JPS61249368A - Drying of laver - Google Patents

Drying of laver

Info

Publication number
JPS61249368A
JPS61249368A JP60092047A JP9204785A JPS61249368A JP S61249368 A JPS61249368 A JP S61249368A JP 60092047 A JP60092047 A JP 60092047A JP 9204785 A JP9204785 A JP 9204785A JP S61249368 A JPS61249368 A JP S61249368A
Authority
JP
Japan
Prior art keywords
humidity
drying
set value
air
drying chamber
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
JP60092047A
Other languages
Japanese (ja)
Other versions
JPS635060B2 (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 JP60092047A priority Critical patent/JPS61249368A/en
Publication of JPS61249368A publication Critical patent/JPS61249368A/en
Publication of JPS635060B2 publication Critical patent/JPS635060B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:A closed drier is divided into the upper and the lower drying chambers, the humidity of each drying chamber is maintained almost to a preset level with a humidifier and a fan, and laver is dried with hot air having regulated humidity. CONSTITUTION:A closed drier 6 is divided with an intermediate floor 20 into the upper drying chamber 4 and the lower drying chamber 24 which are furnished with suction ports 9, 29 and exhaustion ports 8, 28 closable with shutters. Hot air generated by combustion furnaces 2, 22 is circulated in the drying chambers 4, 24 with the fans 3, 23. The humidity values in the drying chambers 4, 24 are detected by the humidity sensors 5, 25. When the detected humidity is lower than a preset level, the humidifiers 10, 30 are energized, and when it is higher than the preset level, the fans 7, 27 are energized, the shutter is operated to open the suction and exhaustion ports 9, 29, 8, 28 to open the drying chamber 4, 24,and hot air having regulated humidity is supplied and circulated to the drying chambers 4, 24.

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、乾燥室内の湿度と温度は仕上製品
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。
``Conventional Technology'' When drying seaweed, the humidity and temperature inside the drying room have a great effect on the finished product, and are considered to be major factors in determining the quality of the product.

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%)であっ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
沢を失ったシ、変色したシする。また乾燥室内の温度が
許容温度であっても、その湿度が設定値を逸脱し10〜
20%くらいKなると、乾燥後の海苔の剥離が困難とな
シ、破れ、縮みをおこし易く、シかもその風味を損なう
など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
たシ一部で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
許容温度よシ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bずれかを基準として、それが設定範囲以下にな
った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59−48630号で、乾燥室を
多孔板を介して上下二つの空間に分割し、各空間にそれ
ぞれ燃焼器具を配備し、上方の空間に、下方の空間よフ
も温度の高い空気を送シ込むようにした海苔乾燥装置が
ある。
In other words, in the condition of normal raw seaweed raw material, even if the humidity in the drying room is at the set value (40 to 50%), if the temperature exceeds the allowable temperature (50°C), the seaweed cells will wither and deteriorate and lose their luster. It may be discolored or discolored. Also, even if the temperature inside the drying room is within the allowable range, the humidity may deviate from the set value.
It is said that when the temperature reaches about 20% K, it becomes difficult to peel off the seaweed after drying, and the seaweed tends to crack, tear, and shrink, and the quality deteriorates significantly, including loss of flavor, 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 heating surface at a temperature lower than the permissible temperature. Japanese Patent Publication No. 57-056872 describes a drying method for raw seaweed that combines drying with a second step of drying at a decreasing rate.
There is a method of drying seaweed in which the burner of the combustion furnace is turned off when the temperature falls below a set range based on the deviation of temperature b. There is a seaweed drying device that is divided into two spaces, upper and lower, each space equipped with a combustion device, and the upper space blows hotter air than the lower space.

ま九一方第4図に示すように乾燥機に生海苔が搬入、乾
燥、搬出される過程を、材料予熱区間、恒率乾燥区間、
減率乾燥区間というように大別し、生海苔の含水率に対
応して材料予熱区間では高温乾燥を、恒率乾燥区間では
加温乾燥を、減率乾燥区間では加温、加湿乾燥をするこ
とが良質な乾海苔の製造に最適であるとされている。
On the other hand, as shown in Figure 4, the process in which raw seaweed is carried into the dryer, dried, and taken out is divided into the material preheating section, constant rate drying section,
It is roughly divided into lapse rate drying sections, and depending on the moisture content of raw seaweed, high temperature drying is performed in the material preheating section, heating drying is performed in the constant rate drying section, and heating and humidification drying is performed in the lapse rate drying section. This is said to be ideal for producing high-quality dried seaweed.

