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JPH0623705B2 - Temperature compensation method of moisture meter for grain dryer - Google Patents
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JPH0623705B2 - Temperature compensation method of moisture meter for grain dryer - Google Patents

Temperature compensation method of moisture meter for grain dryer

Info

Publication number
JPH0623705B2
JPH0623705B2 JP2658386A JP2658386A JPH0623705B2 JP H0623705 B2 JPH0623705 B2 JP H0623705B2 JP 2658386 A JP2658386 A JP 2658386A JP 2658386 A JP2658386 A JP 2658386A JP H0623705 B2 JPH0623705 B2 JP H0623705B2
Authority
JP
Japan
Prior art keywords
temperature
grain
electrode
sample
moisture
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
Application number
JP2658386A
Other languages
Japanese (ja)
Other versions
JPS62184341A (en
Inventor
清明 水津
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.)
Iseki Agricultural Machinery Mfg Co Ltd
Original Assignee
Iseki Agricultural Machinery Mfg Co 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 Iseki Agricultural Machinery Mfg Co Ltd filed Critical Iseki Agricultural Machinery Mfg Co Ltd
Priority to JP2658386A priority Critical patent/JPH0623705B2/en
Publication of JPS62184341A publication Critical patent/JPS62184341A/en
Publication of JPH0623705B2 publication Critical patent/JPH0623705B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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用水分計の温度補正方法に係るも
のである。
TECHNICAL FIELD The present invention relates to a temperature correction method for a moisture meter for grain drying equipment.

(従来技術) 従来、循環式穀物乾燥装置において、乾燥室から排出さ
れて貯留室に循環供給される途中の穀粒をサンプル採取
し、該サンプル粒を摺潰してから水分計にてサンプル粒
の含水率を測定し、該測定含水率を前記サンプル粒の温
度に応じて補正したうえで作業者に表示するものは公知
である。
(Prior Art) Conventionally, in a circulation type grain drying apparatus, a grain of the grain being discharged from the drying chamber and being circulated and supplied to the storage chamber is sampled, the sample grain is crushed, and then the moisture content is measured by a moisture meter. It is known that the water content is measured, and the measured water content is corrected according to the temperature of the sample particles and then displayed to the operator.

前記含水率の補正は、穀温1℃に対して約10%の誤差が
生じるために行なうものである。したがって、正確に含
水率を測定するには、サンプル粒が略外気温度に等しい
電極ロールにより摺潰されて更に冷却された後の穀温を
測定する必要があるが、摺潰したサンプル粒の穀温を直
接測定することは極めて困難であるため、従来は、水分
計の電極ロールまたはその近傍に、電極温度又は電極近
傍温度を検出する温度センサを設けて、該温度センサに
より測定した温度をサンプル粒の穀温Tと見做して、例
えば 補正含水率=測定含水率−(T−20℃)/10 の算術計算により補正含水率を算出・表示していた。
The correction of the water content is performed because an error of about 10% occurs with respect to the grain temperature of 1 ° C. Therefore, in order to accurately measure the water content, it is necessary to measure the grain temperature after the sample grains are crushed by an electrode roll that is substantially equal to the outside air temperature and further cooled, but the grain of the crushed sample grains must be measured. Since it is extremely difficult to directly measure the temperature, conventionally, a temperature sensor for detecting the electrode temperature or the temperature near the electrode is provided in or near the electrode roll of the moisture meter, and the temperature measured by the temperature sensor is sampled. Considering the grain temperature T of the grain, the corrected water content was calculated and displayed by, for example, an arithmetic calculation of corrected water content = measured water content− (T−20 ° C.) / 10.

(発明が解決しようとする問題点) しかしながら、公知のものは電極温度又は電極近傍温度
をサンプル粒の穀温Tと見做していたため、乾燥装置か
ら排出された穀物の温度Tが高くなると、穀物は電極ロ
ールで摺潰された後も電極温度まで冷却されないため、
電極温度と穀温Tとに相当の開きが生じ、正確な穀温T
を測定することができず、水分計の精度が低下する問題
点があった。
(Problems to be Solved by the Invention) However, since the known one regards the electrode temperature or the electrode vicinity temperature as the grain temperature T of the sample grain, when the temperature T of the grain discharged from the drying device becomes high, Since the grain is not cooled to the electrode temperature even after being crushed by the electrode roll,
A considerable difference occurs between the electrode temperature and the grain temperature T, and the accurate grain temperature T
However, there is a problem in that the accuracy of the moisture meter is deteriorated.

