JPH054591B2 - - Google Patents
Info
- Publication number
- JPH054591B2 JPH054591B2 JP30748990A JP30748990A JPH054591B2 JP H054591 B2 JPH054591 B2 JP H054591B2 JP 30748990 A JP30748990 A JP 30748990A JP 30748990 A JP30748990 A JP 30748990A JP H054591 B2 JPH054591 B2 JP H054591B2
- Authority
- JP
- Japan
- Prior art keywords
- hot air
- grain
- temperature
- drying
- chamber
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 238000001035 drying Methods 0.000 claims description 35
- 238000000034 method Methods 0.000 claims description 10
- 235000013339 cereals Nutrition 0.000 description 42
- 235000013405 beer Nutrition 0.000 description 9
- 241000209219 Hordeum Species 0.000 description 6
- 235000007340 Hordeum vulgare Nutrition 0.000 description 6
- 239000000446 fuel Substances 0.000 description 4
- 241000209140 Triticum Species 0.000 description 3
- 235000021307 Triticum Nutrition 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000002828 fuel tank Substances 0.000 description 2
- 238000005303 weighing Methods 0.000 description 2
- 238000004364 calculation method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000010981 drying operation Methods 0.000 description 1
- 230000035784 germination Effects 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000002250 progressing effect Effects 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、穀物乾燥装置における穀粒温度の測
定方法に係るものである。DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a method for measuring grain temperature in a grain drying device.
(従来技術)
従来、穀物乾燥装置において穀物温度を計測器
により計測する方法は周知である。(Prior Art) Conventionally, a method of measuring grain temperature using a measuring device in a grain drying apparatus is well known.
(発明が解決しようとする問題点)
しかし、穀物温度を計測器により直接計測する
という方法は、穀粒の密度が濃い場合と薄い場合
とで相違し、穀粒の密度が濃い場合は高く表わ
れ、穀粒の密度が薄い場合は低く表われるから、
正確を欠く。(Problem to be solved by the invention) However, the method of directly measuring grain temperature with a measuring device differs depending on whether the grain is dense or thin, and when the grain is dense, the temperature is higher. However, if the density of the grain is low, it will appear low.
lack accuracy.
そこで、本発明は、熱風供給温度と、熱風排風
温度の差から、これを求めるようにしたものであ
る。 Therefore, in the present invention, this is determined from the difference between the hot air supply temperature and the hot air exhaust temperature.
この求めかたによると、数式に定数を用いるこ
とにより、最も能率のよい乾燥をすることができ
る。 According to this calculation method, the most efficient drying can be achieved by using constants in the formula.
(問題を解決するための手段)
よつて、本発明は、流下式乾燥室9と、該流下
式乾燥室9に熱風を供給する熱風供給室10と、
前記流下式乾燥室9より排風される熱風排風室1
1とを供えたものにおいて、前記熱風供給室10
内には熱風温度センサaを前記熱風排風室内には
排風温度センサbをそれぞれ取付け、前記両セン
サabの測定値から穀粒温度を想定する穀物穀物
装置における穀粒温度の測定方法としたものであ
る。(Means for Solving the Problem) Therefore, the present invention provides a downstream type drying chamber 9, a hot air supply chamber 10 that supplies hot air to the downstream type drying chamber 9,
Hot air exhaust chamber 1 from which air is discharged from the downstream drying chamber 9
1, in which the hot air supply chamber 10
A method of measuring grain temperature in a grain grain machine is to install a hot air temperature sensor a inside the hot air exhaust chamber and an exhaust air temperature sensor b inside the hot air exhaust chamber, and assume the grain temperature from the measured values of both sensors a and b. It is something.
(実施例)
本発明の方法を実施しうる装置の一例を図面に
より説明すると、1は重量計2上に載置した集穀
部であつて、左右一対の流入部3,3を有し、流
入部3,3の下方にはそれぞれ回転弁4,4を設
け、その下側を受樋5で包囲し、該受樋5の中央
上面に螺旋コンベア6を横設する。(Example) An example of an apparatus capable of carrying out the method of the present invention will be described with reference to the drawings. Reference numeral 1 denotes a grain collection section placed on a weighing scale 2, which has a pair of left and right inflow sections 3, 3, Rotary valves 4, 4 are provided below the inflow portions 3, 3, respectively, the lower sides of which are surrounded by a receiving gutter 5, and a spiral conveyor 6 is installed horizontally on the central upper surface of the receiving gutter 5.
