JPH0316652A - Treatment of harvested rice - Google Patents

Treatment of harvested rice

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Publication number
JPH0316652A
JPH0316652A JP1149836A JP14983689A JPH0316652A JP H0316652 A JPH0316652 A JP H0316652A JP 1149836 A JP1149836 A JP 1149836A JP 14983689 A JP14983689 A JP 14983689A JP H0316652 A JPH0316652 A JP H0316652A
Authority
JP
Japan
Prior art keywords
drying
rice
harvested rice
moisture content
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.)
Granted
Application number
JP1149836A
Other languages
Japanese (ja)
Other versions
JPH0763635B2 (en
Inventor
Satoru Akata
悟 赤田
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.)
Hokoku Kogyo Co Ltd
Original Assignee
Hokoku Kogyo 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 Hokoku Kogyo Co Ltd filed Critical Hokoku Kogyo Co Ltd
Priority to JP1149836A priority Critical patent/JPH0763635B2/en
Publication of JPH0316652A publication Critical patent/JPH0316652A/en
Publication of JPH0763635B2 publication Critical patent/JPH0763635B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Drying Of Solid Materials (AREA)
  • Cereal-Derived Products (AREA)
  • Adjustment And Processing Of Grains (AREA)

Abstract

PURPOSE:To solve problems, such as the yield of pestling, rice hulling rate and surface rubbing, and to maintain an adequate moisture so as to obtain the rice of a good taste by subjecting the harvested rice to an intermediate drying at the moisture between 22 to 17%, then to a finish drying just before the rice hulling. CONSTITUTION:The harvested rice is dried gently in the range of 22 to 17% moisture in intermediate drying stages 10, 11 but even if the drying is by fire power, the temp. rising speed of the hull is low and since the rice is maintained at the high moisture, the overdrying does not rise. The uniformization of the moisture is attained and the finish drying 14 of the ensuing stage is facilitated if the dehumidification drying is adopted for the intermediate drying. The harvested rice which is subjected to this intermediate dying is then subjected to the finish drying just prior to the rice hulling stage 6. The moisture conditions of the rice just prior to the rice hulling are exactly adjusted in this way, by which the yield of the pestling is improved, the rice hulling rate is improved, the surface rubbing is decreased and the taste is maintained. In addition, the dealing with all kinds of treatment forms is possible by the combination of the dehumidification drying and fire power drying.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、収穫米の水分を調整して処理する収穫米の処
理方法に関する. (従来の技術) 先ず、本発明の理解を容易にするために、収穫米の処理
に関する一般的な事項について説明する. 収穫米の品質及び処理(貯留、籾摺等)は、収穫米の含
有水分(重量%)に大きく影響される. 例えば、品質では水分が高いほど食味が向上する.又逆
に水分が高いと貯留中にかびが発生し、又籾摺時の脱プ
率(籾殻除去率)が低下する. このような理由により、農林水産省では、食味の観点か
ら籾摺時の水分を16%以下、貯留時では無通風にて1
7%35日間の貯留というように定められている. すなわち、貯留中の水分と貯留日数との間には、収穫米
がかびない一定の条件がある.次に収穫米一粒について
水分の多い部分と少ない部分があると、胴割れを起し時
には粉になることがあり、搗精歩留りが低下する.籾摺
時において、籾は、このようにして籾殻が脱ブされるの
で、適度の水分と籾のノゲ(毛)が残っている方がよい
.水分が高い場合には、籾摺時のこすりにより玄米の肌
に傷がつき易く (肌すれという)、又籾のノゲが少な
いと脱プ率が低下する. 次に乾燥手段としては、火力乾燥と除湿乾燥の二種類が
あり、その乾燥原理を異にする.先ず火力乾燥の原理は
、熱風にて収穫米の温度を昇温し水分を蒸発して乾燥す
るものであり、短時間に乾燥することができるという利
点がある. これに対して除湿乾燥の原理は、営温に近い空気の潜熱
を利用して水分を吸収除去するもの、すなわち、湿度の
低い空気を発生させ、この空気を収穫米に送風して収穫
米の水分を吸収除去するものであり、水分除去に要する
時間は火力乾燥に比べて長時間を要する. 収穫米の水分は、収穫の時期、天候、或は、稲一抹のう
ちでも開花及び成熟のバラツキにより異る.農林水産省
では、収穫米の処理計画水分として24%を設定してい
る。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method for processing harvested rice by adjusting the moisture content of the harvested rice. (Prior Art) First, general matters regarding the processing of harvested rice will be explained in order to facilitate understanding of the present invention. The quality and processing (storage, hulling, etc.) of harvested rice are greatly influenced by the moisture content (wt%) of harvested rice. For example, in terms of quality, the higher the moisture content, the better the taste. On the other hand, if the moisture content is high, mold will form during storage, and the dehulling rate (husk removal rate) during hulling will decrease. For these reasons, the Ministry of Agriculture, Forestry and Fisheries recommends that from the perspective of taste, the moisture content at the time of hulling should be kept at 16% or less, and at the time of storage, it should be kept at 16% without ventilation.
It is stipulated that 7% can be stored for 35 days. In other words, there are certain conditions between the moisture content in storage and the number of days it is stored to prevent harvested rice from getting moldy. Next, if a grain of harvested rice has parts with high moisture content and parts with low moisture content, the rice grains may crack and sometimes become powder, reducing the milling yield. At the time of hulling, the husks are removed from the paddy, so it is better to have a suitable amount of moisture and hair remaining on the paddy. When the moisture content is high, the skin of brown rice is easily damaged by the rubbing during hulling (called skin abrasion), and if there is little stubble on the rice, the dehulling rate decreases. Next, there are two types of drying methods: thermal drying and dehumidifying drying, which differ in their drying principles. First, the principle of thermal drying is to use hot air to raise the temperature of harvested rice and evaporate the moisture to dry it, which has the advantage of being able to dry in a short time. On the other hand, the principle of dehumidifying and drying is to absorb and remove moisture using the latent heat of air close to the operating temperature, in other words, to generate low-humidity air and blow this air over the harvested rice. It absorbs and removes moisture, and the time required to remove moisture is longer than that of thermal drying. The moisture content of harvested rice varies depending on the time of harvest, the weather, and variations in flowering and ripening within a single rice plant. The Ministry of Agriculture, Forestry and Fisheries has set the moisture content for harvested rice at 24%.

