JPH03181777A - Drying method for wood - Google Patents
Drying method for woodInfo
- Publication number
- JPH03181777A JPH03181777A JP32021789A JP32021789A JPH03181777A JP H03181777 A JPH03181777 A JP H03181777A JP 32021789 A JP32021789 A JP 32021789A JP 32021789 A JP32021789 A JP 32021789A JP H03181777 A JPH03181777 A JP H03181777A
- Authority
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- Japan
- Prior art keywords
- surface layer
- drying
- moisture
- moisture content
- center
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
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- Drying Of Solid Materials (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は木材を前乾燥と後乾燥の二工程に分けて乾燥す
るようにした木材の乾燥方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for drying wood in which wood is dried in two steps: pre-drying and post-drying.
従来、木材の乾燥方法としては、−殻内には外部から熱
風を加えて木材表層部から水分を蒸発させる外部加熱法
が採用されている。Conventionally, as a method for drying wood, an external heating method has been adopted in which hot air is applied from the outside into the shell to evaporate moisture from the surface layer of the wood.
また、高周波を加えて木材を内部から加熱する高周波加
熱法も一部に採用されている。In addition, high-frequency heating methods, which heat wood from the inside by applying high-frequency waves, are also used in some cases.
ところが、上記外部加熱法によると、木材の温度分布が
表層部で高く、中央部で低くなり、中央部から表層部へ
の水分の移動が行なわれにくいため、表層部が乾燥して
も中央部が未乾燥状態のままとなるという事態が起こっ
ていた。このため、乾燥ずみ製品として市場に出された
後、建築物等に使用された場合に収縮や狂いが起こりや
すいという問題があった。However, according to the above external heating method, the temperature distribution of the wood is high at the surface layer and low at the center, making it difficult for moisture to move from the center to the surface layer. A situation was occurring in which the water remained undried. For this reason, there has been a problem in that, after being put on the market as a dried product, it tends to shrink or become distorted when used in buildings or the like.
また、表層部と中央部の含水率の差が大きくなりがちで
あるため、表層部の割れが生じやすいという欠点もあっ
た。Furthermore, since the difference in moisture content between the surface layer and the center tends to be large, there is also a drawback that cracks tend to occur in the surface layer.
一方、高周波加熱法では、上記外部加熱法とは逆に木材
中央部から加熱するため、中央部から表層部への水分の
移動が活発に行なわれるものの、この高周波加熱のみに
よって木材を乾燥させる従来方法によると、中央部が過
乾燥状態となりやすいため、内部割れや焦げが発生しや
すい。そこで、中央部と表層部の含水率の差が極端に大
きくならないように高周波を低エネルギーで長時間加え
ることになるため、結果的に必要乾燥時間が長くなるう
えに、エネルギー効率が悪く、乾燥コストが高くなると
いう問題があった。On the other hand, in the high-frequency heating method, contrary to the above-mentioned external heating method, the wood is heated from the center, so moisture moves actively from the center to the surface layer. According to this method, the center tends to become over-dry, which tends to cause internal cracks and charring. Therefore, in order to prevent the difference in moisture content between the center and the surface layer from becoming extremely large, high frequency waves are applied for a long time at low energy levels, which results in a longer drying time and poor energy efficiency. There was a problem of high cost.
そこで本発明は、中央部と表層部の含水率の差が小さい
良好な乾燥状態が得られ、しかも、乾燥時間を短縮でき
るとともに、乾燥コストを安くすることができる木材の
乾燥方法を提供するものである。SUMMARY OF THE INVENTION Therefore, the present invention provides a method for drying wood that can obtain a good drying condition with a small difference in moisture content between the central part and the surface layer, shorten drying time, and reduce drying costs. It is.
本発明は、木材を高周波によって内部加熱することによ
り蒸気圧を上げ、内部水分を中央部から表層側に移動さ
せて含水率が中央部で低く表層部で高くなる状態まで前
乾燥させた後、外部加熱法により、水分を表層部から発
散させて表層部の含水率が中央部の含水率よりも低くな
る状態まで後乾燥させるものである。In the present invention, the wood is internally heated by high frequency to increase the steam pressure, and the internal moisture is moved from the center to the surface layer. After pre-drying the wood until the moisture content is low in the center and high in the surface layer, By an external heating method, moisture is evaporated from the surface layer, and post-drying is performed until the moisture content of the surface layer is lower than that of the center.