「発明が解決しようとする問題点」 以上の如〈従来の海苔の乾燥方法は、いずれも天板部が
網体等で構成されるいわゆる開放式の乾燥機を用いて、
熱風等を乾燥室の海苔に当てた後、工場内のファンを介
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
機に循環して湿った熱風を再利用する方法がある。この
ようにして湿度管理はなされているが、開放式であるこ
とから、微細にその湿度を制御することがむつかしく、
時には過乾燥となシ品人質の劣化を招来したシ、雨の日
など多湿状態に°おける乾燥では、クモリ海苔いわゆる
艶のない海苔ができるという問題点があること。また特
公昭59−056872号は、温度管理であること、及
び乾燥機が二つの空間に形成されているもOの、それは
多孔板を介するものであることから湿度の流通があシ、
やはシ適切な湿度管理は困難と思われる。更に従来の海
苔の乾燥方法は、第5図に示すように乾燥室(工場)内
に開放式の乾燥機を配備する、いわゆる工場自体が乾燥
室となっていることから、その湿度管理が必ずしも十分
でないこと。
``Problems to be Solved by the Invention'' As mentioned above, all conventional methods of drying seaweed use a so-called open dryer whose top plate is made of a net, etc.
After hot air is applied to the seaweed in the drying room, it is discharged outside the factory via a fan inside the factory to dry it, or the hot air is passed back into the dryer through a shielding member installed inside the factory, such as a curtain. There is a way to circulate and reuse moist hot air. Humidity is controlled in this way, but since it is an open type, it is difficult to precisely control the humidity.
Sometimes, over-drying can lead to deterioration of quality, and drying in humid conditions such as on rainy days can lead to the formation of dull seaweed. In addition, Japanese Patent Publication No. 59-056872 requires temperature control, and although the dryer is formed in two spaces, it is through a perforated plate, so there is no circulation of humidity.
However, proper humidity control seems difficult. Furthermore, in the conventional method of drying seaweed, as shown in Figure 5, an open dryer is installed in the drying room (factory), and the drying room itself is the so-called drying room, so humidity control is not always necessary. Not enough.

「問題点を解決するだめの手段」 そこで本発明は、比較的簡単な方法で区画された乾燥室
の湿度を夫々所望する設定値に維持ノO 潟、恒湿空気を生成し、このX温、恒湿空気を乾燥用と
して利用するものであシ、その要旨は、密閉式の乾燥機
を中間床をもって上側乾燥室と下側乾燥室とに区画し、
夫々の乾燥室にシャッターで開閉する吸気口及び排気口
を設け、かつこの吸気口又は排気口に吸排気用のファン
を配備し、前記夫々の乾燥室に設けた湿度センサーで、
この室内湿度を区々に検出し、その湿度が設定値である
ときは、前記乾燥室で生成される高温、恒湿空気を循環
し、その湿度が設定値以下であるときは、乾燥室の加湿
器を作動させ湿度を設定値に維持し、またその湿度が設
定値以上であるときは、乾燥室を開放して多湿空気を排
出しつつ、外気等を導入して湿度を設定値に維持し、こ
の乾燥室で生成される加温、恒湿空気を循環して生海苔
の乾燥を夫々の乾燥室で個別に制御するようにした海苔
の乾燥方法と、前記加温空気が設定値以上(通常高温空
気)となったときは、燃焼炉のバーナーを切るようにし
た海苔の乾燥方法である。
``Means for Solving the Problem'' Therefore, the present invention uses a relatively simple method to maintain the humidity of each divided drying room at a desired set value. , which uses constant humidity air for drying.The gist is that a closed dryer is divided into an upper drying chamber and a lower drying chamber with an intermediate floor,
Each drying room is provided with an intake port and an exhaust port that are opened and closed by a shutter, and a fan for intake and exhaust is provided at the intake port or the exhaust port, and a humidity sensor is provided in each of the drying rooms.
This indoor humidity is detected separately, and when the humidity is within the set value, the high temperature and constant humidity air generated in the drying room is circulated, and when the humidity is below the set value, the drying room is circulated. The humidifier is operated to maintain the humidity at the set value, and when the humidity is above the set value, the drying room is opened to exhaust humid air and bring in outside air to maintain the humidity at the set value. A seaweed drying method in which drying of fresh seaweed is individually controlled in each drying room by circulating the heated and constant humidity air generated in the drying room, and the drying method is such that the warmed air is not higher than a set value. This is a method of drying seaweed in which the burner of the combustion furnace is turned off when the temperature reaches (usually high temperature air).