さて、従来の収穫米の処理方法として、第9図に示すも
のがあり、刈取り脱穀した収穫米を荷受け工程lに受け
た後に、この収穫米を火力乾燥工程2にて水分24%か
ら農林水産省で定められた水分l7%にまで乾燥する.
次にこの17%にまで乾燥した収穫米を一次貯留槽3に
貯留する.このように一次貯留した収穫米を次に仕上げ
火力乾燥工程4により、規定水分l6%以下にまで仕上
げ乾燥し、サイロ5に貯留される.そして需要量に応じ
てサイロ5かも所要量払い出しながら籾摺工程6を行い
出荷するようにしていた. 第lO図に示す処理方法は、荷受工程lに荷受けした収
穫米を、自然通風されている受け入れ貯留槽7にて受け
入れする. 従って、受け入れ貯留槽7内の収穫米の水分は、24%
である.次に受け入れ貯留槽7から収穫米を払い出して
、仕上げ火力乾燥工程8にて水分24%から16%以下
にまで乾燥した後に、籾摺工程6にて籾摺し出荷するよ
うにしていた.第11図に示す処理方法は、荷受工程l
に荷受けした水分24%の収穫米を、次に仕上げ火力乾
燥工程9にて水分16%以下にまで乾燥して籾摺工程6
にて籾摺し、出荷するようにしていた.(発明が解決し
ようとする課題) 上記従来の処理方法において、第9図に示すものは、次
のような問題がある. 先ず火力乾燥工程2では、水分24%から17%にまで
一気に乾燥するので、収穫米の中には過乾燥するものが
存し、胴割れを来すものがあり、搗精歩留りが低下する
という問題がある.又、火力乾燥工程2で、籾を昇温し
掻き混ぜながら乾燥するので、籾のノゲが落されてしま
い、籾摺による脱プ率が低下するという不具合がある. 次に仕上げ火力乾燥工程4で水分16%以下まで仕上げ
乾燥した後にサイロ5に貯留するのであるが、火力乾燥
の原理上、籾の昇温分布によって水分の蒸発量が異り、
籾の水分含有量が必ずしも一定しない。そこで、サイロ
5内に貯留された籾間において,水分を多く含む籾から
水分の少ない籾に水分が移行して平衡状態(以下水分移
行という)を保ち、サイロ5内の収穫米の水分が必ずし
416%であるという信頼性はない, そのために、もしも水分が16%よりも多い場合は,か
びが発生したり発酵したりして品質が著じるしく低下し
,又玄米がやわらかくなるので籾摺時に肌ずれを起し正
常な玄米にならないという不具合いがあり、又l6%よ
りち水分が少ないときは、食味に影響するという不具合
がある。
Now, as a conventional method for processing harvested rice, there is a method shown in Figure 9. After receiving the harvested rice that has been harvested and threshed in the receiving process 1, the harvested rice is dried in a thermal drying process 2 to reduce the moisture content to 24%. Dry to a moisture content of 17% as specified by the Ministry.
Next, this 17% dried harvested rice is stored in the primary storage tank 3. The harvested rice thus primarily stored is then finished and dried in a finishing fire drying step 4 to a specified moisture content of 16% or less, and stored in a silo 5. Then, depending on the demand, silo 5 also discharged the required amount while carrying out the hulling process 6 and shipping. In the processing method shown in FIG. 1O, the harvested rice received in the receiving process 1 is received in a receiving storage tank 7 which is naturally ventilated. Therefore, the moisture content of the harvested rice in the receiving storage tank 7 is 24%.
It is. Next, the harvested rice is discharged from the receiving storage tank 7, and after drying from 24% moisture content to 16% or less in a finishing fire drying process 8, the rice is hulled in a hulling process 6 and shipped. The processing method shown in FIG.
Harvested rice with a moisture content of 24% received at
The rice was hulled and shipped. (Problems to be Solved by the Invention) Among the conventional processing methods described above, the one shown in FIG. 9 has the following problems. First, in the thermal drying process 2, the moisture content is reduced from 24% to 17% all at once, so some of the harvested rice becomes overdried, causing cracking, which reduces the milling yield. There is. In addition, in the thermal drying step 2, the rice is heated and stirred while drying, so there is a problem that the grains of the rice are removed and the dehulling rate by hulling is reduced. Next, in the finish drying step 4, the rice is finished dried to a moisture content of 16% or less, and then stored in the silo 5. However, due to the principle of heat drying, the amount of water evaporation varies depending on the temperature distribution of the paddy.
The moisture content of paddy is not always constant. Therefore, between the paddy stored in the silo 5, moisture transfers from the paddy containing a lot of moisture to the paddy with a low moisture, maintaining an equilibrium state (hereinafter referred to as moisture transfer), and ensuring that the moisture of the harvested rice in the silo 5 is maintained. Therefore, if the moisture content is higher than 16%, mold and fermentation will occur, resulting in a significant decrease in quality, and the brown rice will become soft. There is a problem in that the skin is rubbed during hulling and the rice does not turn into normal brown rice, and when the moisture content is less than 16%, the taste is affected.

次に第lO図及び第11図に示す処理方法にあってち、
仕上げ火力乾燥工程8.9にて、一気に水分24%から
16%にまで乾燥するので、胴割れによる搗精歩留りの
低下、籾のノゲ落ちによる脱ブ率の低下を来すという問
題がある.これらの問題発生の原因は、火力乾燥のみに
より乾燥しているために起るのであるが、刈取り脱穀さ
れた収穫米をその日のうちに乾燥しなければならないと
いう事情があり、乾燥速度が速い火力乾燥方式を採用せ
ざるを得ないというのが実情である。
Next, according to the processing method shown in FIGS. 10 and 11,
In the finishing fire drying step 8.9, the moisture content is reduced from 24% to 16% at once, which causes problems such as a decrease in the milling yield due to shell cracking and a decrease in dehulling rate due to the sludge of the chaff. The cause of these problems is that drying is done only by fire-power drying, but because the harvested rice that has been harvested and threshed must be dried within the same day, it is necessary to use fire-power, which has a faster drying speed. The reality is that a drying method has no choice but to be adopted.

本発明は除湿乾燥又は除湿乾燥と火力乾燥との組合せに
より、搗精歩留、脱ブ率、肌ずれ等の問題を解決し、適
度の水分を保持して食味のよい収穫米の処理方法を提供
せんとするものである。
The present invention provides a method for processing harvested rice that retains an appropriate amount of moisture and has good taste by using dehumidifying drying or a combination of dehumidifying drying and thermal drying to solve problems such as polishing yield, deblubbling rate, and peeling. This is what I am trying to do.

(課題を解決するための手段) 上記の課題を解決するために本発明は、収穫米を乾燥し
、その後籾摺する収穫米の処理方法において、収穫米の
水分が22%〜17%の間で一旦中間乾燥した後に籾摺
工程前に前記中間乾燥した収穫米を所定の水分になるよ
うに仕上げ乾燥するようにしたちのである. (作 用) このように構成することにより、収穫米は、中間乾燥に
て水分22%〜l7%の範囲で緩やかに乾燥され、たと
え火力乾燥であっても、籾の昇温速度が遅くなり、かつ
高い水分で維持されるので過乾燥がなくなり胴割れや籾
のノゲ落ちは起らない.又中間乾燥を除湿乾燥すると水
分の均一化ができ、次工程の仕上げ乾燥が容易になる。
(Means for Solving the Problems) In order to solve the above problems, the present invention provides a method for processing harvested rice in which the harvested rice is dried and then hulled, and the moisture content of the harvested rice is between 22% and 17%. After the rice is partially dried, the partially dried harvested rice is finished and dried to a predetermined moisture level before the hulling process. (Function) With this configuration, the harvested rice is slowly dried with a moisture content in the range of 22% to 17% during intermediate drying, and even if drying is done by fire, the rate of temperature rise of the paddy is slowed down. , and maintains a high level of moisture, eliminating overdrying and preventing cracking of the hull and shedding of the paddy. Also, by dehumidifying the intermediate drying, the moisture content can be made uniform, making the final drying in the next step easier.

次にこの中間乾燥した収穫米を籾摺する前に仕上げ乾燥
する.これにより籾摺直前の収穫米の水分条件が正確に
行なわれて、脱ブ率の低下や食味の低下を来すようなこ
とはない.(実施例) 以下本発明の一実施例について詳細に説明する.先ず、
中間乾燥において、水分を22%〜17%にした根拠は
次の通りである。
Next, this intermediately dried harvested rice is finished and dried before being hulled. As a result, the moisture conditions of the harvested rice immediately before hulling are controlled accurately, and there is no drop in dehulling rate or deterioration in taste. (Example) An example of the present invention will be described in detail below. First of all,
The basis for setting the moisture content to 22% to 17% in intermediate drying is as follows.

(il収穫米の計画水分は一応24%に定められている
が、収穫米の水分は、収穫時期、天候或は開花成熟の程
度によって異る。
(The planned moisture content of harvested rice is set at 24%, but the moisture content of harvested rice varies depending on the harvest time, weather, and degree of flowering maturity.

