JPH03100439A - Method for controlling microwave heating and drying machine - Google Patents

Method for controlling microwave heating and drying machine

Info

Publication number
JPH03100439A
JPH03100439A JP23698589A JP23698589A JPH03100439A JP H03100439 A JPH03100439 A JP H03100439A JP 23698589 A JP23698589 A JP 23698589A JP 23698589 A JP23698589 A JP 23698589A JP H03100439 A JPH03100439 A JP H03100439A
Authority
JP
Japan
Prior art keywords
weight
heated
microwave
substance
drying
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.)
Pending
Application number
JP23698589A
Other languages
Japanese (ja)
Inventor
Taketeru Noguchi
武揮 野口
Masahiko Ichikawa
市川 昌彦
Osamu Kumazaki
脩 熊崎
Masaaki Yanagi
正明 柳
Takemi Nakane
中根 武美
Kenichiro Kinoshita
木下 健一郎
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.)
Chubu Electric Power Co Inc
Mitsubishi Heavy Industries Ltd
Original Assignee
Chubu Electric Power Co Inc
Mitsubishi Heavy Industries Ltd
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 Chubu Electric Power Co Inc, Mitsubishi Heavy Industries Ltd filed Critical Chubu Electric Power Co Inc
Priority to JP23698589A priority Critical patent/JPH03100439A/en
Publication of JPH03100439A publication Critical patent/JPH03100439A/en
Pending legal-status Critical Current

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  • Drying Of Solid Materials (AREA)

Abstract

PURPOSE:To stably dry a substance to be heated by detecting the weight of the substance to be heated, calculating a weight decreasing speed, discriminating a shifting time to decreasing rate drying from constant rate drying and lowering microwave output from the shifting time. CONSTITUTION:The substance to be heated in a sample dish 4 is rotated by a turntable 5 and irradiated with the microwave which is radiated from a microwave generator 2 and dispersed by a microwave dispersion plate 3 so as to be heated and dried. Then, the weight of the substance to be heated which is decreased by heating is measured momently by a scale 6 and a weight signal is transmitted to a controller 10. The controller 10 momently calculates the weight decreasing speed of the substance to be heated from the weight of the substance to be heated and compares it with the maximum value of the weight decreasing speed. When the weight decreasing speed becomes equal to or below a proper value which is <=90% of the maximum weight speed, the controller 10 lowers the microwave output. Furthermore, when it becomes <=75% thereof and a decreasing rate drying area is obtained, the controller 10 lowers the microwave output to 35% of the maximum output. Thus, stable drying without burning the inflammable substance to be heated is accomplished.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、石炭等の乾燥に適用されるマイクロ波加熱乾
燥機制御方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for controlling a microwave heating dryer applied to drying coal and the like.

〔従来の技術〕[Conventional technology]

従来のマイクロ波加熱乾燥機の制御方法においては、重
量センサーにより検出した重量減少速度から加熱時間を
算出して乾燥時間を制御する方法があった。また、赤外
線温度計により被加熱物の温度を検出してマイクロ波を
制御する方法があった。
In the conventional method of controlling a microwave heating dryer, there has been a method of controlling the drying time by calculating the heating time from the weight reduction rate detected by a weight sensor. There is also a method of controlling microwaves by detecting the temperature of the object to be heated using an infrared thermometer.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

従来の乾燥機制御方法において、重量減少速度から加熱
時間を制御する方法においては、食品の加熱又は炊飯等
あらかじめ蒸発水分が把握されているものには有効であ
る。しかし、水分が未知のものを乾燥する場合1.情事
乾燥域の乾燥時間の設定が不可能であり、また減率乾燥
域に入って、被加熱物の温度が上昇し被加熱物が分解、
横坑する欠点があった。
In the conventional dryer control method, the method of controlling the heating time based on the rate of weight loss is effective for heating foods, cooking rice, etc. where evaporated moisture is known in advance. However, when drying something whose moisture content is unknown, 1. It is impossible to set the drying time in the drying area, and when the lapse rate drying area is entered, the temperature of the heated object increases and the heated object decomposes.
It had the disadvantage of being a horizontal mine.

また、赤外線により被加熱物の温度を検出し、マイクロ
波出力を制御する方法においては、被加熱物の表面がな
めらかで、かつ、含有水分が均一な場合は有効である。
Furthermore, the method of detecting the temperature of the object to be heated using infrared rays and controlling the microwave output is effective when the surface of the object to be heated is smooth and the moisture content is uniform.