順次生海苔が供給されると共に、燃焼炉2,22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4,24はほぼ密閉式となっているので(乾燥室4
,24は海苔簀1が出入する部分と、海苔簀1が迂回す
る部分で一部開放となっている。)、加温空気が生成さ
れ、この加温空気はファン3,23を介して乾燥室4.
24内を循環していき生海苔に接触し湿シ空気となる。
As raw seaweed is sequentially supplied, the burners of the combustion furnaces 2 and 22 are ignited, and hot air is sequentially generated. In this case, since the drying chambers 4 and 24 are almost airtight (drying chamber 4
, 24 are partially open at the part where the seaweed cage 1 enters and exits and the part where the seaweed cage 1 detours. ), heated air is generated, and this heated air is passed through the fans 3, 23 to the drying chamber 4.
The air circulates through the air 24 and comes into contact with the raw seaweed, becoming moist air.

この湿り空気は燃焼炉2,22に送られ、ここで熱せら
れて加温、恒湿空気となシ前述と同様な経過をたどる。
This humid air is sent to the combustion furnaces 2 and 22, where it is heated and becomes constant humidity air, following the same process as described above.

この場合湿度センサー5,25が乾燥室4,24内の湿
度を検出し、その湿度が設定値以下であるときは、夫々
の加湿器10.30を作動させて加湿し設定値にし、過
乾燥を防止しつつこの空気を燃焼炉2.22で熱して加
温、恒湿空気となし、前述と同様な循環経路をたどる。
In this case, the humidity sensors 5 and 25 detect the humidity in the drying chambers 4 and 24, and when the humidity is below the set value, the respective humidifiers 10 and 30 are activated to humidify the humidity to the set value and prevent over-drying. This air is heated in the combustion furnace 2.22 to make it warm and constant humidity air while preventing it from occurring, and follows the same circulation path as described above.

