JPH045985Y2 - - Google Patents
Info
- Publication number
- JPH045985Y2 JPH045985Y2 JP1984060863U JP6086384U JPH045985Y2 JP H045985 Y2 JPH045985 Y2 JP H045985Y2 JP 1984060863 U JP1984060863 U JP 1984060863U JP 6086384 U JP6086384 U JP 6086384U JP H045985 Y2 JPH045985 Y2 JP H045985Y2
- Authority
- JP
- Japan
- Prior art keywords
- veneer
- moisture content
- moisture
- drying
- humidity control
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Landscapes
- Drying Of Solid Materials (AREA)
Description
【考案の詳細な説明】
[技術分野]
本考案は染色後などの高含水率となつた薄い単
板を乾燥させ規格含水率内に調湿する装置に関す
る。[Detailed Description of the Invention] [Technical Field] The present invention relates to an apparatus for drying a thin veneer with a high moisture content after dyeing and controlling the humidity to within a standard moisture content.
[背景技術]
合板の製造工程においては、湿気硬化型接着剤
により単板を接着し成形しているため、その材料
となる単板の含水率を一定の規格内に調整する必
要がある。例えば、染色後の単板の含水率は265
±35%であり、これを24±12%に調湿する必要が
ある。しかしながら、従来より用いられている蒸
気熱風ネツト乾燥機の乾燥処理能力は180〜220%
であり、この処理能力では
染色単板含水率 265±35%
乾燥仕上がり含水率 28±24%
であつて、乾燥調湿能力が低く単板を目的とする
規格内に仕上げることができないという欠点があ
つた。従つて、湿気硬化型接着剤に合つた含水率
調整が行えず、単板の接着不良、目ぼれ不良(単
板の含水率が高いために切削性が大きく影響さ
れ、積層接着後のスライス時に発生する。)が発
生し、また熱風を吹き付ける間接的な乾燥手段で
あるため、乾燥コストも非常に高いという問題が
あつた。[Background Art] In the manufacturing process of plywood, veneers are bonded and formed using a moisture-curing adhesive, so it is necessary to adjust the moisture content of the veneer to be within a certain standard. For example, the moisture content of the veneer after dyeing is 265
±35%, which needs to be adjusted to 24±12%. However, the drying capacity of conventionally used steam hot air net dryers is 180 to 220%.
With this processing capacity, the dyed veneer moisture content is 265 ± 35% and the dry finished moisture content is 28 ± 24%, but the drawback is that the drying humidity control ability is low and it is not possible to finish the veneer to the desired specifications. It was hot. Therefore, it is not possible to adjust the moisture content to suit moisture-curing adhesives, resulting in poor adhesion of veneers and poor glazing. ), and since it is an indirect drying method that blows hot air, the drying cost is also very high.
[考案の目的]
本考案は叙上のような技術的背景に鑑みて為さ
れたものであり、その目的とするところは乾燥能
力及び調湿能力が高く、しかも乾燥コストの低い
単板乾燥調湿装置を提供するにある。[Purpose of the invention] The present invention was developed in view of the technical background described above, and its purpose is to provide a veneer drying control system with high drying and humidity control abilities and low drying costs. Provides moisture equipment.
[考案の開示]
本考案単板の乾燥調湿装置は、互いに対向する
上下の回転自在な加熱ロール2で単板1の圧締と
加熱とを行い単板1を過乾燥状態に乾燥する熱ロ
ール脱水機3と、熱ロール脱水機3通過後の単板
1の含水率を検出する含水率センサー4と、過乾
燥されたた単板1に所定含水率よりも不足する水
分を供給して単板1を所定含水率に調湿する水分
供給装置5とから成ることを特徴とするものであ
り、このように直接加熱方式を採用すると共に絞
り脱水作用を加えることにより低コストでありな
がら高い乾燥能力を発揮させることができ、しか
も含水率センサーにより含水率検知後に水分供給
装置で最終的に含水率調整を行うことにより高い
調湿能力を有するものである。[Disclosure of the invention] The veneer drying and humidity control device of the present invention compresses and heats the veneer 1 with upper and lower rotatable heating rolls 2 facing each other, and generates heat that dries the veneer 1 to an overdry state. A roll dehydrator 3, a moisture content sensor 4 that detects the moisture content of the veneer 1 after passing through the hot roll dehydrator 3, and a moisture content sensor 4 that detects the moisture content of the veneer 1 after passing through the heated roll dehydrator 3, and supplies moisture that is insufficient than a predetermined moisture content to the overdried veneer 1. It is characterized by comprising a moisture supply device 5 that adjusts the moisture content of the veneer 1 to a predetermined moisture content, and by adopting a direct heating method and adding a squeezing dehydration effect, it is possible to achieve a low cost yet high cost. The drying ability can be exhibited, and the moisture content can be finally adjusted by the moisture supply device after the moisture content is detected by the moisture content sensor, so that it has a high humidity control ability.
