JP2020048471A - System for producing laver - Google Patents

System for producing laver Download PDF

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JP2020048471A
JP2020048471A JP2018180512A JP2018180512A JP2020048471A JP 2020048471 A JP2020048471 A JP 2020048471A JP 2018180512 A JP2018180512 A JP 2018180512A JP 2018180512 A JP2018180512 A JP 2018180512A JP 2020048471 A JP2020048471 A JP 2020048471A
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laver
operation state
output
heater
building
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JP6713692B2 (en
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吉田 直人
Naoto Yoshida
直人 吉田
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Itsuwa Kogyo Co Ltd
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Abstract

To provide a system for producing laver, capable of uniformly drying well a laver dough and preventing dried laver from causing shrinkage and unevenness.SOLUTION: In a system (S) for producing laver including a drying chamber (12) installed inside a building (2) to dry a spread laver dough by heated air while conveying it along a conveying path, a heater (13) for feeding the heated air to the drying chamber (12), and a heating device (16) for heating air outside the building (2) and feeding it to the heater (13), the heating device (16) is controlled so as to be gradually raised in an output in a state (initial operation state) where the laver dough is present only at an upstream side of the conveying path inside the drying chamber (12), then maximized in the output in a state (normal operation state) where the laver dough is present all over the conveying path inside the drying chamber (12), and then gradually lowered in the output in a state (final operation state) where the laver dough is present only at a downstream side of the conveying path inside the drying chamber (12).SELECTED DRAWING: Figure 4

Description

本発明は、抄製した海苔生地を乾燥させて乾燥海苔を製造するための海苔製造システムの制御に関するものである。   TECHNICAL FIELD The present invention relates to control of a laver production system for producing a dried laver by drying paper laver dough.

従来より、食用に供される乾燥海苔は、水分を多く含んだ海苔生地を矩形シート状に乾燥させることによって製造されている。この乾燥海苔の製造には、建屋の内部に設置された海苔製造機と建屋の外部に設置された加温機とからなる海苔製造システムが広く用いられている。   2. Description of the Related Art Conventionally, edible dried laver has been manufactured by drying laver dough containing a large amount of water into a rectangular sheet shape. For the production of this dried laver, a laver production system including a laver production machine installed inside a building and a heating machine installed outside the building is widely used.

この海苔製造システムでは、建屋の内部に設置され、抄製した海苔生地を搬送経路に沿って搬送しながら加熱空気で乾燥させる乾燥室と、乾燥室に加熱空気を供給する加熱機と、加熱機に建屋の外部の空気を加温して供給する加温機とを有する構成となっている(たとえば、特許文献1参照。)。   In this laver production system, a drying chamber installed inside the building and drying the dried laver dough with heated air while transporting it along a transport path, a heating machine for supplying heated air to the drying chamber, and a heating machine And a heater for heating and supplying air outside the building (for example, see Patent Document 1).

そして、従来の海苔製造システムでは、海苔生地の抄製を開始した後に、加温機の稼働を開始して、加温機を一定の出力で稼働させ、海苔生地の抄製が終了した後に、加温機の稼働を停止させている。   And, in the conventional laver production system, after starting the lamination of the laver dough, the operation of the heating machine is started, the heating machine is operated at a constant output, and after the lamination of the laver dough is completed, The operation of the heater has been stopped.

特開2017−127198号公報JP-A-2017-127198

ところが、上記従来の海苔製造システムでは、海苔生地の抄製を開始した後に一気に一定の出力で加温機を稼働させることで、乾燥室の内部の気温や湿度などの状態が急激に変化してしまい、海苔生地の乾燥不良が生じて乾燥海苔の縮みやムラなどが発生して乾燥海苔の商品価値を損ねるおそれがあった。   However, in the above-mentioned conventional laver production system, the state of the temperature and humidity inside the drying chamber is rapidly changed by operating the heating machine at a constant output at a stretch after starting the production of the laver dough. As a result, there is a possibility that the dried seaweed dough may be poorly dried and shrinkage or unevenness of the dried seaweed may occur, thereby impairing the commercial value of the dried seaweed.

また、上記従来の海苔製造システムでは、気象状況によって外気の気温や湿度などが変化するために、加温機を一定の出力で稼働させると外気の気温や湿度などの変化によって乾燥室の内部の気温や湿度などの状態まで変化してしまい、これによっても、海苔生地の乾燥不良が生じて乾燥海苔の縮みやムラなどが発生して乾燥海苔の商品価値を損ねるおそれがあった。   In addition, in the above-mentioned conventional laver production system, since the temperature and humidity of the outside air change depending on the weather condition, when the heating device is operated at a constant output, the inside of the drying chamber is changed due to the change in the temperature and humidity of the outside air. The state changes to the temperature and humidity, etc., which may cause poor drying of the nori dough, resulting in shrinkage or unevenness of the dried nori, thereby impairing the commercial value of the dried nori.

さらに、上記従来の海苔製造システムでは、海苔生地の抄製を終了した後に一気に加温機を停止させることによっても、乾燥室の内部の気温や湿度などの状態が急激に変化してしまい、海苔生地の乾燥不良が生じて乾燥海苔の縮みやムラなどが発生して乾燥海苔の商品価値を損ねるおそれがあった。   Furthermore, in the above-mentioned conventional laver production system, even when the heating machine is stopped at a stretch after finishing the laver dough-making, the state such as the temperature and humidity inside the drying chamber suddenly changes, and Poor drying of the dough may cause shrinkage or unevenness of the dried laver, which may impair the commercial value of the dried laver.