またその湿度が設燥室4,24を開放し、夫々の77ン
7.27を駆動して排気口8,28よシ多湿空気を積極
的に排出しつつ、吸気口9,29よシ外気又は工場内の
空気を導入し設定値になし、多湿乾燥を防止しつつこの
空気は燃焼炉2,22で熱せられ加温、恒湿空気となシ
、前述と同様な循環経路をたどる。また第2の発明にお
いては、前述の第1の発明における加温、恒湿空気制御
下において、加温空気が設定値以上(通常高温空気)と
なったときは、乾燥室4.24に配設された温度センサ
ー40.50を介して、乾燥室4゜24に設けた燃焼炉
2,22のバーナーを切ル、加温空気として循環させる
。例えば第2,3図の図表で具体的に説明する0先ず第
1の発明について詳述すると、第2図(イ)の如く、始
動直後の乾燥室34内においては、熱風の供給が今だ十
分でないことから、乾燥室34内に供給された生海苔の
量に左右されることがなく湿度は工場内湿度、外気に順
する。本発明においても同様で、始動直後の乾燥室4内
においては、熱風の供給が今だ十分でないことから、乾
燥室4内に供給された生海苔の量に左右されることなく
湿度は工場内湿度等に順する第3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
供給が乾燥室34の生海苔収容能力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シ第2図(
+−)の状態となシいわゆる過乾燥となる。しかし本発
明では、設定値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3図(→の状態となシ過乾燥を防止
できる。つづいて生海苔の供給が進んで乾燥室34が充
填されると、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2図
(ハ)の状態となるが、従来の乾燥室34は天蓋部が開
放となった開放式となっていることから、外気又は工場
内の空気の影響を受けやすく、例えば雨の日、晴天の日
等によシ湿度にバラツキを生じる0即ち午前剤で午後端
という場合は第2図二点鎖線で示す如く、乾燥室34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
れがあった。本発明においても乾燥室4が生海苔で充填
されると、湿度が順次増加していき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がほぼ密閉式(シャッターが閉止されて
いるとき)となっていることから温度及び湿度が高くな
るおそれがあ夕多湿空気となる(尚高温とな多すぎると
きはバーナーを切る。)0このよう忙多湿空気となると
と即ち湿度が設定値以上となることは好ましくないので
、シャッターを回動して乾燥室4を開放し、湿度センサ
ー5を作動して77ン7を駆動させ乾燥室4内の多湿空
気を排出口8を介して排出しつつ、吸気口9よシ外気等
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
。また乾燥室4が過乾燥となった場合は、前述の如く加
湿器10を作動して加湿していきくして第3図(・うの
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、外気尋の影響を受けることが少
なくほぼ恒湿状態を保持でき、また仮シに影響を受けて
も前述の操作で補完できる。そして生成された加温、恒
湿空気によシ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tl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
第3図(・7)の状態となる。そして上側の乾燥室4か
ら下側の乾燥室24へと生海苔が搬送されてくるが、こ
の下側の乾燥室24の湿度は湿度センサー25と加湿器
30等の作動を介して所定の設定値に維持されておシ、
加温、恒湿空気による正常な乾燥が期待できる。ただし
乾燥室24の湿度が設定値以上若しくは以下となった場
合は、前述の上側の乾燥室4と同様に操作し、その湿度
を設定値に維持していく。尚所望により減率乾燥区間で
、加湿器30等を介して更に加湿乾燥状態を作ることも
できる。このような経過をもって乾燥海苔が順次製造さ
れていく。一方作業終了近くKなると、生海苔の供給が
停止されるので、先ず生海苔の乾燥室34に占める割合
が少なくな9、湿度が順次下っていき設定値以上若なっ
ていくのに対して、温度は熱風による余熱によシ一時的
に上昇し海苔細胞の枯死が生じる第2図(ホ)の状態と
なる。しかし本発明では、湿度が設定値よシ下がると直
ちに湿度センサー5が作動して、加湿器lOを作動し加
湿していきその湿度を設定値に維持する第3図<=11
>の状態となシ海苔細胞の枯死を防止できる0ついで生
海苔の乾燥室34に占める割合の減少に伴って、湿度は
さらに下ル設定値よシかなり下りてい<o一方温度も順
次下っていくが、前過程で温度が一時的に上昇したこと
に帰因して、その降下は緩やかであることから、いわゆ
る過乾燥となる第2図(へ)の状態となる。しかし本発
明では、湿度が設定値よシ下がると直ちに湿度センサー
5が作動して、加湿器10を作動し加湿していきその湿
度を設定値に維持でき、過乾燥を防止できる第3図(勺
の状態となる。このようにして最終の生海苔が下側の乾
燥室24へと搬送されてくる。この場合は乾燥室24に
ほぼ生海苔が充填されておシ、前述第3図(・勺と同様
に加温、恒湿空気による正常な乾燥が期待できる。しか
しこの最終の生海苔の乾燥室24に占める割合の減少に
伴9て、前述の従来例の如く過乾燥等となる第2図(→
、(へ)の状態になると思われる。そこで本発明は前述
の上側の乾燥室4の場合と同様に操作して、乾燥室24
内の加湿器30等を作動して加湿し、その湿度を設定値
に維持しつつ正常な乾燥が可能な第3図(杓、 (−?
)の状態にして乾燥をする。同第2の発明においても、
前述の第1の発明と同様な加温、恒湿空気制御下におい
て、海苔の乾燥がなされていくが、その加温空気が設定
値以上(本発明では乾燥室4,24がほぼ密閉式となっ
ていることから設定値以上いわゆる高温空気となシやす
い。)となったときは、乾燥室4,24に配設されてい
る温度センサー40.50を介して、乾燥室4,24に
夫々設けた燃焼炉2,22のバーナーを切り、設定値の
加温空気として循環させるようにし、第1の発明と同様
な経過をたどる。
In addition, the humidity opens the drying chambers 4 and 24, drives the respective 77 cylinders 7.27, and actively exhausts the humid air through the exhaust ports 8 and 28, while the outside air flows through the intake ports 9 and 29. Alternatively, air from within the factory is introduced to reach the set value, and while preventing high humidity and dryness, this air is heated in the combustion furnaces 2 and 22 to become warm, constant humidity air, and follows the same circulation path as described above. Further, in the second invention, under the heating and constant humidity air control in the first invention, when the heated air reaches a set value or higher (normally high temperature air), the heating air is placed in the drying chamber 4.24. The burners of the combustion furnaces 2, 22 provided in the drying chamber 4.degree. 24 are turned off and heated air is circulated via the provided temperature sensors 40.50. For example, the first invention will be explained in detail using the diagrams in Figs. 2 and 3. As shown in Fig. 2 (a), hot air is not supplied to the drying chamber 34 immediately after startup. Since it is not sufficient, the humidity is not affected by the amount of raw seaweed supplied into the drying room 34, and the humidity is determined by the humidity in the factory and the outside air. The same applies to the present invention, since the supply of hot air is still insufficient in the drying chamber 4 immediately after startup, the humidity within the factory is not affected by the amount of raw seaweed supplied into the drying chamber 4. The state shown in FIG. 3 (a) will occur depending on the humidity, etc. After that, although the supply of hot air was steady, it took time for the supply of raw seaweed to reach the raw seaweed storage capacity of the drying chamber 34, so the humidity decreased and fell below the set value (Figure 2). (
+-), it becomes what is called over-drying. However, in the present invention, as soon as the humidity falls 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. Next, as the supply of raw seaweed progresses and the drying chamber 34 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. The condition shown in Figure (c) is that the conventional drying chamber 34 is an open type with an open canopy, so it is susceptible to the influence of outside air or the air inside the factory, such as on rainy days or sunny days. When the humidity varies from day to day, i.e., when it is in the morning and in the afternoon, the humidity in the drying chamber 34 fluctuates greatly, as shown by the two-dot chain line in Figure 2, and there is a risk of uneven drying. In the present invention, when the drying chamber 4 is filled with fresh seaweed, the humidity gradually increases and maintains the set value, and the temperature is also maintained at the set value.However, in the present invention, when the drying chamber 4 Since it is almost a closed system (when the shutter is closed), there is a risk that the temperature and humidity will become high in the evening, resulting in humid air (if the temperature is too high, turn off the burner.) 0 Like this When it comes to humid air, that is, it is undesirable for the humidity to exceed the set value, so the shutter is rotated to open the drying chamber 4, the humidity sensor 5 is activated, and the 77 is driven to move the air inside the drying chamber 4. While exhausting humid air through the exhaust port 8, outside air etc. is introduced through the intake port 9 to lower the humidity to the set value and maintain that value.Furthermore, if the drying chamber 4 becomes overly dry As mentioned above, the humidifier 10 is operated to humidify the air and keep it in a nearly constant humidity state (as shown in Figure 3), and since the drying chamber 4 is closed, there is no need to worry about the weather or the outside air. It is possible to maintain a nearly constant humidity state without being affected by air, and even if it is affected by temporary humidity, it can be supplemented by the above-mentioned operation.Then, the water contained in the fresh seaweed is It is thought that by activating the activities of molecules, etc., it is possible to dry the raw seaweed in a uniform state down to the center, resulting in the state shown in Figure 3 (-7), which can be expected to produce high-quality dried seaweed. Raw seaweed is transported from the upper drying chamber 4 to the lower drying chamber 24, and the humidity in the lower drying chamber 24 is adjusted to a predetermined set value through the operation of the humidity sensor 25, humidifier 30, etc. It is maintained in
Normal drying can be expected with heated, constant humidity air. However, if the humidity in the drying chamber 24 becomes above or below the set value, the humidity is maintained at the set value by operating in the same manner as in the above-mentioned upper drying room 4. If desired, a humidified and dry state can be created in the lapse rate drying section using a humidifier 30 or the like. Dried seaweed is successively produced through this process. On the other hand, near the end of the work, the supply of raw seaweed is stopped, so firstly the proportion of raw seaweed in the drying chamber 34 decreases9, and the humidity gradually decreases and becomes younger than the set value. The temperature rises temporarily due to residual heat from the hot air, resulting in the state shown in Figure 2 (e), where the seaweed cells 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 IO is activated to humidify and maintain the humidity at the set value.
Then, as the proportion of fresh seaweed in the drying chamber 34 decreases, the humidity further drops from the lower set value. Meanwhile, the temperature also gradually decreases. However, due to the temporary rise in temperature in the previous process, the drop is gradual, resulting in the so-called overdry state shown in Fig. 2 (f). 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, thereby preventing overdrying (see Fig. 3). In this way, the final raw seaweed is transported to the lower drying chamber 24.In this case, the drying chamber 24 is almost completely filled with raw seaweed, as shown in Figure 3 above. - Normal drying due to heated and constant humidity air can be expected as in the case of seaweed. However, as the proportion of this final raw seaweed in the drying chamber 24 decreases, overdrying will occur as in the conventional example described above. Figure 2 (→
, it seems to be in the state of (to). Therefore, in the present invention, the drying chamber 24 is operated in the same manner as in the case of the upper drying chamber 4 described above.
Figure 3 (Ladle, (-?
) and dry. Also in the second invention,
The seaweed is dried under the same heated and constant humidity air control as in the first invention, but the heated air exceeds the set value (in the present invention, the drying chambers 4 and 24 are almost closed type). (This means that it is easy for the air to reach a high temperature higher than the set value. The burners of the provided combustion furnaces 2 and 22 are turned off and heated air at the set value is circulated, following the same process as in the first invention.

