JPH04207175A - Drying of laver sheet by automatically detecting dryness of laver sheet - Google Patents

Drying of laver sheet by automatically detecting dryness of laver sheet

Info

Publication number
JPH04207175A
JPH04207175A JP2340807A JP34080790A JPH04207175A JP H04207175 A JPH04207175 A JP H04207175A JP 2340807 A JP2340807 A JP 2340807A JP 34080790 A JP34080790 A JP 34080790A JP H04207175 A JPH04207175 A JP H04207175A
Authority
JP
Japan
Prior art keywords
drying
seaweed
dryness
temperature
degree
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.)
Granted
Application number
JP2340807A
Other languages
Japanese (ja)
Other versions
JPH0628551B2 (en
Inventor
Mikio Furuta
幹雄 古田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
FURUTA DENKI KK
Original Assignee
FURUTA DENKI KK
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by FURUTA DENKI KK filed Critical FURUTA DENKI KK
Priority to JP2340807A priority Critical patent/JPH0628551B2/en
Publication of JPH04207175A publication Critical patent/JPH04207175A/en
Publication of JPH0628551B2 publication Critical patent/JPH0628551B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To easily control the dryness of laver sheet in improved accuracy by detecting the dryness of a laver sheet and controlling the drying condition based on the detection result. CONSTITUTION:The surface temperature of a laver sheet in a drying stage and the wet-bulb temperature of the drying environment are detected in an automatic laver-drying machine. The detection results are inputted to a computer, the dryness is automatically judged by the difference between the detected values and the drying condition is controlled to the optimum level e.g. by controlling the transfer speed of a laver sheet screen, the flow rate of hot air or the temperature and/or the humidity of the hot air.

Description

【発明の詳細な説明】[Detailed description of the invention] 【産業上の利用分野】[Industrial application field]

本発明は、海苔乾燥の全自動化に係わる乾燥度合いの検
出と、この検出した値に基づ(、海苔の乾燥法に関する
ものである。
The present invention relates to detection of the degree of dryness related to fully automated drying of seaweed, and a method of drying seaweed based on the detected value.