7は集穀部1の上部に載置した乾燥部であり、
下方排出口8,8を前記流入部3,3上に一致さ
せた左右一対の流下式乾燥室9,9を形成する。
該流下式乾燥室9,9の間には熱風供給室10を
形成し、流下式乾燥室9,9の外側には熱風排風
室11,11を形成する。 7 is a drying section placed on the upper part of the grain collection section 1;
A pair of left and right downstream drying chambers 9, 9 are formed with lower discharge ports 8, 8 aligned above the inflow portions 3, 3.
A hot air supply chamber 10 is formed between the downstream drying chambers 9, 9, and hot air exhaust chambers 11, 11 are formed outside the downstream drying chambers 9,9.
前記熱風供給室10内には熱風温度センサaを
設け、前記熱風排風室11には排風温度センサb
を設ける。 A hot air temperature sensor a is provided in the hot air supply chamber 10, and an exhaust air temperature sensor b is provided in the hot air exhaust chamber 11.
will be established.
該熱風温度センサaにより測定された熱風温度
Aと排風温度センサbにより測定された排風温度
Bは、つぎの算術式
K×A+(1−K)B
に代入されることにより、重みつき平均値が求め
られ、該重みつき平均値を流下式乾燥室9から排
出されるときの検出穀温Cとなしうる。 The hot air temperature A measured by the hot air temperature sensor a and the exhaust air temperature B measured by the exhaust air temperature sensor b are weighted by being substituted into the following arithmetic expression K×A+(1−K)B. An average value is determined, and the weighted average value can be used as the detected grain temperature C when the grain is discharged from the down-flow drying chamber 9.
ここで、前記重み定数Kは、種子用穀粒の a 種類 b 穀粒の含水率D の条件に応じて、「可変定数」にするとよい。 Here, the weight constant K is the weight constant of the seed grain. a type b Grain moisture content D It is best to make it a "variable constant" depending on the conditions.
即に、第4図に示したように、ビール麦と普通
の籾とでは、ビール麦の方が乾燥温度の影響を受
けよすいので、「重み定数K」は全体に高く決め
られる。「重み定数K」を高くすると「検出穀温
C」が高くなることにより、低温乾燥ができる。
これに対し、籾はビール麦よりやや高い温度で乾
燥されても発芽するので、能率を考えて「重み定
数K」は全体に低く決める。「重み定数K」を低
くすると「検出穀温C」は低くなることにより、
高温乾燥ができる。 Specifically, as shown in FIG. 4, between beer wheat and ordinary paddy, beer wheat is more easily affected by the drying temperature, so the "weight constant K" is set higher overall. When the "weight constant K" is increased, the "detected grain temperature C" becomes higher, thereby allowing low-temperature drying.
On the other hand, since paddy germinates even if it is dried at a slightly higher temperature than beer wheat, the "weighting constant K" is determined to be low overall in consideration of efficiency. When the "weighting constant K" is lowered, the "detected grain temperature C" becomes lower.
Can be dried at high temperatures.
また、「重み定数K」は、穀物の含水率Dに応
じて段階的に決める。含水率Dが低いときは高温
乾燥しても発芽するからである。 Further, the "weight constant K" is determined in stages according to the moisture content D of the grain. This is because when the moisture content D is low, germination will occur even if the seeds are dried at high temperatures.
12は流下式乾燥室9,9の両側の多孔板、1
3は前記熱風供給室10に接続したバーナー、1
4は乾燥室7に接続した熱風フアン、15は燃料
タンク、16は燃料ポンプ、17は燃料バルブ、
18は乾燥室7の上部に設置した調湿部であり、
大きな調湿タンク19を有し、該調湿タンク19
の下部には左右一対の漏斗20,20が形成さ
れ、漏斗20,20の下端開口部21,21は、
流下式乾燥湿9,9の上端22,22にそれぞれ
嵌合する。前記漏斗20内には穀粒の含水率Dを
測定する水分計dを設ける。 12 are perforated plates on both sides of the downstream drying chambers 9, 1;
3 is a burner connected to the hot air supply chamber 10;
4 is a hot air fan connected to the drying chamber 7, 15 is a fuel tank, 16 is a fuel pump, 17 is a fuel valve,
18 is a humidity control section installed in the upper part of the drying room 7;
It has a large humidity control tank 19, and the humidity control tank 19
A pair of left and right funnels 20, 20 are formed at the bottom of the , and the lower end openings 21, 21 of the funnels 20, 20 are as follows.