「実施例j 図面は本発明の一実施例を示しておシ、6は密閉式の乾
燥機で、この乾燥機6は中間床20をもって上側の乾燥
室4と下側の乾燥室24とに区画されている。そしてこ
の乾燥室4,24にはシャッターで開閉する吸気口9,
29と排気口8,28が夫々設けられていると共に、燃
焼炉2,22及びファン3,23が夫々設けられている
。そしてこの燃焼炉2,22で生成された熱風は7アン
3,23の回転によシ乾燥室4.24内を循環する。5
,25は乾燥室4゜24に夫々設けた湿度センサーで、
この湿度センサー5,25で乾燥室4,24内の湿度を
夫々検出し、その湿度が設定値以下であるときは、乾燥
室4,24に夫々配備する加湿器10.30を作動させ
加湿し、湿度を設定値に維持しつつほぼ密閉式の乾燥室
4,24で生成される加温、恒湿空気を循環供給して、
乾燥室4,24が過うな過乾燥は前述の如く、乾燥機/
の始動時、停止時に発生しやすい。また逆にその湿度が
設定値以上であるときは、湿度センサー5,25を作動
してファン7.27を駆動し、シャッターを回動して吸
、排気口9 、29 、8 、28を開いて乾燥室4,
24を開放し、ファン7.27を介して乾燥室4,24
内の多湿空気を排気口8.28を介して排出しつつ、吸
気口9,29よシ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しつつほぼ密閉式の乾燥室4゜24
で生成される加温、恒湿空気を循環供給して、乾燥室4
,24が多湿乾燥状態となることを個別に制御する。こ
のような多湿空気は、主として本発明が密閉式の乾燥機
2であることから、乾燥の中間過程で発生しやすい。以
上詳述の如く、乾燥室4,24に夫々配備する燃焼炉2
.22、ファン3t23,7,27、湿度センサー5,
25、加湿器10.30はそれぞれの状況忙対応して区
々に作動等する。図中11゜31はスイッチである。4
0,50は乾燥室4゜24に配備した温度センサーで、
この温度センサー40.50が加温空気等を検出し、そ
の温度が設定値以上(通常高温空気)であるときは、燃
焼炉2,22のバーナーを切るようKL、その加温空気
を設定値に維持しつつ、この加温空気を恒湿空気ととも
に循環供給する0そして本発明では密閉式の乾燥機よと
なっていることから、乾燥の中間及び最終過程で発生し
やすいと思われるので、この弊害をも防止できるもので
ある。尚本発明の使用状態は、前述の作用で詳述したの
でその説明は省略します。
Embodiment J The drawing shows an embodiment of the present invention. Reference numeral 6 is a closed type dryer, and this dryer 6 has an intermediate bed 20 and is divided into an upper drying chamber 4 and a lower drying chamber 24. The drying chambers 4 and 24 have air intake ports 9 that are opened and closed by shutters.
29 and exhaust ports 8, 28 are provided, respectively, and combustion furnaces 2, 22 and fans 3, 23 are provided, respectively. The hot air generated in the combustion furnaces 2, 22 is circulated in the drying chamber 4.24 by the rotation of the 7-angs 3, 23. 5
, 25 are humidity sensors installed in each of the drying chambers 4° and 24.
The humidity sensors 5 and 25 detect the humidity in the drying chambers 4 and 24, respectively, and when the humidity is below a set value, the humidifiers 10 and 30 installed in the drying chambers 4 and 24 are activated to humidify the chambers. , while maintaining the humidity at a set value, circulating and supplying heated, constant humidity air generated in the nearly closed drying chambers 4 and 24,
Over-drying in the drying chambers 4 and 24 can be caused by drying in the dryer/
This tends to occur when starting or stopping the machine. Conversely, when the humidity is above the set value, the humidity sensors 5 and 25 are activated to drive the fans 7 and 27, and the shutters are rotated to open the intake and exhaust ports 9, 29, 8, and 28. drying room 4,
24 is opened, and the drying chambers 4, 24 are opened via the fan 7.27.
While exhausting the humid air inside through the exhaust ports 8 and 28, outside air or air inside the factory is introduced through the intake ports 9 and 29, and the humidity is maintained at the set value while the drying room 4 is almost closed.゜24
Drying room 4
, 24 are individually controlled to be in a humid or dry state. Such humid air is likely to be generated during the intermediate process of drying, mainly because the present invention is a closed type dryer 2. As detailed above, the combustion furnaces 2 are installed in the drying chambers 4 and 24, respectively.
.. 22, fan 3t23, 7, 27, humidity sensor 5,
25. The humidifiers 10 and 30 operate differently depending on the situation. In the figure, 11°31 is a switch. 4
0.50 is a temperature sensor installed in the drying room 4°24.
This temperature sensor 40.50 detects heated air, etc., and when the temperature is higher than the set value (normally high temperature air), the KL turns off the burners of the combustion furnaces 2 and 22, and the heated air is heated to the set value. This heated air is circulated and supplied together with constant humidity air while maintaining the same humidity.Since the present invention uses a closed type dryer, it is thought that this is likely to occur during the intermediate and final stages of drying. This problem can also be prevented. The state of use of the present invention has been explained in detail in the above-mentioned operation, so its explanation will be omitted.