【従来の技術] 現在の自動海苔乾燥機(以下、単に乾燥機とする。 )では、チェーンに装備する海苔簀に、自動抄機を介し
て順次海苔混合物が抄かれる。 このようにして、多数の海苔簀に、順次抄かれた抄き海
苔は、乾燥機の乾燥室(以下、単に乾燥室とする0)を
通過するとき、石油バーナ加熱器により加熱された熱風
により乾燥され、乾燥室から出た段階で、自動剥機によ
り海苔簀より剥ぎ取られることにより、ここに乾海苔が
生成される構造となっている。 このとき、海苔の乾燥度合いにより、熱風の温度の設定
値を手動で上げ下げするか、又は換気装置を介して湿度
を手動で調整する方法等が実施されている。 具体的には、製造現場では、乾燥度合いの測定方法は、
乾燥機の後部の、簀枠反転部に設けられた穿孔より、手
を入れ、海苔面に直接手を触れ、その触覚(感覚)によ
り乾き度合いを判定乾燥機内の温湿度の制御をしている
のが、常套手段である。 尚海苔の乾燥方法及びその温度及び/又は湿度制御方法
としては、次のような技術文献が挙げられる。 特公昭63−13665号及び同63−13666号の
海苔乾燥方法、特公昭63−60985号の海苔乾燥設
備に付設する湿度調整装置、特公昭63−60986号
の海苔乾燥室の湿度調整装置、特公昭63−65303
号の海苔連続乾燥機の温湿度調整方法等が散見される。 【発明が解決しようとする課題】 前述の如く、従来は、乾燥度合いを、手の触覚と、勘に
より判断していたので、大変に曖昧であり、種々の弊害
、例えば、過乾燥(後述するように、含水率の低下)に
起因する破れ、剥離不良とか、また未乾燥(後述するよ
うに、含水率の過剰)に起因する濡れ、皺の発生等によ
る品質の低下、コストの低下等が課題となっている。 処で、次の、課題の分析で詳述するように、実際の海苔
乾燥は、最終含水率が、8%〜12%を有する程度に仕
上げたほうがよい。 したがって、海苔の含水率が、前記数値より、少なくな
った場合には(含水率の低下)、破れ、アナ、カケ等の
暇物となり、また逆に、前記数値より、多くなった場合
は(含水率の過剰)、濡れ、縮み、皺等の暇物となる。 結果的に、品質の低下、及び商品価値の低下を招来する
。 よって、最終乾燥時に、適当な含水率を含む程度の乾燥
度合いに仕上げるのが、乾燥のコツであり、試行錯誤し
て乾燥調整しているのが現況である。
[Prior Art] In current automatic seaweed dryers (hereinafter simply referred to as dryers), a seaweed mixture is sequentially shredded into a seaweed basin equipped on a chain via an automatic shredder. In this way, when the dried seaweed that has been sequentially drawn into a large number of seaweed cages passes through the drying chamber of the dryer (hereinafter simply referred to as drying chamber 0), it is heated by hot air heated by an oil burner heater. The structure is such that when the seaweed is dried and leaves the drying room, it is peeled off from the seaweed cage using an automatic peeling machine, thereby producing dried seaweed. At this time, depending on the degree of dryness of the seaweed, methods such as manually increasing or decreasing the temperature setting of the hot air or manually adjusting the humidity via a ventilation device are implemented. Specifically, at the manufacturing site, the method of measuring the degree of dryness is
At the rear of the dryer, the user inserts his/her hand through a hole in the reversible part of the screen frame, and directly touches the surface of the seaweed.The degree of dryness is determined by the sense of touch and the temperature and humidity inside the dryer are controlled. This is the usual method. The following technical documents include methods for drying seaweed and methods for controlling its temperature and/or humidity. Patent Publication No. 63-13665 and No. 63-13666, a method for drying seaweed; Patent Publication No. 63-60985, a humidity control device attached to seaweed drying equipment; Patent Publication No. 63-60986, a humidity control device for a seaweed drying room; Kosho 63-65303
Here and there, you will find information on how to adjust the temperature and humidity of continuous seaweed dryers. [Problems to be Solved by the Invention] As mentioned above, in the past, the degree of dryness was judged by the tactile sensation of the hands and intuition, which was very vague and caused various harmful effects, such as over-drying (described later). As described above, there are problems such as tearing and poor peeling caused by a decrease in moisture content (lower moisture content), and wetting and wrinkling caused by undrying (excessive moisture content, as described later), resulting in lower quality and lower costs. It has become a challenge. However, as will be explained in detail in the next problem analysis, it is better to actually dry the seaweed so that the final moisture content is 8% to 12%. Therefore, if the moisture content of the seaweed becomes less than the above value (decreased moisture content), the seaweed will become damaged, cracked, cracked, etc., and conversely, if it becomes more than the above value ( excessive moisture content), resulting in wetness, shrinkage, wrinkles, etc. As a result, this results in a decline in quality and product value. Therefore, the key to drying is to achieve a degree of dryness that contains an appropriate moisture content during the final drying process, and the current situation is to adjust the dryness through trial and error.

【課題の分析〕[Analysis of the issue]

