JPH035688A - Method of drying lumber and food - Google Patents
Method of drying lumber and foodInfo
- Publication number
- JPH035688A JPH035688A JP14028089A JP14028089A JPH035688A JP H035688 A JPH035688 A JP H035688A JP 14028089 A JP14028089 A JP 14028089A JP 14028089 A JP14028089 A JP 14028089A JP H035688 A JPH035688 A JP H035688A
- Authority
- JP
- Japan
- Prior art keywords
- drying
- temperature
- lumber
- heating element
- pressure
- 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
Links
- 238000001035 drying Methods 0.000 title claims abstract description 44
- 238000000034 method Methods 0.000 title claims abstract description 6
- 235000013305 food Nutrition 0.000 title claims description 7
- 238000010438 heat treatment Methods 0.000 claims abstract description 42
- 239000000463 material Substances 0.000 claims abstract description 35
- 239000002023 wood Substances 0.000 claims description 21
- 238000010981 drying operation Methods 0.000 abstract 3
- 230000001788 irregular Effects 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 4
- 229910001120 nichrome Inorganic materials 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 239000003973 paint Substances 0.000 description 3
- 241001070947 Fagus Species 0.000 description 2
- 235000010099 Fagus sylvatica Nutrition 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 230000008676 import Effects 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 230000035699 permeability Effects 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 238000001291 vacuum drying Methods 0.000 description 2
- 239000002759 woven fabric Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 241000219495 Betulaceae Species 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 229920002531 Rubberwood Polymers 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000007791 dehumidification Methods 0.000 description 1
- 238000002845 discoloration Methods 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 238000007602 hot air drying Methods 0.000 description 1
- 238000010030 laminating Methods 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 229920006267 polyester film Polymers 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 239000012254 powdered material Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 239000011265 semifinished product Substances 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 238000004078 waterproofing Methods 0.000 description 1
Landscapes
- 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、食品等の減圧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, foods, etc. under reduced pressure.
近年、針葉樹材を中心に木材乾燥の重要性が叫ばれ、製
材業界では除湿乾燥をはじめ各種の乾燥機が普及してい
る。In recent years, the importance of drying wood, especially for coniferous wood, has been emphasized, and various dryers, including dehumidifying dryers, have become popular in the lumber industry.
現在、木材の乾燥法として、熱風乾燥、除湿乾燥、減圧
乾燥、太陽熱利用乾燥環条(の乾燥法が実用化されてい
る。この中で、減圧乾燥法、とくに高周波加熱減圧乾燥
法は、大断面材料を短時間で乾燥することができ、突板
を結束したまま短時間で高品質に乾燥できる等の長所が
あるが、設備及びランニングコストが高いという短所が
指摘されている。Currently, hot air drying, dehumidification drying, vacuum drying, and solar drying ring drying methods are in practical use as wood drying methods. Although it has advantages such as being able to dry cross-sectional materials in a short time and drying veneers with high quality in a short time while being bundled, it has been pointed out that the disadvantage is that the equipment and running costs are high.
最近、家具業界の傾向として、オーク材をはじめヒラコ
リ、アルダ−材など多くの北米材の輸入があげられるが
、これらは現地ですでに乾燥されている。また、ゴムツ
キ(変色菌が発生しやすいため現地で乾燥している)や
その他の樹脂も将来NIES’から半製品だけでなく乾
燥材の輸入も考えられる。A recent trend in the furniture industry is the import of many North American materials, including oak, hirakori, and alder, but these materials are already dried locally. In addition, it is also possible to import not only semi-finished products but also dried materials from NIES' in the future for rubber wood (which is dried locally because it is prone to discoloration bacteria) and other resins.
このような厳しい国際的状況のなかで、この競争に打ち
かつためには、木材の乾燥を短時間で、高品質を有し、
種々の樹種、形態に対応できる多様性をもち、省エネル
ギーおよび小スペースで、しかも低設備費で実施できる
ような方法の開発が要請されている。In order to survive this competition in such a harsh international situation, it is necessary to dry wood in a short time, with high quality, and to survive this competition.
There is a need for the development of a method that is versatile enough to accommodate various tree species and forms, and that can be implemented in an energy-saving manner, in a small space, and at low equipment costs.