(問題を解決するための手段) そこで、前記サンプル粒の穀温Tをその他の関連的温度
からより正確に求めるために一連の実験を行ったところ
と、いくつかの温度において相関関係があることが判明
した。
(Means for Solving the Problem) Then, a series of experiments were conducted to more accurately determine the grain temperature T of the sample grain from other relevant temperatures, and there was a correlation at some temperatures. There was found.

第2図は、乾燥室から排風される排風温度Bを横軸に、
穀物循環用の昇降機内を搬送される穀粒温度Rを縦軸に
とったグラフ図であり、排風温度Bと穀粒温度Rとが正
比例の関係にあることが求められ、サンプル粒として採
取される穀粒温度Rが排風温度Bにより求められること
が判明した。
FIG. 2 shows the exhaust air temperature B exhausted from the drying chamber on the horizontal axis,
It is the graph figure which set the vertical axis to the grain temperature R conveyed in the elevator for grain circulation, and it is calculated | required that the exhaust air temperature B and the grain temperature R have a direct proportional relationship, and it collects as a sample grain. It was found that the grain temperature R to be obtained is determined by the exhaust air temperature B.

しかして、前記したようにサンプル粒は、電極ロールに
より圧砕されるときに略外気温度と等しい電極ロールに
より相当の熱量が奪われて冷却されることになる。しか
しながら、冷却割合は一定であり、前記穀粒温度Rが高
いときは多く、低いときは少なくなり、排風温度Bと電
極温度Cとには、前記同様に正比例の関係があることが
判明した。
Therefore, as described above, when the sample particles are crushed by the electrode roll, a considerable amount of heat is taken by the electrode roll whose temperature is substantially the same as the outside air temperature, and the sample particles are cooled. However, it was found that the cooling rate is constant, is large when the grain temperature R is high, and is small when the grain temperature R is low, and the exhaust air temperature B and the electrode temperature C have a direct proportional relationship as described above. .

以上のことから、圧砕された後の穀温Tは、穀粒温度R
と電極温度Cとから求められ、該穀粒温度Rは排風温度
Bから求められることが判明し、実験により求めた定数
K(略0.3)を用いて、 穀温T={K×B+(1−K)×C} 但し、K=定数 B=排風温度 C=電極温度 という算術式を求めることができた。
From the above, the grain temperature T after being crushed is the grain temperature R
And the electrode temperature C, the grain temperature R was found to be obtained from the exhaust air temperature B, and using the constant K (approximately 0.3) obtained by the experiment, the grain temperature T = {K × B + (1−K) × C} However, K = constant B = exhaust air temperature C = electrode temperature was calculated.

よって、本発明は、サンプル粒の穀温Tを、乾燥室から
排風される排風温度Bと、電極温度又は電極近傍温度C
とにより正確に求めるようにしたものであり、乾燥室7
から排出されて貯留室18に上積み循環される間の穀粒か
らサンプル粒を採取し、これを摺潰して水分測定装置27
により含水率を測定し、該含水率は穀温Tにより補正す
るにあたり、前記サンプル穀粒の穀温Tは直接測定しな
いで、乾燥室7から排出される排風温度Bと、前記水分
測定装置27の電極ロール28またはその近傍の電極温度C
とを測定し、該排風温度Bと電極温度Cとの重みつき代
数和から前記穀温Tを求める穀物乾燥装置用水分計の温
度補正方法を要旨とするものである。
Therefore, according to the present invention, the grain temperature T of the sample grain is set to the exhaust air temperature B exhausted from the drying chamber and the electrode temperature or the electrode vicinity temperature C.
It was designed to be more accurately determined by
Sample particles are collected from the grains while being discharged from the storage chamber 18 and circulated in the storage chamber 18 and circulated.
The moisture content is measured by means of the moisture content, and the moisture content is corrected by the grain temperature T. The grain temperature T of the sample grain is not directly measured, but the exhaust air temperature B discharged from the drying chamber 7 and the moisture measuring device. Electrode temperature C of electrode roll 28 of 27 or its vicinity
And a temperature correction method of a moisture meter for a grain drying apparatus for obtaining the grain temperature T from the weighted algebraic sum of the exhaust air temperature B and the electrode temperature C.