海苔の乾燥特性は、−船釣に、乾燥機内に海苔簀が搬送
されるとき、乾燥時間により含水率及び表面温度は、図
1のように変化する。また図2は、そのときの乾燥速度
を示す。 即ち、この図に於ては、乾燥過程を三期間に区画した、
イ:予熱期間、ロ:恒率乾燥期間、ハ:滅率乾燥期間で
ある。 ここで、各期間の特徴を、説明する。 先ず予熱期間とは、始め乾燥熱風により抄き海苔(以下
、原則として海苔とする。)が、予熱される期間である
。 次に、恒率乾燥期間とは、海苔表面より蒸発する水分が
、内部より滲出する水分により補われ、その表面には水
膜が生成され、もって表面温度は、蒸発潜熱により、熱
風より低くなり、その雰囲気におかれた湿球温度に、は
ぼ等しい(以下、単に等しいとする。)。 そして、この期間の含水率は、時間の経過とともに、図
1のようにほぼ直線的(以下、単に直線的しいとする。 )に降下する。また蒸発速度は、図2のようにほぼ一定
(以下、単に一定とする。)であり、また乾燥行程の要
部をなす。 更に減率乾燥期間とは、海苔内部の含水率が低下し、海
苔内部よりの水分の滲出が追い付かず、恨辛限界以降で
は、海苔が乾いてくると同時に、その表面温度は上昇し
、熱風温度に近づき、かつ蒸発速度は急減する。そして
、最終的には、平衡含水率は5%〜6%となる。 そこで、前述の乾燥特性のうち、海苔乾燥表面温度につ
いて詳述する。 即ち、恒率乾燥期間に於ける海苔表面温度は、熱風の温
湿度による乾燥雰囲気に於ける湿球温度に等しい。そし
て、この恒率乾燥期間に於ける慎重限界を過ぎ、減率乾
燥期間に入ると、蒸発速度が低下し、それに伴い温度降
下が減少し、表面温度は、図3のように乾燥雰囲気の湿
球温度より次第に上昇し、乾燥終期には、蒸発しなくな
り、それによる蒸発潜熱の吸収もなくなるため、熱風温
度と等しくなる。 【課題を解決するための手段】 上記に鑑み、本発明は、従来の乾燥度合いを、手の触覚
と、勘により判断していたものを、科学的な手段を講じ
て、より的確かつ簡易に判定しようとするものであり、
下記のような手法を採用した。 即ち、本発明は、海苔自動乾燥機内に於て、乾燥される
途中の海苔の表面温度と、その乾燥雰囲気の湿球温度と
を検出し、この検出した値をコンピュータに入力し、そ
の検出した値の差により乾燥度合いを自動判別し、適正
な乾燥条件、例えば、海苔簀の搬送スピードで制御する
手段、又は熱風の風速で制御する手段、或いは温度及び
/又は湿度で制御する手段を介し、海苔乾燥度合いの自
動検出による海苔の乾燥法である
The drying characteristics of seaweed are: - When a seaweed cage is transported into a dryer while fishing on a boat, the moisture content and surface temperature change depending on the drying time as shown in FIG. Moreover, FIG. 2 shows the drying rate at that time. That is, in this figure, the drying process is divided into three periods.
B: Preheating period, B: Constant rate drying period, C: Low rate drying period. Here, the characteristics of each period will be explained. First, the preheating period is a period during which the dried seaweed (hereinafter referred to as seaweed in principle) is preheated by dry hot air. Next, the constant rate drying period means that the water that evaporates from the surface of the seaweed is compensated for by the water that seeps out from inside, and a water film is formed on the surface, and the surface temperature becomes lower than that of hot air due to the latent heat of evaporation. , is approximately equal to the wet bulb temperature placed in that atmosphere (hereinafter simply referred to as equal). The moisture content during this period decreases almost linearly (hereinafter simply referred to as linear) as shown in FIG. 1 as time passes. Further, the evaporation rate is approximately constant (hereinafter simply referred to as constant) as shown in FIG. 2, and is an important part of the drying process. Furthermore, the lapse rate drying period means that the moisture content inside the seaweed decreases, and the moisture seeping out from inside the seaweed cannot catch up, and after the drying limit, the seaweed dries and at the same time its surface temperature rises, causing hot air to dry out. As the temperature approaches, the evaporation rate decreases rapidly. Finally, the equilibrium moisture content becomes 5% to 6%. Therefore, among the above-mentioned drying characteristics, the seaweed drying surface temperature will be explained in detail. That is, the seaweed surface temperature during the constant rate drying period is equal to the wet bulb temperature in a dry atmosphere due to the temperature and humidity of hot air. When the prudent limit in this constant rate drying period is passed and the decreasing rate drying period begins, the evaporation rate decreases, the temperature drop decreases accordingly, and the surface temperature decreases due to the humidity in the drying atmosphere, as shown in Figure 3. It gradually rises above the bulb temperature, and at the end of the drying period, it stops evaporating and absorbs the latent heat of evaporation, so it becomes equal to the hot air temperature. [Means for Solving the Problems] In view of the above, the present invention uses scientific means to more accurately and easily determine the degree of dryness, which was conventionally determined by the tactile sensation of the hand and intuition. It is intended to determine
The following method was adopted. That is, the present invention detects the surface temperature of seaweed during drying and the wet bulb temperature of the drying atmosphere in an automatic seaweed dryer, inputs the detected values into a computer, and calculates the detected values. Automatically determine the degree of dryness based on the difference in values, and use appropriate drying conditions, for example, by controlling the transport speed of the seaweed cage, by controlling the speed of hot air, or by controlling the temperature and/or humidity, This is a seaweed drying method that automatically detects the degree of seaweed dryness.

