JPH0813241B2 - Hot air supply method in tea making process - Google Patents
Hot air supply method in tea making processInfo
- Publication number
- JPH0813241B2 JPH0813241B2 JP1303579A JP30357989A JPH0813241B2 JP H0813241 B2 JPH0813241 B2 JP H0813241B2 JP 1303579 A JP1303579 A JP 1303579A JP 30357989 A JP30357989 A JP 30357989A JP H0813241 B2 JPH0813241 B2 JP H0813241B2
- Authority
- JP
- Japan
- Prior art keywords
- hot air
- tea
- temperature
- target
- flow rate
- 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 - Fee Related
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- Drying Of Solid Materials (AREA)
- Tea And Coffee (AREA)
Description
【発明の詳細な説明】 《発明の目的》 <産業上の利用分野> 本発明は製茶工程における熱風供給方法に関するもの
である。DETAILED DESCRIPTION OF THE INVENTION << Object of Invention >><Industrial Field of Application> The present invention relates to a hot air supply method in a tea making process.
<従来の技術> 葉打、粗揉、中揉、乾燥、仕上等の製茶工程において
は、茶葉に熱風を与えて乾燥を促進しているが、この際
に茶葉の温度を所定値に保つこと、乾燥状態を恒率乾燥
に近付けることが、製茶品質上、重要な管理事項であ
る。近年、このような管理を製茶機械の自動化、マイコ
ン化により遂行しようという動きが高まっている。<Prior art> In the tea-making process such as leaf-beating, rough-rubbing, medium-rubbing, drying, and finishing, hot air is applied to the tea leaves to accelerate the drying. At this time, keep the temperature of the tea leaves at a predetermined value. It is an important control item in tea production quality to bring the dry state close to constant drying. In recent years, there has been an increasing trend to perform such management by automating tea making machines and using a microcomputer.
特開昭60−75235号、特開昭63−264号に見られる技術
は、共に製茶機械の自動化、マイコン化を目的に開発さ
れたものである。前者は製茶工程中に測定される茶温を
設定値パターンに近似させるように熱風温度と熱風量を
調整しようとするものである。後者は、茶葉の投入含水
率、目標取出含水率、設定工程時間から目標含水率推移
曲線を一義に定め、これに基づいて熱風温度、熱風量、
その他の製茶要素の目標推移曲線を算出するとともに、
茶葉の温度を目標値に維持しようとするものである。The techniques disclosed in JP-A-60-75235 and JP-A-63-264 are both developed for the purpose of automating a tea making machine and using a microcomputer. The former attempts to adjust the hot air temperature and the hot air amount so that the tea temperature measured during the tea making process approximates the set value pattern. In the latter, the target moisture content transition curve is uniquely defined from the input moisture content of tea leaves, the target extraction moisture content, and the setting process time, and based on this, the hot air temperature, hot air volume,
While calculating the target transition curves for other tea-making elements,
This is to maintain the temperature of tea leaves at the target value.
<発明が解決しようとする課題> しかし前者は、単に工程中の茶温を設定値パターンに
近似させることのみを目的として熱風温度と熱風量を変
更しているため、前期管理事項のうちの茶葉の温度を所
定値に保つことは充分満足できるかもしれないが、熱風
温度と熱風量のバランスついては、なおざりにされてい
る。よって恒率乾燥からかけ離れた乾燥状態が生じ、製
茶品質が損なわれるおそれがある。<Problems to be solved by the invention> However, since the former changes the hot air temperature and the hot air amount only for the purpose of approximating the tea temperature in the process to the set value pattern, the tea leaves among the management items in the previous term It may be sufficient to keep the temperature at a predetermined value, but the balance between the hot air temperature and the hot air amount is neglected. Therefore, a dry state far from constant-rate drying occurs, which may impair the quality of tea making.
後者では、茶温は所定値に維持されており、目標含水
率推移曲線及び製茶要素の目標推移曲線は恒率乾燥を目
的として決定されているため、前記管理事項は充足され
ているようである。しかし本技術では、製茶要素の目標
推移曲線は、工程開始前に目標含水率推移曲線に応じて
理論的に決定されるものであるので、実際の含水率が目
標値と異なってしまえば、もはや適切な製茶要素の制御
をしているとは言えなくなる。また本技術には多数の正
確なセンサが必要であるため、コストがかかるという問
題もある。In the latter, the tea temperature is maintained at a predetermined value, and the target moisture content transition curve and the target transition curve of the tea making element are determined for the purpose of constant rate drying, so the above-mentioned management items seem to be satisfied. . However, in the present technology, the target transition curve of the tea-making element is theoretically determined according to the target moisture content transition curve before the process starts, so if the actual moisture content is different from the target value, it will no longer exist. It can no longer be said that they are properly controlling tea-making elements. In addition, since the present technology requires a large number of accurate sensors, there is a problem that it is costly.
よって本発明は製茶工程において、茶温を所定値に保
ちつつ恒率乾燥に近い乾燥を行うことができる製茶工程
における熱風供給方法を提供することを目的とする。Therefore, an object of the present invention is to provide a hot air supply method in a tea making process, which can perform drying close to constant rate drying while maintaining the tea temperature at a predetermined value.
《発明の構成》 <課題を解決するための手段> 本出願に係る第一の発明である製茶工程における熱風
供給方法は、茶葉に対し熱風を与えて乾燥を行う製茶工
程において、目標茶温と実測茶温に応じて目標熱風温度
を選定する熱風温度選定プログラムと、実行熱風温度と
実行茶葉水分値に応じて目標熱風量を選定する熱風量選
定プログラムを具えたことを特徴として成るものであ
る。<Structure of the Invention><Means for Solving the Problems> A hot air supply method in a tea making process, which is the first invention of the present application, has a target tea temperature in a tea making process in which hot air is applied to tea leaves to dry them. It is equipped with a hot air temperature selection program that selects the target hot air temperature according to the measured tea temperature and a hot air flow rate selection program that selects the target hot air flow according to the execution hot air temperature and the execution tea leaf moisture value. .
また本出願に係る第二の発明である製茶工程における
熱風供給方法は、茶葉に対し熱風を与えて乾燥を行う製
茶工程において、目標茶温と実測茶温に応じて目標熱風
温度を選定する熱風温度選定プログラムと、実行熱風温
度と実行茶葉水分値に応じて目標熱風量を選定する熱風
量選定プログラムを具え、熱風量選定プログラムは、実
行熱風温度に応じて算出された目標熱風量が実行茶葉水
分値に応じて求められる熱風量の許容範囲を外れるとき
目標熱風量を任意の値に修正するように構成されている
ことを特徴として成るものである。Further, the hot air supply method in the tea making process which is the second invention according to the present application is a hot air that selects a target hot air temperature according to a target tea temperature and an actually measured tea temperature in a tea making process in which hot air is applied to tea leaves to dry them. It has a temperature selection program and a hot air flow rate selection program that selects the target hot air flow rate according to the execution hot air temperature and the execution tea leaf moisture value.The hot air flow rate selection program executes the target hot air flow calculated according to the execution hot air temperature. It is characterized in that it is configured to correct the target hot air flow rate to an arbitrary value when the hot air flow rate is out of the allowable range determined according to the moisture content.