しかし、粒、塊状又は表面に凹凸がある場合には、表面
温度が一定とならず温度分布を生ずるため、ターンテー
ブル上の被加熱物を赤外線温度計で検出した場合温度変
動が大きく、検出した温度はマイクロ波制御信号として
は不適であり、この温度によって適切な制御が行えない
ことがあった。
However, if the object is grainy, clumpy, or uneven on the surface, the surface temperature will not be constant and a temperature distribution will occur, so when the object to be heated on the turntable is detected with an infrared thermometer, there will be large temperature fluctuations. Temperature is not suitable as a microwave control signal, and appropriate control may not be possible depending on this temperature.

本発明は上記の課題を解決しようとするものである。The present invention seeks to solve the above problems.

〔課題を解決するための手段〕[Means to solve the problem]

本発明のマイクロ波加熱乾燥機制御方法は、マイクロ波
により加熱される被加熱物の重量を検出し、同検出した
重量より重量減少速度を演算し、恒率乾燥より減率乾燥
への移行時点を同重量減少速度の変化より判別し、同移
行時点よりマイクロ波出力を低下させることを特徴とし
ている。
The microwave heating dryer control method of the present invention detects the weight of the object to be heated by microwaves, calculates the weight loss rate from the detected weight, and determines the point at which the transition from constant rate drying to decreasing rate drying occurs. The system is characterized in that it is determined based on the change in the rate of weight loss, and the microwave output is reduced from the point at which the weight changes.

〔作用〕[Effect]

上記において、マイクロ波により加熱され、時々刻々減
少する重量は重量計により検出され、重量信号が制御装
置へ送られる。上記制御装置は、重量信号より時々刻々
の重量減少速度を演算し、同重量減少速度の変化より被
加熱物の乾燥状態が恒率乾燥より減率乾燥へ移行する移
行時点を判別する。上記制御装置は上記移行時点を判別
すると、マイクロ波発生器へ制御信号を送り、マイクロ
波出力を低下させる。
In the above, the weight, which is heated by microwaves and decreases moment by moment, is detected by a weighing scale, and a weight signal is sent to a control device. The control device calculates the rate of weight decrease from moment to moment based on the weight signal, and determines the point in time when the drying state of the heated object shifts from constant rate drying to decreasing rate drying based on changes in the same weight decrease rate. When the controller determines the transition point, it sends a control signal to the microwave generator to reduce the microwave output.

上記により、被加熱物の乾燥状態が減率乾燥へ移行する
とマイクロ波出力を低下させるため、可燃性の被加熱物
の横坑させることのない安定した乾燥が可能となった。
As a result of the above, when the drying state of the heated object shifts to lapse rate drying, the microwave output is lowered, making it possible to stably dry the flammable heated object without causing it to cross.

〔実施例〕〔Example〕

本発明の一実施例に用いる装置を第1図により説明する
An apparatus used in an embodiment of the present invention will be explained with reference to FIG.

第1図に示す本実施例に用いる装置において、lは排気
ファン7を有する空気排出口9と空気取入口8と赤外線
温度計11が設けられた加熱器本体、2は同加熱器本体
l内の上部に設けられ試料を加熱するための熱源である
マイクロ波発生器、3は同マイクロ波発生器の下方に設
けられマイクロ波の集中を防止する回転翼からなるマイ
クロ波分散板、6は上記加熱器本体1内下部に設けられ
た重量計、5は同重量計6の上部に設けられ上面に被加
熱物を入れる試料皿4が配設され被加熱物を均等に加熱
するためのターンテーブル、また、IOは上記重量計6
より重量信号を入力しマイクロ波発生器2へItiII
?111信号を出力する制御装置である。
In the apparatus used in this embodiment shown in FIG. 1, l is a heater main body provided with an air outlet 9 having an exhaust fan 7, an air intake port 8, and an infrared thermometer 11, and 2 is an interior of the heater main body l. 3 is a microwave generator which is a heat source for heating the sample, and 3 is a microwave dispersion plate, which is a rotary blade, which is installed below the microwave generator to prevent concentration of microwaves. 6 is the above-mentioned A weighing scale 5 is provided at the lower part of the heater body 1, and a turntable 5 is provided on the upper part of the weighing scale 6, and a sample plate 4 for placing the object to be heated is disposed on the upper surface to uniformly heat the object. , and IO is the weight scale 6 mentioned above.
Input the weight signal to the microwave generator 2.
? This is a control device that outputs a 111 signal.