そこで、請求項1に係る本発明では、建屋の内部に設置され、抄製した海苔生地を搬送経路に沿って搬送しながら加熱空気で乾燥させる乾燥室と、乾燥室に加熱空気を供給する加熱機と、加熱機に建屋の外部の空気を加温して供給する加温機とを有する海苔製造システムにおいて、乾燥室の内部の搬送経路の上流側だけに海苔生地が存在している状態(初期運転状態)では、加温機の出力を徐々に上昇させ、その後、乾燥室の内部の搬送経路の全てに海苔生地が存在している状態(通常運転状態)では、加温機の出力を最大とし、その後、乾燥室の内部の搬送経路の下流側だけに海苔生地が存在している状態(終期運転状態)では、加温機の出力を徐々に下降させるように制御することにした。   Therefore, in the present invention according to claim 1, a drying chamber that is installed inside a building and that dries the dried laver dough with heated air while being transported along the transport path, and a heating chamber that supplies heated air to the drying chamber. Nori production system that has a heating device and a heating device that heats and supplies air outside the building to the heating device, in a state where the nori dough exists only on the upstream side of the transport path inside the drying chamber ( In the initial operation state), the output of the heater is gradually increased, and then, in a state where the laver dough is present in all of the transport paths inside the drying chamber (normal operation state), the output of the heater is increased. Then, in a state where the laver material is present only on the downstream side of the transport path inside the drying chamber (final operation state), the output of the heater is controlled to be gradually lowered.

また、請求項2に係る本発明では、前記請求項1に係る本発明において、前記通常運転状態における加温機の出力の最大値を、前記初期運転状態における建屋の外部の気温に応じて変更し、変更後の最大値となるように前記初期運転状態で加温機の出力を徐々に上昇させるように制御することにした。   In the invention according to claim 2, in the invention according to claim 1, the maximum value of the output of the heater in the normal operation state is changed according to the outside temperature of the building in the initial operation state. Then, control is performed so that the output of the heater is gradually increased in the initial operation state so as to become the maximum value after the change.

また、請求項3に係る本発明では、前記請求項1又は請求項2に係る本発明において、前記通常運転状態における加温機の出力の最大値を、前記通常運転状態における建屋の外部の気温に応じて変更し、変更後の最大値となるように前記終期運転状態で加温機の出力を徐々に下降させるように制御することにした。   Further, in the present invention according to claim 3, in the present invention according to claim 1 or 2, the maximum value of the output of the heater in the normal operation state is determined by the temperature outside the building in the normal operation state. , And control is performed such that the output of the heater is gradually decreased in the final operation state so as to have the maximum value after the change.

そして、本発明では、以下に記載する効果を奏する。   The present invention has the following effects.

すなわち、本発明では、建屋の内部に設置され、抄製した海苔生地を搬送経路に沿って搬送しながら加熱空気で乾燥させる乾燥室と、乾燥室に加熱空気を供給する加熱機と、加熱機に建屋の外部の空気を加温して供給する加温機とを有する海苔製造システムにおいて、乾燥室の内部の搬送経路の上流側だけに海苔生地が存在している状態(初期運転状態)では、加温機の出力を徐々に上昇させ、その後、乾燥室の内部の搬送経路の全てに海苔生地が存在している状態(通常運転状態)では、加温機の出力を最大とし、その後、乾燥室の内部の搬送経路の下流側だけに海苔生地が存在している状態(終期運転状態)では、加温機の出力を徐々に下降させるように制御することにしているために、初期運転状態から終期運転状態まで乾燥室の内部の状態が急激に変化するのを抑制することができるので、海苔生地を良好に均一に乾燥させることができ、乾燥海苔の縮みやムラなどの発生を防止することができる。   That is, in the present invention, a drying chamber installed inside a building and drying the heated laver dough with heated air while transporting the dried laver dough along a transport path, a heating machine for supplying heated air to the drying chamber, and a heating machine Nori production system having a heating device for heating and supplying the air outside the building to the seaweed in a state where the seaweed dough exists only on the upstream side of the transport path inside the drying chamber (initial operation state) Then, gradually increase the output of the heating device, and then, in a state where the seaweed dough is present in all of the transport paths inside the drying chamber (normal operation state), maximize the output of the heating device, In the state where the laver material is present only on the downstream side of the transport path inside the drying chamber (final operation state), the output of the heating machine is controlled to gradually decrease, so the initial operation Inside the drying room from the state to the final operation state Because the state can be inhibited from changing rapidly, can be satisfactorily homogeneously dry seaweed dough, the occurrence of dry seaweed shrinkage or unevenness can be prevented.

特に、前記通常運転状態における加温機の出力の最大値を、前記初期運転状態における建屋の外部の気温に応じて変更し、変更後の最大値となるように前記初期運転状態で加温機の出力を徐々に上昇させるように制御することにした場合には、初期運転状態の途中で建屋の外部の気温に変化が生じても乾燥室の内部の状態が急激に変化するのを抑制することができるので、海苔生地を良好に均一に乾燥させることができ、乾燥海苔の縮みやムラなどの発生を防止することができる。   In particular, the maximum value of the output of the heater in the normal operation state is changed in accordance with the temperature outside the building in the initial operation state, and the heater in the initial operation state is changed to the changed maximum value. If the output is controlled so as to gradually increase, even if the temperature outside the building changes in the middle of the initial operation state, the state inside the drying chamber is prevented from changing rapidly. Therefore, the laver material can be dried uniformly and satisfactorily, and shrinkage and unevenness of the dried laver can be prevented.