(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って、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の中央上面にラセンコンベア6を横設す
る。7は集穀部1の上部に載置した乾燥室であり、下方
排出口8、8を前記流入部3、3に嵌合した左右一対の
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を形成し、該熱風排風室11内
には排風温度センサbを設ける。12は流下式乾燥室9、
9の両側の多孔板、13は前記熱風供給室10に接続したバ
ーナー、14は乾燥室7に接続した排風ファン、15は燃料
タンク、16は燃料ポンプ、17は燃料バルブである。
(Example) An example of an apparatus capable of carrying out the method of the present invention will be described with reference to the drawings. 1 is a grain collecting section placed on a weighing scale 2, and has a pair of left and right inflow sections 3, 3. Rotary valves 4 and 4 are provided below the inflow portions 3 and 3, respectively, and the lower sides of the rotary valves 4 and 4 are surrounded by a trough 5, and a spiral conveyor 6 is horizontally provided on the center upper surface of the trough 5. Reference numeral 7 denotes a drying chamber placed on the upper part of the grain collecting unit 1, which forms a pair of left and right flow-down type drying chambers 9 and 9 in which the lower outlets 8 and 8 are fitted to the inflow units 3 and 3. The flow-down type drying chamber 9, 9
A hot air supply chamber 10 is formed between them, hot air exhaust chambers 11 and 11 are formed outside the downflow drying chambers 9 and, and an exhaust air temperature sensor b is provided in the hot air exhaust chamber 11. . 12 is a flow-down type drying room 9,
Porous plates on both sides of 9, a burner connected to the hot air supply chamber 10, a blower fan connected to the drying chamber 7, a fuel tank 15, a fuel pump 16, and a fuel valve 17.

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、該漏斗20、20の下端開口部2
1、21は、前記流下式乾燥室9、9の上端22、22にそれ
ぞれ嵌合させる。
Reference numeral 18 denotes a humidity control section installed at the upper part of the drying chamber 7, which has a large humidity control tank 19, and a pair of left and right funnels 20, 20 are formed at the lower part of the humidity control tank 19, and the funnels 20, 20 are provided. Bottom opening 2
The reference numerals 1 and 21 are fitted to the upper ends 22 and 22 of the flow-down type drying chambers 9 and 9, respectively.

23はラセンコンベア6により排出された穀物を揚穀する
昇降機、24はその排出樋、25は上部コンベアであり、前
記昇降機23には前記集穀部1から調湿タンク19に循環供
給される穀粒の一部を採取するサンプル採取部26を設け
る。該サンプル採取部26は穀粒を一粒ずつ採取するラセ
ンコンベアで構成され、その排出側には水分測定装置27
を設ける。該水分測定装置27はサンプル採取部26で採取
したサンプル粒を摺潰してから、その抵抗電圧を測定し
て含水率を求めるもので、周速の異なる一対の電極ロー
ル28、抵抗電圧変換器29、A/D 変換器30、中央演算回路
31、表示部32から構成される。しかして前記電極ロール
28には該電極ロール28の電極温度Cを測定する温度セン
サcを設ける。
23 is an elevator for lifting the grain discharged from the spiral conveyor 6, 24 is a discharge gutter for the grain, 25 is an upper conveyor, and the elevator 23 circulates and supplies the grain from the grain collecting unit 1 to the humidity control tank 19. A sample collecting unit 26 for collecting a part of the grains is provided. The sample collecting section 26 is composed of a spiral conveyor for collecting grains one by one, and a moisture measuring device 27 is provided on the discharge side thereof.
To provide. The water content measuring device 27 grinds the sample particles collected by the sample collecting section 26, and then measures the resistance voltage to obtain the water content. A pair of electrode rolls 28 having different peripheral speeds and a resistance voltage converter 29 are used. , A / D converter 30, central processing circuit
31 and a display unit 32. Then the electrode roll
28 is provided with a temperature sensor c for measuring the electrode temperature C of the electrode roll 28.

しかして、第1図は、本発明の含水率測定に係る全体の
制御回路を示しており、前記排風温度センサbと電極温
度センサcおよび水分測定装置27はA/D 変換器30に接続
する。33はラム、34はロム、35は操作部、36は設定用S
W、37は安全センサ、38は入力ポート、39は出力ポー
ト、40は昇降機23の搬送モータである。
FIG. 1 shows the whole control circuit for measuring the water content of the present invention. The exhaust air temperature sensor b, the electrode temperature sensor c, and the moisture measuring device 27 are connected to the A / D converter 30. To do. 33 is a ram, 34 is a rom, 35 is an operation part, and 36 is a setting S.
W and 37 are safety sensors, 38 is an input port, 39 is an output port, and 40 is a transport motor of the elevator 23.

