JPS6313666B2 - - Google Patents

Info

Publication number
JPS6313666B2
JPS6313666B2 JP60110039A JP11003985A JPS6313666B2 JP S6313666 B2 JPS6313666 B2 JP S6313666B2 JP 60110039 A JP60110039 A JP 60110039A JP 11003985 A JP11003985 A JP 11003985A JP S6313666 B2 JPS6313666 B2 JP S6313666B2
Authority
JP
Japan
Prior art keywords
humidity
drying
air
seaweed
set value
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
Application number
JP60110039A
Other languages
Japanese (ja)
Other versions
JPS61268161A (en
Inventor
Mikio Furuta
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 JP60110039A priority Critical patent/JPS61268161A/en
Publication of JPS61268161A publication Critical patent/JPS61268161A/en
Publication of JPS6313666B2 publication Critical patent/JPS6313666B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 「産業上の利用分野」 本発明は海苔の乾燥方法に関するものである。[Detailed description of the invention] "Industrial application field" The present invention relates to a method for drying seaweed.

「従来の技術」 海苔の乾燥において、乾燥室内の温度と湿度と
は仕上製品に大きな影響を与え、その製品の優劣
を決定する大きな要因であるとされている。即ち
通常の生海苔原料の状態において、乾燥室内の湿
度が設定値(40〜50%)であつてもその温度が許
容温度(50℃)以上になると海苔の細胞が枯死変
質して光沢を失つたり、変色したりする。また乾
燥室内の温度が許容温度であつても、その湿度が
ある値以下例えば20〜30%くらいになると、乾燥
後の海苔の剥離が困難となり、破れ、縮みをおこ
し易く、しかもその風味を損なうこと、一方その
湿度がある値以上例えば60%くらいになるとクモ
リが発生し、艶をなくすなどの品質を著しく劣化
し製品価値が低下するといわれている。このよう
なことからその改良として色々提案され、その内
一部が実用に供されている。例えば技術文献とし
ては、特公昭52−42869号で、生海苔が枯死変質
する限界温度の熱風で恒率乾燥を行なう第1工程
と、前記許容温度より低い温度の加熱面に生海苔
を圧接して減率乾燥を行なう第2工程とを組合せ
た生海苔の乾燥方法とか、特公昭57−056872号
で、乾燥室内の湿度、温度のいずれかを基準とし
て、それが設定範囲以下になつとき燃焼炉のバー
ナーを切るようにした海苔の乾燥方法とか、また
特公昭58−58068号で、通気ダクトを介して連設
された複数の乾燥室内を海苔簀が通過するように
した、比較的低温の乾燥用通気によつて乾燥処理
するようにした生海苔等の連続乾燥装置がある。
そして一般的には第5図に示すように、工場内に
天板部が網体等で形成された開放式の乾燥機を配
設し、工場内に湿度センサーを設け、この湿度セ
ンサーで工場内の湿度を検出し、これにより乾燥
機内の湿度を調整する方法が採用されている。
``Prior Art'' When drying seaweed, the temperature and humidity inside the drying room have a great effect on the finished product, and are said to be major factors in determining the quality of the product. In other words, even if the humidity inside the drying room is at the set value (40 to 50%), if the temperature exceeds the allowable temperature (50°C) for normal raw seaweed raw materials, the seaweed cells will wither and deteriorate and lose their luster. It may become dull or discolored. Furthermore, even if the temperature inside the drying room is within the permissible range, if the humidity drops below a certain value, for example around 20-30%, it becomes difficult to peel off the seaweed after drying, causing it to tear and shrink easily, and furthermore, the flavor is lost. On the other hand, it is said that when the humidity exceeds a certain value, for example around 60%, cloudiness occurs and the quality deteriorates significantly, such as loss of luster, and the value of the product decreases. For this reason, various improvements have been proposed, some of which have been put into practical use. For example, as a technical document, Japanese Patent Publication No. 52-42869 describes the first step of drying at a constant rate with hot air at a critical temperature at which raw seaweed will wither and deteriorate, and the raw seaweed is pressed against a heated surface at a temperature lower than the permissible temperature. According to Japanese Patent Publication No. 57-056872, there is a method for drying raw seaweed that combines a second step of drying at a decreasing rate. There is a method of drying seaweed in which the burner of the furnace is turned off, and in Japanese Patent Publication No. 58-58068, there is a method of drying seaweed in which the seaweed is passed through multiple drying chambers connected through ventilation ducts at a relatively low temperature. There is a continuous drying apparatus for drying raw seaweed and the like using drying ventilation.
Generally, as shown in Figure 5, an open type dryer with a top plate made of a net or the like is installed inside the factory, and a humidity sensor is installed inside the factory. A method is adopted in which the humidity inside the dryer is detected and the humidity inside the dryer is adjusted accordingly.