また、前記通常運転状態における加温機の出力の最大値を、前記通常運転状態における建屋の外部の気温に応じて変更し、変更後の最大値となるように前記終期運転状態で加温機の出力を徐々に下降させるように制御することにした場合には、通常運転状態の途中で建屋の外部の気温に変化が生じても乾燥室の内部の状態が急激に変化するのを抑制することができるので、海苔生地を良好に均一に乾燥させることができ、乾燥海苔の縮みやムラなどの発生を防止することができる。   Further, the maximum value of the output of the heater in the normal operation state is changed in accordance with the outside temperature of the building in the normal operation state, and the heater in the final operation state is changed to the changed maximum value. If the output is controlled so as to gradually decrease, even if the temperature outside the building changes during the normal operation state, it is possible to suppress a sudden change in the state inside the drying chamber. Therefore, the laver material can be dried uniformly and satisfactorily, and shrinkage and unevenness of the dried laver can be prevented.

海苔製造システムを示す説明図。Explanatory drawing which shows a laver manufacturing system. 海苔製造機を示す説明図。Explanatory drawing which shows a laver manufacturing machine. 加温機の出力を示す説明図。Explanatory drawing which shows the output of a heater. 加温機の出力を示す説明図。Explanatory drawing which shows the output of a heater.

以下に、本発明に係る海苔製造システムの具体的な構成について図面を参照しながら説明する。   Hereinafter, a specific configuration of the laver production system according to the present invention will be described with reference to the drawings.

図1に示すように、海苔製造システムSでは、海苔製造機1が建屋2の内部に設置されており、海苔製造機1によって海苔生地を乾燥させることで矩形シート状の乾燥海苔を製造するものである。   As shown in FIG. 1, in the laver production system S, a laver production machine 1 is installed inside a building 2, and the laver fabric is dried by the laver production machine 1 to produce a rectangular sheet-shaped dried laver. It is.

海苔製造機1は、図1及び図2に示すように、海苔生地の抄製を行う抄製装置3と海苔生地の乾燥を行う乾燥装置4とを前後に連設した構成となっている。   As shown in FIGS. 1 and 2, the laver production machine 1 has a configuration in which a papermaking device 3 for producing laver dough and a drying device 4 for drying the laver dough are connected in front and back.

抄製装置3は、複数枚の海苔簀5を並設した簀枠6を搬送するための無端状の搬送機構7を内蔵しており、搬送機構7の搬送経路に沿って、海苔簀5に海苔生地を抄くための抄き機構8と、吸引によって海苔生地の脱水を行うための吸引脱水機構9と、スポンジの押圧によって海苔生地の脱水を行う押圧脱水機構10と、海苔簀5から乾燥海苔を剥離するための剥離機構11とを順に配置している。   The papermaking apparatus 3 incorporates an endless transport mechanism 7 for transporting a cage frame 6 in which a plurality of laver cages 5 are arranged side by side. A laminating mechanism 8 for laminating laver dough, a suction dehydrating mechanism 9 for dehydrating laver dough by suction, a press dewatering mechanism 10 for dehydrating laver dough by pressing a sponge, and drying from laver cage 5 A peeling mechanism 11 for peeling the laver is arranged in order.

そして、抄製装置3は、搬送機構7で簀枠6ごと海苔簀5を搬送しながら、抄き機構8で海苔簀5に海苔生地を抄製し、吸引脱水機構9と押圧脱水機構10とで海苔生地の脱水を行い、その後、乾燥装置4に簀枠6ごと受け渡すとともに、乾燥装置4で乾燥した後の簀枠6を再び受け取り、剥離機構11で海苔簀5から乾燥海苔を剥離するように構成している。   Then, the papermaking apparatus 3 forms the laver material on the laver cage 5 with the papermaking mechanism 8 while transporting the laver cage 5 together with the cage frame 6 by the transport mechanism 7, and the suction dehydration mechanism 9, the press dehydration mechanism 10, and the like. The dehydration of the laver material is carried out, and then the cage frame 6 is transferred to the drying device 4 and the cage frame 6 after being dried by the drying device 4 is received again. The peeling mechanism 11 peels the dried laver from the laver cage 5. It is configured as follows.

乾燥装置4は、前後方向に伸延させた矩形箱型状の乾燥室12の右側部に前後方向に伸延させた矩形箱型状の加熱機13を並設している。   The drying device 4 is provided with a rectangular box-shaped heater 13 extending in the front-rear direction on the right side of a rectangular box-shaped drying chamber 12 extending in the front-rear direction.