そしてこれら発明をもって前記目的を達成しようとす
るものである。Then, these inventions are intended to achieve the above object.
<発明の作用> 本発明は、茶葉に対し供給される熱風の温度と風量を
管理する方法であり、目標熱風温度は、目標茶温と実測
茶温に応じて茶温を目標値に近似させるべく選定し、目
標熱風量は、実行熱風温度と基準熱風温度に応じて選定
することにより、目標熱風温度と目標熱風量とのバラン
スを保つ。<Operation of the Invention> The present invention is a method for managing the temperature and air volume of hot air supplied to tea leaves, and the target hot air temperature approximates the tea temperature to a target value according to the target tea temperature and the measured tea temperature. The target hot air amount is selected according to the execution hot air temperature and the reference hot air temperature, thereby maintaining the balance between the target hot air temperature and the target hot air amount.
これを具体的に説明すれば、茶温を維持するために選
定される熱風温度が高くなるということは、茶温が上が
りにくくなっているということであり、この場合、茶葉
の恒率乾燥がくずれて表面がぐしゃついている可能性が
高いので、熱風量を増加して表面のぐしゃつきを排除す
ることが望ましい。逆に熱風温度が低くなった場合に
は、茶温が上がりやすい、すなわち茶葉の効率乾燥がく
ずれて上乾きしている可能性が高いので、熱風量を減少
して上乾きを防止することが望ましい。Explaining this concretely, the fact that the hot air temperature selected to maintain the tea temperature is high means that the tea temperature is hard to rise, and in this case, the constant rate drying of the tea leaves is performed. Since there is a high possibility that the surface will be crumbled and jerky, it is desirable to increase the amount of hot air to eliminate the jerky surface. Conversely, when the hot air temperature becomes low, the tea temperature tends to rise, that is, there is a high possibility that the efficient drying of the tea leaves has failed and it has dried up, so it is possible to reduce the amount of hot air and prevent overdrying. desirable.
一方、茶葉の水分値によっても、適切な(許容され
る)熱風量の範囲が決定される。すなわち茶葉水分値が
高ければ、与えられた熱量が水分の蒸発に消費されやす
いため、熱風量を高めても恒率乾燥に近い乾燥を行うこ
とができるが、熱風量を低くし過ぎると、茶葉温度を維
持するためには熱風温度を上げるしかないため、熱風温
度と熱風量とのバランスがくずれ製茶品質を損ねるおそ
れがある。逆に茶葉水分値が低ければ、与えられた熱量
が水分の蒸発に消費されにくいため、熱風量を高める
と、恒率乾燥が崩れ上乾きしてしまう。よって本発明で
は、目標熱風量を実行熱風温度と実行茶葉水分値に応じ
て選定することにより、目標熱風量と目標熱風温度との
バランスをとり、茶葉の恒率乾燥を促すのである。On the other hand, an appropriate (allowable) range of hot air flow is also determined by the water content of the tea leaves. That is, if the moisture value of tea leaves is high, the amount of heat given is easily consumed for evaporation of water, so even if the amount of hot air is increased, it is possible to perform drying close to constant rate drying, but if the amount of hot air is too low, Since there is no choice but to raise the hot air temperature to maintain the temperature, there is a risk that the hot air temperature and the hot air amount are out of balance and the quality of tea making is impaired. On the other hand, if the water content of the tea leaves is low, the amount of heat applied is not easily consumed for the evaporation of water, so if the amount of hot air is increased, the constant rate drying will collapse and the material will dry. Therefore, in the present invention, the target hot air amount is selected according to the actual hot air temperature and the actual tea leaf moisture value to balance the target hot air amount and the target hot air temperature and promote constant rate drying of the tea leaves.
<実施例> 以下本発明を図示の実施例に基づいて説明する。本発
明は茶葉に対し熱風を与えて乾燥を行うすべての製茶工
程に適用される。本発明でいう製茶工程とは、特定の製
茶機の茶葉の投入から取り出しまでの間、あるいはその
一部を意味する場合のほか、複数の製茶機の連続した処
理をまとめて意味することもある。本実施例では、本発
明を製茶中揉工程に適用した場合について説明する。<Examples> The present invention will be described below based on illustrated examples. INDUSTRIAL APPLICABILITY The present invention is applied to all tea making processes in which hot air is applied to tea leaves to dry them. The tea-making process in the present invention means not only the time from the feeding of tea leaves of a particular tea-making machine to the taking-out, or a part thereof, but also a collective treatment of a plurality of tea-making machines. . In the present embodiment, a case where the present invention is applied to a tea making and kneading process will be described.
第1図は一般的な中揉機1を示す。中揉機1は胴2内
の茶葉に熱風を与えつつ、胴2の回転と多数の揉手3を
周設した主軸4をそれぞれ回転し、茶葉を胴2の内壁と
揉手3の間に挟み込んで形状を整えつつ乾燥させるもの
である。このうち熱風の供給に関する構成にうちてのみ
以下に説明し、その他の構成は本発明の要旨ではないの
で説明を省略する。FIG. 1 shows a general centering machine 1. The middle kneading machine 1 applies hot air to the tea leaves in the body 2, while rotating the body 2 and the main shaft 4 around which a large number of kneading hands 3 are provided, so that the tea leaves are sandwiched between the inner wall of the body 2 and the kneading hands 3. The shape is adjusted and dried. Of these, only the configuration related to the supply of hot air will be described below, and the other configurations are not the gist of the present invention, so description thereof will be omitted.