(実施例)
第1実施例は第1図に示されており、熱ロール
脱水機3と、含水率センサー4と、2台の水スプ
レー装置6からなる水分供給装置5とから構成さ
れている。まず熱ロール脱水機3を説明する。2
は上下一対の回転自在な加熱ロールであり、単板
1の板厚(圧締前の板厚)よりも小さい間隙(単
板圧締中の加熱ロール2間距離)を隔てて上下に
対向させられている。また、加熱ロール2は高温
を有しており、その表面温度は一例として200℃
の温度範囲内でコントロールできるようにしてあ
る。このような上下一対をなす加熱ロール2は複
数段配設されている。図示例では6段(No.1,
No.2……No.6)となつている。乾燥前の単板1
は、例えば染色、脱色などの化学処理のために高
含水率となつており、例えば初期含水率265±35
%となつている。而して、木材の単板1は加熱ロ
ール2内へ単板1繊維方向に沿つて投入され、加
熱ロール2によつて圧締して脱水される(絞り効
果)と共に加熱ロール2表面で加熱乾燥させられ
(直接加熱効果)、第2図のグラフに示すように各
段において高い乾燥効率で処理され、約10%以下
の含水率に調整され、含水率ばらつきが小さくな
る。また単板1の表面は圧締により平滑に仕上げ
られる。この時の加熱ロール2の送り速度は
15m/minとしているが、これは板厚、樹種、比
重などの材要因、あるいはロール温度、ロール間
の間隙などの加熱ロール2の絞り条件によつて変
わり得るものである。このように熱ロール脱水機
3では加熱乾燥だけでなく、浮遊水の多い単板1
に絞りをかけて脱水しているので、大きな蒸発潜
熱を必要とせず、高含水率の単板1を効果的に低
い乾燥コストで乾燥させられるのである。しかも
単板1は、加熱されることにより軟化させられ、
脱水のための圧締力も小さくて済むという相乗効
果も奏する。4は熱ロール脱水機3の前方に配置
された含水率センサーであり、例えば遠赤外セン
サーやマイクロ波含水率計が使用される。単板1
は含水率センサー4により含水率を検出されなが
ら含水率センサー4を通過して水スプレー装置6
へ搬送され、含水率が10%にされている単板1に
一定量の水(76gr/m2)を上下面から均一に塗布
され、含水率が24±12.5%に調湿される。最後に
前方の含水率センサー4により含水率が24±12.5
%になつたことを確認する。(Embodiment) A first embodiment is shown in FIG. 1, and is composed of a hot roll dehydrator 3, a moisture content sensor 4, and a moisture supply device 5 consisting of two water spray devices 6. . First, the hot roll dehydrator 3 will be explained. 2
are a pair of upper and lower rotatable heating rolls that face each other vertically with a gap (distance between the heating rolls 2 during veneer pressing) that is smaller than the thickness of the veneer 1 (thickness before pressing). It is being In addition, the heating roll 2 has a high temperature, and its surface temperature is, for example, 200°C.
The temperature can be controlled within the temperature range. A plurality of such upper and lower pairs of heating rolls 2 are arranged in multiple stages. In the illustrated example, there are 6 stages (No. 1,
No.2...No.6). Veneer 1 before drying
has a high moisture content due to chemical treatments such as dyeing and bleaching, for example, the initial moisture content is 265±35
%. Thus, the wood veneer 1 is fed into the heating roll 2 along the fiber direction of the veneer, and is compressed and dehydrated by the heating roll 2 (squeezing effect) and heated on the surface of the heating roll 2. It is dried (direct heating effect), and as shown in the graph of Figure 2, it is processed with high drying efficiency at each stage, and the moisture content is adjusted to about 10% or less, reducing the variation in moisture content. Further, the surface of the veneer 1 is finished smooth by pressing. The feeding speed of heating roll 2 at this time is
Although the speed is set at 15 m/min, this may vary depending on material factors such as board thickness, wood species, and specific gravity, or drawing conditions of the heating rolls 2 such as roll temperature and gap between rolls. In this way, the hot roll dehydrator 3 not only heats and dries the veneer 1 with a lot of floating water.