「発明が解決しようとする問題点」 以上の如く従来の海苔の乾燥方法は、いずれも
天板部が網体等で構成されているいわゆる開放式
の乾燥機を用いて、熱風等を乾燥機の海苔に当て
た後、工場内のフアンを介して工場外に排出して
乾燥する方法とか、また工場内に設けた遮閉部材
例えばカーテンを介して熱風を再度乾燥機に循環
して湿つた熱風を再利用する方法とかがある。こ
のようにその湿度管理が乾燥機内を対象とせずあ
くまでも工場内の湿度を基準としていることか
ら、当然のことながら時間帯とか天候等により乾
燥機内の湿度にバラツキが生じ、時には過乾燥と
なつて前述の如く破れ、ワレを生じて品質の劣化
を招来する問題点がある。また温度制御は燃焼炉
のバーナーで、風速はフアンで、時間はコンベア
スピードでそれぞれ比較的簡易に制御できるが、
湿度においては適切な制御手段が見当らずその改
良が望まれていた。更に雨の日などで乾燥機の室
内が多湿状態になると、クモリ海苔という艶のな
い海苔ができるという問題点があつた。
``Problems to be Solved by the Invention'' As described above, conventional seaweed drying methods use a so-called open type dryer whose top plate is made of a net, etc., and blow hot air into the dryer. After applying it to the seaweed, it is discharged outside the factory through a fan inside the factory to dry it, or hot air is circulated again to the dryer through a shielding member installed inside the factory, such as a curtain, to dry it. There are ways to reuse hot air. As this humidity control does not target the inside of the dryer but is based on the humidity inside the factory, it is natural that the humidity inside the dryer will vary depending on the time of day and the weather, resulting in overdrying at times. As mentioned above, there is a problem of tearing and cracking, which leads to deterioration of quality. In addition, the temperature can be controlled relatively easily with the burner of the combustion furnace, the wind speed with the fan, and the time with the conveyor speed.
No suitable means of controlling humidity could be found, and improvements were desired. Furthermore, when the inside of the dryer becomes humid on a rainy day, a dull sheet of seaweed called kumori nori is formed.

また本発明と軌を一にする同時出願(1)の発明に
おいても恒湿状態を維持できるが、フアンの
ON,OFFであるので、恒湿状態といつても一定
の幅が生ずることになる。
Furthermore, the invention of simultaneous application (1), which is on the same track as the present invention, can also maintain a constant humidity state;
Since it is ON and OFF, a constant range will always occur under constant humidity conditions.

「問題点を解決するための手段」 そこで本発明は、比較的簡単な方法で、乾燥室
の湿度を設定値に維持しつつ、密閉式の乾燥室で
生成される加温、恒湿空気を利用して海苔を乾燥
するようにしたものであり、また、一度乾燥機に
生海苔が充填されると、以後生海苔より出る水分
により乾燥機が多湿状態となるので、原則として
吸気口を閉塞した状態で積極的に排出するもの
で、その要旨は、乾燥機にシヤツターで開閉する
吸気口及び排気口を設けて密閉式の乾燥室を形成
し、この乾燥室内に湿度センサーと、加湿器とイ
ンバータで制御されるフアン室とをそれぞれ配備
し、前記湿度センサーで乾燥室の湿度を検出し、
その湿度が設定値であるときは、乾燥室で生成さ
れる加温、恒湿空気を循環し、その湿度が設定値
以下であるときは、前記加湿器を作動させ、逆に
設定値以上であるときは、インバータを介してフ
アンを駆動して乾燥室を開放し、この室内の多湿
空気を排出しつつ外気又は工場内の空気を導入し
て、湿度を設定値に維持し、乾燥室で生成される
加温、恒湿空気を循環して制御するようにした海
苔の乾燥方法である。
``Means for Solving the Problems'' Therefore, the present invention uses a relatively simple method to maintain the humidity of the drying chamber at a set value while controlling the heated, constant humidity air generated in the closed drying chamber. In addition, once the dryer is filled with raw seaweed, the moisture coming out of the raw seaweed will cause the dryer to become humid, so as a general rule, the air inlet should be blocked. The gist of this is that the dryer is equipped with an intake and exhaust port that can be opened and closed by a shutter to form a closed drying chamber, and a humidity sensor and humidifier are installed inside this drying chamber. A fan room controlled by an inverter is installed, and the humidity of the drying room is detected by the humidity sensor,
When the humidity is at the set value, the heated, constant humidity air generated in the drying room is circulated, when the humidity is below the set value, the humidifier is activated, and vice versa. In some cases, a fan is driven via an inverter to open the drying room, and while the humid air in the room is exhausted, outside air or air from inside the factory is introduced to maintain the humidity at the set value. This is a method of drying seaweed that circulates and controls the heated, constant-humidity air that is generated.