【実施例】【Example】

本発明では、乾燥行程中の、乾燥度合いを的確に検出す
るため、乾燥特性の慎重限界が、概ね、海苔表面温度と
、湿球温度との温度差の有無が限界点であることに着目
し、その差を的確に検出する。 これにより、海苔の恒率乾燥期間の慎重限界を把握し、
以後海苔の乾燥度合いを制御する方法である。 具体的には、恒率乾燥期間におる海苔の表面を観察する
と、真っ黒く潤んでいる。それは海苔表面が、水膜で覆
われている証拠である。このような状態の海苔表面が、
慎重限界点を超えると、乾海苔の表面の色が変わり、そ
の表面温度も徐々に上昇する。 例えば、恒率乾燥期間にある海苔表面から放射する赤外
線を測定して、表面温度を検出する。即ち、赤外線温度
計を用いて表面温度を測定し、その測定値信号と同時に
その雰囲気における湿球温度、またはそれに相当する湿
り状態の表面状態を、赤外線温度計で測定した測定信号
とを比較し、差違の有無および差の大小より、海苔乾燥
度合いを判別する(コンピュータ処理)。 より的確に判別するためには、さらに減率乾燥期の中間
点で、前記同様の測定をなし、両者の変化を知れば乾燥
特性曲線上の、どの部位を通過中かを判別することが可
能となり、海苔乾燥度合いをより一層的確に判別するこ
とができる。 本発明による乾燥度合いの判別により、乾燥しすぎのと
きには(いわゆる、過乾燥のときには)、熱風又は乾燥
機内の温度を下げるか、換気又は加湿機等の湿度制御手
段を介して加湿するか湿度を上げるか、海苔簀の搬送速
度を上げて乾燥時間を、短縮するか、或いは熱風の風速
を落とす等の自動処理を行う。 一方乾燥不足のときには(濡れているときには、)、熱
風又は乾燥機内の温度を上げるか、換気又は除湿機の湿
度制御手段を介して除湿するか、または搬送速度を下げ
るか、或いは熱風の風速を速くする等の自動処理を行う
。 従来、自動乾燥機といえども、しばしば手の触覚により
乾燥度合いを判定して、乾燥条件を変更して適正に乾燥
するよう、注意深く監視調整を行っていたちのを、本発
明により、人の手を、煩わせないで乾燥度合いを自動検
出し、かつその結果により、乾燥条件をコンピュータ等
により、自動調整して適正な乾燥を行うことにより、海
苔乾燥の完全自動化を可能にするものである。もって、
省人化、また未熟者運転が可能となる可能にするもので
ある。尚、前記赤外線温度計に限定されない。
In order to accurately detect the degree of dryness during the drying process, the present invention focuses on the fact that the prudent limit of drying characteristics is generally determined by the presence or absence of a temperature difference between the seaweed surface temperature and the wet bulb temperature. , to accurately detect the difference. Through this, we can understand the prudent limits of the constant rate drying period for seaweed, and
This is a method to control the degree of drying of the seaweed. Specifically, when observing the surface of seaweed during a period of constant drying, it is completely black and moist. This is evidence that the surface of the seaweed is covered with a film of water. The seaweed surface in this state is
When the cautious limit is exceeded, the surface color of the dried seaweed changes and its surface temperature gradually rises. For example, the surface temperature is detected by measuring infrared rays emitted from the surface of seaweed during a period of constant drying. That is, the surface temperature is measured using an infrared thermometer, and the measured value signal is simultaneously compared with the wet bulb temperature in the atmosphere, or the surface condition in a corresponding wet state, with the measurement signal measured using the infrared thermometer. , the degree of seaweed dryness is determined based on the presence or absence of a difference and the size of the difference (computer processing). In order to make a more accurate determination, the same measurement as above is carried out at the midpoint of the lapse rate drying period, and by knowing the changes in both, it is possible to determine which part on the drying characteristic curve the drying characteristic curve is passing through. Therefore, the degree of dryness of the seaweed can be determined even more accurately. By determining the degree of dryness according to the present invention, if the dryness is too dry (so-called overdrying), either lower the hot air or the temperature inside the dryer, humidify the dryer through ventilation or humidity control means such as a humidifier, or increase the humidity. Automatic processing such as increasing the conveyance speed of the seaweed cage to shorten the drying time, or reducing the speed of hot air. On the other hand, when the drying is insufficient (when the dryer is wet), increase the temperature of hot air or the inside of the dryer, dehumidify through ventilation or humidity control means of a dehumidifier, reduce the conveying speed, or reduce the speed of the hot air. Perform automatic processing such as speeding up. In the past, even automatic dryers often judged the degree of dryness using the tactile sensation of the hand and carefully monitored and adjusted the drying conditions to ensure proper drying. By automatically detecting the degree of dryness without bothering the user, and then automatically adjusting the drying conditions using a computer or the like based on the results to perform proper drying, it is possible to completely automate the drying of seaweed. With that,
This saves labor and makes it possible for unskilled people to operate the vehicle. Note that the thermometer is not limited to the above-mentioned infrared thermometer.

