に装入する前に、多数本の被乾燥木材(塗装済み木材)を固定用圧締枠にて1個のブロック体として包囲固定した例を示す。すなわち、縦横方向に一定の間隔をおいて複数列(図では4列)および複数段(図では6段)に、上下間に桟木2を挟んで多数(図では合計24)の木材1を並置すると共に、これらを上下から圧締枠3にて締付け固定し、1つのブロック体を構成する。これら木材は、上述した塗装工程により表面に所望の塗膜が形成されたものである。圧締枠3にて固定するのは、乾燥後に水分が木質から排出されたとき、木質内の水分の均衡がくずれ木質に歪みが生じ、これが捩れ、反り、撓み発生の原因となることから、これを防止するために木材全体を圧締枠で固定するのである。板材や構造材の場合、桟木を多くして固定箇所を多くすることで、捩れなどの発生をより効果的に防止することが好ましい。
Next, although the specific example of the drying equipment of this invention is demonstrated, the drying equipment of the heat medium oil immersion system is made into the Example for convenience.
FIG. 2 shows an example in which a large number of wood to be dried (painted wood) is enclosed and fixed as a single block body by a fixing pressing frame before being loaded into a drying facility. That is, a large number (in the figure, 24 in total) of timbers 1 are juxtaposed in a plurality of rows (four rows in the figure) and a plurality of rows (six rows in the figure) with the pier 2 between the upper and lower sides at regular intervals in the vertical and horizontal directions. At the same time, these are clamped and fixed from above and below by the press-clamping frame 3 to constitute one block body. These woods have a desired coating film formed on the surface by the above-described coating process. The reason for fixing with the pressing frame 3 is that when moisture is discharged from the wood after drying, the balance of moisture in the wood is broken and distortion occurs in the wood, which causes twisting, warping, and bending. In order to prevent this, the whole wood is fixed with a pressing frame. In the case of a plate material or a structural material, it is preferable to prevent the occurrence of twisting more effectively by increasing the number of piers and the number of fixing points.

図3は、上記のようにして構成した被乾燥木材のブロックを連続的に乾燥させるベルト走行式の乾燥設備を示す。この方式は生産性を向上させるためには有効であるが、設備スペースに余裕のある場合に採用し得る。
図3において、4は図2の如くブロック状に形成された木材ブロック、5は長尺の乾燥槽で、その内部には熱媒体オイル6が満たされている。7は乾燥槽5に続く洗浄槽である。また、図示の例では少なくとも乾燥槽5の入側から洗浄槽7の出側に至るラインに沿ってチェーンコンベア8が配置されており、該チェーンコンベア8上に複数の木材ブロック4は任意の間隔で載置固定されて移動(連続的もしくは間欠的移動)し、乾燥処理を受ける。洗浄槽7は乾燥処理時に塗膜面に付着したオイルを洗浄するためのものであり、適宜の溶剤が使用される。乾燥槽5内の熱媒体オイルの温度や量、コンベアの速度など、木材の種類やサイズなどに応じて任意に制御すればよい。
FIG. 3 shows a belt-running drying facility for continuously drying a block of wood to be dried configured as described above. This method is effective for improving productivity, but can be employed when there is a sufficient space in the equipment.
In FIG. 3, 4 is a wood block formed in a block shape as shown in FIG. 2, 5 is a long drying tank, and the inside thereof is filled with a heat medium oil 6. Reference numeral 7 denotes a cleaning tank following the drying tank 5. In the illustrated example, a chain conveyor 8 is disposed at least along a line extending from the entry side of the drying tank 5 to the exit side of the washing tank 7, and the plurality of wood blocks 4 are arranged at arbitrary intervals on the chain conveyor 8. It is fixed and moved by (moves continuously or intermittently) and undergoes a drying process. The washing tank 7 is for washing the oil adhering to the coating surface during the drying process, and an appropriate solvent is used. What is necessary is just to control arbitrarily according to the kind of wood, size, etc., such as the temperature and quantity of the heat carrier oil in the drying tank 5, and the speed of a conveyor.

図4は、油槽によるバッチ形式の乾燥設備を示すもので、生産性は高くないが簡易に一定量の木材のオイル乾燥を行うことができる方式である。熱媒体オイルを満たした油槽9内には、上記と同様な木材ブロック4が装入・浸漬され、油槽に付設した加熱装置および攪拌装置などにより油温をコントロールしながら、少なくとも1個の木材ブロック4のオイル乾燥を行う。なお、木材ブロックを空の油槽9内に装入してから熱媒体オイルを充満してもよい。油槽9上部の蓋は開閉自在であり、閉鎖のときには密閉状態を維持できるようにする。   FIG. 4 shows a batch-type drying facility with an oil tank, which is a system that can easily dry a certain amount of wood, although productivity is not high. In the oil tank 9 filled with the heat medium oil, a wood block 4 similar to the above is inserted and immersed, and at least one wood block is controlled while controlling the oil temperature by a heating device and a stirring device attached to the oil tank. 4. Oil drying is performed. Note that the heat medium oil may be filled after the wood block is charged into the empty oil tank 9. The upper lid of the oil tank 9 is openable and closable so that the closed state can be maintained when closed.