「作用」 次に本発明の作用を説明すると、供給側の海苔
簀1に順次生海苔が供給されると共に、燃焼炉2
のバーナーが着火され順次熱風が生成されてい
く。この場合乾燥室4は密閉式となつていること
から、乾燥室4で生成される空気は加温され、こ
の加温空気はフアン3を介して強制的に乾燥室4
を循環していき、乾燥室4の先ず排出側の海苔簀
1′に載置されている生海苔に接触して湿り空気
となるいわゆる通常の正転循環(以下単に循環と
する)経路をたどる。この湿り空気は燃焼炉2に
送られ、ここで熱せられて加温空気となり前述と
同様な経過をたどる。そして、乾燥されて乾燥海
苔となると、乾燥機6の排出側の海苔簀1′より
順次排出されるという経路をたどるのであるが、
下記の条件下では以下のような手段が採用され
る。即ち、湿度センサー5が乾燥室4内の湿度を
検出し、その湿度が設定値以下であるときは、加
湿器10を作動させ加湿し設定値になし、過乾燥
を防止しつつこの空気を燃焼炉2で加熱して加
温、恒湿空気として、前述と同様な経過をたど
る。またその湿度が設定値以上であるときは、そ
の検出値を制御回路11に入力し、例えばこの制
御回路11に配設した入力変換器12を介してそ
の検出値を電気的信号に変換して比較器14に入
力すると、すでにこの比較器14に設定部13を
介して設定値が入力されていることから、この設
定値の入力信号と検出値の入力信号とを比較しそ
の差を増幅器15に入力し、この増幅器15で増
幅し制御信号としてインバータ16に入力する。
この制御信号に基づいてインバータ16で周波数
変換をなし、この変換された周波数に基づきモー
タ3aの回転数を調節し、フアン3の回転を可変
的にしてシヤツターを開放し排気口8より多湿空
気を積極的に排出すると共に、吸気口9より外気
又は工場内の空気を乾燥室4に導入し設定値にな
し、多湿乾燥を防止しつつこの空気を燃焼炉2で
加熱して加温、恒湿空気にし、前述と同様な経過
をたどる。このように湿度が設定値以上のとき
は、僅かの検出値に対してもフアン3を微調節し
て、多湿状況を回避するようにし、恒湿空気を維
持しようとするのである。例えば第3,4図の図
表で具体的に説明すると、第3図イの如く、始動
直後の乾燥室24内においては、これに供給され
た生海苔の量は少ないが、熱風の供給が今だ十分
でないことから、乾燥機24内の湿度は工場内湿
度、外気に順ずる。本発明においても同様で、始
動直後の乾燥室4内の湿度は工場内湿度等に順ず
る第4図イ′の状態となる。その後熱風の供給が
順調であるのに対して、生海苔の供給が乾燥機2
4の生海苔収容能力(海苔簀に生海苔が略全部供
給された状態)に到るまでに時間を要する関係
上、湿度が低下し設定値以下に下り第3図ロの状
態となりいわゆる過乾燥となる。しかし本発明で
は、設定位以下になると直ちに湿度センサー5が
作動して、加湿器10を作動して加湿していきそ
の湿度を設定値に維持する第4図ロ′の状態とな
り過乾燥を防止できる。この場合生海苔が硬い状
態のときは、加温、恒湿空気を先ず供給側の海苔
簀1に吹き付け、この比較的高めの加温、恒湿空
気を硬い状態の生海苔に接触させる逆転循環(第
2図参照)をなす。これにより、硬い状態の生海
苔に高めの加温、恒湿空気を介して積極的に柔ら
かく、しかも比較的短時間に乾燥していく。つづ
いて生海苔の供給が進んで乾燥機24が充填され
てくると、湿度が順次増加して一応設定値を維持
すると共に、温度も設定値を維持して一応正常と
なる第3図ハの状態となるが、従来は前述の如く
乾燥機24が開放式となつていることから、外気
又は工場内の空気の影響を受けやすく、例えば雨
天、晴天というように天候により湿度のバラツキ
が出る。即ち午前雨で午後晴という場合は、第3
図一点鎖線の如く、乾燥機24内の湿度が大きく
変動するので、乾燥ムラが発生するおそれがあつ
た。本発明においても乾燥室4が生海苔で充填さ
れ、湿度が順次増加して設定値を維持すると共
に、温度も設定値に維持される。しかしながら本
発明では、乾燥室4が密閉式(シヤツターが閉止
されているとき)となつていることから温度及び
湿度が高くなるおそれがあり多湿空気となる(尚
高温となりすぎるときはバーナーを切る)。この
ように多湿空気となること即ち湿度が設定値以上
となることは原則として好ましくないので、湿度
センサー5の検出値に基づいて制御回路11を介
してインバータ16で周波数変換をなし、この変
換された周波数に基づきモータ3aの回転数を調
節し、フアン3の回転を可変的にしてシヤツター
を開放し、乾燥室4内の多湿空気を排気口8を介
して排出すると共に、吸気口9より外気等を導入
して湿度を設定値まで下げその値を維持してい
く。このように湿度が設定値以上のときは、僅か
の検出値に対してもフアン3を微調節して、多湿
状況を回避するようにし、恒湿空気の循環を維持
するようになす。また乾燥室4が過乾燥となつた
場合は、前述の如く加湿器10を作動して加湿し
ていき湿度を設定値に維持していく。このような
操作をもつて乾燥室4内の湿度差を図示の如く小
さくして第4図ハ′の如くほぼ恒湿状態に保持し
ていくと共に、乾燥室4が密閉式であるので、天
候、外気等の影響を受けることが少なく、仮りに
影響を受けても前述の操作をもつてすればほ恒湿
状態に保持できる。このようにして生成された加
温、恒湿空気により生海苔に含有する水分子等の
活動を活発にして、生海苔の中心までほぼ均一の
状態で乾燥することができると思われ、良質な乾
海苔の製造が期待できる。この場合生海苔が硬い
状態のときは、加温、恒湿空気を先ず供給側の海
苔簀1に吹き付け、この比較的高めの加温、恒湿
空気を硬い状態の生海苔に接触させる逆転循環
(第2図参照)をなす。これにより、硬い状態の
生海苔を高めの加温、恒湿空気を介して積極的に
柔らかく、しかも比較的短時間に乾燥していく。
そして作業近くになると、生海苔の供給が停止さ
れるので、生海苔の乾燥機24に占める割合が少
なくなり、湿度は順次下つていき設定値以下にな
つていくのに対して、温度は熱風による余熱によ
り一時的に上昇してかなり高温となるので、海苔
細胞の枯死が生じる第3図ホの状態となる。しか
し本発明では、湿度が設定値より下がると直ちに
湿度センサー5が作動して、加湿器10を作動し
て加湿していきその湿度を設定値に維持していく
ので、海苔細胞の故死のない第4図ホ′の状態と
なる。この場合生海苔が硬い状態のときは、加
温、恒湿空気を先ず供給側の海苔簀1に吹き付け
(勿論この場合供給側の海苔簀1には生海苔が付
着されていない。)、幾分湿つた低くなつた加温、
恒湿空気を排出側にある硬い状態にあつた生海苔
に接触させる逆転循環(第2図参照)をなす。こ
れにより、硬い状態にあつた生海苔に補助的に幾
分湿つた低くなつた加温、恒湿空気を介して積極
的に柔らかくなるように、望ましくは緩やかに乾
燥していく。ついで生海苔の乾燥機24に占める
割合の減少に伴つて、湿度はさらに下がつて設定
値よりかなり下がるので、乾燥機24内は過乾燥
となる第3図ヘの状態となる。しかし本発明で
は、乾燥室4に占める割合が減少して、湿度が下
がると直ちに湿度センサー5が作動して、加湿器
10を作動し加湿するので、湿度を設定値に維持
でき、もつて過乾燥を回避できる第4図ヘ′の状
態となる。この場合生海苔が硬い状態のときは、
加温、恒湿空気を先ず供給側の海苔簀1に吹き付
け、この比較的高めの加温、恒湿空気を硬い状態
の生海苔に接触させる逆転循環(第2図参照)を
なす。一方これにより、硬い状態の生海苔を排出
側の海苔簀1′に付着されている乾燥が略終了し
た生海苔に対しては、前述の供給側の生海苔を乾
燥して、幾分湿りぎみで低くなつた加温、恒湿空
気を、この乾燥が略終了した生海苔に当て、幾分
正常循環より湿りぎみの乾燥をなすことにより、
前記の硬い状態の生海苔を柔らか味のある乾海苔
を生成することができるものである。
"Function" Next, to explain the function of the present invention, raw seaweed is sequentially supplied to the seaweed tank 1 on the supply side, and the combustion furnace 2
The burners are ignited and hot air is sequentially generated. In this case, since the drying chamber 4 is of a closed type, the air generated in the drying chamber 4 is heated, and this heated air is forced through the fan 3 into the drying chamber 4.
It first contacts the fresh seaweed placed in the seaweed cage 1' on the discharge side of the drying chamber 4 and becomes moist air, following the so-called normal normal circulation (hereinafter simply referred to as circulation) path. . This humid air is sent to the combustion furnace 2, where it is heated to become heated air and follows the same process as described above. When the seaweed is dried, it is sequentially discharged from the seaweed basin 1' on the discharge side of the dryer 6.
The following measures are adopted under the following conditions. That is, the humidity sensor 5 detects the humidity in the drying chamber 4, and when the humidity is below the set value, the humidifier 10 is activated to humidify the air to the set value and burn this air while preventing overdrying. The same process as described above is followed by heating in the furnace 2 to create warm, constant humidity air. When the humidity is higher than the set value, the detected value is input to the control circuit 11, and the detected value is converted into an electrical signal via an input converter 12 disposed in the control circuit 11, for example. When the input signal is input to the comparator 14, since the set value has already been input to the comparator 14 via the setting section 13, the input signal of this set value and the input signal of the detected value are compared and the difference is sent to the amplifier 15. The signal is input to the inverter 16, amplified by the amplifier 15, and input to the inverter 16 as a control signal.
Based on this control signal, the inverter 16 converts the frequency, adjusts the rotation speed of the motor 3a based on the converted frequency, makes the rotation of the fan 3 variable, opens the shutter, and blows humid air from the exhaust port 8. In addition to actively exhausting air, outside air or air inside the factory is introduced into the drying chamber 4 through the intake port 9 to reach the set value, and this air is heated in the combustion furnace 2 to heat it and maintain humidity while preventing high humidity and drying. Air it and follow the same process as above. In this way, when the humidity is above the set value, the fan 3 is finely adjusted even for a small detected value to avoid a humid situation and maintain constant humidity air. For example, to explain it concretely using the diagrams in Figures 3 and 4, as shown in Figure 3A, the amount of raw seaweed supplied to the drying chamber 24 immediately after startup is small, but the supply of hot air is now Since this is not sufficient, the humidity inside the dryer 24 depends on the humidity inside the factory and the outside air. The same applies to the present invention, and the humidity in the drying chamber 4 immediately after startup becomes the state shown in FIG. 4A', which corresponds to the humidity in the factory. After that, while the supply of hot air was steady, the supply of raw seaweed continued to dryer 2.