本実施例においては、試料皿4に入った被加熱物は、タ
ーンテーブル5により回転しながら、マイクロ波発生器
2が放射しマイクロ波分散板3により分散されたマイク
ロ波が照射され、加熱乾燥される。
In this embodiment, the object to be heated in the sample dish 4 is rotated by the turntable 5 and irradiated with microwaves emitted by the microwave generator 2 and dispersed by the microwave dispersion plate 3, and then heated and dried. be done.

上記被加熱物を加熱乾燥するマイクロ波加熱乾燥機の制
御は、次の手順で行われる。まず、加熱により減少する
被加熱物の重量が重量計6によって時々刻々計測され、
重量信号が制御装置10に送信される。同制御装置10
は、重量計6から送信される被加熱物重量より被加熱物
の重量減少速度を時々刻々演算し、重量減少速度の最高
値と比較し、重量減少速度が最高重量減少速度の90%
以下の適当な値以下になった時点をもって、マイクロ波
出力を低下させる制御信号をマイクロ波発生器2に送信
し、マイクロ波出力を低下させる。更に、重量減少速度
が最高重量減少速度の75%以下になり恒率乾燥域から
減率乾燥域に入った時点をもって、被加熱物を分解、横
坑させないためにマイクロ波出力を最高出力の35%に
低下させる。
The microwave heating dryer for heating and drying the object to be heated is controlled by the following procedure. First, the weight of the object to be heated, which decreases due to heating, is measured moment by moment by a weighing scale 6.
A weight signal is sent to the control device 10. The control device 10
calculates the weight reduction rate of the heated object from time to time based on the weight of the heated object transmitted from the scale 6, compares it with the maximum weight reduction speed, and determines that the weight reduction speed is 90% of the maximum weight reduction speed.
A control signal for reducing the microwave output is sent to the microwave generator 2 at the point when the value falls below the appropriate value below, thereby reducing the microwave output. Furthermore, at the point when the weight reduction rate becomes 75% or less of the maximum weight reduction rate and enters the reduction rate drying area from the constant rate drying area, the microwave output is increased to 35% of the maximum output in order to prevent the heated material from decomposing and collapsing. %.

上記により、可燃性の被加熱物を横坑させることのない
安定した乾燥が可能となった。
As a result of the above, stable drying without causing combustible materials to be heated is allowed to occur.

次に本実施例に用いる装置により行った乾燥試験とその
結果について説明する。
Next, a drying test conducted using the apparatus used in this example and its results will be explained.

上記乾燥試験に用いた被加熱物は50m1φ以下の粒塊
炭1500gであり、その試験結果を第2図に示す、第
2図は、重量計6からの信号を制御装置10に内蔵した
演算器に入力して1分ごとの重量変化から重量減少速度
を演算し、最高重量減少速度の75%以下になった時点
でマイクロ波出力を80%(120ow、最高1500
W)から35%に低下させる方法でマイクロ波発生器2
の出力を制御した場合の重量減少曲線及び被加熱物の温
度曲線を示しており、被加熱物の温度を減率乾燥域にお
いても極めて安定したものとすることが可能であること
が判る。
The object to be heated used in the drying test was 1,500 g of granular coal with a size of 50 m1φ or less, and the test results are shown in FIG. 2. The weight loss rate is calculated from the weight change every minute, and when the weight decrease rate is 75% or less of the maximum weight loss rate, the microwave output is reduced to 80% (120OW, maximum 1500OW).
Microwave generator 2 with a method of reducing W) to 35%
The figure shows a weight loss curve and a temperature curve of the heated object when the output of the heated object is controlled, and it is seen that it is possible to make the temperature of the heated object extremely stable even in the lapse rate drying region.