「発明の効果」 本発明は以上詳述したように、密閉式の乾燥機を上側と
下側の乾燥室に区画し、この夫々の乾燥室にシャッター
で開閉する吸気口及び排気口を設けると共に、この夫々
の乾燥室に湿度センサーを設け、この湿度センサーの検
出値忙基づいて加湿器若しくはファンを介して乾燥室内
の湿度をほぼ設定値に維持して乾燥する方法であるので
、加温、恒湿空気による乾燥ができ、過乾燥、多湿乾燥
を回避できる効果があると共よ多発生するといわれる色
ムラがなくなる等良質な、保存のきく乾海苔ができる0
また本発明は、乾燥機を二つの乾燥室に区画し、かつほ
ぼ密閉式の乾燥室で区々に湿度管理をするものである故
、よシ適確な湿度管理ができるし、生海苔、気象条件等
の各々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。更に十分なる加湿状態における乾燥であるので
、清めらかで、艶のある、柔らかい乾海苔を能率よく製
造できる。更にまた加温、恒湿乾燥であるので、過乾燥
に起因する破れ、ワレとか、乾燥不足によるチヂミ、部
分的なヌレ等を防止でき、良質な乾海苔が製造できる。
"Effects of the Invention" As detailed above, the present invention divides a closed dryer into upper and lower drying chambers, and each drying chamber is provided with an intake port and an exhaust port that are opened and closed by shutters. A humidity sensor is installed in each of these drying chambers, and based on the detected value of this humidity sensor, the humidity in the drying chamber is maintained at approximately the set value via a humidifier or fan. Drying can be done using constant humidity air, which has the effect of avoiding over-drying and drying due to high humidity, and also eliminates the color unevenness that often occurs, producing dried seaweed that is of high quality and has a long shelf life.
Furthermore, in the present invention, the dryer is divided into two drying chambers, and the humidity is controlled separately in each of the nearly closed drying chambers. It is possible to create an optimal humidity environment corresponding to each situation such as weather conditions. Furthermore, since drying is carried out in a sufficiently humidified state, smooth, glossy, and soft dried seaweed can be efficiently produced. Furthermore, since drying is carried out at a constant temperature and humidity, it is possible to prevent tearing and cracking caused by over-drying, as well as stiffness and partial wetting caused by insufficient drying, thereby producing high-quality dried seaweed.