Because it takes time to reach the raw seaweed storage capacity of 4 (the state in which almost all raw seaweed is supplied to the seaweed pond), the humidity decreases and falls below the set value, resulting in the state shown in Figure 3 B, which is called over-drying. becomes. However, in the present invention, as soon as the humidity falls below the set level, the humidity sensor 5 is activated, and the humidifier 10 is activated to humidify and maintain the humidity at the set value. can. In this case, when the raw seaweed is in a hard state, heated, constant-humidity air is first blown into the seaweed tank 1 on the supply side, and this relatively high temperature, constant-humidity air is brought into contact with the hard raw seaweed in reverse circulation. (See Figure 2). This actively softens the hard raw seaweed by heating it at a high temperature and exposing it to constant humidity air, and dries it in a relatively short time. Next, as the supply of fresh seaweed progresses and the dryer 24 is filled, the humidity gradually increases and temporarily maintains the set value, and the temperature also maintains the set value and becomes normal for the time being, as shown in Figure 3 (c). However, since the dryer 24 is conventionally of an open type as described above, it is easily influenced by the outside air or the air inside the factory, and the humidity varies depending on the weather, for example, rainy or sunny. In other words, if it is raining in the morning and sunny in the afternoon, the third
As shown by the one-dot chain line in the figure, since the humidity inside the dryer 24 fluctuated greatly, there was a risk that uneven drying would occur. Also in the present invention, the drying chamber 4 is filled with fresh seaweed, and the humidity is gradually increased to maintain the set value, and the temperature is also maintained at the set value. However, in the present invention, since the drying chamber 4 is a closed type (when the shutter is closed), the temperature and humidity may become high, resulting in humid air (if the temperature becomes too high, turn off the burner). . In principle, it is undesirable for the air to become humid, that is, for the humidity to exceed a set value. The rotation speed of the motor 3a is adjusted based on the frequency, the rotation of the fan 3 is made variable, and the shutter is opened. etc. to lower the humidity to the set value and maintain that value. In this way, when the humidity is above the set value, the fan 3 is finely adjusted even for a small detected value to avoid a humid situation and maintain constant humidity air circulation. Furthermore, if the drying chamber 4 becomes overly dry, the humidifier 10 is operated to humidify and maintain the humidity at the set value as described above. Through such operations, the humidity difference in the drying chamber 4 is reduced as shown in the figure, and the humidity is maintained at almost constant humidity as shown in Figure 4 C'. , it is less affected by outside air, etc., and even if it is affected, it can be maintained at constant humidity by performing the above-mentioned operations. It is thought that the heated, constant humidity air generated in this way activates the activity of water molecules contained in the raw seaweed, allowing the raw seaweed to dry almost uniformly to the center, resulting in high-quality The production of dried seaweed is expected. In this case, when the raw seaweed is in a hard state, heated, constant-humidity air is first blown into the seaweed tank 1 on the supply side, and this relatively high temperature, constant-humidity air is brought into contact with the hard raw seaweed in reverse circulation. (See Figure 2). This actively softens and dries the hard raw seaweed in a relatively short time by heating it at a high temperature and exposing it to constant humidity air.
Then, as the work approaches, the supply of raw seaweed is stopped, so the proportion of raw seaweed in the dryer 24 decreases, and the humidity gradually decreases to below the set value, while the temperature decreases with hot air. Due to the residual heat caused by this, the temperature temporarily rises to a considerably high temperature, resulting in the state shown in Figure 3 (e) where the seaweed cells wither and die. However, in the present invention, as soon as the humidity drops below the set value, the humidity sensor 5 is activated, and the humidifier 10 is activated to humidify and maintain the humidity at the set value. The state shown in Fig. 4, E', is reached. In this case, when the raw seaweed is in a hard state, heated, constant-humidity air is first blown onto the nori basin 1 on the supply side (of course, in this case, no raw seaweed is attached to the nori basin 1 on the supply side), and then Heating became damp and low.
A reverse circulation (see Figure 2) is created in which constant humidity air is brought into contact with hard raw seaweed on the discharge side. As a result, the raw seaweed, which is in a hard state, is desirably slowly dried so that it is actively softened through the slightly moistened, low-temperature, constant-humidity air. Then, as the proportion of raw seaweed in the dryer 24 decreases, the humidity further decreases and becomes considerably lower than the set value, so that the inside of the dryer 24 becomes overdried, as shown in FIG. 3. However, in the present invention, as soon as the proportion of the drying chamber 4 decreases and the humidity drops, the humidity sensor 5 is activated and the humidifier 10 is activated to perform humidification. The state shown in Fig. 4F' is reached in which drying can be avoided. In this case, when the raw nori is hard,
Warmed, constant-humidity air is first blown onto the seaweed cage 1 on the supply side, and a reverse circulation (see Figure 2) is created in which this relatively high-temperature, constant-humidity air is brought into contact with the hard raw seaweed. On the other hand, as a result, the hard raw seaweed is removed from the raw seaweed that has almost completely dried and is attached to the seaweed cage 1' on the discharge side, and the raw seaweed on the supply side is dried and slightly moistened. By applying the heated, constant humidity air that has been lowered by the drying process to the raw seaweed that has almost finished drying, the drying process is slightly more humid than the normal circulation.
It is possible to produce soft dry dried seaweed from the hard fresh seaweed described above.