前記の課題を達成するため、本発明にあっては、減圧ま
たは真空容器中において、木材、食品その他の被乾燥物
の表面に面状発熱体を被せ、または面状発熱体の間に被
乾燥物を挟んで、該面状発熱体の通電により水分の蒸発
乾燥に必要な熱量を供給し、減圧しながら乾燥する構成
を採用した。In order to achieve the above-mentioned object, in the present invention, a planar heating element is placed over the surface of wood, food, or other material to be dried in a reduced pressure or vacuum container, or a sheet of material to be dried is placed between the planar heating elements. A configuration was adopted in which an object was sandwiched between the objects, and the amount of heat necessary for evaporating and drying the moisture was supplied by energizing the planar heating element, and the object was dried while being depressurized.
減圧または真空容器は15〜20wmHg程度の耐圧容
器であればよい。容器内の温度は、通常20〜50°C
1とくに30〜40°Cであり、この温度に維持できる
排気量の真空吸引ポンプと発熱量をもつ面状発熱体を備
えているものを使用する。The reduced pressure or vacuum container may be a pressure-resistant container of about 15 to 20 wmHg. The temperature inside the container is usually 20-50°C
1. In particular, the temperature is 30 to 40° C., and a device equipped with a vacuum suction pump with a displacement that can maintain this temperature and a planar heating element with a calorific value is used.
面状発熱体としては、銅製のitt極線を織り込んだ織
布にカーボン系導電性塗料を塗布重合させ、電極用端子
を取付けて、これを防水のためポリエステルフィルムに
よりラミネートとし、さらに塩ビシートで保護外装した
ものを使用するのが好ましい。電極線に通電することに
より、抵抗材料であるカーボンが発熱する。The planar heating element is made by coating and polymerizing carbon-based conductive paint on a woven fabric woven with copper ITT wires, attaching electrode terminals, laminating it with a polyester film for waterproofing, and then using a PVC sheet. It is preferable to use one with a protective exterior. By applying electricity to the electrode wire, carbon, which is a resistance material, generates heat.
この面状発熱体は、ニクロム等の金属抵抗線と異なり、
繊維織布であって、柔軟軽量で折損が生じ難く、折りた
たみ自在であるから、可撓性、耐久性および加工性にす
ぐれている。また、導電性塗料が繊維織布に網目状に分
布しているから、ニクロム線のような抵抗線を所定間隔
で配列する方式と比べ、発熱温度分布が均一となる熱特
性を有し、通電後の温度の立上りが早いという温度特性
をもつ。This sheet heating element is different from metal resistance wires such as nichrome,
It is a woven fiber fabric that is flexible, lightweight, difficult to break, and can be folded freely, so it has excellent flexibility, durability, and workability. In addition, since the conductive paint is distributed in a mesh pattern on the woven fiber fabric, it has thermal properties that make the heat generation temperature distribution even, compared to a method in which resistance wires such as nichrome wire are arranged at predetermined intervals. It has a temperature characteristic that the temperature rises quickly afterward.
もちろん、従来のニクロム線等の金属抵抗体を密に配列
したタイプのものや、導電性セラミックを発熱抵抗体と
したタイプの面状発熱体を使用してもよい。Of course, a sheet heating element of the type in which metal resistors such as conventional nichrome wires are closely arranged, or a type in which the heating resistor is made of conductive ceramic may be used.
木材、食品その他の乾燥に際しては、被乾燥物の表面に
前記緒特性をもつ面状発熱体を直接波せて、或いは面状
発熱体の間に被乾燥物を挾み込んだ状態で積層する。When drying wood, food, and other materials, planar heating elements having the above-mentioned characteristics are waved directly on the surface of the material to be dried, or they are stacked with the material to be dried sandwiched between the surface heating elements. .
板材、柱材などの乾燥の際には、被乾燥物をベタ積みす
るだけでもよいが、狂いを防止するため、耐圧容器内に
は油圧シリンダ等によるプレス装置を装備するのが好ま
しい。When drying plate materials, pillar materials, etc., it is sufficient to simply pile up the materials to be dried, but in order to prevent distortion, it is preferable to equip the pressure container with a press device using a hydraulic cylinder or the like.