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

図面は本発明の方法に使用する装置の一例を示し、第1
図は説明図、s2図は従来法の温、湿度経過状態を示す
図表、第3図は本発明方法の温、湿度経過状態を示す図
表、第4図は乾燥機内の乾燥区間を示す模式図、第5図
は従来の乾燥機の一例を示す説明図である0 1.21・・・海苔簀、2,22・・・燃焼炉、3゜2
3・・・ファン、4,24・・・乾燥室、5,25・・
・湿度センサー、6・・・乾燥機、7,27・・・ファ
ン、8.28・・・排気口、9,29・・・吸気口、1
0.30・・・加湿器、11.31・・・スイッチ、2
0・・・中間床、40.50・・・温度センサー特許出
願人   フルタ電機株式会社 キJ IN
The drawing shows an example of the apparatus used in the method of the present invention.
The figure is an explanatory diagram. Figure s2 is a chart showing the temperature and humidity progress of the conventional method. Figure 3 is a chart showing the temperature and humidity progress of the method of the present invention. Figure 4 is a schematic diagram showing the drying section in the dryer. , Fig. 5 is an explanatory diagram showing an example of a conventional dryer.
3...Fan, 4,24...Drying room, 5,25...
・Humidity sensor, 6... Dryer, 7, 27... Fan, 8.28... Exhaust port, 9, 29... Intake port, 1
0.30... Humidifier, 11.31... Switch, 2
0...Intermediate floor, 40.50...Temperature sensor patent applicant Furuta Electric Co., Ltd. KiJ IN

Claims (2)