なお、従来の制御方法である赤外線温度計の検出温度に
よりマイクロ波出力を制御した乾燥試験の結果を第3図
に示す。上記乾燥試験においては、被加熱物の温度の制
御温度を150℃に設定し、マイクロ波出力の制限を8
0%とした。被加熱物が減率乾燥域となり、マイクロ波
の制御が開始されると、微少温度変化でマイクロ波出力
が大きく変化し、マイクロ波出力の変化により埋戻への
電波集中が起り、温度分布が大きく変化して制御不能と
なった。また電波集中が起った部分は分解1発煙を起し
、正常な乾燥が不可能であった。
Note that FIG. 3 shows the results of a drying test in which the microwave output was controlled by the temperature detected by an infrared thermometer, which is a conventional control method. In the above drying test, the control temperature of the heated object was set at 150°C, and the microwave output limit was set at 8°C.
It was set to 0%. When the object to be heated reaches the lapse rate drying region and microwave control is started, the microwave output changes greatly due to slight temperature changes, and the change in microwave output causes radio waves to concentrate on the backfill, causing the temperature distribution to change. Things have changed so much that it's out of control. In addition, areas where radio wave concentration occurred caused decomposition and smoke, making normal drying impossible.

上記第2図及び第3図より、被加熱物の加熱乾燥を重量
減少速度を演算しながら行い、減率乾燥域に入るとそれ
を判別してマイクロ波出力を低下させることにより、従
来は困難であった可燃性の被加熱物の損焼させることの
ない安定した乾燥ができるようになることが判る。
As shown in Figures 2 and 3 above, heating and drying of the heated object is performed while calculating the weight loss rate, and when it enters the loss rate drying region, it is determined and the microwave output is lowered, which is difficult to do in the past. It can be seen that stable drying can be performed without causing damage to the flammable heated object.

〔発明の効果〕〔Effect of the invention〕

本発明のマイクロ波加熱乾燥機制御方法は、被加熱物の
重量を検出し、重量減少速度を演算し、同重量減少速度
の変化より恒率乾燥より減率乾燥への移行時点を判別し
、同移行時点よりマイクロ波出力を低下させることによ
って、可燃性の被加熱物の損焼させることのない安定し
た乾燥が可能となった。
The microwave heating dryer control method of the present invention detects the weight of the object to be heated, calculates the weight reduction rate, and determines the transition point from constant rate drying to lapse rate drying based on the change in the weight reduction rate, By lowering the microwave output from this transition point, stable drying of flammable objects to be heated without burning them became possible.

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

第1図は本発明の一実施例に用いられる装置の説明図、
第2図は上記一実施例による加熱乾燥結果の説明、第3
図は従来の方法による加熱乾燥結果の説明図である。 1・・・加熱器本体、 2・・・マイクロ波発生器、3
・・・マイクロ波分散板、 4・・・試料皿、5・・・
ターンテーブル、 6・・・重量計、7・・・排気ファ
ン、 8・・・空気取入口、9・・・空気排出口、 1
0・・・制御装置、11・・・赤外線温度計。 荊1閉
FIG. 1 is an explanatory diagram of an apparatus used in an embodiment of the present invention;
Figure 2 is an explanation of the heat drying results according to the above example;
The figure is an explanatory diagram of the results of heat drying by a conventional method. 1... Heater main body, 2... Microwave generator, 3
...Microwave dispersion plate, 4...Sample dish, 5...
Turntable, 6... Weight scale, 7... Exhaust fan, 8... Air intake port, 9... Air outlet port, 1
0...Control device, 11...Infrared thermometer. 1 close

Claims (1)

【特許請求の範囲】[Claims] マイクロ波により加熱される被加熱物の重量を検出し、
同検出した重量より重量減少速度を演算し、恒率乾燥よ
り減率乾燥への移行時点を同重量減少速度の変化より判
別し、同移行時点よりマイクロ波出力を低下させること
を特徴とするマイクロ波加熱乾燥機制御方法。
Detects the weight of the object heated by microwaves,
The microprocessor is characterized in that the weight loss rate is calculated from the detected weight, the time point of transition from constant rate drying to loss rate drying is determined from the change in the same weight loss rate, and the microwave output is reduced from the time of the same transition point. Wave heating dryer control method.
JP23698589A 1989-09-14 1989-09-14 Method for controlling microwave heating and drying machine Pending JPH03100439A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23698589A JPH03100439A (en) 1989-09-14 1989-09-14 Method for controlling microwave heating and drying machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23698589A JPH03100439A (en) 1989-09-14 1989-09-14 Method for controlling microwave heating and drying machine

Publications (1)