本中揉機1の熱風供給構造は、外気を加熱するガス火
炉5、吸引ファン6及びこれらの各操作部7、8から成
る。ガス火炉の操作部7はガスバーナ9の燃焼量を調節
して、熱風温度センサ10の測定値が目標値を維持するよ
うに働く。吸引ファンの操作部8は吸引ファン6の回転
数を調節して所定の熱風量を作り出す。なお吸引ファン
6の回転数と熱風量との関係は外的要因の影響を受けな
いため、いわゆるフィードバック制御は行わない。符号
11は水分センサであり、胴2内の茶葉をサンプリングし
てその水分値を測定し、その後、再度胴2内へ返還する
ものである。符号12は排気温度センサであるが、中揉機
1における茶葉の温度は排気温度と一致するという研究
結果に基づき、茶葉温度の代替値として排気温度を設定
するためのものである。もちろん適宜個所に茶温センサ
を配して、その値を利用することもできる。符号13はい
わゆるマイコンを主体とした熱風制御部であり、後述す
るプログラムを記憶し、必要に応じて水分センサ11、排
気温度センサ12の測定値を入力し、ガス火炉の操作部
7、吸引ファンの操作部8への指令を出力する。よって
熱風制御部13から指令が発せられると、ガス火炉5、吸
引ファン6が作動し、外気は外気取込口14からガス火炉
5内に取り込まれ、ガスバーナ9によって目標値に加熱
されて胴2内に供給され、茶葉を加熱した後に排出口15
から胴2外に排出される。なお以上は、ガス火炉5を用
いた中揉機1独特の熱風供給装置を説明したが、本実施
例に限定されるものではなく、例えば前記特開昭63−26
4号に記載された乾燥媒体供給手段(15)のような構成
をとることも可能である。The hot air supply structure of the central kneading machine 1 is composed of a gas furnace 5 for heating the outside air, a suction fan 6 and respective operation parts 7 and 8 thereof. The operation part 7 of the gas furnace adjusts the combustion amount of the gas burner 9 so that the measured value of the hot air temperature sensor 10 maintains the target value. The operation unit 8 of the suction fan adjusts the number of rotations of the suction fan 6 to generate a predetermined amount of hot air. Since the relationship between the rotation speed of the suction fan 6 and the hot air flow rate is not influenced by external factors, so-called feedback control is not performed. Sign
Reference numeral 11 denotes a moisture sensor, which measures the moisture value of tea leaves sampled in the body 2 and then returns them to the body 2 again. Reference numeral 12 denotes an exhaust gas temperature sensor, which is for setting the exhaust gas temperature as an alternative value of the tea leaf temperature based on the research result that the temperature of the tea leaves in the central kneading machine 1 matches the exhaust gas temperature. Of course, it is also possible to place a tea temperature sensor at an appropriate place and use the value. Reference numeral 13 is a hot air control unit mainly composed of a so-called microcomputer, which stores a program to be described later, inputs measured values of the moisture sensor 11 and the exhaust temperature sensor 12 as necessary, and operates the operation unit 7 of the gas furnace and the suction fan. And outputs a command to the operation unit 8. Therefore, when a command is issued from the hot air control unit 13, the gas furnace 5 and the suction fan 6 are operated, and the outside air is taken into the gas furnace 5 through the outside air intake port 14 and heated to a target value by the gas burner 9 and the body 2 After the tea leaves are heated and heated, the outlet 15
Is discharged to the outside of the body 2. Although the hot air supply device unique to the central kneading machine 1 using the gas furnace 5 has been described above, the present invention is not limited to this embodiment.
It is also possible to adopt a structure such as the drying medium supply means (15) described in No. 4.
次に本実施例装置による熱風供給方法について説明す
る。なお説明に先立ち用語の一部について定義する。目
標熱風温度、目標熱風量等に使用される「目標」とは、
これからガス火炉の操作部7、吸引ファンの操作部8に
より各部を操作して得ようとする製茶要素の目標値を意
味し、実測茶温等に使用される「実測」とは、実際にセ
ンサ類によって測定された現時点あるいは過去の任意の
時の測定値を意味し、実行熱風温度、実行熱風量等に使
用される「実行」とは、一般に使用される「実行」と同
義であり、実際に行うことを意味する。例えば実行熱風
温度について述べれば、それが目標熱風温度と等しくな
る場合もあるし、それが実際の数値とかけ離れている場
合には、実測値をもって実行熱風温度とする場合もあ
る。従って本明細書で使用する「実行」とは、現時点あ
るいは過去の任意の時の目標値または実測値を意味する
ということができる。また基準熱風温度等に使用される
「基準」とは、一般に使用される「基準」と同義であ
り、後述する制御プログラムを動作させるにあたって設
けた便宜上の標準を意味する。なお各プログラムのフロ
ーチャートのSTARTからRETURNまでの処理をピリオドと
呼び、各ステップを制御ステップとして記号Sで表す。Next, a method for supplying hot air by the apparatus of this embodiment will be described. Prior to the explanation, some terms will be defined. "Target" used for target hot air temperature, target hot air volume, etc.
The “actual measurement” used for the actual measurement tea temperature and the like means the target value of the tea-making element to be obtained by operating each section with the operation section 7 of the gas furnace and the operation section 8 of the suction fan. It means a measured value at any time in the past or at any time measured by a class, and “execution” used for the execution hot air temperature, execution hot air volume, etc. is synonymous with the commonly used “execution”, and actually Means to do. For example, when the execution hot air temperature is described, it may be equal to the target hot air temperature, and when it is far from the actual numerical value, the actual measurement value may be used as the execution hot air temperature. Therefore, “execution” used in the present specification can be said to mean a target value or an actual measurement value at any point in time or in the past. The “reference” used for the reference hot air temperature and the like is synonymous with the “reference” generally used and means a standard provided for operating a control program described later for convenience. The process from START to RETURN in the flow chart of each program is called a period, and each step is represented by a symbol S as a control step.