「実施例」 図面は本発明の一実施例を示しており、6はシ
ヤツターで開閉する吸気口9と排気口8とを設け
てなる密閉式の乾燥機であり、この乾燥機6の乾
燥室4はシヤツターの回動で開閉する構成となつ
ている。そしてこの乾燥室4には海苔簀1,1′
と燃焼炉2及びフアン3が設けられている。この
燃焼炉2で生成された熱風はフアン3を介して乾
燥室4内を左回りいわゆる正転循環(第1図の反
時計方向)右回りいわゆる逆転循環(第2図の時
計方向)の如く循環する。即ち熱風はフアン3の
正転により逆転循環し先ず排出側の海苔簀1′に
設けた生海苔に接触した後、供給側の海苔簀1に
設けた生海苔に接触して湿り空気となり、この湿
り空気はフアン3を介して燃焼炉2に到り、ここ
で熱せられて加温、恒湿空気となつて再び排出側
の海苔簀1′へと到る左回りと、前述とは逆にフ
アン3の逆転により熱風は、フアン3を介して正
転循環し先ず供給側の海苔簀1の設けた生海苔に
接触した後、排出側の海苔簀1′に設けたの生海
苔に接触して湿り空気となり、この湿り空気は直
接燃焼炉2に到り、ここで熱せられて加温、恒湿
空気となつて再びフアン3を介して供給側の海苔
簀1へと到る右回りの如くなり、この循環方式は
乾燥機の構造、外気等の温、湿度、生海苔の硬さ
等により適宜選択される。5は乾燥室4に設けた
湿度センサーで、この湿度センサー5で乾燥室4
の湿度を検出し、その検出値が設定値以下である
ときは、乾燥室4に配備する加湿器10を作動さ
せ、加湿して湿度を設定値に維持し、密閉式の乾
燥室4で生成される加温、恒湿空気を循環供給し
過乾燥を防止する。また湿度センサー5が設定値
以上を検出したときは、その検出値は制御回路1
1を介してインバータ16に制御信号として入力
され、このインバータ16で変換された周波数に
基づいて、フアン用のモータ3aの回転数を調節
し、もつてフアン3の回転を検出値に基づいて可
変する。このフアン3の回転によりシヤツターを
回動して吸、排気口9,8を開き、乾燥室4を開
放して室内の多湿空気を排気口8より排出すると
共に、吸気口9より外気又は工場内の空気を導入
し、その湿度を設定値に維持する。そして設定値
となつたならばフアン3の回転を停止し、シヤツ
ターを回動して吸、排気口9,8を閉じ、乾燥室
4を閉塞すると共に、ここで生成される加温、恒
湿空気を循環供給し低湿乾燥、多湿乾燥を防止す
る。尚制御回路11は、湿度センサー5よりの検
出値を電気的信号に変換する入力変換器12と、
この入力変換器12より入力される検出値信号と
予め設定部13を介して入力された設定値信号と
を比較する比較器14と、この比較器14におけ
る比較された差が入力される増幅器15とで構成
されている。図中17はスイツチである。尚本発
明における作用は前記「作用」で詳述したので、
その説明は割愛する。
``Embodiment'' The drawing shows an embodiment of the present invention. Reference numeral 6 indicates a closed type dryer having an intake port 9 and an exhaust port 8 that are opened and closed by a shutter. 4 is configured to open and close by rotating the shutter. In this drying room 4, there are seaweed cages 1 and 1'.
A combustion furnace 2 and a fan 3 are provided. The hot air generated in the combustion furnace 2 passes through the fan 3 and circulates inside the drying chamber 4 in a counterclockwise direction (counterclockwise in FIG. 1) and in a clockwise direction (clockwise in FIG. 2). circulate. That is, the hot air circulates in the reverse direction by the forward rotation of the fan 3, and first comes into contact with the raw seaweed provided in the seaweed cage 1' on the discharge side, and then comes into contact with the raw seaweed provided in the seaweed cage 1 on the supply side, becoming moist air. The humid air reaches the combustion furnace 2 via the fan 3, where it is heated, becomes constant humidity air, and returns to the discharge side seaweed cage 1' counterclockwise. By reversing the rotation of the fan 3, the hot air circulates in the normal direction via the fan 3, and first comes into contact with the raw seaweed provided in the nori pen 1 on the supply side, and then comes into contact with the raw nori provided in the nori pen 1' on the discharge side. This humid air reaches the combustion furnace 2 directly, where it is heated, becomes constant humidity air, and returns to the seaweed cage 1 on the supply side via the fan 3. This circulation method is appropriately selected depending on the structure of the dryer, the temperature and humidity of the outside air, the hardness of the raw seaweed, etc. Reference numeral 5 denotes a humidity sensor installed in the drying chamber 4.
When the detected humidity is below the set value, the humidifier 10 installed in the drying chamber 4 is activated to humidify and maintain the humidity at the set value, and the humidity generated in the closed drying chamber 4 is Circulating and supplying heated, constant humidity air prevents overdrying. Furthermore, when the humidity sensor 5 detects a humidity higher than the set value, the detected value is transferred to the control circuit 1.
1 is input as a control signal to the inverter 16, and based on the frequency converted by the inverter 16, the rotation speed of the fan motor 3a is adjusted, and the rotation of the fan 3 is varied based on the detected value. do. The rotation of the fan 3 rotates the shutter to open the intake and exhaust ports 9 and 8, which opens the drying chamber 4 and exhausts humid indoor air from the exhaust port 8. air and maintain its humidity at the set value. When the set value is reached, the rotation of the fan 3 is stopped, the shutter is rotated to close the intake and exhaust ports 9 and 8, and the drying chamber 4 is closed. Circulate and supply air to prevent low humidity and dryness and high humidity and dryness. The control circuit 11 includes an input converter 12 that converts a detected value from the humidity sensor 5 into an electrical signal,
A comparator 14 that compares the detection value signal inputted from this input converter 12 with a set value signal inputted in advance via the setting section 13, and an amplifier 15 to which the compared difference in this comparator 14 is inputted. It is made up of. In the figure, 17 is a switch. Note that the effects of the present invention have been detailed in the above “effects”, so
I will omit that explanation.