図5は、効率的な作業とメンテナンスの容易な圧力釜方式の乾燥設備を示すもので、円筒形の本体10の一端面側を開閉・密閉可能な蓋11としており、本体10には熱媒体オイルの注入と排出を行うための適宜な手段が併設されている。乾燥作業に際してはこの蓋11を開にして上述した木材ブロック4を本体内に搬入し、蓋を閉め密閉してから本体内に所望の熱媒体オイルを注入し、塗装済み木材のオイル乾燥を行う。オイルの温度管理は注入後に行えばよい。乾燥終了後は、オイルを排出してから蓋11を開放し、木材を取出せばよい。   FIG. 5 shows a pressure cooker type drying facility that facilitates efficient work and maintenance. One end of the cylindrical main body 10 is a lid 11 that can be opened and closed, and the main body 10 has a heating medium. Appropriate means for injecting and discharging oil are provided. In the drying operation, the lid 11 is opened and the above-described wood block 4 is carried into the main body, the lid is closed and sealed, and then a desired heat medium oil is injected into the main body to dry the painted wood oil. . Oil temperature control may be performed after injection. After the drying is finished, the oil is discharged, the lid 11 is opened, and the wood is taken out.

なお、本発明の対象とする木材は、特に、床暖房用フローリング材が最適であるが、これに限ることなく、他の用途の板材、柱材、梁材、丸太、ログ材など他の木材全てに適用し得ることは勿論である。   The wood targeted by the present invention is particularly suitable for floor heating flooring materials, but is not limited to this, and other wood materials such as plate materials, pillar materials, beam materials, logs, log materials for other purposes. Of course, it can be applied to all.

[実施条件]
(1)被乾燥木材:縦12mm×横75mm×長さ1818mmの原板であって、用途は床暖房用フローリング材
(2)塗装条件 :木材用ポリウレタン樹脂塗料を吹付けにより上記原板全面に塗装、その後UV処理を施した。
(3)乾燥条件 :乾燥槽は、図4に示すタイプの浸漬槽であって槽内を130℃まで加熱可能とする。
(4)熱媒体オイル:出光興産(株)の「ダイナフレシア」(商品名)W−32
[実施結果]
上記の原板について塗装前の含水率を変えた5枚のものに対し上記の塗装を施したもの(No.1〜No.5 本発明例)、原板2枚について塗装をしなかったもの(No.6、No.7 比較例)とし、オイル乾燥前後の各板の重量と幅、含水率を測定した結果を表1に示す。
[Conditions]
(1) Wood to be dried: Original 12 mm long x 75 mm wide x 1818 mm long, flooring flooring material used (2) Coating conditions: Wood polyurethane resin paint is sprayed on the entire surface of the original plate, Thereafter, UV treatment was performed.
(3) Drying conditions: The drying tank is an immersion tank of the type shown in FIG. 4, and the inside of the tank can be heated to 130 ° C.
(4) Heat transfer oil: “Dyna Fresia” (trade name) W-32 from Idemitsu Kosan Co., Ltd.
[Result]
For the above-mentioned original plate, the above-mentioned coating was applied to the five sheets whose moisture content before coating was changed (No. 1 to No. 5 example of the present invention), and the two original plates were not coated (No. .6, No. 7 Comparative Example), and Table 1 shows the results of measuring the weight, width, and moisture content of each plate before and after oil drying.

Figure 2006035435
Figure 2006035435

表1に示すように、本発明例(No.1〜5)では、重量差が乾燥前後で−10g以上有るが、これは乾燥時に木質からの水分の蒸発によるもので、塗膜の存在によりこの重量はその後も変わりなかった。これに対し比較例(No.6,7)では塗膜が無いため乾燥時に熱媒体オイルの一部がしみ込み重量は増えている。含水率では本発明例および比較例共に、低位にすることができ、この含水率は本発明では塗膜の存在、比較例では表面の油膜の存在により変化はなかった。このため板幅についても乾燥前後でも大きな差異は無いが、比較例のものは表面が美麗でなく、床材としては不合格であった。
なお、因みに原板のままで他の乾燥法で同様な含水率まで乾燥させた場合には、乾燥後に水分を吸収してしまうため、板幅収縮量は1mmを超えてしまい、床暖房用としては不合格であった。
As shown in Table 1, in the present invention examples (Nos. 1 to 5), the weight difference is -10 g or more before and after drying. This is due to the evaporation of moisture from the wood during drying, and due to the presence of the coating film. This weight did not change thereafter. On the other hand, in the comparative examples (Nos. 6 and 7), since there is no coating film, a part of the heat medium oil saturates during drying and the weight increases. In the present invention and the comparative example, the moisture content can be lowered in both the present invention and the comparative example, and this moisture content was not changed by the presence of the coating film in the present invention and the presence of the oil film on the surface in the comparative example. For this reason, although there is no big difference also about board width before and behind drying, the thing of the comparative example was not beautiful as the surface, and was rejected as a flooring.
In addition, when it is dried to the same moisture content by other drying methods with the original plate as it is, moisture is absorbed after drying, so the plate width shrinkage exceeds 1 mm, and for floor heating It was a failure.