(作用)
このように、高周波加熱による前乾燥工程で、中央部を
高温状態として内部水分を中央部から表層部に押出して
表層部を高含水率状態とした後、外部加熱による後乾燥
工程で、この表層部に集めた水分を外部に蒸発させるた
め、高周波加熱時間、外部加熱時間とも短縮されて乾燥
効率が良くなり、しかも中央部と表層部の含水率の差が
小さい均一な乾燥状態を得ることができる。従って、建
築物等に使用中に収縮や狂いの発生が少ない。(Function) In this way, in the pre-drying process using high-frequency heating, the central part is kept in a high temperature state and the internal moisture is pushed out from the central part to the surface layer to make the surface layer a high moisture content state, and then in the post-drying process by external heating. Since the moisture collected in the surface layer is evaporated to the outside, both the high-frequency heating time and the external heating time are shortened, improving drying efficiency and achieving a uniform drying state with a small difference in moisture content between the center and surface layers. Obtainable. Therefore, shrinkage and distortion are less likely to occur during use in buildings, etc.
また、高周波加熱のみによって乾燥させる従来方法と比
較して、乾燥時間が短く、投下エネルギーも少なくて乾
燥コストが安くてすむ。Furthermore, compared to the conventional method of drying using only high-frequency heating, the drying time is shorter, less energy is required, and the drying cost is lower.
〔実施例)
本発明を以下の実施例に基づいてさらに詳細に説明する
。[Example] The present invention will be explained in more detail based on the following example.
実施例1
被乾燥材として90aaX 90iigzX 4000
m11のベイツガ角材を用い、これに防腐剤を注入した
後、前乾燥として高周波加熱し、さらに後乾燥として熱
風による外部加熱を行なうという手順で、防腐剤注入I
(初期含水量)を異ならせた4種類の試料イ、口、ハ、
二について複数本ずつ乾燥させ、それぞれの乾燥状態(
含水率分布)を測定した。Example 1 90aaX 90iigzX 4000 as material to be dried
The preservative injection I
Four types of samples with different (initial water content)
2. Dry several pieces at a time, and check the drying state of each (
moisture content distribution) was measured.
その結果を表1に示す。The results are shown in Table 1.
(他の乾燥条件)
■ 高周波加熱−高周波シールドを施した乾燥室内に防
腐剤注入直後の複数本ずつ5種類の角材を搬入し、10
0℃(角材内部m度〉までの立上がり2時間、100℃
での保持2時間で高周波加熱を行なった。(Other drying conditions) ■ High-frequency heating - Five types of square lumber immediately after injecting preservatives were brought into a drying room equipped with a high-frequency shield, and 10
Rise to 0℃ (m degrees inside the square material) for 2 hours, 100℃
High frequency heating was performed while holding at 2 hours.
■ 外部加熱−高周波加熱に引続き、別の乾燥室内に試
料を移し、約50℃の室温下で熱風による加熱を3日間
連続して行なった。(2) External heating - Following high-frequency heating, the sample was transferred to another drying chamber and heated with hot air at a room temperature of about 50° C. for three consecutive days.
■ 測定方法
外部加熱による処理終了後に各試料の断片をとり、90
jw+X90amの断面において、表面から20M厚の
表側表層部分、同20〜7〇−厚の中央部分、同70〜
90am厚の裏側表層部分の含水率を全乾法によって測
定した。なお、各試料の注入後の初期平均含水率は、試
料イが113%、試料口が110%、試料ハが129%
であった。■Measurement method After finishing the external heating process, take a piece of each sample and heat it for 90 minutes.
In the cross section of jw +
The moisture content of the 90-am-thick back surface layer portion was measured by a total dry method. The initial average moisture content of each sample after injection is 113% for sample A, 110% for sample opening, and 129% for sample C.
Met.
表
上表に示す通り、高周波加熱が4時間、外部加熱が3日
間という短時日でありながら、最高含水率が表側表層部
で25%(平均では23%)、裏側表層部では26%(
平均では24%)、中央部で33%(平均で32%)と
なり、各試料とも乾燥ずみ製品として好適な高乾燥状態
が得られた。As shown in the table above, despite the short time of 4 hours for high-frequency heating and 3 days for external heating, the maximum moisture content was 25% in the front surface layer (23% on average) and 26% in the back surface layer (
24% on average) and 33% in the center (32% on average), indicating that each sample had a highly dry state suitable as a dried product.
また、表層部と中央部の含水率の差が平均で8〜9%の
小さな範囲におさまり、試料全体として均一な乾燥状態
が得られた。このことは、従来の外部加熱法では2〜4
週間を要していた乾燥日数を4〜5日に短縮したことに
なる。Further, the difference in moisture content between the surface layer and the center was within a small range of 8 to 9% on average, and a uniform dry state was obtained as a whole sample. This means that in conventional external heating methods, 2 to 4
This means that the drying time, which used to take weeks, has been shortened to 4 to 5 days.