「発明の効果」 本発明は以上詳述したように、シヤツターで開
閉する吸気口及び排気口を有する密閉式の乾燥室
に湿度センサーを設け、この湿度センサーの検出
に基づいて作動する加湿器若しくはフアンを配備
すると共に、フアンををインバータを介して制御
する構成であるので、乾燥室内をほぼ設定湿度に
維持でき、加温、恒湿空気による乾燥が可能とな
り、過乾燥、多湿乾燥が回避できる。したがつて
過乾燥に起因する破れ、ワレとか、乾燥不足によ
る縮み、部分的なヌレとかを防止できること、生
海苔の中心までほぼ均一に乾燥することができ、
乾燥の均一化が達成され例えば焙焼により発生す
るといわれる色ムラがなくなること等良質な、保
存のきく乾海苔が得ることができる。また十分な
る加湿状態における乾燥であるので、滑めらか
で、艶のある、柔らかい乾海苔を能率よく製造で
きる。ことにインバータを介してモータの回転数
を可変し、フアンの回転を調節するので、乾燥室
の恒湿状況を常に維持でき、もつて生海苔を恒湿
空気にて乾燥することが可能となり、これに基づ
く前述の効果が期待できる。殊に本発明は、生海
苔が硬い状態の時に、供給側の生海苔より加温、
恒湿空気を当てる構成いわゆる逆転循環するもの
であるので、このような状態の生海苔に対しても
有効に対処できるもので、略均一な硬さの乾海苔
とか、口当りのよい乾海苔を生成できるものであ
る。更には生海苔の硬軟に対応して、最適でかつ
状況に応じた湿度管理が可能となるし、在来のよ
うに過乾燥による弊害例えばワレ、部分的な縮
み、破れ等の防止と、不良海苔の発生を最小にと
どめることができること、また前記のように吸気
口及び排気口による空気の置換方式であるので、
最適な加温空気を比較的迅速に供給できるもので
あり、またフアンを介してインバータを介して制
御する方式であるので、乾燥室内の湿度の微調整
もできること、また乾燥不足が回避され、もつて
乾燥不足に起因する縮み、部分的なヌレ等を防止
でき良質な乾海苔が製造できる卓効がある。更に
は同様に制御することにより、生海苔、気象条件
等の状況に対応して最適な湿度環境をつくること
ができる。
"Effects of the Invention" As described in detail above, the present invention provides a humidity sensor in a closed drying chamber having an intake port and an exhaust port that are opened and closed by a shutter, and a humidifier or a humidifier that operates based on the detection of the humidity sensor. Since a fan is installed and the fan is controlled via an inverter, the humidity inside the drying room can be maintained at approximately the set humidity, making it possible to dry with heated and constant humidity air, avoiding overdrying and drying with too much humidity. . Therefore, it is possible to prevent tears and cracks caused by over-drying, shrinkage and partial wetting caused by insufficient drying, and it is possible to dry almost evenly to the center of raw seaweed.
Uniform drying is achieved and, for example, the color unevenness that is said to occur due to roasting is eliminated, making it possible to obtain dried seaweed that is of good quality and has a long shelf life. Furthermore, since drying is carried out in a sufficiently humidified state, smooth, glossy, and soft dried seaweed can be efficiently produced. In particular, since the rotation speed of the motor is varied via an inverter and the rotation of the fan is adjusted, a constant humidity condition in the drying room can be maintained at all times, making it possible to dry raw seaweed in constant humidity air. Based on this, the aforementioned effects can be expected. In particular, in the present invention, when the raw seaweed is in a hard state, the raw seaweed on the supply side is heated,
Since it has a configuration that applies constant humidity air, so-called reverse circulation, it can effectively deal with raw seaweed in such conditions, and can produce dry seaweed with approximately uniform hardness and a good texture. It is. Furthermore, it is possible to control humidity optimally and according to the situation, depending on the hardness and softness of raw seaweed, and prevents problems such as cracking, partial shrinkage, and tearing caused by overdrying, and reduces defects. The generation of seaweed can be kept to a minimum, and as mentioned above, the air is replaced by an intake port and an exhaust port.
It can supply optimally heated air relatively quickly, and since it is controlled via a fan and an inverter, it is possible to finely adjust the humidity in the drying room, and it also prevents insufficient drying. It is extremely effective in producing high-quality dried seaweed by preventing shrinkage and partial wetting caused by insufficient drying. Furthermore, by controlling in the same way, it is possible to create an optimal humidity environment corresponding to the situation such as raw seaweed and weather conditions.

