JPH0622890U - Dryer for paddy rice without cracks - Google Patents

Dryer for paddy rice without cracks

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Publication number
JPH0622890U
JPH0622890U JP6312092U JP6312092U JPH0622890U JP H0622890 U JPH0622890 U JP H0622890U JP 6312092 U JP6312092 U JP 6312092U JP 6312092 U JP6312092 U JP 6312092U JP H0622890 U JPH0622890 U JP H0622890U
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Japan
Prior art keywords
paddy rice
casing
rice
hollow body
inner cylinder
Prior art date
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Granted
Application number
JP6312092U
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Japanese (ja)
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JP2513078Y2 (en
Inventor
井 修 一 坂
Original Assignee
株式会社八光電機製作所
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Priority to JP1992063120U priority Critical patent/JP2513078Y2/en
Publication of JPH0622890U publication Critical patent/JPH0622890U/en
Application granted granted Critical
Publication of JP2513078Y2 publication Critical patent/JP2513078Y2/en
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Abstract

(57)【要約】 【目的】 この考案は乾燥中に胴割れの生じない籾米の
乾燥装置を提供することを目的としている。 【構成】 ケ−シング1内にホッパ状の内筒8を、その
上端縁部をケ−シング1に接続して配設し、内筒8内に
中空体7を配設し、中空体7と内筒8の間に籾米通路9
を形成し、該通路9部分の中空体7と内筒8の壁にそれ
ぞれ通気孔10,11を形成し、中空体7の内部には前
記通気孔10,11の上方から順次、高温,中温,低温
となるように遠赤外線放熱管12aを配設し、ケ−シン
グ1に排気ファン23を配設して中空体7内の熱気を吸
引させる。。
(57) [Abstract] [Purpose] The present invention aims to provide a drying apparatus for paddy rice that does not cause barrel cracks during drying. A hopper-shaped inner cylinder 8 is arranged in the casing 1, the upper end of the inner cylinder 8 is connected to the casing 1, and a hollow body 7 is arranged in the inner cylinder 8. Rice paddy passage 9 between
And the ventilation holes 10 and 11 are formed in the walls of the hollow body 7 and the inner cylinder 8 in the passage 9, and inside the hollow body 7, the high temperature and the medium temperature are sequentially arranged from above the ventilation holes 10 and 11. The far-infrared radiation pipe 12a is arranged so as to have a low temperature, and the exhaust fan 23 is arranged in the casing 1 to suck the hot air inside the hollow body 7. .

Description

【考案の詳細な説明】[Detailed description of the device]

【0001】[0001]

【産業上の利用分野】[Industrial applications]

本考案は生籾米の乾燥において、籾米の水分乾減率を1.0%/時〜2.0%/時に 乾燥する胴割れのない籾米を得る装置に関するものである。本考案にいう籾米と は、玄米が穎(通称籾がら)によって包まれた状態のものをいう。 The present invention relates to an apparatus for obtaining unhulled rice that has a moisture loss rate of 1.0% / hour to 2.0% / hour when drying unhulled rice. The unhulled rice referred to in the present invention means a state in which unpolished rice is wrapped with sprouts (commonly called unhulled rice).

【0002】[0002]

【従来の技術】[Prior art]