【特許請求の範囲】[Claims] (1)密閉式の乾燥機を中間床をもつて上側乾燥室と下
側乾燥室とに区画し、夫々の乾燥室にシャッターで開閉
する吸気口及び排気口を設け、かつこの吸気口又は排気
口にファンを配備し、前記夫々の乾燥室に設けた湿度セ
ンサーで、この室内湿度を区々に検出し、その湿度が設
定値であるときは、前記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、乾
燥室の加湿器を作動させ湿度を設定値に維持し、またそ
の湿度が設定値以上であるときは、乾燥室を開放して多
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、この乾燥室で生成される加温、
恒湿空気を循環して生海苔の乾燥を夫々の乾燥室で個別
に制御するようにした海苔の乾燥方法。
(1) A closed type dryer is divided into an upper drying chamber and a lower drying chamber with an intermediate floor, and each drying chamber is provided with an intake port and an exhaust port that can be opened and closed with a shutter, and the intake port or exhaust port is A fan is installed at the mouth, and a humidity sensor installed in each of the drying chambers detects the indoor humidity separately, and when the humidity is at the set value, the heating and constant temperature generated in the drying chamber is detected. Humid air is circulated, and when the humidity is below the set value, the humidifier in the drying room is operated to maintain the humidity at the set value, and when the humidity is above the set value, the drying room is opened. The humidity generated in this drying room is
A method of drying seaweed in which drying of fresh seaweed is controlled individually in each drying room by circulating constant humidity air.
(2)密閉式の乾燥機を中間床をもつて上側乾燥室と下
側乾燥室とに区画し、夫々の乾燥室にシャッターで開閉
する吸気口及び排気口を設け、かつこの吸気口又は排気
口にファンを配備し、前記夫々の乾燥室に設けた湿度セ
ンサーで、この室内湿度を区々に検出し、その湿度が設
定値であるときは、前記乾燥室で生成される加湿、恒湿
空気を循環し、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湿度を設定値に維持し、またそ
の湿度が設定値以上であるときは、乾燥室を開放して多
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、この乾燥室で生成される加温、
恒湿空気を循環して生海苔の乾燥を夫々の乾燥室で個別
に制御しつつ、前記加温空気が設定値以上となつたとき
は、燃焼炉のバーナーを切るようにした海苔の乾燥方法
(2) A closed type dryer is divided into an upper drying chamber and a lower drying chamber with an intermediate floor, and each drying chamber is provided with an intake port and an exhaust port that can be opened and closed with a shutter, and the intake port or exhaust port is A fan is installed at the mouth, and a humidity sensor installed in each of the drying chambers detects the indoor humidity separately, and when the humidity is at the set value, the humidification and constant humidity generated in the drying chamber are detected. When the air is circulated and the humidity is below the set value, the humidifier in the drying room is operated to maintain the humidity at the set value, and when the humidity is above the set value, the drying room is opened. While exhausting humid air, outside air or factory air is introduced to maintain the humidity at the set value, and the heating generated in this drying room is
A method of drying seaweed in which the drying of fresh seaweed is controlled individually in each drying room by circulating constant humidity air, and the burner of the combustion furnace is turned off when the heated air exceeds a set value. .
JP60092047A 1985-04-27 1985-04-27 Drying of laver Granted JPS61249368A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60092047A JPS61249368A (en) 1985-04-27 1985-04-27 Drying of laver

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60092047A JPS61249368A (en) 1985-04-27 1985-04-27 Drying of laver

Publications (2)

Publication Number Publication Date
JPS61249368A true JPS61249368A (en) 1986-11-06
JPS635060B2 JPS635060B2 (en) 1988-02-02

Family

ID=14043601

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60092047A Granted JPS61249368A (en) 1985-04-27 1985-04-27 Drying of laver

Country Status (1)

Country Link
JP (1) JPS61249368A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0223852A (en) * 1988-07-13 1990-01-26 Furuta Denki Kk Humidity control of laver drying machine
JPH02247486A (en) * 1989-03-20 1990-10-03 Hisaka Works Ltd Moisture conditioning device in high pressure hot air drier
JPH03133366A (en) * 1989-10-19 1991-06-06 Ootsubo Tekko:Kk Laver dryer
JP2018011543A (en) * 2016-07-20 2018-01-25 千葉県 Method for producing dried laver

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5753196A (en) * 1980-09-16 1982-03-30 Sony Corp Acoustic diaphragm
JPS5756872A (en) * 1980-09-24 1982-04-05 Ricoh Co Ltd Transfer separating method of electrophotography copying machine
JPS5948630A (en) * 1982-09-13 1984-03-19 Shimadzu Corp Leak detector

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5753196A (en) * 1980-09-16 1982-03-30 Sony Corp Acoustic diaphragm
JPS5756872A (en) * 1980-09-24 1982-04-05 Ricoh Co Ltd Transfer separating method of electrophotography copying machine
JPS5948630A (en) * 1982-09-13 1984-03-19 Shimadzu Corp Leak detector

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0223852A (en) * 1988-07-13 1990-01-26 Furuta Denki Kk Humidity control of laver drying machine
JPH02247486A (en) * 1989-03-20 1990-10-03 Hisaka Works Ltd Moisture conditioning device in high pressure hot air drier
JPH0737879B2 (en) * 1989-03-20 1995-04-26 株式会社日阪製作所 Humidity control device for high pressure hot air dryer
JPH03133366A (en) * 1989-10-19 1991-06-06 Ootsubo Tekko:Kk Laver dryer
JP2018011543A (en) * 2016-07-20 2018-01-25 千葉県 Method for producing dried laver

Also Published As

Publication number Publication date
JPS635060B2 (en) 1988-02-02

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