(作用) 次に作用を述べる。(Operation) Next, the operation will be described.

昇降機23の下端の張込口より穀物を次から次に供給する
と、穀物は、昇降機23、排出樋24を介して上部コンベア
25から調湿タンク19内と流下式乾燥室9内に充満し、こ
こでバーナー13から熱風供給室10を介して供給される約
50℃の熱風により乾燥を受けて、回転弁4、4により繰
出されてラセンコンベア6で昇降機23に排出され、再び
昇降機23により調湿タンク19内に上積み循環供給され
る。
When grains are supplied one after another from the inlet at the lower end of the elevator 23, the grains will pass through the elevator 23 and the discharge gutter 24, and the upper conveyor.
From 25, the humidity control tank 19 and the downflow-type drying chamber 9 are filled, and here the burner 13 supplies the hot air through the hot air supply chamber 10.
After being dried by hot air of 50 ° C., it is fed out by the rotary valves 4 and 4 and discharged to the elevator 23 by the spiral conveyor 6, and is again circulated and supplied into the humidity control tank 19 by the elevator 23.

しかして、穀粒の含水率は昇降機23内を上昇する穀粒
を、サンプル採取部26により一粒づつ採取して、これを
圧砕して水分測定装置27により測定して求めるが、この
とき圧砕されたサンプル粒の穀温Tは、前記排風温度セ
ンサbにより求められた排風温度Bと、電極温度センサ
cにより求められた電極温度Cと、実験により求められ
た定数K(略0.3)より求められる。
Then, the water content of the grains is obtained by collecting grains rising in the elevator 23 one by one by the sample collecting unit 26, crushing them, and measuring them with the water content measuring device 27. The grain temperature T of the sample grain thus obtained is the exhaust air temperature B obtained by the exhaust air temperature sensor b, the electrode temperature C obtained by the electrode temperature sensor c, and the constant K obtained by the experiment (approximately 0. It is obtained from 3).

即ち、例えば、 イ.排風温度Bが33℃ ロ.電極温度Cが20℃、 ニ.定数Kが0.3 のときは、穀温Tは前記の式 T={K×B+(1−K)×C} により求められる。これに、前記数値をそれぞれ代入す
ると T={0.3×33+(1−0.3)×20} となり、これにより、穀温Tは23.9℃となる。
That is, for example, a. Exhaust air temperature B is 33 ℃. Electrode temperature C is 20 ° C, d. When the constant K is 0.3, the grain temperature T is obtained by the above equation T = {K * B + (1-K) * C}. Substituting the above numerical values into these results in T = {0.3 × 33 + (1-0.3) × 20}, and the grain temperature T becomes 23.9 ° C.

これを、従来の公式 補正含水率=測定含水率−(T−20℃)/10 に代入すると、 補正含水率=測定含水率−(23.9℃−20℃)/10 となり、水分測定装置27より測定した測定含水率が例え
ば15%だとすると、15%から0.39%減算した数値14.61
%が表示部32に表示される。
Substituting this into the conventional formula corrected moisture content = measured moisture content− (T−20 ° C.) / 10, the corrected moisture content = measured moisture content− (23.9 ° C.−20 ° C.) / 10 is obtained. If the measured water content is 15%, for example, the value obtained by subtracting 0.39% from 15% is 14.61.
% Is displayed on the display unit 32.