本発明の乾燥方法によれば、たとえば含水率140%を
もつ厚さ5値、幅30C1ll、長さ188値のブナ材
は面状発熱体の表面温度40°C1真空度40wHHの
減圧乾燥条件で60〜70時間で含水率lO%程度まで
乾燥される。これに対して同一寸法のブナ材を高周波加
熱減圧乾燥法に従って行った場合は90〜100時間を
要し、乾燥時間は大幅に短縮される。According to the drying method of the present invention, for example, beech wood with a moisture content of 140%, a thickness of 5 values, a width of 30 cm, and a length of 188 values is dried under reduced pressure conditions of a surface temperature of a planar heating element of 40° C. and a degree of vacuum of 40 wHH. It is dried to a moisture content of about 10% in 60 to 70 hours. On the other hand, when beech wood of the same size is dried using high frequency heating and reduced pressure drying, it takes 90 to 100 hours, which significantly shortens the drying time.
本発明の乾燥方法は、木材のみならず食品、薬物等の粉
粒体、湿式セラミックのような高温を嫌う製品の迅速乾
燥にも適用することが可能である。The drying method of the present invention can be applied not only to wood but also to the rapid drying of products that do not like high temperatures, such as powdered materials such as foods and drugs, and wet ceramics.
本発明の乾燥方法は、被乾燥物の表面に面状発熱体を被
せ、または面状発熱体間に被乾燥物を挟み込んで、面状
発熱体を被乾燥物と直接接触させて減圧下に乾燥を行う
ものであるから、次のような作用がある。The drying method of the present invention involves covering the surface of the object to be dried with a planar heating element or sandwiching the object to be dried between the planar heating elements, bringing the sheet heating element into direct contact with the object to be dried, and drying the object under reduced pressure. Because it dries, it has the following effects:
接触加熱であるため熱損失が少なく、面状発熱体の温度
分布がほぼ均一であるため、仕上りおよび含水率にムラ
がなく、短時間の乾燥が可能である。Since contact heating is used, there is little heat loss, and the temperature distribution of the planar heating element is almost uniform, so the finish and moisture content are uniform, and drying can be done in a short time.
また、面状発熱体の温度コントロールが容易で、複雑な
電気系統の制御技術を要しないから、装置の保守管理も
容易である。Furthermore, since the temperature of the planar heating element can be easily controlled and complicated electrical system control technology is not required, maintenance and management of the device is also easy.
さらに、乾燥の際には桟木などを要せず、発熱体が薄い
ために、小スペースで多くの材を乾燥できる。Furthermore, since there is no need for wooden crosspieces during drying, and the heating element is thin, a large amount of wood can be dried in a small space.
面状発熱体が可撓性に高み、材料の形状に沿われて自由
に被覆することができ、ニクロム線のような抵抗線を用
いた場合の断線や使用によるクセが生じず取扱いが容易
である。The planar heating element is highly flexible and can be coated freely along the shape of the material, making it easy to handle without causing breakage or curling when using resistance wire such as nichrome wire. be.
以下、本発明の効果を実施例により具体的に説明する。 Hereinafter, the effects of the present invention will be specifically explained using examples.
実施例1
(1)試験方法
第1図に示すように、減圧缶体1(内径75cm、長さ
250cm)内に乾燥する木材2を面状発熱体3で挟ん
でベタ積みした。乾燥中の狂いを防止するために上部か
ら油圧シリンダによりプレス4を行った。面状発熱体3
は、厚さ2璽lで、大面積用(45X200cm+)と
小面積用(23X100cm)の二種を用い、それぞれ
木材2の表裏面に置き、両側から直接加熱した。乾燥中
の材温は、木材に挿入された温度センサー(白金抵抗体
ptloo)によって検出し、所定の温度でコントロー
ルした。Example 1 (1) Test method As shown in FIG. 1, wood 2 to be dried was stacked in a vacuum can body 1 (inner diameter 75 cm, length 250 cm), sandwiched between planar heating elements 3. In order to prevent distortion during drying, a press 4 was performed from above using a hydraulic cylinder. Planar heating element 3
The test pieces were 2 liters thick, and two types, one for large area (45 x 200 cm+) and one for small area (23 x 100 cm), were placed on the front and back surfaces of wood 2 and heated directly from both sides. The temperature of the material during drying was detected by a temperature sensor (platinum resistor ptloo) inserted into the wood, and was controlled at a predetermined temperature.