周知のように生籾米の乾燥には、一般に軽油(灯油)の燃焼熱を熱源とした乾 燥機が賞用されているが、この乾燥は水分の乾減率を常時1.0%/時以下(0.8〜1 .0%/時)に限定する必要がある。その主因は、水分乾減率を上記範囲以上とす ると、乾燥能率の向上は期待できても、加熱温度が籾米の表面(籾がら)から内 部玄米の中心部まで効率良く伝導することが殆どないために、表面からの水分蒸 発が内部からの水分移動より大きく先行して表面温度と内部温度との均衡が得ら れず、このため玄米は胴割れを多発して良品質の玄米を歩留まり良く得られない ばかりか、適用する籾米の含水量は通常25%前後であることから、これを乾燥 基準である15.0%および15.5%(北陸以北)まで乾燥するためには少な くとも10〜10.5時間の長時間を必要とするためであった。このようなこと から籾米の乾燥方法について、その改善方が特に緊急課題となるに至った。しか るところ、その後湿潤状態にある粉粒体用乾燥機として従来知られた竪型多重円 盤式乾燥機の改良型に、遠赤外線発熱体を熱源とする乾燥機が開発され公知であ る(特開昭60−101477号公報参照)。しかしながらこの乾燥機は、竪型 筒状または多角形状のケ−シング内に落下口を有する円盤を上下多段に架設し、 円盤上には適宜間隔をおいて遠赤外線発熱体を下向きに輻射するよう水平に横架 し、前記ケ−シングの中心には回転軸を垂直に軸支し、該回転軸には前記円盤上 面に摺接するスクレ−パ−を放射状に固着した構成からなるため、原料供給口か ら投入される粉粒体の乾燥はできても、その粒体が本考案で対象とする籾米であ る場合には、この籾米は多段に架設された円盤上を次々と降下して各段ごとに横 架した同一構成の放熱管から放射される遠赤外線の輻射熱に曝されかつ混合を繰 り返すこととなるため、乾燥後の籾米は過乾燥となることが避けられず、このた め脱穀時にくず米(玄米)が多発し易く良品質の玄米を歩留まり良く得ることが できない。このことは本考案者の多数次に亘る各種実験結果に徴しても自明であ り、上記の点を解消するためには、籾米の乾燥が過乾燥とならぬよう配慮しつつ 胴割れのない範囲での乾燥を必要とするものである。 As is well known, a dryer that uses the heat of combustion of light oil (kerosene) as a heat source is generally used to dry raw rice, and this drying always reduces the moisture loss rate of 1.0% / hour or less ( It should be limited to 0.8 to 1.0% / hour). The main reason for this is that if the moisture loss rate exceeds the above range, the heating temperature can be expected to improve efficiently, but the heating temperature will efficiently conduct from the surface of the paddy rice (rice husk) to the center of the inner brown rice. Since there is almost no moisture, moisture evaporating from the surface precedes the movement of moisture from the inside, and the balance between the surface temperature and the internal temperature cannot be obtained. In addition to not being able to obtain good yields, the moisture content of the applied paddy rice is usually around 25%, so in order to dry it to the dry standard of 15.0% and 15.5% (north of Hokuriku) Is because it requires a long time of at least 10 to 10.5 hours. Therefore, how to improve the method of drying paddy rice has become an urgent issue. However, after that, a dryer using a far-infrared heating element as a heat source was developed and is known as an improved version of the vertical type multi-disc dryer that was conventionally known as a dryer for powder and granular material in a wet state. (See JP-A-60-101477). However, in this dryer, a vertical cylinder-shaped or polygonal casing is installed with disks having drop ports in multiple stages, and the far-infrared heating elements are radiated downward at appropriate intervals on the disk. Since it is constructed by horizontally laying horizontally, a rotating shaft is vertically supported at the center of the casing, and a scraper that is in sliding contact with the upper surface of the disk is fixed to the rotating shaft in a radial manner. Even if the granules fed from the supply port can be dried, if the granules are the paddy rice that is the object of the present invention, the paddy rice will drop one after another on the disks laid in multiple stages. Since it is exposed to the radiant heat of far infrared rays radiated from the radiating pipes of the same structure that are laid horizontally for each stage and repeats the mixing, it is unavoidable that the paddy rice after drying becomes overdried. For this reason, waste rice (brown rice) is likely to occur frequently during threshing, and good-quality brown rice is retained. Ri can not be obtained well. This is obvious from the results of various experiments conducted by the present inventors, and in order to solve the above point, there is no cracking of the hull while taking care not to overdry the paddy rice. It requires drying in the range.