【発明の効果】【Effect of the invention】

以上説明したように本発明の乾燥度合いの検出と、この
検出した値に基づいて、乾燥条件を制御する方法であり
、下記のような効果を有する。 先ず、本発明は、従来の乾燥度合いを、手の触覚と、勘
により判断していたものを、科学的な手段を講じて、よ
り的確かつ簡易に判定し得る効果がある。 またこれにより、乾燥条件のコンピュータ制御による自
動運転が可能となった実用上の効果を有する。 更に従来、自動乾燥機といえども、しばしば手の触覚に
より乾燥具合いを判定して、乾燥条件を変更して適正に
乾燥するよう、注意深く監視調整を行っていた。しかし
ながら、本発明により、人の手を、煩わせないで乾燥度
合いを自動検出し、かつその結果により、乾燥条件をコ
ンピュータ等により、自動調整して適正な乾燥を行うこ
とにより、海苔乾燥の完全自動化を可能にするものであ
る。省人化、また未熟者運転が可能となるもので、省人
化、未熟者運転が可能となる等の実用上の優れた効果を
有する。 更にまた、品質のよい乾海苔を、効率よく、かつ比較的
簡易に製造できる効果がある。
As explained above, the present invention is a method of detecting the degree of dryness and controlling drying conditions based on the detected value, and has the following effects. First, the present invention has the effect of making it possible to more accurately and easily determine the degree of dryness using scientific means, instead of the conventional method of determining the degree of dryness based on the tactile sensation of the hand and intuition. This also has the practical effect of enabling automatic operation through computer control of drying conditions. Furthermore, in the past, even with automatic dryers, the degree of drying was often judged by the touch of the hand, and drying conditions were changed to ensure proper drying, with careful monitoring and adjustment performed. However, according to the present invention, the degree of dryness is automatically detected without human intervention, and based on the results, the drying conditions are automatically adjusted using a computer etc. to perform proper drying, thereby completely drying the seaweed. It enables automation. It has excellent practical effects, such as saving labor and making it possible for unskilled people to operate the vehicle. Furthermore, there is an effect that high quality dried seaweed can be produced efficiently and relatively easily.