It fits into the upper ends 22, 22 of the down-flow type dryer 9, 9, respectively. A moisture meter d is installed in the funnel 20 to measure the moisture content D of the grains.
25は螺旋コンベア6より排出された穀物を揚
穀する昇降機、26はその排出樋、27は上部コ
ンベアであり、昇降機25の外方所望位置には昇
降機25の外周の外気温度を測定する外気温度セ
ンサ28を設ける。 Reference numeral 25 indicates an elevator for lifting the grain discharged from the spiral conveyor 6, 26 indicates a discharge gutter thereof, and 27 indicates an upper conveyor. At a desired position outside the elevator 25, there is an outside temperature sensor for measuring the outside air temperature around the outer periphery of the elevator 25. A sensor 28 is provided.
しかして、第3図は、本発明の水分測定に利用
できる制御回路を示しており、前記熱風温度セン
サaと温度センサ排風温度センサbと外気温度セ
ンサ28および水分計水分計dはA/D変換器2
9に接続する。30は中央処理部、31はラム、
32はロム、33は操作部、34は入力ポート、
35は表示部、36と37は出力ポート、38は
昇降機25の搬送モータである。 FIG. 3 shows a control circuit that can be used for moisture measurement according to the present invention. D converter 2
Connect to 9. 30 is a central processing unit, 31 is a ram,
32 is a ROM, 33 is an operation unit, 34 is an input port,
35 is a display section, 36 and 37 are output ports, and 38 is a transport motor of the elevator 25.
(作用) 次に作用を述べる。(effect) Next, we will discuss the effect.
先ず、操作部33により乾燥させる穀物の種類
および張込両を、例えば「ビール麦を4石」のよ
うに入力すると、このデータに合せた乾燥設定温
度Tが中央処理部30で計算される。 First, when the type of grain to be dried and the amount of grain to be dried are inputted using the operation section 33, for example, "4 koku of beer barley", the central processing section 30 calculates the drying temperature T in accordance with this data.
張込んだ未乾燥のビール麦の水分は、32%であ
つたとすると、そのときのビール麦の「重み定数
K」は、「0.8」だから、中央処理部30にその旨
入力し、昇降機25の下端の張込口よりビール麦
を供給すると、昇降機25を上昇して、その排出
樋26を介して上部コンベア27から調湿タンク
19内に落下して、流下式乾燥湿9内に充満し、
バーナー13から熱風供給湿10を介して供給さ
れる熱風を受けて、回転弁4,4により繰出され
て螺旋コンベア6で昇降機25に排出され、該昇
降機25により調湿タンク19内に循環供給され
る。 Assuming that the moisture content of the loaded undried beer barley is 32%, the "weight constant K" of the beer barley at that time is "0.8", so this is input to the central processing unit 30, and the elevator 25 is operated. When beer barley is supplied from the loading port at the lower end, it ascends the elevator 25 and falls from the upper conveyor 27 through the discharge gutter 26 into the humidity control tank 19, filling the flowing drying humidity 9.
The hot air supplied from the burner 13 via the hot air supply humidifier 10 is delivered by the rotary valves 4, 4 and discharged to the elevator 25 by the spiral conveyor 6, and is circulated and supplied into the humidity control tank 19 by the elevator 25. Ru.
しかして、初期乾燥作業特に熱風温度センサa
と排風温度センサbと水分計dにより
熱風温度=A=42℃
排風温度B=20℃
であつたとすると、(ビール麦の重み定数Kは第
4図から水分32%のときは「0.8」であるから)、
重みつき平均値である「検出穀温C」は
検出穀温C=K×A+(1−K)B
の算術式より、
0.8×42+(1−0.8)×20=37.6℃
となるものである。この場合、前記乾燥設定温度
Tが例えば38℃のときは、
C=37.6℃<T=38℃
となり、上限内に治まつていることになり、その
まま乾燥作業が行なわれる。 Therefore, during the initial drying process, especially with the hot air temperature sensor a.