Since the veneer 1 is squeezed to remove water, a large amount of latent heat of vaporization is not required, and the veneer 1 with a high moisture content can be effectively dried at a low drying cost. Moreover, the veneer 1 is softened by being heated,
It also has the synergistic effect of requiring less clamping force for dewatering. 4 is a moisture content sensor placed in front of the hot roll dehydrator 3; for example, a far-infrared sensor or a microwave moisture content meter is used. Veneer 1
While the water content is detected by the water content sensor 4, it passes through the water content sensor 4 and is sprayed into the water spray device 6.
A certain amount of water (76 gr/m 2 ) is evenly applied from the top and bottom of the veneer 1 whose moisture content is 10%, and the moisture content is adjusted to 24±12.5%. Finally, the moisture content sensor 4 at the front detects the moisture content as 24±12.5.
%.
第3図に示すものは本考案の他例であり、2対
のスポンジロール7により水分供給装置5を構成
したものである。しかして、第4図のグラフに示
すように、熱ロール脱水機3によつて含水率が8
±4%のばらつきの少ない単板1に仕上げ、含水
率センサー4はこの8±4%の含水率を検知し、
この設定範囲を外れて調湿不可能な単板1につい
ては作業者に報知し、この単板1は作業者により
取り除かれ、含水率が保証される。 The device shown in FIG. 3 is another example of the present invention, in which the moisture supply device 5 is constructed by two pairs of sponge rolls 7. As shown in the graph of FIG.
The veneer 1 is finished with a small variation of ±4%, and the moisture content sensor 4 detects this moisture content of 8±4%.
The operator is notified of any veneer 1 that is out of this setting range and whose humidity cannot be controlled, and the operator removes the veneer 1 to ensure the moisture content.
[考案の効果]
本考案は叙述のごとく構成されているから、加
熱ロールにより単板を圧締して水分を絞り出せ、
高含水率の単板であつても蒸発潜熱を必要とする
ことなく低コストで乾燥させられ、しかもこれに
加熱によつ乾燥方法を加えることにより高い乾燥
能力を発揮できると共に熱で単板を軟化させ単板
の圧締を容易にできる利点がある。また、熱ロー
ル脱水機で単板の圧締と加熱とを行つて、単板を
過乾燥状態に乾燥しているので、過乾燥すること
により単板の含水率のばらつきを小さくすること
ができ、しかもその後含水率センサーで単板の含
水率を検知し、過乾燥された単板に所定含水率よ
りも不足する水分を供給して単板を所定含水率に
調湿するので、単板の含水率が一定になる利点が
ある。[Effects of the invention] Since the invention is constructed as described above, the veneer can be pressed with heated rolls to squeeze out moisture.
Even veneers with high moisture content can be dried at low cost without requiring latent heat of vaporization.Additionally, by adding a heating drying method to this method, high drying ability can be demonstrated and veneers can be dried using heat. It has the advantage of softening and making it easier to press the veneer. In addition, the veneer is compressed and heated using a hot roll dehydrator to dry the veneer to an over-dry state, so over-drying can reduce variations in the moisture content of the veneer. Moreover, after that, the moisture content of the veneer is detected by a moisture content sensor, and the moisture that is insufficient than the predetermined moisture content is supplied to the overdried veneer to adjust the moisture content of the veneer to the predetermined moisture content. It has the advantage of keeping the moisture content constant.
第1図は本考案の一実施例を示す概略全体図、
第2図は同上の各工程毎の含水率推移を示すグラ
フ、第3図は本考案の他例を示す概略全体図、第
4図は同上の各工程毎の含水率推移を示すグラフ
であり、1は単板、2は加熱ロール、3は熱ロー
ル脱水機、4は含水率センサー、5は水分供給装
置、6は水スプレー装置、7はスポンジロールで
ある。
FIG. 1 is a schematic overall diagram showing an embodiment of the present invention;
Figure 2 is a graph showing the transition of moisture content in each step of the same as above, Figure 3 is a schematic overall diagram showing another example of the present invention, and Figure 4 is a graph showing the transition of moisture content in each step of the same as above. , 1 is a veneer, 2 is a heated roll, 3 is a heated roll dehydrator, 4 is a moisture content sensor, 5 is a moisture supply device, 6 is a water spray device, and 7 is a sponge roll.