【0003】[0003]

【考案が解決しようとする課題】[Problems to be solved by the device]

前述したように、石油燃焼熱を熱源とした乾燥機においては、籾米の表面が過 乾燥となるために水分の乾減率を1.0%/時以下にしなければならず、すなわち乾 燥に要する時間を長く要し、燃費もかさむ難点がある。また特開昭60−101 477号公報や実開昭56−49487号公報に記載される遠赤外線使用の乾燥 では籾米の上から照射する方式のため乾燥むらが生じ、表層の過乾燥になる難点 がある。考案は、それらの実情に鑑みて、常に一定の熱が均等に籾米に当り水分 が早く拡散するようにして胴割れの生じない籾米の乾燥装置を提供することを目 的として開発されたものである。 As described above, in a dryer that uses the heat of burning oil as a heat source, the drying rate of water must be 1.0% / hour or less because the surface of paddy rice is overdried, that is, the time required for drying. It takes a long time, and has the drawback of increasing fuel consumption. Further, in the drying method using far infrared rays described in JP-A-60-101477 and Japanese Utility Model Application Laid-Open No. 56-49487, the unevenness of drying occurs due to the method of irradiating from the top of the paddy rice, resulting in overdrying of the surface layer. There is. In consideration of these circumstances, the present invention was developed with the aim of providing a drying device for paddy rice in which a constant heat is uniformly applied to the paddy rice and moisture is quickly diffused so that cracks in the barrel do not occur. is there.

【0004】[0004]

【課題を解決するための手段】[Means for Solving the Problems]

この考案は上記課題を解決し目的を達成するために次のような手段を講じた。 The present invention has taken the following means in order to solve the above problems and achieve the object.

【0005】 (1) 熱風と遠赤外線を併用して籾米の芯部と外表部の乾燥を同等の水分乾減率 とするようにした。(1) By using hot air and far infrared rays together, the core portion and the outer surface portion of the paddy rice were dried at the same moisture loss rate.

【0006】 (2) 乾燥機中の風流は、風上と風下とがあること、風流路の風上と風下とに位 置する籾米の水分乾減率は当然に異なることから同時間内の均一乾燥は困難であ るという事実関係を重視して、風流路の風上と風下に対する遠赤外線照射熱量を 風上から風下へかけて順次強,中,少と差をつけた。(2) The wind flow in the dryer is upwind and leeward, and the moisture drying rate of the paddy rice located on the leeward and the leeward of the air flow passage is naturally different. Emphasizing the fact that uniform drying is difficult, the far infrared irradiation heat quantity for the windward and leeward of the air flow passage is gradually increased from the windward side to the leeward side, and is differentiated from strong to medium to small.

【0007】 (3) 装置の構造としては、ケ−シング内に有底ホッパ状内筒を、その上開口端 周部をケ−シング内壁に接続して配設し、該内筒の中心部に、中央部の高い中空 体を配設して中空体外周面と内筒側壁間に上下に連通する籾米通路を形成し、該 籾米通路の各対向壁にはそれぞれ籾米の通過し得ない無数の通気孔を貫通形成し 、前記中空体内には、反射面を通気孔に対面させて反射板を立設し該反射板と通 気孔間に遠赤外線放熱管群を区分的に立設し、該遠赤外線放熱管群は区分毎にそ れぞれ通風の流路上流側から下流側へ順次高温放熱、中温放熱、低温放熱となる よう放熱管を配列し、前記ケ−シングの天井部内には投入用スクリュ−コンベア を架設し、前記籾米通路には温度調節器の測温子を配設し、ケ−シングには排気 ファンを有する風胴を前記中空体の気流と連通状に設けた。(3) As for the structure of the device, a hopper-shaped inner cylinder with a bottom is disposed in the casing, the upper opening end of the inner cylinder is connected to the inner wall of the casing, and the central portion of the inner cylinder is arranged. The upper part of the hollow body has a high hollow body, and a paddy rice passage is formed vertically between the outer peripheral surface of the hollow body and the side wall of the inner cylinder. A through hole, a reflection plate is erected in the hollow body with the reflection surface facing the ventilation hole, and a far infrared radiation tube group is erected in a sectioned manner between the reflection plate and the air hole. The far-infrared heat radiation tube group is arranged in the ceiling part of the casing by arranging the heat radiation tubes in order from the upstream side to the downstream side of the ventilation passage in order of high temperature heat radiation, medium temperature heat radiation, and low temperature heat radiation. Is equipped with a screw conveyor for charging, a temperature sensor of a temperature controller is installed in the paddy rice passage, and an exhaust fan is installed in the casing. The wind tunnel having a down provided airflow communication with shape of said hollow body.