Assuming that hot air temperature = A = 42℃ and exhaust air temperature B = 20℃ using exhaust air temperature sensor b and moisture meter d, (from Figure 4, the weight constant K for beer barley is 0.8 when the moisture content is 32%). ”),
"Detected grain temperature C", which is a weighted average value, is 0.8 × 42 + (1-0.8) × 20 = 37.6 °C from the arithmetic formula of detected grain temperature C = K × A + (1-K) B. . In this case, when the drying set temperature T is, for example, 38°C, C=37.6°C<T=38°C, which means that the drying temperature is within the upper limit, and the drying operation is continued as is.
しかして、乾燥作業が進行して、熱風温度セン
サaと排風温度センサbと水物計dにより、
熱風温度A=44℃
排風温度B=24℃
水分=28%
のようにそれぞれ測定されたときは、ビール麦の
「重み定数K」は第4図から水分28%のときは
「0.6」であるから、このときの重みつき平均値で
ある「検出穀温C」は
K×A+(1−K)B
の算術式より、
0.6×44+(1−0.6)×24=36℃
となるものである。 As the drying process progresses, hot air temperature sensor a, exhaust air temperature sensor b, and moisture meter d measure the following: hot air temperature A = 44°C, exhaust air temperature B = 24°C, and moisture content = 28%. In this case, the "weight constant K" of beer barley is "0.6" when the moisture content is 28% from Figure 4, so the "detected grain temperature C" which is the weighted average value at this time is K×A+( From the arithmetic formula 1-K)B, 0.6×44+(1-0.6)×24=36℃.
この方法によると、穀物作業が進行したとき
で、重み定数Kをそのまま変更しないときは、た
とえば
熱風温度A=44℃
排風温度B=24℃
K=0.8
となるとがあり、この結果を、
K×A+(1−K)B
に代入すると、
0.8×44+(1−0.8)×24=40℃
となり、
C=40℃>T=38℃
となつて、上限をオーバーすることが知れる。 According to this method, when grain work is progressing and the weighting constant K is not changed, for example, the hot air temperature A = 44℃, the exhaust air temperature B = 24℃, and K = 0.8, and these results are expressed as K When substituted into ×A+(1-K)B, it becomes 0.8×44+(1-0.8)×24=40℃, which means that C=40℃>T=38℃, which exceeds the upper limit.
(効果)
従来、穀物乾燥装置において穀物温度を計測器
により計測する方法は周知である。しかし、穀物
温度を計測器により計測する方法は、穀粒の密度
が濃い場合と薄い場合とで相違し、正確に測定で
きない。(Effects) Conventionally, a method of measuring grain temperature using a measuring device in a grain drying apparatus is well known. However, the method of measuring grain temperature using a measuring device differs depending on whether the grain is dense or thin, and cannot be measured accurately.
しかるに、本発明は流下式乾燥室9と、該流下
式乾燥室9に熱風を供給する熱風供給室10と、
前記流下式乾燥室9より排風される熱風排風室1
1とを供えたものにおいて、前記熱風供給室10
内には熱風温度センサaを前記熱風排風室内には
排風温度センサbをそれぞれ取付け、前記両セン
サabの測定値から穀粒温度を想定する穀物乾燥
装置における穀粒温度の測定方法としたものであ
るから、穀物密度に影響なく穀粒温度の測定がで
きる。また、自動温度制御にも利用できる。 However, the present invention includes a downstream drying chamber 9, a hot air supply chamber 10 that supplies hot air to the downstream drying chamber 9,
Hot air exhaust chamber 1 from which air is discharged from the downstream drying chamber 9
1, in which the hot air supply chamber 10
A method of measuring grain temperature in a grain drying apparatus is to install a hot air temperature sensor a inside the hot air exhaust chamber and an exhaust air temperature sensor b inside the hot air exhaust chamber, and to assume the grain temperature from the measured values of both sensors a and b. Because of this, grain temperature can be measured without affecting grain density. It can also be used for automatic temperature control.