まずメインルーチンである熱風供給プログラムについ
て第2図に基づいて説明する。本プログラムを実行する
にあたり、あらかじめ初期基準熱風温度SKNEP(後述の
処理で毎回変更される)、初期熱風温度SNEP、初期熱風
量SKAZE(後述の処理で毎回変更される)、目標茶温MT
を設定しておく。目標茶温MTは時間の経過に従い複数設
定してもよいが、これは後述する。なお中揉機1への茶
葉の投入に先立って、胴2内の雰囲気温度を上げておく
必要があるため、投入待ちの状態では、初期熱風温度SN
EP、初期熱風量SKAZEをそれぞれ目標値としてガス火炉
の操作部7、吸引ファンの操作部8へ出力する。そして
茶葉が中揉機1内に投入されると同時に本プログラムが
実行され、まずステップS1で目標熱風温度NEPに初期基
準熱風温度SKNEPが目標熱風量KAZEに初期熱風量SKAZEが
入力される(二回目以降のピリオドでは、それぞれ前回
のピリオドで変更された初期基準熱風温度SKNEP、同じ
く初期熱風量SKAZEが入力される)。S2では、基準熱風
温度KNEPにその時点での初期基準熱風温度SKNEPが入力
される。S3では、カウンタTが0に初期化される。S4〜
S300はループを成し、S4では、中揉処理が終了して茶葉
が取り出されたかを判断し、真ならば次回初期熱風量選
定プログラムS400(後述)を実行した後、本ピリオドは
終了し、偽ならばS5に進む。なお中揉工程は、、あらか
じめ設定した工程時間が経過したとき、茶葉が設定した
水分値まで乾燥したとき等に終了させることができる
が、詳細は省略する。S5では、目標熱風温度NEP、目標
熱風量KAZEの値をそれぞれガス火炉の操作部7、吸引フ
ァンの操作部8に出力する。S6では、タイマにて20秒の
経過を待機する。S7ではカウンタTに1を加える。S8で
は、T=6か、すなわちプログラム開始後2分経過した
かを判断し、真ならば初期熱風量変更プログラムS100
(後述)を実行する。偽ならばS9に進み、T≧15か、す
なわち中揉処理開始後5分以上経過しているかを判断
し、真ならば熱風温度選定プログラムS200(後述)を実
行する。偽ならばS4に戻る。熱風温度選定プログラムS2
00を実行した後にS10に進み、T=3n(nは自然数)を
判断し、真ならば熱風量選定プログラムS300を実行し、
偽ならばS4に戻る。すなわち中揉処理開始後5分以上経
過すると、20秒毎に熱風温度選定プログラムS200を実行
し、1分毎に熱風量選定プログラムS300(後述)を実行
する。なお本プログラム終了後も続いて次の中揉処理が
予定されている場合は、投入待ちの状態で、初期熱風温
度SNEPと次回初期熱風量選定プログラムS400で変更され
た初期熱風量SKAZEをそれぞれ目標値としてガス火炉の
操作部7、吸引ファンの操作部8へ出力しておく。First, the hot air supply program, which is the main routine, will be described with reference to FIG. Before executing this program, the initial reference hot air temperature SKNEP (changed each time in the process described below), initial hot air temperature SNEP, initial hot air flow SKAZE (changed each time in the process described below), target tea temperature MT
Is set. A plurality of target tea temperatures MT may be set as time passes, which will be described later. In addition, since it is necessary to raise the ambient temperature in the body 2 prior to the introduction of tea leaves into the middle kneader 1, the initial hot air temperature SN
The EP and the initial hot air flow SKAZE are output to the operation part 7 of the gas furnace and the operation part 8 of the suction fan as target values, respectively. Then, this program is executed at the same time when the tea leaves are put into the central kneading machine 1. First, in step S1, the initial reference hot air temperature SKNEP is input to the target hot air temperature NEP and the initial hot air flow SKAZE is input to the target hot air flow KAZE (second time). In the subsequent periods, the initial reference hot air temperature SKNEP and the initial hot air flow SKAZE, which were changed in the previous period, are entered respectively. In S2, the initial reference hot air temperature SKNEP at that time is input to the reference hot air temperature KNEP. At S3, the counter T is initialized to 0. S4 ~
S300 forms a loop, and in S4, it is determined whether or not the tea leaves have been taken out after the middle kneading process, and if true, the next initial hot air flow rate selection program S400 (described later) is executed, and then this period ends, If false, proceed to S5. The middle kneading process can be ended when a preset process time elapses, when the tea leaves have dried to a set moisture value, etc., but details thereof will be omitted. In S5, the values of the target hot air temperature NEP and the target hot air amount KAZE are output to the operation unit 7 of the gas furnace and the operation unit 8 of the suction fan, respectively. In S6, the timer waits for 20 seconds. In S7, 1 is added to the counter T. In S8, it is determined whether T = 6, that is, whether 2 minutes have elapsed after the program started. If true, the initial hot air flow rate change program S100
Execute (described later). If it is false, the process proceeds to S9, and it is determined whether T ≧ 15, that is, whether 5 minutes or more have elapsed after the start of the middle kneading process, and if true, the hot air temperature selection program S200 (described later) is executed. If false, return to S4. Hot air temperature selection program S2
After executing 00, proceed to S10, judge T = 3n (n is a natural number), and if true, execute the hot air flow rate selection program S300,
If false, return to S4. That is, when 5 minutes or more have passed after the start of the medium kneading process, the hot air temperature selection program S200 is executed every 20 seconds, and the hot air flow rate selection program S300 (described later) is executed every 1 minute. If the next crumpling process is scheduled to continue after the end of this program, the initial hot air temperature SNEP and the initial hot air flow rate SKAZE changed by the next initial hot air flow rate selection program S400 are set in the standby state. The value is output to the operation unit 7 of the gas furnace and the operation unit 8 of the suction fan.
次にサブルーチンたる初期熱風量変更プログラムS100
について説明する。まずS101では、前回ピリオド2分経
過時の水分値(ドライベース)ZSが、ZS>0かを判断す
る。第一回目のピリオドではZSは初期値0をとっている
ため偽となり直接S103に進み、二回目以降のピリオドで
はS101の判断は真となりS102に進む。S102では、前回ピ
リオド2分経過時の水分値ZSと今回ピリオド2分経過時
(現時点)の水分値BSの差に基づく目標熱風量KAZEの変
更が次式により行われる。Next is the initial hot air flow rate change program S100 which is a subroutine
Will be described. First, in S101, it is determined whether the moisture value (dry base) ZS at the time when two minutes have passed last time is ZS> 0. In the first period, ZS has an initial value of 0, so it becomes false and the process directly proceeds to S103. In the second and subsequent periods, the determination in S101 becomes true and the process proceeds to S102. In S102, the target hot air flow rate KAZE is changed based on the difference between the moisture value ZS when the previous period 2 minutes passed and the moisture value BS when the current period 2 minutes elapsed (current time) is performed by the following equation.
DF=(BS−ZS)*K1 KAZE=KAZE+DF (K1=1.5) S103では、次回のピリオドに具えてZSにBSを代入す
る。続くS104〜S108の処理では、それ自体新規な技術で
あるところの実行茶温(実測茶温JT)と実行水分値(今
回ピリオド2分経過時(現時点)の水分値BS)による熱
風量の修正処理が行われる。まずS104では、次式により
現時点における熱風量の許容範囲を求める。これは恒率
乾燥に近似させる上で適切な熱風量は、茶葉の水分値と
温度によって、ある程度規定されるという研究結果に基
づくものである。DF = (BS-ZS) * K1 KAZE = KAZE + DF (K1 = 1.5) In S103, BS is substituted for ZS in preparation for the next period. In the subsequent processing of S104 to S108, the hot air amount is corrected by the execution tea temperature (actual measurement tea temperature JT) and the execution moisture value (the moisture value BS at the time when 2 minutes have elapsed (current time) this time), which is a new technology in itself. Processing is performed. First, in S104, the allowable range of the hot air amount at the present time is obtained by the following formula. This is based on the research result that the appropriate amount of hot air for approximating constant-rate drying is regulated to some extent by the water content and temperature of tea leaves.