実施例2
実施例1と同じベイツガ90MX 90MX 4000
Mの角材について、実施例1とは高周波加熱および防腐
剤注入量の条件を少し変えて同様の乾燥を行ない、しか
も高周波加熱(前乾燥〉後と、これに続く外部加熱(後
乾燥)後のそれぞれについて乾燥状態を調べた。その結
果を表2に示す。Example 2 Same as Example 1 Hemlock 90MX 90MX 4000
Regarding the square timber of M, the same drying was carried out as in Example 1 with slightly different conditions of high frequency heating and preservative injection amount, and in addition, after high frequency heating (pre-drying) and subsequent external heating (post-drying). The drying state of each was investigated.The results are shown in Table 2.
乾燥条件
■ 高周波加熱−100℃までの立上がり3時間、保持
2時間で高周波加熱を行なった。Drying conditions (1) High frequency heating High frequency heating was performed by rising to -100°C for 3 hours and holding for 2 hours.
■ 外部加熱一実施例1と同じ。■ External heating - Same as Example 1.
■ 測定方法−高周波加熱終了後と外部加熱終了後とに
それぞれ各試料の断片をとり、実施例1と同様の方法に
よって含水率を測定した。(2) Measuring method - A piece of each sample was taken after the high-frequency heating and after the external heating, and the water content was measured in the same manner as in Example 1.
なお、防腐剤注入後の初期含水率は次の通りであった。The initial moisture content after the preservative injection was as follows.
試料二・・・表側平均が120%、裏側平均が127%
、中央平均が100%。Sample 2...Front side average is 120%, back side average is 127%
, the median average is 100%.
試料ホ・・・表側平均が172%、裏側平均が138%
、中央平均が160%。Sample E...Front side average is 172%, back side average is 138%
, the median average is 160%.
表
工:高周波加熱後
■:外部加熱後
上表から明らかなように、内部含水率が、高周波加熱終
了時点では、中央部で低く、表層部で高くなり、外部加
熱終了後にはこの関係が逆転し、実施例1の場合と同様
に相対的に表層部で低く、中央部で高くなった。Surface treatment: After high-frequency heating ■: After external heating As is clear from the table above, at the end of high-frequency heating, the internal moisture content is low in the center and high in the surface layer, and this relationship is reversed after the end of external heating. However, as in Example 1, it was relatively low at the surface layer and high at the center.
この乾燥状況をより明確に把握するため、本発明者にお
いては、試料二について、防腐剤注入直後、高周波加熱
後、外部加熱1日後、同2日後、同3日後とより細かく
測定した。この結果(含水率推移)を図に示す。In order to understand this drying situation more clearly, the present inventor conducted more detailed measurements of sample 2 immediately after preservative injection, after high frequency heating, 1 day after external heating, 2 days after that, and 3 days after. The results (moisture content transition) are shown in the figure.
同図に示すように、防腐剤の注入直後では、含水率が中
央部および表層部(表側のみ例示〉とも100〜120
%と高含水状態となっている。As shown in the figure, immediately after the preservative is injected, the moisture content is 100 to 120 in both the central and surface areas (only the surface side is shown).
% and has a high water content.
次に、高周波加熱により、中央部、表層部とも含水率が
低下するが、内部加熱によって水分が中央部から表II
部に向けて押出されることにより、含水率の低下の度合
は中央部の方が大きく、表層部に水分が集められる傾向
となった。Next, due to high frequency heating, the moisture content decreases in both the center and surface layers, but internal heating removes moisture from the center to Table II.
By being extruded toward the center, the degree of decrease in moisture content was greater in the center, and water tended to collect in the surface layer.
この後、外部加熱の開始に伴って、表層部に溜まった水
分が蒸発し、表層部の含水率は急カーブで低下する。こ
れに対し、中央部の含水率低下はゆるやかとなる。Thereafter, with the start of external heating, the moisture accumulated in the surface layer evaporates, and the moisture content of the surface layer decreases in a sharp curve. On the other hand, the moisture content in the center decreases more slowly.
そして、外部加熱2日後には含水率の関係が逆転し、中
央部で高く、表層部で低くなる。Then, after two days of external heating, the relationship of moisture content is reversed, being higher in the center and lower in the surface layer.
さらに、外部加熱3日目に入ると、表層部、中央部とも
乾燥度は鈍化し、最終的に含水率が表層部で28%、中
央部で41%となった。また、この方法によれば、中央
部と表層部に生ずる乾燥応力が小さく、割れや狂い等の
損傷を小さく抑えることができる。Furthermore, on the third day of external heating, the degree of dryness slowed down in both the surface layer and the center, and the final moisture content was 28% in the surface layer and 41% in the center. Further, according to this method, the drying stress generated in the center portion and the surface layer portion is small, and damage such as cracking and distortion can be suppressed to a small level.
ここで比較のために、熱風を用いた外部加熱のみによる
従来方法での乾燥状況を表3に示す。For comparison, Table 3 shows the drying conditions obtained by the conventional method using only external heating using hot air.