図中、5は油圧ポンプ、6は真空ポンプ、7は電源、8
は温度およびタイム調節計、9は温度記録計である。In the figure, 5 is a hydraulic pump, 6 is a vacuum pump, 7 is a power supply, 8
is a temperature and time controller, and 9 is a temperature recorder.
面状発熱体3および真空ポンプ6の電気的仕様は次の通
りである。The electrical specifications of the planar heating element 3 and the vacuum pump 6 are as follows.
(2)試験材
試験に用いた材は、厚さ3.5cm、幅10.30c1
1.長さ90. 188CJlのハルニレ材(シベリア
産)である。(2) Test material The material used for the test was 3.5 cm thick and 10.30 cm wide.
1. Length 90. It is 188CJl elm wood (produced in Siberia).
(3)面状発熱体
面状発熱体は、前述したようにカーボン系導電性塗料を
抵抗体とする織布状のものを使用した。(3) Planar heating element The planar heating element used was a woven fabric having a carbon-based conductive paint as a resistor, as described above.
(4)試験結果
(a)発熱体の温度分布
木材乾燥の仕上がりの含水率ムラに影響を及ぼす発熱体
の温度分布を測定した結果を第2図に示す。幅方向では
中央が高く、周囲が低い分布となった。これは中央では
熱が籠るのに対して、周囲は放熱するためと考えられる
。このことは乾燥初期の高含水率時では試験材の全面で
ほぼ均一な温度分布となるが、乾燥末期には前述の分布
と同様に周囲の温度が低下する傾向が観察されたことか
らもわかる。(4) Test results (a) Temperature distribution of the heating element Figure 2 shows the results of measuring the temperature distribution of the heating element, which affects the unevenness of moisture content in the finished wood drying process. In the width direction, the distribution was high at the center and low at the periphery. This is thought to be because heat is trapped in the center, while heat is radiated around the area. This can be seen from the fact that when the moisture content is high at the beginning of drying, the temperature distribution is almost uniform over the entire surface of the test material, but at the end of drying, the surrounding temperature tends to decrease, similar to the distribution described above. .
(b)乾燥経過
本試験で用いたハルニレ材は通気性が良好であり、減圧
乾燥には最適な材料である。第3図に幅10ca+、長
さ90cmの結果を示す。初期含水率130〜140%
材で3CI11.5〔厚でそれぞれ50及び70時間と
いう非常に短時間で10%まで乾燥していることがわか
る。乾燥割れは生じなかった。次に5cffl厚材を4
段積みし、2段おきに発熱体を挿入した場合の乾燥結果
を第4図に示す。乾燥時間は第3図の結果より長かった
が、その差は著しいものではなかった。(b) Drying process The elm material used in this test has good air permeability and is the most suitable material for vacuum drying. Figure 3 shows the results for a width of 10ca+ and a length of 90cm. Initial moisture content 130-140%
It can be seen that the material was dried to 3CI11.5 (thickness) to 10% in a very short time of 50 and 70 hours, respectively. No drying cracks occurred. Next, 4 pieces of 5cffl thick material
FIG. 4 shows the drying results when stacked in layers and heating elements were inserted every two layers. Although the drying time was longer than the results shown in Figure 3, the difference was not significant.
第5図a −cは発熱体の寸法を大きくして、大きな面
積の試験材を乾燥したときの、5cm厚の乾燥経過及び
厚さ、長さ方向の含水率分布の結果を示す。Figures 5a to 5c show the results of the drying process and the moisture content distribution in the thickness and length directions for a 5 cm thick test material when the dimensions of the heating element were increased to dry a large area test material.
通気性が良好なため長さの増加に対して乾燥時間がそれ
ほど増加していない。試験材間の含水率のバラツキも小
さいことがわかる。材温の変化は乾燥初期には周囲の空
気圧力に相当する沸点付近で一定となる。その後中期頃
は試験材間で6〜7°C1末期は3〜4 ”Cの温度差
となる。また、接触加熱のため厚さ方向の含水率の分布
に著しい差が生じると予想していたが、意外と少ないこ
とがわかる。これは発熱体のカバー材料によって表面蒸
発が適度に調整されたのが原因と思われる。長さ方向の
分布も含水率差が少なかった。いずれの材とも乾燥中は
油圧プレスによって圧締されていたため、材のアバレも
少なかった。Due to good air permeability, the drying time does not increase much as the length increases. It can be seen that the variation in moisture content among the test materials is also small. At the beginning of drying, the change in material temperature remains constant around the boiling point, which corresponds to the surrounding air pressure. After that, the temperature difference between the test materials will be 6 to 7 degrees Celsius in the middle period, and 3 to 4 degrees Celsius in the final period.Also, we expected that there would be a significant difference in the moisture content distribution in the thickness direction due to contact heating. However, it can be seen that the amount of water content is surprisingly small. This is probably because the surface evaporation was moderately adjusted by the cover material of the heating element. There was also little difference in moisture content in the distribution in the length direction. During drying for both materials. Since the material was compacted using a hydraulic press, there were fewer cracks in the material.