(効果) 前記したように、従来、循環式穀物乾燥装置において、
乾燥室から排出されて貯留室に循環供給される途中の穀
粒をサンプル採取し、該サンプル粒を摺潰してから水分
計にてサンプル粒の含水率を測定し、該測定含水率を前
記サンプル粒の温度に応じて補正したうえで作業者に表
示するものは公知である。しかして、前記含水率の補正
は、サンプル粒の穀温により測定結果に一定(穀温1℃
に対して約10%)の誤差が生じるために行なうものであ
る。したがって、正確に含水率を測定するには、サンプ
ル粒が略外気温度に等しい電極ロールにより摺潰されて
更に冷却された後の穀温を測定する必要があるが、摺潰
したサンプル粒の穀温を直接測定することは極めて困難
であるため、従来は、水分計の電極ロールまたはその近
傍に、電極温度又は電極近傍温度を検出する温度センサ
を設けて、該温度センサにより測定した温度をサンプル
粒の穀温Tと見做して、例えば 補正含水率=測定含水率−(T−20℃)/10 の算術計算により補正含水率を算出・表示していた。し
かしながら、公知のものは電極温度又は電極近傍温度を
サンプル粒の穀温Tと見做していたため、乾燥装置から
排出された穀物の温度Tが高くなると、穀物は電極ロー
ルで摺潰された後も電極温度まで冷却されないため、電
極温度と穀温Tとに相当の開きが生じ、正確な穀温Tを
測定することができず、水分計の精度が低下する問題点
があった。
(Effect) As described above, in the conventional circulation type grain drying device,
Samples of the grains discharged from the drying chamber and being circulated and supplied to the storage chamber are sampled, and the water content of the sample grains is measured with a moisture meter after crushing the sample grains, and the measured water content is the sample. It is publicly known that the correction is displayed according to the temperature of the grain and then displayed to the operator. Therefore, the correction of the water content is fixed in the measurement result depending on the grain temperature of the sample grain (grain temperature 1 ° C.
Error is about 10%). Therefore, in order to accurately measure the water content, it is necessary to measure the grain temperature after the sample grains are crushed by an electrode roll that is substantially equal to the outside air temperature and further cooled, but the grain of the crushed sample grains must be measured. Since it is extremely difficult to directly measure the temperature, conventionally, a temperature sensor for detecting the electrode temperature or the temperature near the electrode is provided in or near the electrode roll of the moisture meter, and the temperature measured by the temperature sensor is sampled. Considering the grain temperature T of the grain, the corrected water content was calculated and displayed by, for example, an arithmetic calculation of corrected water content = measured water content− (T−20 ° C.) / 10. However, since the known one regards the electrode temperature or the temperature near the electrode as the grain temperature T of the sample grain, when the temperature T of the grain discharged from the drying device becomes high, the grain is crushed by the electrode roll and then crushed. Since it is not cooled to the electrode temperature, there is a considerable difference between the electrode temperature and the grain temperature T, an accurate grain temperature T cannot be measured, and the accuracy of the moisture meter deteriorates.

しかるに、本発明は、乾燥室7から排出されて貯留室18
に上積み循環される間の穀粒からサンプル粒を採取し、
これを摺潰して水分測定装置27により含水率を測定し、
該含水率は穀温Tにより補正するにあたり、前記サンプ
ル穀粒の穀温Tは直接測定しないで、乾燥室7から排出
される排風温度Bと、前記水分測定装置27の電極ロール
28またはその近傍の電極温度Cとを測定し、該排風温度
Bと電極温度Cとの重みつき代数和から前記穀温Tを求
める穀物乾燥装置用水分計の温度補正方法を要旨とした
ものであるから、サンプル粒の穀温Tを、圧砕前の穀温
Rを直接求めることなく、乾燥室から排風される排風温
度Bと、電極温度又は電極近傍温度Cとにより正確に求
めることができる効果を奏する。
However, according to the present invention, the storage chamber 18 discharged from the drying chamber 7 is
Sample grain is collected from the grain while being piled up and circulated in the
Smash this and measure the water content with a moisture measuring device 27,
When the moisture content is corrected by the grain temperature T, the grain temperature T of the sample grain is not directly measured, but the exhaust air temperature B discharged from the drying chamber 7 and the electrode roll of the moisture measuring device 27.
The temperature correction method of a moisture meter for grain dryers, which measures the electrode temperature C of 28 or its vicinity and obtains the grain temperature T from the weighted algebraic sum of the exhaust air temperature B and the electrode temperature C Therefore, the grain temperature T of the sample grain can be accurately determined from the exhaust air temperature B exhausted from the drying chamber and the electrode temperature or the electrode vicinity temperature C without directly determining the grain temperature R before crushing. There is an effect that can.