例えば同日に収穫した収穫米でも、田の日当り、肥料等
の土壌の状況により開花成熟が異ること、又稲一抹の中
でも開花成熟が異ることがら当然に籾一粒毎に水分含有
量が異なる.従って一律に水分17%にまで乾燥した場
合には、当然に水分が極度に少ない籾(過乾燥)が存す
ることになり、胴割れ及び食味低下を来す籾が存するこ
とになる.そこで、収穫初期(中間乾燥)の段階では、
乾燥に所定の巾をもたせるようにした. 又従来では、天候や土壌の状況により水分が異ることか
ら、荷受けする際に水分わけをして荷受けしていたが、
収穫初期の段階での乾燥に所定の巾をもたせることによ
り、水分わけの荷受けをする必要がなくなり、胴割れ及
び食味低下をなくすと共に作業を簡略化するようにした
. [ii)収穫米の処理は、その日に収穫したものはその
日のうちに乾燥して貯留中のかび発生や食味低下をなく
すようにするのが一般的である. 従って乾燥機の能力もこれに見合うものでなければなら
ない. 火力乾燥の場合の毎時乾5城率(1時間当りの乾燥割合
)は、0.6%/時間〜0.8%/時間であり、農林水
産省基準の1日20時間(1日24時間であるが4時間
余裕を見込んだ時間)で換算すると、水分を1日当り1
2%〜16%乾燥可能である. 従って火力乾燥の場合は、計画水分24%に対し12%
〜8%にまで収穫米の乾燥能力を有する. 従来において、火力乾燥のみにて乾燥処理していた根拠
はこの点にある. しかしながら発明者は、収穫米の乾燥にとって除゛湿乾
燥の優位性に着目し実験を行った.除湿乾燥の優位性と
は、潜熱を利用してすなわち、収穫米が規定水分以下に
は乾燥しない温度調節した空気で収穫米の水分を除去す
るので、水分の少ない籾からの水分の蒸発は少なく、水
分の多い籾からは多くの水分が蒸発する(この現象を水
分の平衡という)ことをいう.これに対して、火力乾燥
は、籾を昇温して蒸発させる加熱蒸発であるので,水分
が少ない籾も水分が多い籾も一律に加熱される.従って
水分の少ない籾は過乾燥になる.除湿乾燥では、このよ
うな過乾燥はなく、除湿乾燥処理後の籾の含有水分は、
平均化される. 除湿乾燥についての実験によれば、毎時乾減率は0.1
5%/時間〜0.3%/時間が最適であることが得られ
た. すなわち、この時間当りの乾減率は、貯留している収穫
米に除湿調整した空気を流入させた場合に、収穫米の乾
燥に寄与する空気量に相当する乾減率を求める実験結果
である.収穫米の乾燥に寄与しないで単に通過していく
空気は、除湿乾燥機の損失となり、実験により求めた0
.15%/時間〜0.3%/時間の値は、除湿乾燥の最
も効率のよい値であるということができる. この除湿乾燥の毎時乾減率を用いて演算すると、除湿乾
燥の1日当りの乾減はO.l5x20日=3%、0.3
X20日=6%となり,計画水分24%に対しては、2
1%〜18%になる.そこで上限21%に対して1%の
余祐(仕上げ乾燥に対する余裕)を見て22%にした.
又下限17%は収穫米の水分にバラッキがあり一次貯留
で通風貯留したときの過乾燥防止と仕上げ乾燥の基準1
6%水分とを見込んで定めたものである. これにより、これまで火力乾燥のみであった乾燥に対し
て除湿乾燥の使用が可能になる.このように、中間乾燥
において水分を22%〜17%にすることにより、荷受
時において水分わけする必要がなく、水分わけ誤りによ
る胴割れや食味低下が防止される. 又、除湿乾燥の使用により,胴割れや食味低下がより確
実に防止される. そして中間乾燥に火力乾燥を用いた場合でも、毎時乾減
率が0.1〜0、3%/時間になり{  (24−22
) /20日=  0.1%,  (24−18)  
/20日=0.3%}籾の昇温速度を緩やかにし、これ
により胴割れや食味低下が防止される.次に籾摺直前の
仕上げ乾燥においても、1日当り乾減率が22%−16
%=6%,18%−16%=2%であることから、毎時
乾減率は0.1〜0.3%になり、中間乾燥とほぼ同一
条件で仕上げ乾燥を行うことができる. 次にこの方法を実施するために直接使用される収穫米の
処理方法について説明する.第1図において、刈取し脱
穀した収穫米は、水分わけすることなしに荷受工程1に
て荷受けされる.そして除湿乾燥による中間乾燥工程l
Oにて水分が22%〜17%の範囲で乾燥する。この除
湿乾燥による中間乾燥工程10において籾は、規定水分
以下にならないように湿度及び温度調節された空気が保
有する潜熱により除湿される.この潜熱による除湿の特
徴は、空気温度が常温に近いので籾粒は昇温されないこ
と、及び籾を掻き混ぜることなく、水分の少ない籾粒か
らの水分の蒸発は少なく、水分の多い籾粒からの水分の
蒸発は多くなっていわゆる自然乾燥と同じようにその雰
囲気での平衡状態を保った状態で乾燥されることから、
胴割れ、ノゲ落ち、過乾燥による食味の低下をもたらす
ことなく、均一に乾燥される. このように中間乾燥された収穫米は次に一次貯留槽11
に貯留される.そして必要に応じて通風機l3から貯留
槽11内に通風し貯留する.この通風貯留においても、
通風乾燥されるのであるが、一次貯留槽l1内の収穫米
の水分は、22%〜17%であるので、その水分は通風
乾燥による乾減率に対して十分であるので、過乾燥され
て食味が低下するようなことはない.次に一次貯留槽1
1に貯留された収穫米は2需要量に応じて払い出されて
、除湿乾燥による仕上げ乾燥工程l2にて所定の水分に
乾燥される。
For example, even if rice is harvested on the same day, the flowering maturity will vary depending on the field exposure, fertilizer, etc., and the flowering maturity will also vary even within a single grain of rice. different. Therefore, if the paddy is uniformly dried to a moisture content of 17%, there will naturally be some paddy with extremely low moisture content (overdrying), and there will also be paddy that suffers from cracking and poor taste. Therefore, at the early stage of harvest (mid-drying),
It was made to have a specified width for drying. In addition, in the past, the moisture content varied depending on the weather and soil conditions, so the moisture content was separated when receiving the cargo.
By allowing a specified width for drying in the early stages of harvest, there is no need to separate the moisture from the cargo, which eliminates cracking and loss of flavor, and simplifies the work. [ii) Harvested rice is generally dried on the same day to prevent mold growth and deterioration in taste during storage. Therefore, the dryer's capacity must match this. In the case of fire-powered drying, the hourly drying rate (drying rate per hour) is 0.6%/hour to 0.8%/hour, which is 20 hours a day (24 hours a day) according to the Ministry of Agriculture, Forestry and Fisheries standard. However, if you convert the amount of water by 1 hour per day (with a 4-hour allowance),
It is possible to dry 2% to 16%. Therefore, in the case of thermal drying, the planned moisture content is 12% compared to 24%.
It has the ability to dry up to 8% of harvested rice. This is the basis for conventional drying using only thermal drying. However, the inventor conducted experiments focusing on the superiority of dehumidification and drying for drying harvested rice. The advantage of dehumidifying drying is that it uses latent heat to remove moisture from harvested rice using temperature-controlled air that does not dry the harvested rice below a specified moisture content, so there is less evaporation of moisture from paddy with low moisture content. , a large amount of moisture evaporates from rice with a high moisture content (this phenomenon is called moisture equilibrium). On the other hand, thermal drying involves heating and evaporating paddy by raising its temperature, so both paddy with low moisture content and paddy with high moisture content are uniformly heated. Therefore, paddy with low moisture content becomes overdried. In dehumidifying drying, there is no such overdrying, and the moisture content of paddy after dehumidifying drying is
It is averaged. According to experiments on dehumidification and drying, the hourly drying loss rate is 0.1
It was found that 5%/hour to 0.3%/hour is optimal. In other words, this drying rate per hour is the result of an experiment to find the drying rate corresponding to the amount of air that contributes to drying the harvested rice when dehumidified air is introduced into the stored harvested rice. .. The air that simply passes through without contributing to the drying of the harvested rice causes loss in the dehumidifying dryer, and the
.. A value of 15%/hour to 0.3%/hour can be said to be the most efficient value for dehumidification and drying. When calculated using this hourly drying loss rate of dehumidifying and drying, the drying loss per day of dehumidifying and drying is O. l5 x 20 days = 3%, 0.3
x20 days = 6%, and for the planned moisture of 24%, 2
It will be 1% to 18%. Therefore, considering the upper limit of 21%, I decided to take a 1% margin (margin for finish drying) and set it to 22%.
In addition, the lower limit of 17% is the standard 1 for preventing overdrying and finishing drying when the moisture content of harvested rice varies and it is stored with ventilation in primary storage.
This was determined based on an expected moisture content of 6%. This makes it possible to use dehumidifying drying instead of drying that was previously only possible using fire-powered drying. In this way, by controlling the moisture content to 22% to 17% during intermediate drying, there is no need to separate the moisture at the time of receiving the goods, and cracking of the shell and deterioration of flavor due to incorrect moisture separation can be prevented. In addition, by using dehumidifying drying, cracking of the shell and deterioration of flavor can be more reliably prevented. Even when thermal drying is used for intermediate drying, the hourly drying loss rate is 0.1 to 0.3%/hour { (24-22
) /20 days = 0.1%, (24-18)
/20 days = 0.3% The temperature increase rate of the rice is slowed down, thereby preventing shell cracking and deterioration of flavor. Next, in the final drying just before hulling, the drying loss rate per day was 22%-16
Since % = 6% and 18% - 16% = 2%, the hourly drying loss rate is 0.1 to 0.3%, and the final drying can be performed under almost the same conditions as the intermediate drying. Next, we will explain the processing method for harvested rice that is directly used to implement this method. In Figure 1, the harvested rice that has been harvested and threshed is received in receiving process 1 without separating the moisture. And an intermediate drying process l by dehumidifying drying.
Dry at O until the moisture content is in the range of 22% to 17%. In this intermediate drying step 10 by dehumidifying and drying, the paddy is dehumidified using the latent heat held by the air whose humidity and temperature are controlled so that the moisture content does not fall below a specified level. The characteristics of dehumidification using latent heat are that the air temperature is close to room temperature, so the rice grains are not heated, and because the rice is not stirred, there is little evaporation of water from the rice grains with low moisture content, and there is less evaporation of water from the rice grains with high moisture content. The amount of moisture evaporates increases, and drying is performed while maintaining an equilibrium state in the atmosphere, similar to so-called natural drying.
It is dried evenly without any deterioration in flavor due to cracking, falling off, or overdrying. The harvested rice that has been intermediately dried in this way is then transferred to the primary storage tank 11.
It is stored in Then, if necessary, the air is ventilated into the storage tank 11 from the ventilation fan l3 and stored. Even in this ventilation storage,
The harvested rice in the primary storage tank l1 has a moisture content of 22% to 17%, which is sufficient for the drying loss rate due to ventilation drying, so it is not overdried. There is no loss of taste. Next, primary storage tank 1
The harvested rice stored in 1 is discharged according to the required amount 2, and is dried to a predetermined moisture content in a final drying step 12 by dehumidification and drying.