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

図面は本発明の一実施例を示しており、第1図
は断面図、第2図は他の一例を示す断面図、第3
図は従来装置による温、湿度経過状態を示す図
表、第4図は本発明の温、湿度経過状態を示す図
表、第5図は湿度センサーとインバータ及びフア
ンの関係を示す構成図、第6図は従来装置の一例
を示す断面図である。 1,1′……海苔簀、2……燃焼炉、3……フ
アン、3a……モータ、4……乾燥室、5……湿
度センサー、6……乾燥機、7……フアン、8…
…排気口、9……吸気口、10……加湿器、11
……制御回路、12……入力変換器、13……設
定部、14……比較器、15……増幅器、16…
…インバータ、17……スイツチ。
The drawings show one embodiment of the present invention, and FIG. 1 is a sectional view, FIG. 2 is a sectional view showing another example, and FIG. 3 is a sectional view showing another example.
Figure 4 is a chart showing the temperature and humidity progress of the conventional device, Figure 4 is a chart showing the temperature and humidity progress of the present invention, Figure 5 is a configuration diagram showing the relationship between the humidity sensor, inverter, and fan, and Figure 6. 1 is a sectional view showing an example of a conventional device. 1, 1'...Seaweed cage, 2...Combustion furnace, 3...Fan, 3a...Motor, 4...Drying room, 5...Humidity sensor, 6...Dryer, 7...Fan, 8...
...Exhaust port, 9...Intake port, 10...Humidifier, 11
... Control circuit, 12 ... Input converter, 13 ... Setting section, 14 ... Comparator, 15 ... Amplifier, 16 ...
...Inverter, 17...Switch.