乾燥室12の内部には、簀枠6を搬送するための搬送機構14,15が上下に収容されている。簀枠6(海苔生地)は、上側の搬送機構14の上側前端部で抄製装置3の搬送機構7の上側後端部から受け渡され、上側の搬送機構14の上側前端部から上側後端部に搬送された後に下側後端部から下側前端部に搬送され、上側の搬送機構14から下側の搬送機構15に受け渡され、下側の搬送機構15の上側前端部から上側後端部に搬送された後に下側後端部から下側前端部に搬送され、再び、抄製装置3の搬送機構7の下側後端部に受け渡される。これにより、乾燥室12の内部に簀枠6(海苔生地)の搬送経路(乾燥室12の内部を簀枠6(海苔生地)が2往復する経路)が形成される。   Inside the drying chamber 12, transport mechanisms 14, 15 for transporting the gantry 6 are housed vertically. The pouring frame 6 (seaweed dough) is delivered from the upper rear end of the transport mechanism 7 of the papermaking apparatus 3 at the upper front end of the upper transport mechanism 14 and is moved from the upper front end to the upper rear end of the upper transport mechanism 14. Transported from the lower rear end to the lower front end, transferred from the upper transport mechanism 14 to the lower transport mechanism 15, and moved from the upper front end of the lower transport mechanism 15 to the upper rear end. After being conveyed to the end, it is conveyed from the lower rear end to the lower front end, and is again delivered to the lower rear end of the conveying mechanism 7 of the papermaking apparatus 3. As a result, a transport path for the pens 6 (seaweed dough) is formed inside the drying chamber 12 (a path through which the pens 6 (seaweed dough) reciprocates two times inside the drying chamber 12).

加熱機13には、建屋2の外部(屋外)の空気(外気)を加熱して供給するための加温機16が設けられている。加温機16は、建屋2の外部に本体が設置され、本体で加熱した外気をダクトから加熱機13に供給する。これにより、加熱機13は、建屋2の内部(屋内)の空気(内気)と加温機16で加熱した外気とを加熱して乾燥室12に供給する。   The heater 13 is provided with a heater 16 for heating and supplying air (outside air) outside (outdoor) of the building 2. The heater 16 has a main body installed outside the building 2 and supplies outside air heated by the main body to the heater 13 from a duct. Thereby, the heater 13 heats the air (inside air) inside (indoor) of the building 2 and the outside air heated by the heater 16 and supplies the air to the drying chamber 12.

そして、乾燥装置4は、乾燥室12の内部において搬送機構14,15で簀枠6ごと海苔簀5を2往復搬送し、その間に、加熱機13から供給された加熱空気を用いて海苔簀5に抄製された海苔生地を乾燥させるようにしている。   The drying device 4 transports the sea laver 5 together with the cage frame 2 in the drying chamber 12 two times by the transport mechanisms 14 and 15, and uses the heated air supplied from the heating device 13 during this time. The dried seaweed dough is dried.

上記海苔製造システムSでは、制御装置17が設けられており、制御装置17で各部を制御している。この制御装置17には、外気や内気の温度や湿度を検出するセンサ18,19が接続されている。   In the laver production system S, a control device 17 is provided, and the control device 17 controls each unit. Sensors 18 and 19 for detecting the temperature and humidity of outside air and inside air are connected to the control device 17.

制御装置17によって海苔製造機1の運転を開始すると、抄き機構8で海苔簀5に抄製された海苔生地が脱水後に乾燥室12の内部に順に受け渡され、乾燥室12の内部の搬送経路に沿って搬送された後に、剥離機構11に受け渡される。   When the operation of the laver production machine 1 is started by the control device 17, the laver dough produced in the laver cage 5 by the laminating mechanism 8 is sequentially transferred to the inside of the drying chamber 12 after dehydration, and transported inside the drying chamber 12. After being transported along the path, it is transferred to the peeling mechanism 11.

そのため、海苔製造機1の運転開始直後(抄製装置3による抄製開始から所定時間経過以降)には、乾燥室12の内部の搬送経路の上流側だけに海苔生地が存在している状態(初期運転状態)となっており、その後、乾燥室12の内部の搬送経路の全てに海苔生地が存在している状態(通常運転状態)となり、海苔製造機1の運転終了間際(抄製装置3による抄製終了から所定時間経過以降)には、乾燥室12の内部の搬送経路の下流側だけに海苔生地が存在している状態(終期運転状態)となる。通常運転状態では、初期運転状態や終期運転状態よりも海苔生地の量が多く、乾燥室12の内部の水分量が多くなる。また、初期運転状態では、海苔生地が全く搬送されていない部分が存在するために終期運転状態よりも乾燥室12の内部の水分量が少なくなる。   Therefore, immediately after the start of the operation of the laver production machine 1 (after a lapse of a predetermined time from the start of the papermaking by the papermaking apparatus 3), the laver dough is present only on the upstream side of the transport path inside the drying chamber 12 ( (The initial operation state), and after that, the laver dough is present in all the transport routes inside the drying chamber 12 (normal operation state), and immediately before the end of the operation of the laver manufacturing machine 1 (the papermaking apparatus 3). (After a lapse of a predetermined time from the end of the papermaking by the above), the laver dough is present only on the downstream side of the transport path inside the drying chamber 12 (final operation state). In the normal operation state, the amount of the nori dough is larger than in the initial operation state or the final operation state, and the amount of water inside the drying chamber 12 is larger. Further, in the initial operation state, the moisture content in the drying chamber 12 is smaller than in the final operation state because there is a portion where nori dough is not transported at all.

海苔製造システムSでは、制御装置17が、海苔製造機1の運転開始後に、加温機16を駆動制御する。その際に、制御装置17は、図3に示すように、初期運転状態では、加温機16の出力を徐々に上昇させ、その後、通常運転状態では、加温機16の出力を最大とし、その後、終期運転状態では、加温機16の出力を徐々に下降させるように制御する。   In the laver production system S, the control device 17 drives and controls the heating device 16 after the operation of the laver production machine 1 starts. At that time, as shown in FIG. 3, the control device 17 gradually increases the output of the heater 16 in the initial operation state, and thereafter, maximizes the output of the heater 16 in the normal operation state, Thereafter, in the final operation state, the output of the heater 16 is controlled to gradually decrease.