この時の基準水分は16%以下であるので、食味が最も
よいl6%水分にするのがよい.この水分16%の調節
は、中間乾燥工程lOで除湿乾燥しているので、例えば
一次貯留槽ll内では22%水分に均一になっており、
その水分にバラツキがないので、正確に16%水分にな
るように乾燥される. そして、この仕上げ乾燥工程12においても除湿乾燥を
使用しているので、籾の温度は常温であり、胴割れ、ノ
ゲ落ち、過乾燥による食味の低下はない.そして籾摺工
程6にて籾摺が行なわれる. この籾摺工程6において籾は、水分、温度、ノゲ落ち等
の条件が全べて満されており,脱ブ率及び搗精歩留りを
低下させることなく、かつ肌ずれもなく食味のよい玄米
が得られる.この実施例の場合は、中間乾燥工程lO及
び仕上げ乾燥工程l2共に除湿乾燥を行うので、乾減負
荷を同一にした除湿機を使用して,その日に収穫した収
穫米をその翌日のうちに籾摺して処理することもできる
し、中間乾燥工程lOにて水分17%にして35日間無
通風にして一次貯留するようにし、仕上げ乾燥工程l2
の乾減負荷を少なくするように制御することも可能であ
る.次に第2図に示す実施例について説明すると、荷受
1、除湿乾燥を用いた中間乾燥工程lO、及び一次貯留
槽11.通風機l3は、第l図に示した実施例と同じで
ある。
The standard moisture content at this time is 16% or less, so it is best to use 6% moisture for the best taste. This adjustment to 16% moisture is achieved by dehumidifying and drying in the intermediate drying step 10, so for example, the moisture content in the primary storage tank 11 is uniformly 22%.
Since there is no variation in its moisture content, it is dried to an exact 16% moisture content. Since dehumidifying drying is also used in this finishing drying step 12, the temperature of the paddy is at room temperature, and there is no deterioration in flavor due to cracking of the shell, falling of sludge, or overdrying. Then, in the hulling process 6, hulling is carried out. In this hulling process 6, the rice satisfies all conditions such as moisture, temperature, and removal of sludge, and brown rice with good taste is obtained without reducing the dehulling rate and milling yield, and without peeling. It will be done. In the case of this example, since dehumidification drying is performed in both the intermediate drying step 1O and the final drying step 12, a dehumidifier with the same drying load is used to unhull the harvested rice on the same day the next day. It can be treated by rubbing, or it can be treated by reducing the moisture content to 17% in the intermediate drying step 10 and storing it for 35 days without ventilation, and then in the final drying step 12.
It is also possible to control the drying load to reduce the drying load. Next, the embodiment shown in FIG. 2 will be described. The cargo receiver 1, the intermediate drying process lO using dehumidification and drying, and the primary storage tank 11. The ventilator l3 is the same as the embodiment shown in FIG.

この実施例においては、仕上げ乾燥工程l4に火力乾燥
を用いている。従って、火力乾燥を用いた仕上げ乾燥工
程l4の乾減負荷を少なくするのがよい. 例えば、除湿乾燥を用いた中間乾燥工程lOにて水分l
7%にまで除湿乾燥し、無通風にて一次貯留槽11に貯
留する. このように除湿乾燥されて貯留槽11に貯留された収穫
米は、除湿乾燥の原理により,水分が一律に17%にな
っており、かつノゲ落ちや胴割れはない. 次にこのように貯留槽11に貯留された収穫米を貯留槽
11より、需要量に応じて払い出し、火力乾燥を用いた
仕上げ乾燥工程l4にて水分16%にまで乾燥する. すなわち、水分17%から水分16%の1%水分を蒸発
すればよいことになる.毎時乾減率に換算すると0.0
5%/時間となり、籾の温度をそれほど高くすることな
くその乾燥速度を緩やかにし、かつ籾の掻き混ぜも少な
くしてノゲ落ちをなくし、水分16%になるように正確
に水分調整が可能になる. これにより、搗精歩留り、脱プ率、肌ずれ及び食味の点
で問題なく、籾摺工程6にて籾摺される. この実施例の場合は、除湿乾燥を用いた中間乾燥工程l
Oの乾減負荷を大きくし、火力乾燥を用いた仕上げ乾燥
工程14の乾減負荷を小さくして処理するのに適してい
る. 次に第3図に示す実施例について説明すると、この実施
例は、中間乾燥工程l5に火力乾燥を用い、仕上げ乾燥
工程l6に除湿乾燥を用いている。
In this embodiment, thermal drying is used in the final drying step l4. Therefore, it is better to reduce the drying load in the final drying step 14 using thermal drying. For example, in the intermediate drying process lO using dehumidifying drying, moisture l
It is dehumidified and dried to 7% and stored in the primary storage tank 11 without ventilation. The harvested rice thus dehumidified and dried and stored in the storage tank 11 has a uniform moisture content of 17% due to the principle of dehumidification and drying, and there is no sloughing or cracking. Next, the harvested rice thus stored in the storage tank 11 is discharged from the storage tank 11 according to the required amount, and is dried to a moisture content of 16% in a final drying step 14 using thermal drying. In other words, it is only necessary to evaporate 1% water, from 17% water to 16% water. 0.0 when converted to hourly drying rate
5%/hour, slowing down the drying speed without raising the temperature of the paddy so much, and reducing the amount of stirring of the paddy to eliminate sludge, making it possible to accurately adjust the moisture content to 16%. Become. As a result, the rice can be hulled in the hulling process 6 without any problems in terms of milling yield, pulp removal rate, peeling, and taste. In the case of this example, an intermediate drying step l using dehumidifying drying
It is suitable for processing by increasing the drying load of O and reducing the drying load of the final drying step 14 using thermal drying. Next, the embodiment shown in FIG. 3 will be described. In this embodiment, thermal drying is used in the intermediate drying step 15, and dehumidifying drying is used in the final drying step 16.