Claims (1)
で単板の圧締と加熱とを行い単板を過乾燥状態
に乾燥する熱ロール脱水機と、熱ロール脱水機
通過後の単板の含水率を検出する含水率センサ
ーと、過乾燥された単板に所定含水率よりも不
足する水分を供給して単板を所定含水率に調湿
する水分供給装置とから成る単板の乾燥調湿装
置。 (2) 単板に水を吹き付ける水スプレー装置により
水分供給装置を構成して成る実用新案登録請求
の範囲第1項記載の単板の乾燥調湿装置。 (3) 単板に水を塗布するスポンジロールにより水
分供給装置を構成して成る実用新案登録請求の
範囲第1項記載の単板の乾燥調湿装置。[Scope of Claim for Utility Model Registration] (1) A hot roll dehydrator that dries the veneer to an overdry state by compressing and heating the veneer with upper and lower rotatable heating rolls facing each other, and a hot roll dehydrator. A moisture content sensor that detects the moisture content of the veneer after passing through the machine, and a moisture supply device that controls the moisture content of the veneer to a predetermined moisture content by supplying moisture that is less than the predetermined moisture content to the overdried veneer. A veneer drying and humidity control device consisting of. (2) The veneer drying and humidity control device according to claim 1, wherein the moisture supply device is constituted by a water spray device that sprays water onto the veneer. (3) The veneer drying and humidity control device according to claim 1, wherein the moisture supply device is constituted by a sponge roll that applies water to the veneer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6086384U JPS60173891U (en) | 1984-04-25 | 1984-04-25 | Veneer drying and humidity control device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6086384U JPS60173891U (en) | 1984-04-25 | 1984-04-25 | Veneer drying and humidity control device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60173891U JPS60173891U (en) | 1985-11-18 |
| JPH045985Y2 true JPH045985Y2 (en) | 1992-02-19 |
Family
ID=30588602
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6086384U Granted JPS60173891U (en) | 1984-04-25 | 1984-04-25 | Veneer drying and humidity control device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60173891U (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2681808B2 (en) * | 1988-09-20 | 1997-11-26 | 宮崎県 | Method for drying wood with tree heart |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5650183B2 (en) * | 1972-04-17 | 1981-11-27 | ||
| JPS58123079A (en) * | 1982-01-15 | 1983-07-22 | 松下電工株式会社 | Method of selectively drying veneer |
-
1984
- 1984-04-25 JP JP6086384U patent/JPS60173891U/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60173891U (en) | 1985-11-18 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US5203043A (en) | Method for continuously intensively wetting a flat article, especially a textile strip | |
| RU95117871A (en) | METHOD AND DEVICE FOR PRODUCTION OF FORMED PRODUCTS AND FORMED PRODUCTS | |
| US4112587A (en) | Method and means for drying a fibre material containing cellulose | |
| JPH045985Y2 (en) | ||
| US2711591A (en) | Method for dehydrating and drying of web-like material | |
| JPS6366370A (en) | Continuous decatizing machine of fabric and knitted article | |
| JP2609555B2 (en) | Method for continuously durable steaming and form fixing of band-shaped fiber articles such as woven fabric and knitted fabric | |
| GB1241177A (en) | Wall coverings and methods of making, applying and removing same | |
| CN215295712U (en) | Water thorn non-woven fabrics production line dehumidifier | |
| JPH0212555Y2 (en) | ||
| SU480547A1 (en) | Plywood production method | |
| CN206030152U (en) | Fibreboard slab system of preheating | |
| US2904893A (en) | Process of humidifying hardboard | |
| US2437254A (en) | Drum drier for sheet material | |
| US4756036A (en) | Continuous treatment of strip textile fabrics | |
| JPH0226570B2 (en) | ||
| JP5679703B2 (en) | Wet paper dryer for paper machine | |
| JP3624197B2 (en) | Method for producing compressed wood | |
| JPS60155883A (en) | Method and device for dehydrating woody veneer | |
| JPH0274660A (en) | Pad dryer | |
| US2960428A (en) | Method of treating sheets of ligno cellulose | |
| JPS60173888U (en) | Veneer drying and humidity control device | |
| JPS60173889U (en) | Veneer drying and humidity control device | |
| SU1062018A1 (en) | Composition for treating wood fibre mat in production of fibreboard | |
| JPS626475Y2 (en) |