そして、図4に示すように、通常運転状態における加温機16の出力の最大値は、初期運転状態前に予めセンサ18で検出した建屋2の外部の気温に基づいて決定しておき、初期運転状態における建屋2の外部の気温が変化した場合にはそれに応じて最大値を変更し、変更後の最大値となるように初期運転状態で加温機16の出力を徐々に上昇させるように制御する。また、通常運転状態における加温機16の出力の最大値も、通常運転状態における建屋2の外部の気温が変化した場合にはそれに応じて最大値を変更し、変更後の最大値となるように終期運転状態で加温機16の出力を徐々に下降させるように制御する。   Then, as shown in FIG. 4, the maximum value of the output of the heater 16 in the normal operation state is determined based on the outside temperature of the building 2 detected by the sensor 18 in advance before the initial operation state. When the outside temperature of the building 2 changes in the operating state, the maximum value is changed accordingly, and the output of the heater 16 is gradually increased in the initial operating state so as to become the changed maximum value. Control. In addition, the maximum value of the output of the heater 16 in the normal operation state is also changed in accordance with the change in the temperature outside the building 2 in the normal operation state, and becomes the maximum value after the change. In the final operation state, the output of the heater 16 is controlled to gradually decrease.

たとえば、図3に示すように、制御装置17は、時刻T0から抄製装置3による抄製を開始し、その時点で予めセンサ18,19で建屋2の内外の気温及び湿度を検出し、その気温及び湿度に基づいて加温機16の出力の最大値M1を決定する。そして、制御装置17は、初期運転状態となった時刻T1に加温機16の駆動を開始する。その際に、制御装置17は、初期運転状態となった時刻T1での加温機16の出力を0とし、初期運転状態から通常運転状態にかわる時刻T2での加温機16の出力が最大値M1となるように加温機16の出力を徐々に上昇させる。その後、制御装置17は、通常運転状態において、加温機16の出力を最大値M1となるように維持し、抄製装置3による抄製を終了した時刻T3から所定時間が経過して終期運転状態となった時刻T4から加温機16の出力を徐々に下降させ、終期運転状態が終了する時刻T5での加温機16の出力が0となるように加温機16の駆動を停止する。   For example, as shown in FIG. 3, the control device 17 starts the papermaking by the papermaking device 3 from time T0, and at that time, the temperature and humidity inside and outside the building 2 are detected by the sensors 18 and 19 in advance. The maximum value M1 of the output of the heater 16 is determined based on the temperature and the humidity. Then, the control device 17 starts driving the heater 16 at time T1 at which the initial operation state is set. At that time, the control device 17 sets the output of the heater 16 at time T1 at which the initial operation state was set to 0, and the output of the heater 16 at time T2 at which the initial operation state changes to the normal operation state is the maximum. The output of the heater 16 is gradually increased so as to be the value M1. Thereafter, in the normal operation state, the control device 17 maintains the output of the heating device 16 at the maximum value M1, and performs the final operation after a predetermined time has elapsed from the time T3 when the papermaking by the papermaking device 3 was completed. The output of the heater 16 is gradually lowered from the time T4 when the state is changed, and the driving of the heater 16 is stopped so that the output of the heater 16 at the time T5 when the terminal operation state ends is 0. .

制御装置17は、センサ18,19で検出した建屋2の内外の気温及び湿度並びに内外差(内部の気温や湿度と外部の気温や湿度との差)が所定の範囲内で変動する場合には、上述した制御を行うが、センサ18,19で検出した建屋2の内外の気温及び湿度並びに内外差が所定の範囲を超えて変動する場合には、以下のような制御を行う。   When the temperature and humidity inside and outside the building 2 detected by the sensors 18 and 19 and the difference between inside and outside (the difference between the inside temperature and humidity and the outside temperature and humidity) detected by the sensors 18 and 19 fluctuate within a predetermined range, The above-described control is performed. When the temperature and humidity inside and outside the building 2 and the difference between the inside and outside of the building 2 detected by the sensors 18 and 19 fluctuate beyond a predetermined range, the following control is performed.

たとえば、制御装置17は、初期運転状態中の時刻T6においてセンサ18,19で検出した建屋2の内外の気温及び湿度並びに内外差が所定の範囲を超えて変動した場合、その気温及び湿度に基づいて改めて加温機16の出力の最大値M2を決定し直し、そこから、通常運転状態にかわる時刻T2での加温機16の出力が最大値M2となるように加温機16の出力を徐々に上昇させ、通常運転状態において加温機16の出力が最大値M2となるように維持する。   For example, when the temperature and humidity inside and outside the building 2 and the difference between inside and outside of the building 2 detected by the sensors 18 and 19 at time T6 during the initial operation state fluctuate beyond a predetermined range, the control device 17 Once again, the maximum value M2 of the output of the heater 16 is determined again, and from there, the output of the heater 16 is adjusted so that the output of the heater 16 at the time T2 when the normal operation state is changed becomes the maximum value M2. The temperature is gradually increased to maintain the output of the heater 16 at the maximum value M2 in the normal operation state.