H1=K2+K3*(BS−K4) +K5*(JT−K6) L1=K7+K8*(BS−K9) +K10*(JT−K11) (K2=45,K3=2.0,K4=35,K5=1.1,K6=35,K7=30,K8=
1.5,K9=35,K10=1.1,K11=35) なお上式H1,L1の右辺第2項〔K5*(JT−K6),K10*
(JT−K11)〕は、第1項に比し値が小さいため、省略
することも可能である。本実施例では精度を高めるため
採用した。そしてS105、S107で求められた熱風量の許容
範囲H1〜L1に現時点の目標熱風量KAZEが含まれているか
判断し、上方に外れている場合には、S106にて目標熱風
量KAZEに前記許容範囲の上限値H1を代入し、下方に外れ
ている場合にはS108にて同じく下限値L1を代入する。S1
09では、後述する次回初期熱風量選定プログラムS400で
利用するためにKM(初期熱風量変更プログラム終了時の
熱風量)に目標熱風量KAZEの値を、KH(一ピリオドにお
ける最大熱風量)にKAZEの値を、KL(一ピリオドの中で
最初にKMより小さくなったときの熱風量)に0を入力す
る。以上で初期熱風量変更プログラムS100の説明を終え
る。H1 = K2 + K3 * (BS-K4) + K5 * (JT-K6) L1 = K7 + K8 * (BS-K9) + K10 * (JT-K11) (K2 = 45, K3 = 2.0, K4 = 35, K5 = 1.1, K6 = 35, K7 = 30, K8 =
1.5, K9 = 35, K10 = 1.1, K11 = 35) The second term on the right side of the above formulas H1 and L1 [K5 * (JT-K6), K10 *
(JT-K11)] has a smaller value than that of the first term, and can be omitted. In this embodiment, it is adopted to improve accuracy. Then, it is determined whether or not the target hot air amount KAZE at the present time is included in the allowable range H1 to L1 of the hot air amount obtained in S105 and S107. The upper limit value H1 of the range is substituted, and if it falls below, the lower limit value L1 is similarly substituted in S108. S1
In 09, the target hot air flow rate KAZE is set to KM (the hot air flow rate at the end of the initial hot air flow rate change program) and KAZE is set to KH (the maximum hot air flow rate in one period) for use in the next initial hot air flow rate selection program S400 described later. Enter 0 for KL (the amount of hot air when it becomes smaller than KM for the first time in one period). This is the end of the description of the initial hot air flow rate changing program S100.
次にサブルーチンたる熱風温度選定プログラムS200に
ついて説明する。まずS201では、あらかじめ設定されて
いる目標茶温MTを読み出す。S202では、排気温度センサ
12の測定値を実測茶温JTとして読み出す。S203では20秒
前の実測茶温ZTが、ZT=0かを判断する。第一回目のピ
リオドでは、ZTは初期値0をとっているため真となりS2
04に進み、ZTに現在の実測茶温JTを代入する。第二回目
以降のピリオドでは、S203の判断は偽となり、S204を迂
回してS205に進む。S205では、後述する熱風量選定プロ
グラムS300で利用するためにZNEPにNEPの値を入力した
上で、S206では、次式より新たな目標熱風温度NEPを選
定する。Next, the hot air temperature selection program S200 which is a subroutine will be described. First, in S201, a preset target tea temperature MT is read. In S202, exhaust temperature sensor
Read the 12 measured values as the measured tea temperature JT. In S203, it is determined whether the measured tea temperature ZT 20 seconds ago is ZT = 0. In the first period, it becomes true because ZT has an initial value of 0, so S2
Go to 04 and substitute the current measured tea temperature JT into ZT. In the second and subsequent periods, the determination in S203 becomes false, bypassing S204 and proceeding to S205. In S205, the NEP value is input to ZNEP for use in the hot air flow rate selection program S300, which will be described later, and in S206, a new target hot air temperature NEP is selected from the following equation.
DT=K12*(JT−MT) +K13*(JT−ZT) NEP=NEP+DT (K12=1.0,K13=3.0) その後、S207では、次回の処理に具えてZTにJTを代入
する。以上で熱風温度選定プログラムS200の説明を終え
る。DT = K12 * (JT-MT) + K13 * (JT-ZT) NEP = NEP + DT (K12 = 1.0, K13 = 3.0) After that, in S207, JT is substituted into ZT for the next process. This is the end of the description of the hot air temperature selection program S200.
次にサブルーチンたる熱風量選定プログラムS300につ
いて説明する。まずS301では、基準熱風温度KNEP、実行
熱風温度に応じて風量変更量DKを算出する。本実施例で
は、実行熱風温度として目標熱風温度NEP(熱風温度の
現在値)と前回(20秒前)の目標熱風温度ZNEPを用い
て、次式より風量変更量DKを求める。Next, the hot air flow rate selection program S300 that is a subroutine will be described. First, in S301, the air volume change amount DK is calculated according to the reference hot air temperature KNEP and the execution hot air temperature. In this embodiment, the target hot air temperature NEP (current value of hot air temperature) and the target hot air temperature ZNEP of the previous time (20 seconds before) are used as the execution hot air temperature, and the air flow rate change amount DK is calculated from the following equation.
DK=K14*(NEP−KNEP) +K15*(NEP−ZNEP) (K14=0.15,K15=0.45) なお上式右辺第2項の(NEP−ZNEP)は、目標熱風温
度の変化量を表す。S302では、後述の処理のためS104と
同様に熱風量の許容範囲H1〜L1を求めておく。S303〜S3
06の処理は、それ自体新規な基準熱風温度選定プログラ
ムの一例である。本実施例では、本プログラムに必要な
実行熱風温度として目標熱風温度NEPを実行熱風量とし
て目標熱風量KAZEを利用する。まずS303にて次式を判断
する。DK = K14 * (NEP-KNEP) + K15 * (NEP-ZNEP) (K14 = 0.15, K15 = 0.45) The second term (NEP-ZNEP) on the right side of the above equation represents the amount of change in the target hot air temperature. In S302, the allowable ranges H1 to L1 of the hot air amount are calculated in the same manner as in S104 for the processing described later. S303 ~ S3
The process of 06 is an example of a novel standard hot air temperature selection program. In this embodiment, the target hot air temperature NEP is used as the execution hot air temperature required for this program, and the target hot air flow KAZE is used as the execution hot air flow rate. First, in S303, the following equation is determined.
KAZE<m1 and NEP<(KNEP−3) (m1=70,andは論理積を意味する) S303の判断の結果が真ならばS304に進んで、次式に示
すように基準熱風温度KNEPの変更を行い、偽ならばその
ままS305に進む。KAZE <m1 and NEP <(KNEP-3) (m1 = 70, and means AND) If the result of S303 is true, proceed to S304 and change the reference hot air temperature KNEP as shown in the following equation. If it is false, the process directly proceeds to S305.