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

第1図は全体の制御ブロック回路図、第2図は排風温度
Bと穀温Rとの関係を示したグラフ図、第3図は穀物乾
燥装置の縦断面図、第4図は同側面図、第5図は水分測
定装置の斜視図である。 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……ラセンコンベア、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
ーナー、14……排風ファン、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、23……昇降機、24……排出樋、25……上部コンベ
ア、26……サンプル採取部、27……水分測定装置、28…
…電極ロール、29……抵抗電圧変換器、30……A/D 変換
器、31……中央演算回路、32……表示部、33……ラム、
34……ロム、35……操作部、36……設定用SW、37……
安全センサ、38……入力ポート、39……出力ポート、40
……搬送モータ、B……排風温度、C……電極温度、R
……圧砕前のサンプル粒の穀温、T……圧砕後のサンプ
ル粒の穀温、b……排風温度センサ、c……電極温度セ
ンサ。
FIG. 1 is an overall control block circuit diagram, FIG. 2 is a graph showing the relationship between exhaust air temperature B and grain temperature R, FIG. 3 is a vertical sectional view of a grain drying device, and FIG. 5 and 5 are perspective views of the moisture measuring device. Explanation of symbols 1 ... Grain collecting unit, 2 ... Weight scale, 3 ... Inflow unit, 4 ... Rotating valve, 5 ... Gutter, 6 ... Spiral conveyor, 7 ... Drying chamber, 8 ... Downward Exhaust port, 9 ... Downflow drying chamber, 10 ... Hot air supply chamber, 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 ... Bottom opening, 22 ... Top, 23 ... Elevator, 24 ... Discharge gutter, 25 ... Upper conveyor, 26 ... Sampling section, 27 ... Moisture measurement Device, 28 ...
… Electrode roll, 29 …… Resistance voltage converter, 30 …… A / D converter, 31 …… Central processing circuit, 32 …… Display unit, 33 …… Ram,
34 …… Rom, 35 …… Operating section, 36 …… Setting SW, 37 ……
Safety sensor, 38 …… input port, 39 …… output port, 40
…… Conveyor motor, B …… Exhaust air temperature, C …… Electrode temperature, R
... Temperature of sample grain before crushing, T ... Temperature of sample grain after crushing, b ... Exhaust air temperature sensor, c ... Electrode temperature sensor.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】乾燥室7から排出されて貯留室18に上積み
循環される間の穀粒からサンプル粒を採取し、これを摺
潰して水分測定装置27により含水率を測定し、該含水率
は穀温Tにより補正するにあたり、前記サンプル穀粒の
穀温Tは直接測定しないで、乾燥室7から排出される排
風温度Bと、前記水分測定装置27の電極ロール28または
その近傍の電極温度Cとを測定し、該排風温度Bと電極
温度Cとの重みつき代数和から前記穀温Tを求める穀物
乾燥装置用水分計の温度補正方法。
1. A sample grain is collected from a grain discharged from a drying chamber 7 and piled up and circulated in a storage chamber 18, and the sample grain is crushed to measure a moisture content by a moisture measuring device 27. Is corrected by the grain temperature T, the grain temperature T of the sample grain is not directly measured, but the exhaust air temperature B discharged from the drying chamber 7 and the electrode roll 28 of the moisture measuring device 27 or an electrode in the vicinity thereof. A temperature correction method for a moisture meter for a grain drying device, which measures a temperature C and obtains the grain temperature T from a weighted algebraic sum of the exhaust air temperature B and the electrode temperature C.
JP2658386A 1986-02-08 1986-02-08 Temperature compensation method of moisture meter for grain dryer Expired - Lifetime JPH0623705B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2658386A JPH0623705B2 (en) 1986-02-08 1986-02-08 Temperature compensation method of moisture meter for grain dryer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2658386A JPH0623705B2 (en) 1986-02-08 1986-02-08 Temperature compensation method of moisture meter for grain dryer

Publications (2)

Publication Number Publication Date
JPS62184341A JPS62184341A (en) 1987-08-12
JPH0623705B2 true JPH0623705B2 (en) 1994-03-30

Family

ID=12197565

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2658386A Expired - Lifetime JPH0623705B2 (en) 1986-02-08 1986-02-08 Temperature compensation method of moisture meter for grain dryer

Country Status (1)

Country Link
JP (1) JPH0623705B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01263546A (en) * 1988-04-15 1989-10-20 Nomura Sangyo Kk Method of measuring moisture value of grain
CN113960126A (en) * 2021-10-22 2022-01-21 南京禾信创微波测控技术有限公司 Be used for online moisture content measuring device of sodium alginate production line

Also Published As

Publication number Publication date
JPS62184341A (en) 1987-08-12

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