この実施例の場合ら、火力乾燥を用いた中間乾燥工程l
5の乾減負荷を少なくするのがよい.例えば、火力乾燥
を用いた中間乾燥工程15にて水分22%にまで乾燥す
る. すなわち、荷受lにて受け入れられた収穫米の水分24
%から22%の2%水分を蒸発すればよいことになる.
毎時乾減率に換算すると 0.1%/時間となり、籾の
温度をそれ程高くすることなくその乾燥速度を緩やかに
し、かつ籾の掻き混ぜも少なくしてノゲ落ちをなくすよ
うにする.そして次に一次貯留槽1lに貯留する.一次
貯留槽1lに貯留された水分22%の収穫米は、その日
の内に仕上げ乾燥工程に送られれば問題はないが、数日
間貯留される場合は、通風機l3にて一次貯留槽11に
通風し貯留する.この通風により、一次貯留槽11内の
収穫米の水分は蒸発するが、水分22%であるから過乾
燥になることはない.又通風貯留により、一次貯留槽1
1内の収穫米の水分及び、中間乾燥l5が火力乾燥であ
って、その水分が不均一であっても、仕上げ乾燥工程1
6が除湿乾燥であるから、仕上げ乾燥水分16%は、均
一に.調整される.このようにして,搗精歩留り、脱プ
率、肌ずれ食味の問題はなく籾摺工程6にて籾摺される
. 上記第1図乃至第3図に示した実施例について、最も可
能性の高い処理態様について説明したが、中間乾燥工程
及び仕上げ乾燥工程の乾減負荷の制御は、収穫米の処理
状況、消費エネルギ及び搗精歩留りや食味等との関係で
任意に制御されるものである. 次に第4図乃至第6図に示す実施例について説明する.
ここに示す実施例は、一次貯留槽ll内で水分を22%
〜17%に調整するようにしたものである.又この実施
例は、荷受lにて荷受けした収穫米を、直接に一次貯留
槽11に貯留するようにして、農繁期における刈取り脱
穀、運搬の渋滞を緩和するように配慮したものである.
第4図において、荷受lに荷受けした収穫米は、直接に
一次貯留槽11に貯留される.そして貯留された水分2
4%の収穫米は、除湿乾燥機l8から送られる所定の湿
度と温度の空気により、一次貯留檀1l内で、水分22
%から17%の範囲で中間乾燥される.この一次貯留槽
ll内での中間乾燥においても除湿乾燥であるので、除
湿乾燥の原理により貯留されている収穫米は、ほぼ常温
にて掻き混ぜることなく、かつ均一に乾燥される. これにより貯留されている収穫米は、過乾燥されず、胴
割れ、食味低下はなくかつノゲ落ちもない.又この方式
の場合は、一次貯留槽1l内に空気を送り込むので、通
風貯留と中間乾燥の両方を兼ねている.従って一次貯留
槽l1から払い出される収穫米の水分は、22%〜l7
%の範囲でのある水分%である. すなわち、除湿乾燥であるから貯留されている収穫米の
水分のバラツキ はなく、例えば水分22%〜17%の
範囲内の20%に均一化された水分となって払い出され
る. このようにして嚢要量に応じて払い出された収穫米は、
除湿乾燥を用いた仕上げ乾燥工程l7にて水分16%に
乾燥されて、籾摺工程6にて籾摺される. この仕上げ乾燥工程l7において除湿乾燥されるので、
胴割れ,食味低下、ノゲ落ちはなく、水分16%に正確
に調整されて籾摺される.従って搗精歩留りの低下、肌
ずれの発生、食味低下、脱プ率の低下をもたらすことな
く籾摺される. 第5図に示す実施例は、第4図に示す実施例の除湿乾燥
機l8の代りに火力乾燥機l9を用いて、一次貯留槽l
1内で水分22%から17%の範囲で中間乾燥するよう
にしたものである.この実施例の場合は,一次貯留槽l
1内での中間乾燥の乾減負荷を少なくし、除湿乾燥を用
いた仕上げ乾燥工程l7の乾減負荷を大きくする方が望
ましい. 又この実施例も通風貯留と中間乾燥の両方を兼ねている
から、長期間の貯留に適している.すなわち、火力乾燥
機l9から送られる空気の温度を低くして、乾減負荷を
十分小さくすることにより、貯留されている籾の温度を
緩やかに昇温しかつ掻き混ぜち緩やかにして、過乾燥に
よる胴割れや食味低下の防止及びノゲ落ちの防止が可能
になる. 又収穫した翌日に籾摺する場合でも、中間乾燥における
毎時乾減率を0.1%にすることにより処理可能である
から、その乾減速度は緩やがであり,過乾燥による胴割
れ、食味低下、ノゲ落ちは起らない. このようにして、一次貯留檀11内で中間乾燥された収
穫米は、次に仕上げ乾燥工程l7で乾燥される.中間乾
燥は火力乾燥であるので、一次貯留槽11から払い出さ
れる収穫米の水分には多少のバラツキはあるが、仕上げ
乾燥工程l7は除湿乾燥であるから、水分16%に均一
にかつ正確に乾燥される. そして水分16%、ノゲ落ちなし、胴割れなしの状態で
籾摺されるので、搗精歩留り、脱プ率、肌ずれ及び食味
の点で問題なく籾摺工程6にて籾摺される. 次に第6図に示す実施例は、第4図に示した実施例の仕
上げ乾燥工程l7の除湿乾燥の代りに火力乾燥を用いた
ものである. この実施例の場合も、火力乾燥を用いた仕上げ乾燥工程
20の乾減負荷を少なくし、除湿乾燥機l8による一次
貯留槽11内での中間乾燥工程の乾減負荷を大きくする
のが望ましい. すなわち、一次貯留槽11内での中間乾燥は、除湿乾燥
機l8で湿度及び温度が調節された空気により、除湿乾
燥される. 従って、一次貯留槽11内に貯留されている収穫米は、
ほぼ常温で水分が均一になるように乾燥される.又,除
湿乾燥の原理により、中間乾燥工程での下限水分l7%
にまで乾燥しても部分的に過乾燥になることはないから
、下限水分まで乾燥して、仕上げ乾燥工程20での火力
乾燥の乾減負荷を極力小さくすることが可能である.こ
れにより、籾摺工程6では、搗精歩留り、脱プ率、肌ず
れ及び食味の点で問題なく籾摺される.この実施例も、
通風貯留と中間乾燥の両方を兼ねている. 上記第4図乃至第6図に示した実施例について、最も可
能性の高い処理態様について説明したが、中間乾燥工程
及び仕上げ乾燥工程の乾減負荷の制御は、収穫米の処理
状況、消費エネルギ及び搗精歩留りや食味等との関係で
任意に制御されるものである.又、第4図における仕上
げ乾燥工程l7の除湿機を除湿機l8の代りに共用させ
ることも可能である. 次に第7図及び第8図に示す実施例について説明する. この実施例は、荷受1にて荷受けした収穫米を受入れ貯
留槽2lに受け入れて、水分を平均化する前工程を設け
たものである. この実施例の場合は、農繁期の刈取、脱穀及び運搬の渋
滞の緩和と、天候等による水分のバラツキ、及び長期全
量貯留を配慮したものである. 受入れ貯留槽2lでは、通風貯留と水分平均化乾燥の両
方を兼ねるようにしている。
In the case of this example, an intermediate drying step l using thermal drying
It is better to reduce the drying load in step 5. For example, in the intermediate drying step 15 using thermal drying, the material is dried to a moisture content of 22%. In other words, the moisture content of the harvested rice received at the receiving station is 24
It is sufficient to evaporate 2% moisture from % to 22%.
When converted to hourly drying loss rate, it is 0.1%/hour, so the drying speed is slowed down without raising the temperature of the paddy so much, and the amount of stirring of the paddy is reduced to eliminate sludge dropping. Then, it is stored in a 1 liter primary storage tank. Harvested rice with a moisture content of 22% stored in the primary storage tank 1l will not cause any problems if sent to the final drying process within the same day, but if it is stored for several days, it will be transferred to the primary storage tank 11 using a ventilation fan l3. Ventilate and store. Due to this ventilation, the moisture in the harvested rice in the primary storage tank 11 evaporates, but since the moisture content is 22%, it will not become over-dry. Also, due to ventilation storage, primary storage tank 1
Even if the moisture content of the harvested rice in step 1 and the intermediate drying step 15 is thermal drying, and the moisture content is uneven, the final drying step 1
Since step 6 is dehumidifying and drying, the final dry moisture content of 16% is uniform. It will be adjusted. In this way, the rice can be hulled in the hulling process 6 without problems with the milling yield, pulp removal rate, and texture. Regarding the embodiments shown in Figs. 1 to 3 above, the most likely processing mode has been explained, but the control of the drying load in the intermediate drying process and the final drying process depends on the processing status of harvested rice and the energy consumption. It is also controlled arbitrarily in relation to the milling yield and taste. Next, the embodiment shown in Figs. 4 to 6 will be explained.
The example shown here has a moisture content of 22% in the primary storage tank.
It was adjusted to ~17%. Further, in this embodiment, the harvested rice received at the receiving area 1 is stored directly in the primary storage tank 11, so as to alleviate congestion during harvesting, threshing, and transportation during the busy farming season.
In FIG. 4, the harvested rice received at the receiving tank 1 is directly stored in the primary storage tank 11. and stored water 2
4% harvested rice has a moisture content of 22% in the primary storage tank 1l due to the air at a predetermined humidity and temperature sent from the dehumidifying dryer l8.
% to 17%. Since the intermediate drying in this primary storage tank 11 is also dehumidified drying, the harvested rice stored according to the principle of dehumidifying drying is dried uniformly at almost room temperature without stirring. Harvested rice stored in this way is not over-dried, has no cracking, no loss of flavor, and no sludge falling off. In addition, in the case of this method, since air is sent into the 1 liter primary storage tank, it serves both as ventilation storage and intermediate drying. Therefore, the moisture content of the harvested rice discharged from the primary storage tank l1 is 22% to l7
It is a certain moisture percentage in the range of %. In other words, since the rice is dehumidified and dried, there is no variation in the moisture content of the stored harvested rice, and the moisture content of the harvested rice is equalized to 20% within the range of 22% to 17%, for example. The harvested rice that is dispensed according to the required amount of rice in this way is
The rice is dried to a moisture content of 16% in a final drying process 17 using dehumidification and drying, and then hulled in a hulling process 6. Since it is dehumidified and dried in this final drying step l7,
There is no cracking, no deterioration of flavor, and no grain loss, and the rice is hulled with the moisture content precisely adjusted to 16%. Therefore, the rice can be hulled without reducing the milling yield, causing peeling, degrading the taste, or reducing the rate of dehulling. The embodiment shown in FIG. 5 uses a thermal dryer l9 instead of the dehumidifying dryer l8 of the embodiment shown in FIG.
1, with intermediate drying at a moisture content ranging from 22% to 17%. In this example, the primary storage tank l
It is desirable to reduce the drying loss load of the intermediate drying in step 1 and increase the drying loss load of the final drying step 17 using dehumidifying drying. This embodiment also functions as both ventilation storage and intermediate drying, so it is suitable for long-term storage. In other words, by lowering the temperature of the air sent from the thermal dryer 19 and sufficiently reducing the drying load, the temperature of the stored paddy is gradually raised and the agitation is moderated, thereby preventing overdrying. This makes it possible to prevent cracking of the shell, loss of taste, and falling of the sludge. In addition, even when hulling is done the day after harvesting, it can be handled by setting the hourly drying loss rate to 0.1% during intermediate drying, so the drying loss rate is slow and there is no chance of hull cracking due to overdrying. No deterioration in taste or loss of texture occurs. The harvested rice that has been intermediately dried in the primary storage tank 11 in this way is then dried in a final drying step 17. Since the intermediate drying is thermal drying, there is some variation in the moisture content of the harvested rice discharged from the primary storage tank 11, but since the final drying step 17 is dehumidifying drying, the rice is dried uniformly and accurately to a moisture content of 16%. It will be done. Since the rice is hulled with a moisture content of 16%, no sludge falling off, and no hull cracking, the rice can be hulled in the hulling process 6 without any problems in terms of milling yield, plastic removal rate, skin slippage, and taste. Next, the embodiment shown in FIG. 6 uses thermal drying instead of the dehumidifying drying in the final drying step 17 of the embodiment shown in FIG. In the case of this embodiment as well, it is desirable to reduce the drying loss load in the final drying process 20 using thermal drying, and to increase the drying loss load in the intermediate drying process in the primary storage tank 11 using the dehumidifying dryer 18. That is, intermediate drying in the primary storage tank 11 is performed by dehumidification and drying using air whose humidity and temperature have been adjusted in the dehumidification dryer 18. Therefore, the harvested rice stored in the primary storage tank 11 is
It is dried at almost room temperature so that the moisture is evenly distributed. Also, due to the principle of dehumidifying drying, the lower limit of moisture content in the intermediate drying process is 17%.
Even if the product is dried to a maximum of 100%, it will not become partially over-dried, so it is possible to dry the product to the minimum moisture content and minimize the drying load of the thermal drying in the final drying step 20. As a result, in the hulling process 6, the rice is hulled without any problems in terms of milling yield, plastic removal rate, skin slippage, and taste. This example also
It serves as both ventilation storage and intermediate drying. Regarding the embodiments shown in FIGS. 4 to 6 above, the most likely processing mode has been explained, but the control of the drying load in the intermediate drying process and the final drying process depends on the processing status of harvested rice and the energy consumption. It is also controlled arbitrarily in relation to the milling yield and taste. It is also possible to use the dehumidifier used in the final drying step 17 in FIG. 4 instead of the dehumidifier 18. Next, the embodiment shown in FIGS. 7 and 8 will be explained. This embodiment is provided with a pre-process of receiving harvested rice received at a receiving tank 1 into a receiving storage tank 2 liters and equalizing the moisture content. In the case of this example, consideration was given to alleviating congestion during harvesting, threshing, and transportation during the busy farming season, as well as taking into consideration variations in moisture due to weather and other factors, and long-term storage of the entire amount. The receiving storage tank 2L is designed to serve both as ventilation storage and moisture averaging drying.