KNEP=KNEP +K16*(NEP−KNEP) (K16=0.2) この処理は、熱風量KAZEが低く(m1=70%未満)、熱
風温度NEPも基準熱風温度KNEPよりも3度を超えて低い
ときは、基準熱風温度KNEPを下方に移動せる必要がある
と判断し、目標熱風温度NEPと基準熱風温度KNEPの差に
応じて、基準熱温度KNEPを変更するものである。KNEP = KNEP + K16 * (NEP-KNEP) (K16 = 0.2) This treatment is performed when the hot air volume KAZE is low (m1 = less than 70%) and the hot air temperature NEP is lower than the reference hot air temperature KNEP by more than 3 degrees. It is determined that the reference hot air temperature KNEP needs to be moved downward, and the reference heat temperature KNEP is changed according to the difference between the target hot air temperature NEP and the reference hot air temperature KNEP.
次にS305にて次式を判断する。 Next, in S305, the following equation is judged.
KAZE>m2 amd NEP>(KNEP+3) (m2=85,andは論理積を意味する) S305の判断の結果が真ならばS306に進んで次式に示す
ように基準熱風温度KNEPの変更を行い、偽ならばそのま
まS307に進む。KAZE> m2 amd NEP> (KNEP + 3) (m2 = 85, and means AND) If the result of S305 is true, proceed to S306 and change the reference hot air temperature KNEP as shown in the following equation. If false, the process directly proceeds to S307.
KNEP=KNEP +K17*(NEP−KNEP) (K17=0.2) この処理は、目標熱風量KAZEが高く(m2=85%超)、
目標熱風温度NEPも基準熱風温度KNEPよりも3度を超え
て高いときは、基準熱風温度KNEPを上方に移行させる必
要があると判断し、目標熱風温度NEPと基準熱風温度NEP
の差に応じて基準熱風温度KNEPを変更するものである。
なお上記したm1,m2の値は、全工程一貫した最大公約数
的な値であるが、これをS302で求めた熱風量の許容範囲
の上限値H1,下限値L1に応じて次式より求めてもよい。KNEP = KNEP + K17 * (NEP-KNEP) (K17 = 0.2) This process has a high target hot air volume KAZE (m2 = more than 85%),
When the target hot air temperature NEP is also higher than the reference hot air temperature KNEP by more than 3 degrees, it is determined that the reference hot air temperature KNEP needs to be moved upward, and the target hot air temperature NEP and the reference hot air temperature NEP
The reference hot air temperature KNEP is changed according to the difference of
The values of m1 and m2 described above are the values of the greatest common divisor consistent throughout the process, and are calculated from the following formula according to the upper limit value H1 and the lower limit value L1 of the allowable range of the hot air flow obtained in S302. May be.
m1=(3*H1+7*L1)/10 m2=(7*H1+3*L1)/10 続くS307〜S310の処理は、熱風量が経験的に求められ
る製茶品質上の危険値に近付くのを未然に防止するため
に行われるもので、まずS307にて次式を判断する。m1 = (3 * H1 + 7 * L1) / 10 m2 = (7 * H1 + 3 * L1) / 10 The subsequent processing of S307 to S310 will prevent the hot air volume from approaching the empirically required dangerous value for tea quality. This is done to prevent it. First, the following equation is determined in S307.
KAZE<m3 and DK<0 (m3=65,andは論理積を意味する) S307の判断の結果が真ならばS308に進んで次式に示す
ように風量変更量DKと基準熱風温度KNEPの変更を行い、
偽ならばそのままS309に進む。KAZE <m3 and DK <0 (m3 = 65, and means AND) If the result of S307 is true, proceed to S308 and change the air flow rate change amount DK and the reference hot air temperature KNEP as shown in the following equation. And then
If false, the process directly proceeds to S309.
DK=DK/2 KNEP=KNEP−1 S309では次式が判断される。DK = DK / 2 KNEP = KNEP-1 In S309, the following equation is judged.
KAZE>m4 and DK>0 (m4=90,andは論理積を意味する) S309の判断の結果が真ならばS310に進んで次式に示す
ように風量変更量DKと基準熱風温度KNEPの変更を行い、
偽ならばそのままS311に進む。KAZE> m4 and DK> 0 (m4 = 90, and means AND) If the result of S309 is true, proceed to S310 and change the air flow rate change amount DK and the reference hot air temperature KNEP as shown in the following equation. And then
If false, proceed directly to S311.
なお上記したm3,m4の値は、全工程一貫した最大公約
数的な値であるが、これをS302で求めた熱風量の許容範
囲の上限値H1,下限値L1に応じて、次式より求めてもよ
い。The values of m3 and m4 described above are the greatest common divisor values consistent throughout the process, but depending on the upper limit H1 and the lower limit L1 of the allowable range of the hot air volume obtained in S302, You may ask.
m3=(H1+9*L1)/10 m4=(9*H1+L1)/10 S311では、風量変更量DKに基づき、次式により目標熱
風量KAZEを変更する。m3 = (H1 + 9 * L1) / 10 m4 = (9 * H1 + L1) / 10 In S311, the target hot air volume KAZE is changed according to the following equation based on the air volume change amount DK.
KAZE=KAZE+DK 続くS312では、S311で選定された目標熱風量KAZEが、
S302で求められた熱風量の許容範囲H1を超えているか判
断し、真ならばS313にて、次式により強制修正量DHを算
出した後、目標熱風量KAZEにH1の値を入力する。KAZE = KAZE + DK In the subsequent S312, the target hot air volume KAZE selected in S311
It is determined whether the allowable range H1 of the hot air amount obtained in S302 is exceeded, and if true, the forced correction amount DH is calculated by the following equation in S313, and then the value of H1 is input to the target hot air amount KAZE.
DH=H1−KAZE KAZE=H1 偽ならば、S314にて、同じく目標熱風量KAZEがL1未満
かを判断し、真ならばS315にて、次式により強制修正量
DHを算出した後、目標熱風量KAZEにL1の値を入力する。DH = H1-KAZE KAZE = H1 If it is false, in S314, it is also determined whether the target hot air volume KAZE is less than L1, and if it is true, in S315, the forced correction amount is calculated by the following formula.
After calculating DH, enter the value of L1 in the target hot air volume KAZE.
DH=L1−KAZE KAZE=L1 偽ならば、直接S318に進む。S313、S315に続いて、S3
16では、次式により基準値変更量DNを算出する。DH = L1-KAZE KAZE = L1 If false, proceed directly to S318. Following S313 and S315, S3
At 16, the reference value change amount DN is calculated by the following formula.
DK=K18*DH (K18=−0.35) そしてS317では、次式により基準熱風温度KNEP,初期
基準熱風温度SKNEPを変更する。DK = K18 * DH (K18 = -0.35) Then, in S317, the reference hot air temperature KNEP and the initial reference hot air temperature SKNEP are changed by the following equations.