【図面の簡単な説明】[Brief explanation of the drawing]

【図1】 海苔乾燥における時間、含水率と温度の変化を示す説明
図である。
FIG. 1 is an explanatory diagram showing changes in time, moisture content, and temperature during drying of seaweed.

【図2】 海苔乾燥における時間、蒸発速度の変化を示す説明図で
ある。
FIG. 2 is an explanatory diagram showing changes in time and evaporation rate during drying of seaweed.

【図3】 海苔表面温度の特性を説明図である。 特許出願人         フルタ電機株式会社代理
人  弁理士      竹 中 −宣吋1tJ ”
FIG. 3 is an explanatory diagram of the characteristics of seaweed surface temperature. Patent applicant: Furuta Electric Co., Ltd. Agent: Patent attorney: Takenaka - Nobuo 1tJ”

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】海苔自動乾燥機内に於て、乾燥される途中
の海苔の表面温度と、その乾燥雰囲気の湿球温度とを検
出し、この検出した値をコンピュータに入力し、その検
出した値の差により乾燥度合いを自動判断し、適正な乾
燥条件を自動設定制御する海苔乾燥度合いの自動検出に
よる海苔の乾燥法。
Claim 1: In an automatic seaweed dryer, the surface temperature of seaweed that is being dried and the wet bulb temperature of the drying atmosphere are detected, the detected values are input into a computer, and the detected values are A method of drying seaweed that automatically determines the degree of dryness based on the difference in seaweed and automatically sets and controls the appropriate drying conditions.
【請求項2】請求項1の乾燥条件が、海苔簀の搬送スピ
ードで制御する請求項1の海苔乾燥度合いの自動検出に
よる海苔の乾燥法。
2. The method for drying seaweed by automatically detecting the degree of dryness of the seaweed according to claim 1, wherein the drying conditions according to claim 1 are controlled by the conveyance speed of the seaweed cage.
【請求項3】請求項1の乾燥条件が、熱風の風速で制御
する請求項1の海苔乾燥度合いの自動検出による海苔の
乾燥法。
3. The method for drying seaweed by automatically detecting the degree of dryness of the seaweed according to claim 1, wherein the drying conditions according to claim 1 are controlled by the speed of hot air.
【請求項4】請求項1の乾燥条件が、温度及び/又は湿
度で制御する請求項1の海苔乾燥度合いの自動検出によ
る海苔の乾燥法。
4. The method for drying seaweed by automatically detecting the degree of dryness of seaweed according to claim 1, wherein the drying conditions according to claim 1 are controlled by temperature and/or humidity.
JP2340807A 1990-11-30 1990-11-30 Drying method of seaweed by automatic detection of dryness of seaweed Expired - Fee Related JPH0628551B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2340807A JPH0628551B2 (en) 1990-11-30 1990-11-30 Drying method of seaweed by automatic detection of dryness of seaweed

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2340807A JPH0628551B2 (en) 1990-11-30 1990-11-30 Drying method of seaweed by automatic detection of dryness of seaweed

Publications (2)

Publication Number Publication Date
JPH04207175A true JPH04207175A (en) 1992-07-29
JPH0628551B2 JPH0628551B2 (en) 1994-04-20