【0008】[0008]

【作用】[Action]

上記のように構成されたこの考案は次のような作用を有している。 The present invention configured as described above has the following operation.

【0009】 籾米通路を経由する籾米に対して遠赤外線が照射され、かつ気流が当たるので 、籾米は遠赤外線によって芯部から発熱して内部熱が拡散するため水分が表面へ と移行し、表面の水分は気流によって乾燥されるから、籾米の芯部と表層の水分 がほぼ同時に均等的に乾燥される。Far-infrared rays are radiated to the paddy-rice that passes through the paddy-rice passage, and the air current strikes the paddy-rice, and the far-infrared rays generate heat from the core portion of the paddy-rice, causing internal heat to diffuse and moisture to migrate to the surface. Since the water in the rice is dried by the air flow, the water in the core and the surface of the paddy rice is dried almost simultaneously.

【0010】 次に気流は排気ファンに外側から吸引されて生ずるので風上から冷たい外気が 入り、風下は遠赤外線で加熱されて温かくなっているため、籾米通路に風上から 入る気流と風下から入る気流の温度が異なっている。そのため、籾米通路の風上 に位置する遠赤外線の照射量は強くし、風下になるに従って順次弱くすると、籾 米に対する加熱量は略同じに調節することができて乾燥むらが生じない。この遠 赤外線の温度調節は、籾米通路に配設された幾つかの測温子で区画毎の温度を測 定して調節する。このことから籾米は早く均一に乾燥されるため、胴割れは生じ にくく水分乾減率は1.0%時〜2.0%/時という効率のよい乾燥をすることができる 。Next, since the airflow is generated by being sucked into the exhaust fan from the outside, cold outside air enters from the windward, and the leeward is heated by far infrared rays and is warm, so that the airflow entering the paddy rice passage from the upwind and the leeward. The temperature of the incoming airflow is different. Therefore, if the irradiation amount of far-infrared rays located on the windward side of the paddy rice passage is increased and then gradually decreased as it goes downwind, the heating amount for the paddy rice can be adjusted to be substantially the same, and uneven drying will not occur. This far-infrared temperature control is performed by measuring the temperature of each compartment with several temperature sensors installed in the paddy rice passage. From this fact, since the paddy rice is dried quickly and uniformly, cracks in the barrel are unlikely to occur and the moisture loss rate can be efficiently dried from 1.0% to 2.0% / hour.

【0011】[0011]