KNEP=KNEP+DN SKNEP=SKNEP+DN なお中揉処理中に作業者が強制的に目標熱風量KAZEを
KAZE′に修正した場合には、次式により強制修正量DHを
求め、続くS316、S317の処理を同様に行う。KNEP = KNEP + DN SKNEP = SKNEP + DN Note that the worker forcibly sets the target hot air volume KAZE during the middle kneading process.
When corrected to KAZE ′, the forced correction amount DH is obtained by the following equation, and the subsequent processing of S316 and S317 is performed in the same manner.
DH=KAZE′−KAZE すなわち強制修正量DHが正の値をとるときは、熱風量
が足りないため強制的に増加したということであり、こ
れは基準熱風温度KNEPが高過ぎることに起因することが
考えられるため、基準熱風温度KNEP及び初期基準熱風温
度SKNEPを減少する方向に補正する。逆に強制修正量DH
が負の値をとるときは、熱風量が多過ぎたため強制的に
減らしたということであり、これは基準熱風温度KNEPが
低過ぎることに起因することが考えられるため、基準熱
風温度KNEP及び初期基準熱風温度SKNEPを増加する方向
に補正する。この意味では、以上の処理も基準熱風温度
選定プログラムの一部と考えることもできる。次のS318
〜S321における処理は、後述する次回初期熱風量選定プ
ログラムS400のために、KH(一ピリオドにおける最大熱
風量)とKL(一ピリオドの中で最初に前述KMにより小さ
くなったときの熱風量)を求めるものである。以上で、
熱風量選定プログラムS300の説明を終える。DH = KAZE'-KAZE That is, when the forced correction amount DH takes a positive value, it means that the hot air volume was forcibly increased because it was insufficient. This is because the reference hot air temperature KNEP is too high. Therefore, the reference hot air temperature KNEP and the initial reference hot air temperature SKNEP are corrected to decrease. Conversely, the forced correction amount DH
Is a negative value, it means that the amount of hot air was too large, so it was forcibly reduced.This may be because the reference hot air temperature KNEP is too low. Correct the reference hot air temperature SKNEP in the increasing direction. In this sense, the above processing can be considered as part of the reference hot air temperature selection program. Next S318
The process in S321 is to set KH (maximum hot air amount in one period) and KL (hot air amount when it becomes smaller by KM first in one period) for the next initial hot air amount selection program S400 described later. It is what you want. Above,
This completes the explanation of the hot air flow rate selection program S300.
次にサブルーチンたる次回初期熱風量選定プログラム
S400について説明する。まずS401では次式を判断し、真
ならばS402へ、偽ならばS403へ進む。Program for selecting next initial hot air volume which is a subroutine
The S400 will be described. First, in S401, the following expression is determined. If true, the process proceeds to S402, and if false, the process proceeds to S403.
KM≦KH S402では、次式にて次回の初期熱風量SKAZEを算出す
る。In KM ≦ KH S402, calculate the next initial hot air flow rate SKAZE by the following formula.
SKAZE=(KM+KH)/2 S403では、次式にて次回の初期熱風量SKAZEを算出す
る。SKAZE = (KM + KH) / 2 In S403, calculate the next initial hot air volume SKAZE using the following formula.
SKAZE=(KM+KL)/2 以上で次回初期熱風量選定プログラムS400の説明を終
える。SKAZE = (KM + KL) / 2 With the above, the explanation of the next initial hot air flow rate selection program S400 is completed.
以上のように熱風供給プログラムによれば、茶葉の投
入から取り出しまでの間に熱風温度は茶温を所定値に維
持するため茶葉の乾燥とともに減少する方向に推移し、
熱風温度が減少すればその度合いに応じて熱風量も減少
していく。前記度合いは基準熱風温度KNEPを利用して求
めるが、この基準熱風温度KNEPは工程中、茶葉、その他
の条件に応じて徐々に減少していく。また本工程に投入
される茶葉の性状が同一ならば、本プログラムが回数を
重ねるにつれて初期基準熱風温度SKNEPは適切な値に集
束されていく。これらが相乗的に作用して、茶葉に対し
供給される熱風温度、熱風量は、常にバランスをもった
適切な値に維持されるのである。As described above, according to the hot air supply program, the hot air temperature changes in the direction of decreasing with the drying of the tea leaves in order to maintain the tea temperature at a predetermined value during the period from the introduction of the tea leaves to the removal thereof.
When the hot air temperature decreases, the hot air amount also decreases according to the degree. The degree is determined by using the reference hot air temperature KNEP, and this reference hot air temperature KNEP gradually decreases according to the tea leaves and other conditions during the process. If the properties of the tea leaves fed to this process are the same, the initial reference hot air temperature SKNEP will be converged to an appropriate value as the number of times this program is repeated. These act synergistically, and the hot air temperature and the hot air amount supplied to the tea leaves are always maintained at appropriate values with a balance.
次に工程が前後で二分され、それぞれで目標茶温MTが
MT1、MT2と異なって設定されている場合について説明す
る。この場合もプログラムの流れはほとんど同じであ
り、ただ目標茶温MTがMT1からMT2に移行したときに、次
式による割込処理により目標熱風温度NEPを変更する。Next, the process is divided into two parts, the target tea temperature MT for each.
The case where it is set differently from MT1 and MT2 will be described. In this case as well, the flow of the program is almost the same. However, when the target tea temperature MT shifts from MT1 to MT2, the target hot air temperature NEP is changed by the interrupt process according to the following equation.
DT=MT2−MT1 NEP=NEP+K19*DT (K19=7.0) この処理は工程中、作業者が強制的に目標茶温MTを変
更した場合にも利用される。なお前工程の目標茶温MT
(工程開始直後の目標茶温MT)が変更された場合には、
変更量を同様にDTとして、初期基準熱風温度SKNEPにつ
いても、次式で変更する。DT = MT2-MT1 NEP = NEP + K19 * DT (K19 = 7.0) This process is also used when the operator forcibly changes the target tea temperature MT during the process. The target tea temperature MT in the previous process
If the target tea temperature MT immediately after the start of the process is changed,
The amount of change is also set as DT, and the initial reference hot air temperature SKNEP is also changed by the following formula.
SKNEP=SKNEP+K20*DT (K20=7.0) 以上、本発明の実施例を説明したが、本発明の実施に
あたっては、本実施例のほかにも本発明の要旨の範囲内
において種々の応用が可能である。SKNEP = SKNEP + K20 * DT (K20 = 7.0) The embodiments of the present invention have been described above. However, in implementing the present invention, various applications are possible within the scope of the present invention in addition to the embodiments. is there.