また、制御装置17は、通常運転状態中の時刻T7においてセンサ18,19で検出した建屋2の内外の気温及び湿度並びに内外差が所定の範囲を超えて変動した場合、その気温及び湿度に基づいて改めて加温機16の出力の最大値M3を決定し直し、そこから、加温機16の出力が最大値M3となるように加温機16の出力を徐々に上昇させ、通常運転状態において、加温機16の出力を最大値M3となるように維持し、抄製装置3による抄製を終了した時刻T3から所定時間が経過して終期運転状態となった時刻T4から加温機16の出力を徐々に下降させ、終期運転状態が終了する時刻T5での加温機16の出力が0となるように加温機16の駆動を停止する。   When the temperature and humidity inside and outside the building 2 detected by the sensors 18 and 19 and the difference between the inside and outside detected by the sensors 18 and 19 at a time T7 during the normal operation state fluctuate beyond a predetermined range, the control device 17 Once again, the maximum value M3 of the output of the heater 16 is determined again, and from there, the output of the heater 16 is gradually increased so that the output of the heater 16 becomes the maximum value M3. Then, the output of the heating device 16 is maintained at the maximum value M3, and the heating device 16 is started at a time T4 when a predetermined time elapses from the time T3 when the papermaking by the papermaking device 3 is completed and the terminal device enters the terminal operation state. Is gradually lowered, and the driving of the heater 16 is stopped so that the output of the heater 16 at time T5 at which the final operation state ends is 0.

なお、上記説明では、加温機16の出力を直線的に上昇又は下降させているが曲線的に上昇又は下降させてもよい。また、初期運転状態となった時刻T1から加温機16の駆動を開始しているが、これに限られず、抄製開始の時刻T0から所定時間が経過した(又は、抄製装置3で所定枚数の抄製を行った)時刻から加温機16の稼働を開始してもよい。また、通常運転状態となった時刻T2に加温機16の出力が最大値M1(M2)となるようにしているが、これに限られず、抄製開始の時刻T0から所定時間が経過した(又は、抄製装置3で所定枚数の抄製を行った)時刻に加温機16の出力が最大値M1(M2)となるようにしてもよい。また、終期運転状態となった時刻T4から加温機16の出力を下降させているが、これに限られず、抄製開始の時刻T0から所定時間が経過した(又は、抄製装置3で所定枚数の抄製を行った)時刻から加温機16の出力を下降させてもよい。また、通常運転状態が終了した時刻T4に加温機16の出力が最大値M1(M3)となるようにしているが、これに限られず、抄製開始の時刻T0から所定時間が経過した(又は、抄製装置3で所定枚数の抄製を行った)時刻に加温機16の出力が最大値M1(M3)となるようにしてもよい。また、建屋2の外部の気温が低下した場合や内外の気温差が増大した場合に加温機16の出力の最大値を増大させるのが望ましいが、その際に、建屋2の外部の湿度が上昇した場合や内外の湿度差が増大した場合には加温機16の出力の最大値を増大させないか増大幅を抑制するのがより好ましい。   In the above description, the output of the heater 16 is increased or decreased linearly, but may be increased or decreased in a curved line. Further, the driving of the heater 16 is started from the time T1 at which the initial operation state is reached, but the invention is not limited to this. The operation of the heating device 16 may be started from the time when the number of sheets has been manufactured). Further, the output of the heater 16 is set to the maximum value M1 (M2) at the time T2 when the normal operation state is set, but the present invention is not limited to this, and a predetermined time has elapsed from the time T0 of the papermaking start ( Alternatively, the output of the heating device 16 may be set to the maximum value M1 (M2) at the time when a predetermined number of sheets are produced by the papermaking apparatus 3). Further, the output of the heating device 16 is decreased from the time T4 when the final operation state is reached, but the invention is not limited to this, and a predetermined time has elapsed from the time T0 of the papermaking start (or a predetermined time The output of the heating device 16 may be lowered from the time when the number of sheets is manufactured). Further, the output of the heater 16 is set to the maximum value M1 (M3) at the time T4 when the normal operation state ends, but is not limited thereto, and a predetermined time has elapsed from the time T0 of the papermaking start ( Alternatively, the output of the heater 16 may be set to the maximum value M1 (M3) at the time when a predetermined number of sheets have been produced by the papermaking apparatus 3). It is also desirable to increase the maximum value of the output of the heater 16 when the temperature outside the building 2 decreases or when the temperature difference between the inside and outside increases. When the temperature rises or when the difference between the inside and outside humidity increases, it is more preferable not to increase the maximum value of the output of the heater 16 or to suppress the increase.

以上に説明したように、上記海苔製造システムSは、建屋2の内部に設置され、抄製した海苔生地を搬送経路に沿って搬送しながら加熱空気で乾燥させる乾燥室12と、乾燥室12に加熱空気を供給する加熱機13と、加熱機13に建屋2の外部の空気を加温して供給する加温機16とを有する構成となっている。   As described above, the laver manufacturing system S is installed inside the building 2 and includes a drying chamber 12 for drying the dried laver dough with heated air while transporting the produced laver dough along the transport path. It has a configuration in which a heater 13 for supplying heated air and a heater 16 for supplying air to the heater 13 by heating air outside the building 2 are provided.

しかも、上記海苔製造システムSは、乾燥室12の内部の搬送経路の上流側だけに海苔生地が存在している状態(初期運転状態)では、加温機16の出力を徐々に上昇させ、その後、乾燥室12の内部の搬送経路の全てに海苔生地が存在している状態(通常運転状態)では、加温機16の出力を最大とし、その後、乾燥室12の内部の搬送経路の下流側だけに海苔生地が存在している状態(終期運転状態)では、加温機16の出力を徐々に下降させるように制御している。   Moreover, the laver production system S gradually increases the output of the heating device 16 in a state where the laver material is present only on the upstream side of the transport path inside the drying chamber 12 (initial operation state). In a state where the laver dough is present in all the transport paths inside the drying chamber 12 (normal operation state), the output of the heating device 16 is maximized, and then the downstream side of the transport path inside the drying chamber 12 is used. In a state in which nori dough is present only (final operation state), the output of the heating device 16 is controlled to gradually decrease.