第7図において、荷受1に受゜.け入れた収穫米は、直
接に受入れ貯留槽21に受入れされる.そして、除湿乾
燥機22で湿度及び温度調節した空気を受入れ貯留槽2
lに送気して、水分24%〜20%の範囲で除湿乾燥す
る. これにより受入れ貯留槽2l内の収穫米の水分は平均化
されると共に通風貯留される.次に収穫米は、除湿乾燥
を用いた中間乾燥工程lOにて水分22%から17%の
範囲で乾燥され、一次貯留槽11に貯留される. そして、需要量に応じて払い出し、除湿乾燥を用いた仕
上げ乾燥工程l2にて水分16%にまで乾燥し、籾摺工
程6にて籾摺される. この処理工程において、例えば、全量の収穫米を35日
間貯留する場合は、除湿乾燥を用いた中間工程lOで水
分17%まで乾燥し、無通風にて全量一次貯留槽1lで
貯留するのが消費エネルギ上好ましく、又中間乾燥工程
10は除湿乾燥であるので、籾粒についての水分は均一
であり、一次貯留槽ll内での水分の移動はない.従っ
て、一次貯留槽ll内に貯留されている収穫米の水分1
7%は信頼性が高く、長期間貯留してもかび発生の管理
が容易になる. 又、35日間以上更に長期間貯留する場合は、受入れ貯
留槽21にて通風貯留し、水分l6%以下の過乾燥にな
らないように、貯留日数に対する除湿乾燥機22の乾減
負荷を制御する.又、受入れ貯留槽21.中間乾燥工程
10及び仕上げ乾燥工程l2は、いずれも除湿乾燥であ
るので、籾摺工程6での搗精歩留り、脱ブ率、肌ずれ及
び食味は、前に説明した第1図に示す実施例と同じであ
るのでその説明は省略する.次に第8図に示す実施例は
、第7図に示した実施例のうち、除湿乾燥機22に代え
て火力乾燥$3123を設けたものである. すなわち、受入れ貯留槽21内に直接に受入れられた収
穫米は,火力乾燥機23から送気される温風により、水
分24%から20%の範囲で火力乾燥すると共に通風貯
留する. そして、乾減負荷を少なくして乾燥することにより過乾
燥はなく、胴割れ、ノゲ落ち、食味低下はなく、水分が
均一化される.又、受入れ貯留槽2l内では、長期間の
貯留により水分の移動が行なわれて、水分の均一化に寄
与する.このように前工程として水分を均一化すること
は、後の中間乾燥工程,仕上げ乾燥工程及び籾摺工程の
制御、例えば,後の乾減負荷を少なくして、搗精歩留り
、脱プ率、肌ずれ及び食味を損うことなく、需要に対し
てその対応を速やかに行うことが可能になると共に、長
期貯留、或は短期処理など多種の処理態様への適用が可
能である. なお、除湿乾燥機22及び火力乾燥機23に代えて自然
通風してちよい. (発明の効果) 以上詳述した通り本発明によれば、収穫米を中間乾燥し
、その水分を22%から17%の範囲にしたので、その
日に収穫したものを数日のうちに処理するという処理態
様に対して除湿乾燥の使用を可能にすることができると
共に、除湿乾燥の乾減率が最もよい状態で収穫米の処理
をすることができ、更に長期貯留も可能にして農繁期に
おける刈取、荷受け、乾燥、籾摺等の労働力集中化を分
散し、労力軽減を図ることができる. 又、このように除湿乾燥の使用が可能になることにより
、搗精歩留りの向上、脱ブ率の向上、肌ずれの低減及び
食味の維持が達成されると共に、除湿乾燥と火力乾燥の
組合せにより、上記搗精歩留り等の向上を図ると共に、
あらゆる処理態様への対応が可能になる等の優れた効果
を有する.
In FIG. The harvested rice is directly received into the receiving storage tank 21. Then, the storage tank 2 receives the air whose humidity and temperature have been adjusted by the dehumidifying dryer 22.
1, and dehumidify and dry at a moisture content of 24% to 20%. As a result, the moisture content of the harvested rice in the 2L receiving storage tank is averaged and the rice is ventilated and stored. Next, the harvested rice is dried to a moisture content ranging from 22% to 17% in an intermediate drying step 10 using dehumidifying drying, and stored in a primary storage tank 11. The rice is then discharged according to demand, dried to a moisture content of 16% in a finishing drying process 12 using dehumidifying drying, and hulled in a hulling process 6. In this processing process, for example, when storing the entire amount of harvested rice for 35 days, it is best to dry it to 17% moisture in the intermediate step 1O using dehumidification and drying, and then store the entire amount in a 1L primary storage tank without ventilation. It is preferable in terms of energy, and since the intermediate drying step 10 is dehumidifying drying, the moisture content of the rice grains is uniform, and there is no movement of moisture in the primary storage tank 11. Therefore, the moisture 1 of harvested rice stored in the primary storage tank 1
7% is highly reliable and makes it easy to manage mold growth even if stored for a long time. In addition, when storing for a longer period of 35 days or more, ventilation is stored in the receiving storage tank 21, and the drying reduction load of the dehumidifying dryer 22 is controlled with respect to the number of storage days to prevent overdrying with a moisture content of 16% or less. In addition, the receiving storage tank 21. Since the intermediate drying step 10 and the final drying step 12 are both dehumidifying drying, the milling yield, dehulling rate, skin slippage, and taste in the hulling step 6 are similar to the example shown in FIG. 1 described above. Since they are the same, their explanation will be omitted. Next, the embodiment shown in FIG. 8 is the same as the embodiment shown in FIG. 7 except that the dehumidifying dryer 22 is replaced with a thermal dryer $3123. That is, the harvested rice directly received into the receiving storage tank 21 is thermally dried to a moisture content in the range of 24% to 20% by hot air sent from the thermal dryer 23, and is stored in ventilation storage. By drying with a reduced drying load, there is no overdrying, no cracking, no sloughing, no deterioration in flavor, and the moisture content is evened out. In addition, within the receiving storage tank 2l, water is moved due to long-term storage, contributing to uniformity of the water content. Equalizing the moisture as a pre-process in this way helps control the subsequent intermediate drying process, final drying process, and hulling process. It is possible to quickly respond to demand without causing deviations or loss of flavor, and it can be applied to a variety of processing methods such as long-term storage or short-term processing. Note that natural ventilation may be used instead of the dehumidifying dryer 22 and the thermal dryer 23. (Effects of the Invention) As detailed above, according to the present invention, harvested rice is intermediately dried and its moisture content is in the range of 22% to 17%, so that rice harvested on the same day can be processed within a few days. In addition to making it possible to use dehumidifying drying for this processing mode, it is also possible to process harvested rice in a state where the drying rate of dehumidifying drying is the best, and it is also possible to store it for a long time, so that it can be harvested during the busy farming season. It is possible to reduce labor by distributing labor intensive tasks such as receiving cargo, drying, and hulling rice. In addition, by making it possible to use dehumidifying drying in this way, it is possible to improve the milling yield, improve the deblubbling rate, reduce skin slippage, and maintain flavor. By combining dehumidifying drying and thermal drying, In addition to improving the above-mentioned milling yield, etc.,
It has excellent effects such as being able to handle all types of processing.