【実施例】【Example】

以下この考案の実施例を図面に基づいて説明する。乾燥装置のケ−シング1は 平面方形の箱型である。内部に平面方形で略ホッパ状の有底内筒8を配し、該有 底内筒8は上部をテ−パ面8Aに形成し、該テ−パ面8A上端部は前記ケ−シン グ1内壁面に接続されている。有底内筒8の中心部には平面方形で断面山形の中 空体7が内設されている。しかして、該中空体7の傾斜上板7Aと前記テ−パ面 8Aとの上部に収容部Rが構成され中空体7底面と有底内筒8の下側壁8C間に ピット8Dが構成されている。また中空体7の左右両側壁7Bと有底内筒8の左 右両側壁8B間に籾米通路9が形成されて、収容部Rとピット8D間に連通され ている。前記中空体7の側壁7Bと有底内筒の側壁8Bには、それぞれ籾米が通 過できないが可及的に大きな通気孔10・・・,11・・・が多数開口されている。従 って、この両側壁7B,8Bは同目的のために金網で代用することもできる。前 記有底内筒8の底部8Eにはスクリュ−コンベア24が有底内筒8外に籾米5を 排出可能に配設されている。前記収容部Rの上空帯中央部には、ケ−シングの天 井に垂設された支持杆6の下端部に受皿3が水平に架設されている。該受皿3上 には回転翼4が回転手段(図示せず)により回転可能に配設されている。また前 記収容部Rの上空帯には、スクリュ−コンベア2が、その排出口を前記受皿3上 に位置するように配設され、該スクリュ−コンベア2の取入口と前記下部のスク リュ−コンベア24の排出口間にエレベ−タ25が配設されている。前記中空体 7内部には、反射板18・・・がその反射面を前記両側壁7B・・・方向に平行に向け て支承体19を介して配設されている。また該反射板18・・・と側壁7B間には 遠赤外線を放射する放熱管群12a〜12c,12a’〜12c’が配設されて いる。前記ケ−シング1には図4に示すように、中空体7へ外気を連通する吸気 口21が開設されている。またケ−シング1には、前記両側壁7B,8Bの通気 孔10・・・11・・・を介して吸気口21と気流の連通する排気口22が開設されて おり、該排気口22には排気ファン23を有する風胴23Aが連設されている。 従ってケ−シング1内には図4に矢線で示すように吸気口21から排気口に至る 通風経路が形成されていて、吸気口21側が風上となり、排気口22側が風下と なって外気が流通する。 An embodiment of the present invention will be described below with reference to the drawings. The casing 1 of the drying device has a box shape of a flat square. Inside, a bottomed inner cylinder 8 having a flat rectangular shape and a substantially hopper shape is arranged. The bottomed inner cylinder 8 has an upper portion formed on a taper surface 8A, and an upper end portion of the taper surface 8A is the casing. 1 is connected to the inner wall surface. At the center of the bottomed inner cylinder 8, a flat rectangular rectangular hollow 7 is provided. Then, a housing portion R is formed above the inclined upper plate 7A of the hollow body 7 and the taper surface 8A, and a pit 8D is formed between the bottom surface of the hollow body 7 and the lower side wall 8C of the bottomed inner cylinder 8. ing. Further, a rice grain passage 9 is formed between the left and right side walls 7B of the hollow body 7 and the left and right side walls 8B of the bottomed inner cylinder 8 to communicate between the storage part R and the pit 8D. On the side wall 7B of the hollow body 7 and the side wall 8B of the bottomed inner cylinder, a large number of vent holes 10 ... Therefore, both side walls 7B and 8B can be replaced by wire mesh for the same purpose. A screw conveyor 24 is arranged at the bottom portion 8E of the bottomed inner cylinder 8 so that the paddy rice 5 can be discharged to the outside of the bottomed inner cylinder 8. In the central part of the upper part of the accommodation section R, a tray 3 is horizontally installed on the lower end of a support rod 6 which is suspended from the ceiling of the casing. Rotating blades 4 are rotatably arranged on the tray 3 by a rotating means (not shown). The screw conveyor 2 is arranged above the accommodation section R so that its discharge port is located above the tray 3, and the intake port of the screw conveyor 2 and the screw at the lower part are arranged. An elevator 25 is arranged between the outlets of the conveyor 24. Inside the hollow body 7, reflectors 18 ... Are arranged via bearings 19 with their reflecting surfaces parallel to the side walls 7B. Further, heat radiation tube groups 12a to 12c and 12a 'to 12c' for radiating far infrared rays are arranged between the reflection plates 18 ... And the side wall 7B. As shown in FIG. 4, the casing 1 is provided with an intake port 21 for communicating the outside air with the hollow body 7. Further, the casing 1 is provided with an exhaust port 22 communicating with the intake port 21 through the ventilation holes 10 ... 11 ... Of the both side walls 7B, 8B. Is continuously provided with a wind tunnel 23A having an exhaust fan 23. Therefore, as shown by the arrow in FIG. 4, a ventilation path is formed in the casing 1 from the intake port 21 to the exhaust port. The intake port 21 side is upwind and the exhaust port 22 side is downwind. Will be distributed.