そのため、上記海苔製造システムSでは、初期運転状態から終期運転状態まで乾燥室12の内部の状態が急激に変化するのを抑制することができるので、海苔生地を良好に均一に乾燥させることができ、乾燥海苔の縮みやムラなどの発生を防止することができる。   Therefore, in the laver production system S, it is possible to suppress a sudden change in the state of the inside of the drying chamber 12 from the initial operation state to the final operation state, and thus it is possible to dry the laver dough satisfactorily and uniformly. In addition, shrinkage and unevenness of the dried laver can be prevented.

また、上記海苔製造システムSは、通常運転状態における加温機16の出力の最大値を、初期運転状態における建屋2の外部の気温に応じて変更し、変更後の最大値となるように初期運転状態で加温機16の出力を徐々に上昇させるように制御している。   Further, the seaweed production system S changes the maximum value of the output of the heating device 16 in the normal operation state according to the outside temperature of the building 2 in the initial operation state, and sets the maximum value to the changed maximum value. In the operating state, the output of the heater 16 is controlled to gradually increase.

そのため、上記海苔製造システムSでは、初期運転状態の途中で建屋2の外部の気温に変化が生じても乾燥室12の内部の状態が急激に変化するのを抑制することができるので、海苔生地を良好に均一に乾燥させることができ、乾燥海苔の縮みやムラなどの発生を防止することができる。   Therefore, in the laver production system S, even if the temperature outside the building 2 changes in the middle of the initial operation state, it is possible to suppress the abrupt change in the state inside the drying chamber 12. Can be satisfactorily and uniformly dried, and the occurrence of shrinkage and unevenness of dried nori can be prevented.

また、上記海苔製造システムSは、通常運転状態における加温機16の出力の最大値を、通常運転状態における建屋2の外部の気温に応じて変更し、変更後の最大値となるように終期運転状態で加温機16の出力を徐々に下降させるように制御している。   Further, the laver production system S changes the maximum value of the output of the heating device 16 in the normal operation state according to the temperature outside the building 2 in the normal operation state, and ends the operation so that the maximum value after the change is obtained. In the operating state, the output of the heater 16 is controlled to gradually decrease.

そのため、上記海苔製造システムSでは、通常運転状態の途中で建屋2の外部の気温に変化が生じても乾燥室12の内部の状態が急激に変化するのを抑制することができるので、海苔生地を良好に均一に乾燥させることができ、乾燥海苔の縮みやムラなどの発生を防止することができる。 For this reason, in the laver production system S, even if the temperature outside the building 2 changes during the normal operation state, it is possible to suppress a sudden change in the internal state of the drying chamber 12. Can be satisfactorily and uniformly dried, and the occurrence of shrinkage and unevenness of dried nori can be prevented.

S 海苔製造システム
1 海苔製造機 2 建屋
3 抄製装置 4 乾燥装置
5 海苔簀 6 簀枠
7 搬送機構 8 抄き機構
9 吸引脱水機構 10 押圧脱水機構
11 剥離機構 12 乾燥室
13 加熱機 14,15 搬送機構
16 加温機 17 制御装置
18,19 センサ
S Nori production system 1 Nori production machine 2 Building 3 Paper making device 4 Drying device 5 Seaweed cage 6 Cradle frame 7 Transport mechanism 8 Drawing mechanism 9 Suction dehydration mechanism 10 Press dehydration mechanism
11 Peeling mechanism 12 Drying room
13 Heater 14,15 Transport mechanism
16 Heater 17 Controller
18,19 sensor

そこで、請求項1に係る本発明では、建屋の内部に設置され、抄製した海苔生地を搬送経路に沿って搬送しながら加熱空気で乾燥させる乾燥室と、乾燥室に加熱空気を供給する加熱機と、加熱機に建屋の外部の空気を加温して供給する加温機とを有する海苔製造システムにおいて、乾燥室の内部の搬送経路の上流側だけに海苔生地が存在している状態(初期運転状態)では、加温機の出力を徐々に上昇させ、その後、乾燥室の内部の搬送経路の全てに海苔生地が存在している状態(通常運転状態)では、加温機の出力を最大とし、その後、乾燥室の内部の搬送経路の下流側だけに海苔生地が存在している状態(終期運転状態)では、加温機の出力を徐々に下降させ、前記通常運転状態における加温機の出力の最大値を、前記初期運転状態における建屋の外部の気温に応じて変更し、変更後の最大値となるように前記初期運転状態で加温機の出力を徐々に上昇させ、建屋の外部の気温が低下した場合や建屋の内外の気温差が増大した場合に、建屋の外部の湿度が上昇した場合や建屋の内外の湿度差が増大した場合には、加温機の出力の最大値を増大させないか増大幅を抑制するように制御することにした。
Therefore, in the present invention according to claim 1, a drying chamber that is installed inside a building and that dries dried laver dough with heated air while being transported along a transport path, and a heating chamber that supplies heated air to the drying chamber. Nori production system having a heating device and a heating device that heats and supplies air outside the building to the heating device, in a state where the nori dough exists only on the upstream side of the transport path inside the drying chamber ( In the initial operation state), the output of the heater is gradually increased, and then, in a state where the laver dough is present in all the transport paths inside the drying chamber (normal operation state), the output of the heater is increased. After that, in a state where the laver material is present only on the downstream side of the transport path inside the drying chamber (final operation state), the output of the heating machine is gradually lowered, and the heating in the normal operation state is performed. The maximum value of the output of the The temperature of the outside of the building changes when the outside temperature of the building decreases, or when the temperature inside or outside the building changes, according to the outside temperature of the building. when the temperature difference between is increased, if the humidity difference between the inside and outside of or buildings if the external humidity of the building is increased is increased, that to suppress the increase in width or not to increase the maximum value of the output of the heating device Decided to control.