【図面の簡単な説明】 第1図乃至第′8図は本発明の一実施例であり,第1図
は中間乾燥及び仕上げ乾燥に除湿乾燥を用いた場合の模
式図、第2図は第1図の仕上げ乾燥に火力乾燥を用いた
場合の模式図、第3図は第1図の中間乾燥に火力乾燥を
用いた場合の.模式図、第4図は除湿乾燥機を用いて一
次貯留しながら中間乾燥し、仕上げ乾燥に除湿乾燥を用
いた場合の模式図、第5図は第4図の除湿乾燥機の代り
に火力乾燥機を用いた場合の模式図、第6図は第4図の
仕上げ乾燥に火力乾燥を用いた場合の模式図、第7図は
除湿乾燥機を用いて受入れ貯留するようにした模式図、
第8図は第7図の除湿乾燥機の代りに火力乾燥を用いた
場合の模式図である. 第9図は従来の収穫米の処理方法を示す模式図、第10
図は他の従来例の模式図、第11図は更に他の従来例の
模式図である. 1・・・荷受、  6・・・籾摺工程、10, 11,
 18. 19・・・中間乾燥工程、12, 14, 
16, 17. 20・・・仕上げ乾燥工程特 許 出 願 人 豊国王業株式会社 (ばか2名) 第4 凶 第1 12 E ゛3 三 13 1..a受       6・#7摺工程10,11,
18.19  中FA乾糧工糧12,14,16,77
,二≧(:) 一 イ:=:.:: ・f垂七5ノゼと
二哩第7L1 冥8 ヨ
[Brief explanation of the drawings] Figures 1 to '8 show one embodiment of the present invention, and Figure 1 is a schematic diagram when dehumidifying drying is used for intermediate drying and final drying. Figure 1 is a schematic diagram of the case where thermal drying is used for the final drying, and Figure 3 is a schematic diagram of the case where thermal drying is used for the intermediate drying of Figure 1. Schematic diagram, Figure 4 is a schematic diagram of a case where a dehumidifying dryer is used to perform intermediate drying while primary storage, and dehumidifying drying is used for final drying. Figure 5 is a schematic diagram of a case where a dehumidifying dryer is used instead of the dehumidifying dryer shown in Figure 4. Fig. 6 is a schematic diagram of the case in which thermal drying is used for the final drying in Fig. 4, Fig. 7 is a schematic diagram of the case in which a dehumidifying dryer is used to receive and store the product,
Figure 8 is a schematic diagram when a thermal dryer is used instead of the dehumidifying dryer shown in Figure 7. Figure 9 is a schematic diagram showing the conventional processing method for harvested rice, Figure 10
The figure is a schematic diagram of another conventional example, and FIG. 11 is a schematic diagram of still another conventional example. 1... Receiving goods, 6... Husking process, 10, 11,
18. 19... intermediate drying step, 12, 14,
16, 17. 20...Finishing drying process patent applicant Toyooh Industries Co., Ltd. (2 idiots) 4th 1st 12 E ゛3 313 1. .. a receiving 6/#7 sliding process 10, 11,
18.19 Central FA Dry Food 12, 14, 16, 77
, 2≧(:) 1 i:=:. :: ・f 7th 5th Nose and 2nd 7th L1 Mei 8 yo