Claims (1)

【特許請求の範囲】[Claims] 1 乾燥機にシヤツターで開閉する吸気口及び排
気口を設けて密閉式の乾燥室を形成し、この乾燥
室内に湿度センサーと、加湿器と、インバータで
制御されるフアンとをそれぞれ配備し、前記乾燥
室に設けた湿度センサーで、この室内湿度を検出
し、その湿度が設定値であるときは、乾燥室で生
成される加温、恒湿空気を正転循環するか、生海
苔が硬い状態の場合は、乾燥室で生成される加
温、恒湿空気を逆転循環するかの手段を採用し、
一方その湿度が設定値以下であるときは、乾燥室
の加湿器を作動させ、逆に設定値以上であるとき
は、インバータを介してフアンを駆動して乾燥室
を開放し、乾燥室内の多湿空気を排出させ、外気
又は工場内の空気を乾燥室内に導入し空気の置換
を介して乾燥室内の湿度を設定値に維持しつつ、
乾燥室で生成される加温、恒湿空気を正転循環す
るか、生海苔が硬い状態の場合は、乾燥室で生成
される加温、恒湿空気を逆転循環するかの手段を
採用して生海苔を乾燥するようにした海苔の乾燥
方法。
1. A dryer is provided with an intake port and an exhaust port that are opened and closed by a shutter to form a closed drying chamber, and a humidity sensor, a humidifier, and a fan controlled by an inverter are installed in this drying chamber, and the above-mentioned A humidity sensor installed in the drying room detects the indoor humidity, and when the humidity is at the set value, either the heated and constant humidity air generated in the drying room is circulated in the normal direction, or the raw seaweed is hardened. In the case of
On the other hand, when the humidity is below the set value, the humidifier in the drying room is activated, and when the humidity is above the set value, the fan is driven via the inverter to open the drying room, causing high humidity in the drying room. Air is exhausted and outside air or factory air is introduced into the drying chamber to maintain the humidity inside the drying chamber at the set value through air replacement.
The heated and constant humidity air generated in the drying room is circulated in the normal direction, or if the raw nori is hard, the heated and constant humidity air generated in the drying room is circulated in the reverse direction. A method of drying seaweed that involves drying raw seaweed.
JP60110039A 1985-05-22 1985-05-22 Method for drying laver Granted JPS61268161A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60110039A JPS61268161A (en) 1985-05-22 1985-05-22 Method for drying laver

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60110039A JPS61268161A (en) 1985-05-22 1985-05-22 Method for drying laver

Publications (2)

Publication Number Publication Date
JPS61268161A JPS61268161A (en) 1986-11-27
JPS6313666B2 true JPS6313666B2 (en) 1988-03-26

Family

ID=14525558

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60110039A Granted JPS61268161A (en) 1985-05-22 1985-05-22 Method for drying laver

Country Status (1)

Country Link
JP (1) JPS61268161A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0263981U (en) * 1988-10-29 1990-05-14

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61271967A (en) * 1985-05-27 1986-12-02 Yoshiharu Uchihashi Humidity regulator for laver drying chamber
JP2590427B2 (en) * 1994-03-23 1997-03-12 農林水産省北陸農業試験場長 Grain dryer with humidity controller
JP5951657B2 (en) * 2014-01-21 2016-07-13 株式会社大坪鉄工 Nori production system
JP6941792B2 (en) * 2017-02-15 2021-09-29 パナソニックIpマネジメント株式会社 Sludge dryer

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS506757A (en) * 1973-05-25 1975-01-23
JPS5553195U (en) * 1978-10-06 1980-04-09
JPS5753196U (en) * 1980-09-12 1982-03-27
JPS57152873A (en) * 1981-03-17 1982-09-21 Toshiba Corp Drying system in laver sheet maker
JPS6055388B2 (en) * 1976-09-02 1985-12-04 スコツト・ペ−パ−・コンパニ− Disposable, compact, moisture-impermeable packaging for wet paper
JPS6125671U (en) * 1984-07-13 1986-02-15 株式会社明電舎 vending machine

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6055388U (en) * 1983-09-20 1985-04-18 合名会社 大坪鉄工所 Nori drying equipment

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS506757A (en) * 1973-05-25 1975-01-23
JPS6055388B2 (en) * 1976-09-02 1985-12-04 スコツト・ペ−パ−・コンパニ− Disposable, compact, moisture-impermeable packaging for wet paper
JPS5553195U (en) * 1978-10-06 1980-04-09
JPS5753196U (en) * 1980-09-12 1982-03-27
JPS57152873A (en) * 1981-03-17 1982-09-21 Toshiba Corp Drying system in laver sheet maker
JPS6125671U (en) * 1984-07-13 1986-02-15 株式会社明電舎 vending machine

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0263981U (en) * 1988-10-29 1990-05-14

Also Published As

Publication number Publication date
JPS61268161A (en) 1986-11-27

Similar Documents

Publication Publication Date Title
US3199213A (en) Method of changing the moisture content of wood
US5195251A (en) Drying kiln
CA2229276C (en) Method for drying wood
JPS6313666B2 (en)
JPS6313665B2 (en)
JPH07289226A (en) Method for carrying out humidity control of leaf tobacco
JPS635060B2 (en)
JP2012127621A (en) Grain dryer
JPH01289475A (en) Drying of leaf tobacco
JP3142648B2 (en) Agricultural and seafood drying control
JP2005225103A (en) Wood drier
JPH02119744A (en) Drying method for 'shiitake' (mushroom)
JPH10160349A (en) Timber dryer, timber drying method and electrode for drying timber
JPS58187779A (en) Circulation type cereal drier
JPH01200185A (en) Dryness control device for grain drier of circulation type
JPH01165361A (en) Method for drying leaf tobacco
JPS6017682A (en) Automatic controller for cereal grain heat-treating device
JPS6120257B2 (en)
JPH03247263A (en) Process for drying soybean
JPH0114155Y2 (en)
JPH02135077A (en) Laver-drying method and apparatus using heat pump-type dehumidifier
KR0160357B1 (en) Drying apparatus of silica-gel and the method thereof
JPS5851186B2 (en) Kukumotsukansouchi
JP2024046705A (en) Koji making device and method
JPH01189483A (en) Dusting controller for circulating grain dryer