以上説明したように、本発明は木材を減圧下に面状発熱
体により接触加熱するものであるから、仕上がりおよび
含水率にムラがなく、短時間で乾燥し良好な仕上がりの
ものを得ることができる。As explained above, since the present invention involves contact heating of wood with a planar heating element under reduced pressure, it is possible to obtain a good finish with uniform finish and moisture content and drying in a short time. can.
また、面状発熱体は温度制御が容易で、装置の保守管理
も簡単であり、熱損失が少なく、省エネルギー、小スペ
ース化により低コストで木材を乾燥することができる。In addition, the planar heating element allows easy temperature control, easy maintenance and management of the device, low heat loss, energy saving, and space saving, making it possible to dry wood at low cost.
第1図は本発明の実施に使用する装置の一例を示す説明
図、
第2図は本発明の実施に用いた面状発熱体の温度分布の
一例を示す図、
第3図および第4図はそれぞれ本発明の実施例による乾
燥時間と含水率との関係を示すグラフ、第5図a −c
は同じく本発明の実施例を示し、(5)は乾燥時間と含
水率との関係を示すグラフ、(blおよび(C1はそれ
ぞれ木材の厚さ方向と長さ方向の含水率分布を示すグラ
フである。FIG. 1 is an explanatory diagram showing an example of the apparatus used to carry out the present invention, FIG. 2 is a diagram showing an example of the temperature distribution of the planar heating element used to carry out the present invention, and FIGS. 3 and 4. are graphs showing the relationship between drying time and moisture content according to the embodiments of the present invention, FIGS. 5a to 5c, respectively.
also shows an example of the present invention, (5) is a graph showing the relationship between drying time and moisture content, (bl and (C1) are graphs showing the moisture content distribution in the thickness direction and length direction of the wood, respectively. be.
Claims (1)
乾燥物の表面に面状発熱体を被せ、または面状発熱体の
間に被乾燥物を挟んで、該面状発熱体の通電により水分
の蒸発乾燥に必要な熱量を供給し、減圧しながら乾燥す
ることを特徴とする木材、食品等の乾燥方法。In a reduced pressure or vacuum container, a sheet heating element is placed over the surface of wood, food, or other material to be dried, or the material is sandwiched between sheet heating elements, and moisture is removed by energizing the sheet heating element. A method for drying wood, food, etc., characterized by supplying the amount of heat necessary for evaporative drying and drying while reducing pressure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14028089A JPH035688A (en) | 1989-06-02 | 1989-06-02 | Method of drying lumber and food |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14028089A JPH035688A (en) | 1989-06-02 | 1989-06-02 | Method of drying lumber and food |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH035688A true JPH035688A (en) | 1991-01-11 |
Family
ID=15265108
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14028089A Pending JPH035688A (en) | 1989-06-02 | 1989-06-02 | Method of drying lumber and food |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH035688A (en) |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS49860A (en) * | 1972-04-18 | 1974-01-07 | ||
| JPS56105286A (en) * | 1980-01-23 | 1981-08-21 | Ota Masayuki | Treating device for veneer in hottboard drier |
| JPS5932776A (en) * | 1982-08-18 | 1984-02-22 | 共和「真」空技術株式会社 | Vacuum drier |
-
1989
- 1989-06-02 JP JP14028089A patent/JPH035688A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS49860A (en) * | 1972-04-18 | 1974-01-07 | ||
| JPS56105286A (en) * | 1980-01-23 | 1981-08-21 | Ota Masayuki | Treating device for veneer in hottboard drier |
| JPS5932776A (en) * | 1982-08-18 | 1984-02-22 | 共和「真」空技術株式会社 | Vacuum drier |
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