なお、試料a、b、cとも、ベイツガ90 m X90
ai+X40001w+の角材を用い、それぞれについ
て防腐剤注入後に養生3日、夏期天日乾燥20日、熱風
乾燥3日の乾燥スケジュールで乾燥を行なった。In addition, all samples a, b, and c are Japanese hemlock 90 m x 90
Using ai+X40001w+ square lumber, each was dried on a drying schedule of 3 days of curing, 20 days of summer sun drying, and 3 days of hot air drying after injecting a preservative.
表
■=養養生3後
後:天天日乾燥2口
後防腐剤注入量の単位はKy/d)
この結果、全乾燥終了後には、各部の平均含水率が、表
側、裏裏の表層部で23%、中央部で49%となった。Table ■ = After 3 curing: After 2 drying in the sun, the unit of preservative injection amount is Ky/d) As a result, after complete drying, the average moisture content of each part is 23%, and 49% in the central region.
これから明らかなように、従来方法によると、表層部が
十分乾燥されるまで26日ときわめて長時日を要し、し
かも全乾燥終了後でも中央部ではいまだ高含水率状態で
表層部との差が大きくなる。As is clear from this, according to the conventional method, it takes an extremely long time of 26 days for the surface layer to be sufficiently dried, and even after complete drying, the center still has a high moisture content and there is no difference between the surface layer and the surface layer. becomes larger.
ところで、上記各実施例では、最も一般的なケースとし
て乾燥前に防腐処理を行なった木材を適用対象として例
にとったが、本発明はこの防腐処理を行なわず、生材か
ら乾燥を行なう場合にも勿論適用可能である。Incidentally, in each of the above embodiments, wood that has been preservative treated before drying is taken as an example of the most common case, but the present invention is applicable to the case where the wood is dried from raw material without this preservative treatment. Of course, it is also applicable to
上記のように本発明によるときは、高周波加熱による前
乾燥工程と、熱風を用いる外部加熱による後吃燥工程の
二工程に分け、前乾燥工程で、中央部を高温状態として
、従来の乾燥法では抜けにくかった内部水分を中央部か
ら表層部に押出して表層部を高含水率状態とした後、後
乾燥工程で、この表層部に集めた水分を蒸発させるため
、乾燥効率が良く、木材全体として高乾燥状態、かつ、
中央部と表層部の含水率の差が小さい均一な乾燥状態を
得ることができる。しかも、高周波加熱のみによって乾
燥させる従来方法と比較して、乾燥時間を大幅に短縮で
きるとともに、乾燥コストを安くすることができ、また
木材の損傷が少ないため歩留りを高くすることができる
ものである。As described above, according to the present invention, the process is divided into two steps: a pre-drying step using high-frequency heating and a post-drying step using external heating using hot air. After that, the internal moisture that was difficult to remove is pushed out from the center to the surface layer, making the surface layer a high moisture content state. In the post-drying process, the moisture collected in the surface layer is evaporated, resulting in high drying efficiency and drying throughout the wood. as a highly dry condition, and
A uniform dry state with a small difference in moisture content between the center and surface areas can be obtained. Moreover, compared to the conventional method of drying using only high-frequency heating, this method can significantly shorten the drying time, reduce drying costs, and increase yields because there is less damage to the wood. .
図は本発明方法による実験例での木材試料の乾燥状況を
説明するためのグラフである。The figure is a graph for explaining the drying status of wood samples in experimental examples using the method of the present invention.
Claims (1)
圧を上げ、内部水分を中央部から表層側に移動させて、
含水率が中央部で低く表層部で高くなる状態まで前乾燥
させた後、外部加熱法により、水分を表層部から発散さ
せて表層部の含水率が中央部の含水率よりも低くなる状
態まで後乾燥させることを特徴とする木材の乾燥方法。1. By internally heating the wood using high frequency waves, the steam pressure is increased and internal moisture is moved from the center to the surface layer.
After pre-drying until the moisture content is low in the center and high in the surface layer, external heating is used to evaporate moisture from the surface layer until the moisture content in the surface layer is lower than that in the center. A method for drying wood characterized by post-drying.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP32021789A JPH03181777A (en) | 1989-12-08 | 1989-12-08 | Drying method for wood |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP32021789A JPH03181777A (en) | 1989-12-08 | 1989-12-08 | Drying method for wood |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH03181777A true JPH03181777A (en) | 1991-08-07 |
Family
ID=18119028
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP32021789A Pending JPH03181777A (en) | 1989-12-08 | 1989-12-08 | Drying method for wood |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03181777A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008254952A (en) * | 2007-04-03 | 2008-10-23 | Isolite Insulating Products Co Ltd | Method for producing inorganic fiber formed member |
-
1989
- 1989-12-08 JP JP32021789A patent/JPH03181777A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008254952A (en) * | 2007-04-03 | 2008-10-23 | Isolite Insulating Products Co Ltd | Method for producing inorganic fiber formed member |
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