Claims (1)

【特許請求の範囲】 (1)収穫米を乾燥し、その後籾摺する収穫米の処理方
法において、収穫米の水分が22%〜17%の間で一旦
中間乾燥した後に籾摺工程前に前記中間乾燥した収穫米
を所定の水分になるように仕上げ乾燥することを特徴と
する収穫米の処理方法。 (2)荷受けした収穫米を水分22%〜17%まで中間
乾燥した後に一次貯留し、この一次貯留した収穫米を籾
摺する前に所定の水分にまで仕上げて乾燥することを特
徴とする請求項1記載の収穫米の処理方法。 (3)中間乾燥及び仕上げ乾燥を除湿乾燥にしたことを
特徴とする請求項2記載の収穫米の処理方法。 (4)中間乾燥を除湿乾燥にし、仕上げ乾燥を火力乾燥
にしたことを特徴とする請求項2記載の収穫米の処理方
法。 (5)中間乾燥を火力乾燥にし、仕上げ乾燥を除湿乾燥
にしたことを特徴とする請求項2記載の収穫米の処理方
法。 (6)荷受けした収穫米を受け入れ貯留し、この受け入
れ貯留中に収穫米の水分を22%〜17%に中間乾燥し
、この受け入れ貯留しかつ中間乾燥した収穫米を籾摺す
る前に所定の水分になるように仕上げ乾燥することを特
徴とする請求項1記載の収穫米の処理方法。(7)中間
乾燥及び仕上げ乾燥を除湿乾燥にしたことを特徴とする
請求項6記載の収穫米の処理方法。 (8)中間乾燥を火力乾燥にし、仕上げ乾燥を除湿乾燥
にしたことを特徴とする請求項6記載の収穫米の処理方
法。 (9)中間乾燥を除湿乾燥にし、仕上げ乾燥を火力乾燥
にしたことを特徴とする請求項6記載の収穫米の処理方
法。 (10)荷受けした収穫米を受け入れ貯留し、この受け
入れ貯留中に収穫米の水分平均化乾燥を行い、この受け
入れ貯留し水分が平均化された収穫米の水分を22%〜
17%になるように中間乾燥して一次貯留し、この一次
貯留した収穫米を籾摺する前に所定の水分になるように
仕上げ乾燥することを特徴とする請求項1記載の収穫米
の処理方法。 (11)水分平均化乾燥、中間乾燥及び仕上げ乾燥を除
湿乾燥にしたことを特徴とする請求項10記載の収穫米
の処理方法。 (12)水分平均化乾燥を火力乾燥にし、中間乾燥及び
仕上げ乾燥を除湿乾燥にしたことを特徴とする請求項1
0記載の収穫米の処理方法。 (13)水分平均化乾燥を自然通風乾燥にし、中間乾燥
及び仕上げ乾燥を除湿乾燥にしたことを特徴とする請求
項10記載の収穫米の処理方法。
[Scope of Claims] (1) In a method for processing harvested rice in which the harvested rice is dried and then hulled, the moisture content of the harvested rice is once intermediately dried between 22% and 17%, and then the A method for processing harvested rice characterized by finishing and drying intermediately dried harvested rice to a predetermined moisture content. (2) A claim characterized in that the received harvested rice is intermediately dried to a moisture content of 22% to 17% and then primary stored, and the primary stored harvested rice is finished to a predetermined moisture content and dried before being hulled. The method for processing harvested rice according to item 1. (3) The method for processing harvested rice according to claim 2, characterized in that intermediate drying and final drying are dehumidified drying. (4) The method for processing harvested rice according to claim 2, characterized in that the intermediate drying is dehumidified drying and the final drying is thermal drying. (5) The method for processing harvested rice according to claim 2, characterized in that the intermediate drying is thermal drying and the final drying is dehumidifying drying. (6) Receive and store the harvested rice that has been received, intermediately dry the moisture content of the harvested rice to 22% to 17% during this reception and storage, and dry the harvested rice that has been received and stored and intermediately dried before hulling. 2. The method for processing harvested rice according to claim 1, further comprising finishing and drying the rice to reduce moisture. (7) The method for processing harvested rice according to claim 6, characterized in that intermediate drying and final drying are dehumidified drying. (8) The method for processing harvested rice according to claim 6, characterized in that the intermediate drying is thermal drying and the final drying is dehumidifying drying. (9) The method for processing harvested rice according to claim 6, characterized in that the intermediate drying is dehumidified drying and the final drying is thermal drying. (10) Receive and store the harvested rice that has been received, and dry the harvested rice to equalize the moisture content during the reception and storage, and reduce the moisture content of the harvested rice to 22% or more.
Processing of harvested rice according to claim 1, characterized in that the harvested rice is intermediately dried to a moisture content of 17% and then stored for the first time, and the harvested rice that has been stored for the first time is finished and dried to a predetermined moisture content before hulling. Method. (11) The method for processing harvested rice according to claim 10, characterized in that moisture-averaging drying, intermediate drying, and final drying are dehumidified drying. (12) Claim 1 characterized in that the moisture-averaging drying is performed by thermal drying, and the intermediate drying and final drying are performed by dehumidifying drying.
The method for processing harvested rice described in 0. (13) The method for processing harvested rice according to claim 10, characterized in that the moisture-averaging drying is carried out by natural ventilation drying, and the intermediate drying and finishing drying are carried out by dehumidifying drying.
JP1149836A 1989-06-13 1989-06-13 How to treat harvested rice Expired - Lifetime JPH0763635B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1149836A JPH0763635B2 (en) 1989-06-13 1989-06-13 How to treat harvested rice

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1149836A JPH0763635B2 (en) 1989-06-13 1989-06-13 How to treat harvested rice

Publications (2)

Publication Number Publication Date
JPH0316652A true JPH0316652A (en) 1991-01-24
JPH0763635B2 JPH0763635B2 (en) 1995-07-12

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007032900A (en) * 2005-07-26 2007-02-08 Satake Corp Circulation prevention operation method of circulation type grain dryer
CN111589495A (en) * 2020-05-28 2020-08-28 福建浦之玉米业有限公司 A kind of processing technology of retained germ

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6142183B2 (en) 2013-06-05 2017-06-07 株式会社テージーケー solenoid valve

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007032900A (en) * 2005-07-26 2007-02-08 Satake Corp Circulation prevention operation method of circulation type grain dryer
CN111589495A (en) * 2020-05-28 2020-08-28 福建浦之玉米业有限公司 A kind of processing technology of retained germ

Also Published As

Publication number Publication date
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