本発明に係る乾燥方法の基本的な工程を示す工程図である。It is process drawing which shows the basic process of the drying method which concerns on this invention. 本発明の乾燥設備に装入するための被乾燥木材ブロックの正面図(a)、側面図(b)である。It is the front view (a) and side view (b) of the to-be-dried wood block for charging to the drying equipment of this invention. 本発明に係る乾燥設備の1実施例を示す全体概略図である。1 is an overall schematic diagram showing one embodiment of a drying facility according to the present invention. 本発明に係る乾燥設備の他の実施例を示す説明図である。It is explanatory drawing which shows the other Example of the drying equipment which concerns on this invention. 本発明に係る乾燥設備の更に他の実施例を示す全体概略図である。It is the whole schematic which shows the further another Example of the drying equipment which concerns on this invention.

符号の説明Explanation of symbols

A 加工工程 B 塗装工程
C 乾燥工程
1 塗装済み木材 2 桟木
3 圧締枠 4 木材ブロック
5 乾燥槽 6 熱媒体オイル
7 洗浄槽 8 チェーンコンベア
9 油槽 10 本体
11 蓋
A Processing Process B Painting Process C Drying Process 1 Painted Wood 2 Crosspiece 3 Clamping Frame 4 Wood Block 5 Drying Tank 6 Heat Transfer Oil 7 Washing Tank 8 Chain Conveyor 9 Oil Tank 10 Main Body 11 Lid

Claims (5)

所要の寸法に加工され、表面に耐熱性の塗膜を形成した木材を乾燥工程にて乾燥温度以上に加熱し、木材中の水分を蒸発拡散させることを特徴とする木材の乾燥方法。   A method for drying wood, comprising: heating a wood having a heat-resistant coating film on a surface thereof having a heat-resistant coating film to a drying temperature or higher in a drying step to evaporate and diffuse moisture in the wood. 耐熱性の塗膜がポリウレタン樹脂製塗膜或いはセラミック製塗膜であることを特徴とする請求項1記載の木材の乾燥方法。   2. The method for drying wood according to claim 1, wherein the heat-resistant coating film is a polyurethane resin coating film or a ceramic coating film. 乾燥工程は、鉱物油、植物油、動物油もしくは使用済みの廃油の1種又は2種以上の油脂類で構成される熱媒体オイル中に木材を浸漬することにより乾燥を行うことを特徴とする請求項1又は2記載の木材の乾燥方法。   The drying step is performed by immersing wood in a heat medium oil composed of one or more kinds of oils such as mineral oil, vegetable oil, animal oil or used waste oil. 3. A method for drying wood according to 1 or 2. 所要の寸法に加工され、表面に耐熱性の塗膜を形成した木材間に桟木を挟んで外部から締付固定した複数の木材ブロックを、熱媒体オイル槽中に浸漬して木材を乾燥温度以上に加熱することを特徴とする木材の乾燥設備。   A plurality of wood blocks that have been processed to the required dimensions and have a heat-resistant coating film on the surface and sandwiched and fixed from the outside with a pierced timber are immersed in a heat medium oil bath to bring the wood above the drying temperature Wood drying equipment, characterized by heating to 熱媒体オイル槽が、木材ブロックを連続的に移動し得る乾燥槽、木材ブロックを浸漬する油槽、もしくは熱媒体オイルの注入と排出を可能とする筒状槽であることを特徴とする請求項4記載の乾燥設備。   5. The heat medium oil tank is a drying tank capable of continuously moving the wood block, an oil tank in which the wood block is immersed, or a cylindrical tank capable of injecting and discharging the heat medium oil. The drying equipment described.
JP2004213980A 2004-07-22 2004-07-22 Wood drying method and wood drying equipment Pending JP2006035435A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100755777B1 (en) * 2006-12-08 2007-09-05 박근수 Manufacturing method of log furniture
JP2016057048A (en) * 2014-09-08 2016-04-21 航 青木 Wood chip burning thermal medium oil burner
CN111306903A (en) * 2020-03-26 2020-06-19 苏州昊昇木驿生物科技有限公司 Microwave oil bath drying system and method for heavy and hard wood

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100755777B1 (en) * 2006-12-08 2007-09-05 박근수 Manufacturing method of log furniture
JP2016057048A (en) * 2014-09-08 2016-04-21 航 青木 Wood chip burning thermal medium oil burner
CN111306903A (en) * 2020-03-26 2020-06-19 苏州昊昇木驿生物科技有限公司 Microwave oil bath drying system and method for heavy and hard wood

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