Publication Number Publication Date
JPH03100439A true JPH03100439A (en) 1991-04-25

Family

ID=17008686

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23698589A Pending JPH03100439A (en) 1989-09-14 1989-09-14 Method for controlling microwave heating and drying machine

Country Status (1)

Country Link
JP (1) JPH03100439A (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003509679A (en) * 1999-09-17 2003-03-11 シーイーエム・コーポレーション How to correct weighing errors during microwave heating
JP2004502169A (en) * 2000-06-28 2004-01-22 シーイーエム・コーポレーション Microwave assisted content analyzer
JP2007292764A (en) * 2006-04-25 2007-11-08 Mettler-Toledo Ag Measuring device for moisture weight measurement
JP2008020448A (en) * 2006-07-07 2008-01-31 Mettler-Toledo Ag Measuring device for gravimetric moisture determination
JP2008026315A (en) * 2006-07-07 2008-02-07 Mettler-Toledo Ag Weight measurement type moisture content measuring apparatus
JP2011007809A (en) * 1998-09-17 2011-01-13 Cem Corp Method and apparatus for measuring volatile content
JP2011123030A (en) * 2009-12-14 2011-06-23 Ohbayashi Corp Method for confirming dry state of cement composition
CN102980833A (en) * 2012-11-29 2013-03-20 华南理工大学 Microwave heating weight detection device
CN110160320A (en) * 2018-02-12 2019-08-23 中冶长天国际工程有限责任公司 A kind of sintering fuel deep bed sintering method for microwave drying and device
CN110160329A (en) * 2018-02-12 2019-08-23 中冶长天国际工程有限责任公司 A kind of intelligent control method and device of the dry terminal of sintering fuel

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51136489A (en) * 1975-05-22 1976-11-25 Toshiba Corp Microwave heating moisture measuring device
JPS55141654A (en) * 1979-04-21 1980-11-05 Fujisash Co Moisture measuring method using high-frequency dielectric drying and its apparatus

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51136489A (en) * 1975-05-22 1976-11-25 Toshiba Corp Microwave heating moisture measuring device
JPS55141654A (en) * 1979-04-21 1980-11-05 Fujisash Co Moisture measuring method using high-frequency dielectric drying and its apparatus

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011007809A (en) * 1998-09-17 2011-01-13 Cem Corp Method and apparatus for measuring volatile content
JP2003509679A (en) * 1999-09-17 2003-03-11 シーイーエム・コーポレーション How to correct weighing errors during microwave heating
JP4908707B2 (en) * 1999-09-17 2012-04-04 シーイーエム・コーポレーション How to correct gravimetric error during microwave heating
JP2004502169A (en) * 2000-06-28 2004-01-22 シーイーエム・コーポレーション Microwave assisted content analyzer
JP4684529B2 (en) * 2000-06-28 2011-05-18 シーイーエム・コーポレーション Microwave assisted content analyzer
JP2012168202A (en) * 2006-04-25 2012-09-06 Mettler-Toledo Ag Measuring device for moisture weight measurement
JP2007292764A (en) * 2006-04-25 2007-11-08 Mettler-Toledo Ag Measuring device for moisture weight measurement
JP2008026315A (en) * 2006-07-07 2008-02-07 Mettler-Toledo Ag Weight measurement type moisture content measuring apparatus
JP2008020448A (en) * 2006-07-07 2008-01-31 Mettler-Toledo Ag Measuring device for gravimetric moisture determination
JP2011123030A (en) * 2009-12-14 2011-06-23 Ohbayashi Corp Method for confirming dry state of cement composition
CN102980833A (en) * 2012-11-29 2013-03-20 华南理工大学 Microwave heating weight detection device
CN110160320A (en) * 2018-02-12 2019-08-23 中冶长天国际工程有限责任公司 A kind of sintering fuel deep bed sintering method for microwave drying and device
CN110160329A (en) * 2018-02-12 2019-08-23 中冶长天国际工程有限责任公司 A kind of intelligent control method and device of the dry terminal of sintering fuel
CN110160320B (en) * 2018-02-12 2020-08-28 中冶长天国际工程有限责任公司 Microwave drying method and device for thick sintering fuel layer
CN110160329B (en) * 2018-02-12 2021-03-05 中冶长天国际工程有限责任公司 Intelligent control method and device for drying end point of sintering fuel

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