《発明の効果》 本発明の製茶工程における熱風供給方法によれば、目
標熱風温度を目標茶温と実測茶温に応じて選定すること
により茶温を目標値に保ちつつ、実行熱風温度と実行茶
葉水分値に応じて適切な目標熱風量を選定するため、目
標熱風温度と目標熱風量とがバランス良く茶葉の状態に
適合しながら推移し、製茶品質が向上する。<Effects of the Invention> According to the hot air supply method in the tea making process of the present invention, the target hot air temperature is selected according to the target tea temperature and the actually measured tea temperature, thereby maintaining the tea temperature at the target value and performing the hot air temperature execution. Since an appropriate target hot air flow rate is selected according to the tea leaf moisture value, the target hot air temperature and the target hot air flow rate change in a well-balanced manner while adapting to the state of the tea leaf, thus improving tea production quality.
第1図は本発明の実施例装置を簡潔に示す正面図、第2
図〜第6図は本発明の実施例プログラムを示す流れ図で
あり、第2図は熱風供給プログラムを示す流れ図、第3
図は初期熱風量変更プログラムを示す流れ図、第4図は
熱風温度選定プログラムを示す流れ図、第5図は熱風量
選定プログラムを示す流れ図、第6図は初回初期熱風量
選定プログラムを示す流れ図である。 1;中揉機 2;胴 3;揉手 4;主軸 5;ガス火炉 6;吸引ファン 7;ガス火炉の操作部 8;吸引ファンの操作部 9;ガスバーナ 10;熱風温度センサ 11;水分センサ 12;排気温度センサ 13;熱風制御部 14;外気取込口 15;排出口 S100;初期熱風量変更プログラム S200;熱風温度選定プログラム S300;熱風量選定プログラム S400;次回初期熱風量選定プログラム T;カウンタ BS;今回ピリオド2分経過時(現時点)の水分値(実行
水分値) DK;風量変更量 DH;強制修正量 DN;基準値変更量 DT;変更量 H1〜L1;熱風量の許容範囲(H1;上限値、L1;下限値) JT;実測茶温 KAZE;目標熱風量 KH;一ピリオドにおける最大熱風量 KL;一ピリオドの中で最初にKMより小さくなったときの
熱風量 KM;初期熱風量変更プログラム終了時の熱風量 KNEP;基準熱風温度 MT;目標茶温 NEP;目標熱風温度 SKAZE;初期熱風量 SKNEP;初期基準熱風温度 SNEP;初期熱風温度 ZNEP;前回(20秒前)の目標熱風温度 ZS;前回ピリオド2分経過時の水分値(ドライベース) ZT;20秒前の実測茶温FIG. 1 is a front view briefly showing an apparatus according to an embodiment of the present invention, and FIG.
FIG. 6 to FIG. 6 are flow charts showing an embodiment program of the present invention, and FIG. 2 is a flow chart showing a hot air supply program, and FIG.
FIG. 4 is a flow chart showing an initial hot air flow rate changing program, FIG. 4 is a flow chart showing a hot air flow rate selecting program, FIG. 5 is a flow chart showing a hot air flow rate selecting program, and FIG. 6 is a flow chart showing a first initial hot air flow rate selecting program. . 1; Middle kneading machine 2; Body 3; Rubbing hand 4; Main shaft 5; Gas furnace 6; Suction fan 7; Gas furnace operation part 8; Suction fan operation part 9; Gas burner 10; Hot air temperature sensor 11; Moisture sensor 12; Exhaust temperature sensor 13; Hot air control unit 14; Outside air intake 15; Outlet S100; Initial hot air flow rate change program S200; Hot air temperature selection program S300; Hot air flow rate selection program S400; Next initial hot air flow rate selection program T; Counter BS; Moisture value (actual moisture value) after 2 minutes (current time) from this period DK; Air volume change amount DH; Forced correction amount DN; Reference value change amount DT; Change amount H1 to L1; Allowable range of hot air volume (H1; Upper limit) Value, L1; lower limit value) JT; measured tea temperature KAZE; target hot air volume KH; maximum hot air volume in one period KL; hot air volume when it becomes smaller than KM first in one period KM; initial hot air volume change program Hot air volume at the end KNEP; Reference hot air temperature MT; Target tea temperature NEP; Target hot air temperature SKAZE; Initial hot air flow SKNEP; Initial reference heat Temperature SNEP; initial hot air temperature ZNEP; previous period 2 minutes elapsed time the moisture content (dry basis) ZT;; previous target hot air temperature ZS (20 seconds before) 20 seconds before the actual tea warm
Claims (2)
程において、目標茶温と実測茶温に応じて目標熱風温度
を選定する熱風温度選定プログラムと、実行熱風温度と
実行茶葉水分値に応じて目標熱風量を選定する熱風量選
定プログラムを具えた、製茶工程における熱風供給方
法。1. A hot-air temperature selection program for selecting a target hot-air temperature according to a target tea temperature and an actually-measured tea temperature in a tea-making process in which hot air is applied to tea leaves to be dried, and an execution hot-air temperature and an execution tea-leaf moisture value are set. A hot air supply method in a tea making process, which includes a hot air flow rate selection program for selecting a target hot air flow rate according to the target hot air flow rate.
程において、目標茶温と実測茶温に応じて目標熱風温度
を選定する熱風温度選定プログラムと、実行熱風温度と
実行茶葉水分値に応じて目標熱風量を選定する熱風量選
定プログラムを具え、熱風量選定プログラムは、実行熱
風温度に応じて算出された目標熱風量が実行茶葉水分値
に応じて求められる熱風量の許容範囲を外れるとき目標
熱風量を任意の値に修正するように構成されている、製
茶工程における熱風供給方法。2. A hot-air temperature selection program for selecting a target hot-air temperature according to a target tea temperature and an actually-measured tea temperature in a tea-making process in which hot air is applied to tea leaves to dry them, and an execution hot-air temperature and an execution tea-leaf moisture value are set. According to the hot air flow rate selection program, the target hot air flow rate calculation program selects the target hot air flow rate according to the execution hot air flow temperature, and the target hot air flow rate deviates from the allowable range of the hot air flow rate determined according to the execution tea leaf moisture value. At this time, the hot air supply method in the tea making process is configured to correct the target hot air amount to an arbitrary value.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1303579A JPH0813241B2 (en) | 1989-11-22 | 1989-11-22 | Hot air supply method in tea making process |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1303579A JPH0813241B2 (en) | 1989-11-22 | 1989-11-22 | Hot air supply method in tea making process |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH03164133A JPH03164133A (en) | 1991-07-16 |
JPH0813241B2 true JPH0813241B2 (en) | 1996-02-14 |
Family
ID=17922703
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1303579A Expired - Fee Related JPH0813241B2 (en) | 1989-11-22 | 1989-11-22 | Hot air supply method in tea making process |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0813241B2 (en) |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6439943A (en) * | 1987-08-04 | 1989-02-10 | Toyo Denso Kogyo Kk | Rolling apparatus for tea-processing |
-
1989
- 1989-11-22 JP JP1303579A patent/JPH0813241B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH03164133A (en) | 1991-07-16 |
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