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0655675A (en) * 1992-08-10 1994-03-01 Mitsubishi Heavy Ind Ltd Single-faced corrugated board producing machine
JP2012029644A (en) * 2010-07-30 2012-02-16 Itsuwa Kogyo:Kk Laver-producing machine
JP2015132402A (en) * 2014-01-10 2015-07-23 三菱電機株式会社 Stationary induction machine drying method and stationary induction machine drying device

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109453970B (en) * 2018-11-01 2021-11-02 首钢智新迁安电磁材料有限公司 Drying control method and device for magnesium oxide on surface of strip steel

Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51133446A (en) * 1975-05-02 1976-11-19 Nichimo Kk Method of drying laver
JPS51136854A (en) * 1975-05-20 1976-11-26 Masamitsu Kinoshita Method of drying raw laver
JPS5753196U (en) * 1980-09-12 1982-03-27
JPS5756872A (en) * 1980-09-24 1982-04-05 Ricoh Co Ltd Transfer separating method of electrophotography copying machine
JPS6313666A (en) * 1986-07-02 1988-01-20 Matsushita Electric Ind Co Ltd Soldering device
JPS6360986A (en) * 1986-08-29 1988-03-17 Idemitsu Petrochem Co Ltd Dithiocarbamate and production thereof
JPS6360985A (en) * 1986-08-08 1988-03-17 Yoshitomi Pharmaceut Ind Ltd 4,7-dihydropyrazolo(1,5-a)pyrimidine derivative
JPS6365303A (en) * 1986-09-08 1988-03-23 Hitachi Ltd Weld line detector
JPS63167771U (en) * 1987-04-22 1988-11-01
JPS63279769A (en) * 1986-11-25 1988-11-16 Yoshiharu Uchihashi Control of laver drying chamber
JPH01191663A (en) * 1988-01-27 1989-08-01 Furuta Denki Kk Apparatus for drying laver and method therefor
JPH03160974A (en) * 1989-11-20 1991-07-10 Chikanosuke Oki Drying of laver of leaf material temperature control type and device therefor

Patent Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51133446A (en) * 1975-05-02 1976-11-19 Nichimo Kk Method of drying laver
JPS51136854A (en) * 1975-05-20 1976-11-26 Masamitsu Kinoshita Method of drying raw laver
JPS5753196U (en) * 1980-09-12 1982-03-27
JPS5756872A (en) * 1980-09-24 1982-04-05 Ricoh Co Ltd Transfer separating method of electrophotography copying machine
JPS6313666A (en) * 1986-07-02 1988-01-20 Matsushita Electric Ind Co Ltd Soldering device
JPS6360985A (en) * 1986-08-08 1988-03-17 Yoshitomi Pharmaceut Ind Ltd 4,7-dihydropyrazolo(1,5-a)pyrimidine derivative
JPS6360986A (en) * 1986-08-29 1988-03-17 Idemitsu Petrochem Co Ltd Dithiocarbamate and production thereof
JPS6365303A (en) * 1986-09-08 1988-03-23 Hitachi Ltd Weld line detector
JPS63279769A (en) * 1986-11-25 1988-11-16 Yoshiharu Uchihashi Control of laver drying chamber
JPS63167771U (en) * 1987-04-22 1988-11-01
JPH01191663A (en) * 1988-01-27 1989-08-01 Furuta Denki Kk Apparatus for drying laver and method therefor
JPH03160974A (en) * 1989-11-20 1991-07-10 Chikanosuke Oki Drying of laver of leaf material temperature control type and device therefor

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0655675A (en) * 1992-08-10 1994-03-01 Mitsubishi Heavy Ind Ltd Single-faced corrugated board producing machine
JP2012029644A (en) * 2010-07-30 2012-02-16 Itsuwa Kogyo:Kk Laver-producing machine
JP2015132402A (en) * 2014-01-10 2015-07-23 三菱電機株式会社 Stationary induction machine drying method and stationary induction machine drying device

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