第1図は穀物乾燥装置の縦断面図、第2図は同
側面図、第3図はブロツク回路図、第4図は重み
定数と含水率との関係を示すグラフ図である。
符号の説明、1……集穀部、2……重量計、3
……流入部、4……回転弁、5……受樋、6……
螺旋コンベア、7……乾燥室、8……下方排出
口、9……流下式乾燥室、10……熱風供給室、
11……熱風排風室、12……多孔板、13……
バーナ、14……排風フアン、15……燃料タン
ク、16……燃料ポンプ、17……燃料バルブ、
18……調湿部、19……調湿タンク、20……
漏斗、21……下端開口部、22……上端、24
……穀粒温度センサ、25……昇降機、26……
排出樋、27……上部コンベア、28……外気温
度センサ、29……A/D変換器、30……中央
処理部、31……ラム、32……ロム、33……
操作部、34……入力ポート、35……表示部、
36,37……出力ポート、38……搬送モー
タ、a……熱風温度センサ、b……排風温度セン
サ、d……水分計、A……熱風温度、B……排風
温度、C……検出穀温、T……乾燥設定温度。
FIG. 1 is a longitudinal sectional view of the grain drying apparatus, FIG. 2 is a side view thereof, FIG. 3 is a block circuit diagram, and FIG. 4 is a graph showing the relationship between weighting constants and moisture content. Explanation of symbols, 1...Grain collecting section, 2...Weighing scale, 3
...Inflow section, 4... Rotary valve, 5... Receiving gutter, 6...
Spiral conveyor, 7... Drying room, 8... Lower discharge port, 9... Downstream drying room, 10... Hot air supply room,
11... Hot air exhaust chamber, 12... Perforated plate, 13...
Burner, 14...Exhaust fan, 15...Fuel tank, 16...Fuel pump, 17...Fuel valve,
18...Humidity control section, 19...Humidity control tank, 20...
Funnel, 21... Lower end opening, 22... Upper end, 24
... Grain temperature sensor, 25 ... Elevator, 26 ...
Discharge gutter, 27... Upper conveyor, 28... Outside temperature sensor, 29... A/D converter, 30... Central processing section, 31... Ram, 32... ROM, 33...
Operation unit, 34...input port, 35...display unit,
36, 37... Output port, 38... Conveyance motor, a... Hot air temperature sensor, b... Exhaust air temperature sensor, d... Moisture meter, A... Hot air temperature, B... Exhaust air temperature, C... ...detected grain temperature, T...drying set temperature.
Claims (1)
を供給する熱風供給室10と、前記流下式乾燥室
9より排風される熱風排風室11とを供えたもの
において、前記熱風供給室10内には熱風温度セ
ンサaを前記熱風排風室内には排風温度センサb
をそれぞれ取付け、前記両センサaの測定値から
穀粒温度を想定する穀物乾燥装置における穀粒温
度の測定方法。1 A device comprising a downstream drying chamber 9, a hot air supply chamber 10 that supplies hot air to the downstream drying chamber 9, and a hot air exhaust chamber 11 that discharges air from the downstream drying chamber 9, in which the hot air A hot air temperature sensor a is installed in the supply chamber 10, and an exhaust air temperature sensor b is installed in the hot air exhaust chamber.
A method for measuring grain temperature in a grain drying apparatus in which the grain temperature is estimated from the measured values of both sensors a and
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP30748990A JPH03164687A (en) | 1990-11-14 | 1990-11-14 | Measuring method for grain temperature in grain drying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP30748990A JPH03164687A (en) | 1990-11-14 | 1990-11-14 | Measuring method for grain temperature in grain drying device |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP19042785A Division JPS6252393A (en) | 1985-08-29 | 1985-08-29 | Drying temperature control method for grain drying equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03164687A JPH03164687A (en) | 1991-07-16 |
| JPH054591B2 true JPH054591B2 (en) | 1993-01-20 |
Family
ID=17969706
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP30748990A Granted JPH03164687A (en) | 1990-11-14 | 1990-11-14 | Measuring method for grain temperature in grain drying device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03164687A (en) |
-
1990
- 1990-11-14 JP JP30748990A patent/JPH03164687A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03164687A (en) | 1991-07-16 |
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Legal Events
| Date | Code | Title | Description |
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| EXPY | Cancellation because of completion of term |