また、請求項2に係る本発明では、前記請求項1に係る本発明において、前記通常運転状態における加温機の出力の最大値を、前記通常運転状態における建屋の外部の気温に応じて変更し、変更後の最大値となるように前記終期運転状態で加温機の出力を徐々に下降させるように制御することにした。 In the present invention according to claim 2 , in the present invention according to claim 1 , the maximum value of the output of the heater in the normal operation state is changed according to the outside temperature of the building in the normal operation state. Then, control is performed such that the output of the heater is gradually decreased in the final operation state so as to have the changed maximum value.

Claims (3)

建屋の内部に設置され、抄製した海苔生地を搬送経路に沿って搬送しながら加熱空気で乾燥させる乾燥室と、乾燥室に加熱空気を供給する加熱機と、加熱機に建屋の外部の空気を加温して供給する加温機とを有する海苔製造システムにおいて、
乾燥室の内部の搬送経路の上流側だけに海苔生地が存在している状態(初期運転状態)では、加温機の出力を徐々に上昇させ、
その後、乾燥室の内部の搬送経路の全てに海苔生地が存在している状態(通常運転状態)では、加温機の出力を最大とし、
その後、乾燥室の内部の搬送経路の下流側だけに海苔生地が存在している状態(終期運転状態)では、加温機の出力を徐々に下降させる
ように制御することを特徴とする海苔製造システム。
A drying room installed inside the building and drying the dried seaweed dough with heated air while transporting it along the transport path, a heating device that supplies heated air to the drying room, and air outside the building to the heating device Nori production system having a heating machine for heating and supplying
In a state where nori dough exists only on the upstream side of the transport path inside the drying chamber (initial operation state), gradually increase the output of the heating machine,
Thereafter, in a state where the laver dough is present in all of the transport paths inside the drying chamber (normal operation state), the output of the heating machine is maximized,
Thereafter, in a state where the laver material is present only on the downstream side of the transport path inside the drying chamber (final operation state), the output of the heating machine is controlled to gradually decrease, and the laver production is characterized in that system.
前記通常運転状態における加温機の出力の最大値を、前記初期運転状態における建屋の外部の気温に応じて変更し、変更後の最大値となるように前記初期運転状態で加温機の出力を徐々に上昇させるように制御することを特徴とする請求項1に記載の海苔製造システム。   The maximum value of the output of the heater in the normal operation state is changed according to the temperature outside the building in the initial operation state, and the output of the heater in the initial operation state is changed to the changed maximum value. The seaweed production system according to claim 1, wherein the seaweed production system is controlled so as to gradually rise. 前記通常運転状態における加温機の出力の最大値を、前記通常運転状態における建屋の外部の気温に応じて変更し、変更後の最大値となるように前記終期運転状態で加温機の出力を徐々に下降させるように制御することを特徴とする請求項1又は請求項2に記載の海苔製造システム。   The maximum value of the output of the heater in the normal operation state is changed in accordance with the temperature outside the building in the normal operation state, and the output of the heater in the final operation state is changed to the changed maximum value. The nori production system according to claim 1 or 2, wherein the laver is controlled so as to be gradually lowered.
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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH044861A (en) * 1990-04-21 1992-01-09 Togami Electric Mfg Co Ltd Temperature and humidity-controlling device of laver-drying chamber
JPH0430778A (en) * 1990-05-24 1992-02-03 Kyushu Electric Power Co Inc Drying control in laver drying and laver dryer
JP2012029644A (en) * 2010-07-30 2012-02-16 Itsuwa Kogyo:Kk Laver-producing machine
JP2015136306A (en) * 2014-01-21 2015-07-30 株式会社大坪鉄工 Laver manufacturing system
JP2015159792A (en) * 2014-02-28 2015-09-07 株式会社イツワ工業 Laver production machine and control method thereof
JP2017127198A (en) * 2016-01-18 2017-07-27 株式会社大坪鉄工 Laver manufacturing apparatus

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH044861A (en) * 1990-04-21 1992-01-09 Togami Electric Mfg Co Ltd Temperature and humidity-controlling device of laver-drying chamber
JPH0430778A (en) * 1990-05-24 1992-02-03 Kyushu Electric Power Co Inc Drying control in laver drying and laver dryer
JP2012029644A (en) * 2010-07-30 2012-02-16 Itsuwa Kogyo:Kk Laver-producing machine
JP2015136306A (en) * 2014-01-21 2015-07-30 株式会社大坪鉄工 Laver manufacturing system
JP2015159792A (en) * 2014-02-28 2015-09-07 株式会社イツワ工業 Laver production machine and control method thereof
JP2017127198A (en) * 2016-01-18 2017-07-27 株式会社大坪鉄工 Laver manufacturing apparatus

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