【0012】 以上のことから排気ファン23を稼働すれば吸気口21から入った冷たい外気 がすぐに籾米通路9内に入る場合と、放熱管群12a・・・で加熱されてから籾米 通路9内に入る場合とが生ずる。そのことは籾米通路9を通過する籾米5・・・に 対する加熱量に部分的な差違が生ずることを意味している。これを解消して平均 的な加熱を計るために次のような手段を講じた。すなわち、通風経路の風上に位 置する放熱管群は放熱量を多くし、風下に位置する放熱管群は放熱量を少なくし て配設するものである。具体的には図5に示すように放熱管(カ−トリッジ)1 3は焼結棒15に発熱体(ニクロム線)14が巻着され、耐熱絶縁体Mで被覆し て金属管16(表面に遠赤外線放射塗料を塗工)を被着して形成されているが、 ニクロム線14の巻数を密,稍々密,粗に変化させてあり、(D),(E),(F)のシ −スタイプの放熱管13’も同様にニクロム線14・・・の巻回は密〜粗に変化さ せてある。これらシ−スタイプ13’は図6に示すように金属板17,17’に 埋め込まれて面発熱体に形成されている。この場合、金属板17に埋め込む放熱 管13’・・・はニクロム線の巻数が変化するようにしてもよい。しかして、図4 における左方から右方へ順次ニクロム線14・・・の巻数が少なくなるように設定 して放熱管群12a〜12c,12a’〜12c’を配列すれば、吸気口21に 近い方の放熱管群は発熱量が高く、排気口22に近くなるに従って放熱量が低く なる。従って籾米通路9を通過する籾米5・・・に対して加えられる熱量は遠赤外 線の熱量が多い部分では風流による熱量が少なく、風流による熱量が多い部分で は遠赤外線の熱量が少なく照射されてト−タル的には均等熱量が籾米に与えられ るように配慮されている。そのコントロ−ルは図4において籾米通路9内に配設 された温度調節器(図示せず)の測温子20・・・の検温値に基づいて、温度調節 器が放熱管群のニクロム線14に対する電流を調節して、籾米の含有水分の乾減 率を1.0%/時〜2.0%/時になるよう温度調節する。From the above, when the exhaust fan 23 is operated, the cold outside air that has entered from the intake port 21 immediately enters the rice grain passage 9 and the case where the cold outside air enters the rice grain passage 9 after being heated by the heat radiating tube group 12a. When you enter This means that there is a partial difference in the heating amount for the paddy rice 5 ... Which passes through the paddy rice passage 9. The following measures were taken to eliminate this and measure the average heating. That is, the heat radiation pipes located on the windward side of the ventilation path are arranged to increase the heat radiation amount, and the heat radiation pipes located on the downwind side are arranged to reduce the heat radiation amount. Specifically, as shown in FIG. 5, a heat radiating pipe (cartridge) 13 has a heating rod (nichrome wire) 14 wound around a sintered rod 15 and covered with a heat resistant insulator M to cover a metal pipe 16 (surface). It is formed by applying far-infrared radiation paint on the surface. However, the number of turns of the nichrome wire 14 is densely, densely and roughly changed, and (D), (E), (F) Similarly, in the case type radiating pipe 13 ', the winding of the nichrome wire 14 ... Is changed from dense to coarse. As shown in FIG. 6, these sheet types 13 'are embedded in metal plates 17 and 17' to form a surface heating element. In this case, the number of windings of the nichrome wire may be changed in the heat radiating tubes 13 '... Embedded in the metal plate 17. Then, by setting the number of windings of the nichrome wire 14 ... In order from the left to the right in FIG. 4 and arranging the heat radiation pipe groups 12a to 12c and 12a 'to 12c', the intake port 21 The heat radiation amount is high in the heat radiation pipe group closer to the heat radiation pipe, and the heat radiation amount decreases as the heat radiation pipe group approaches the exhaust port 22. Therefore, the amount of heat applied to the paddy rice 5 that passes through the paddy rice passage 9 is small due to the wind flow in the portion where the far infrared ray has a large amount of heat, and the far infrared ray has a small amount of heat in the portion where the amount of heat due to the wind stream is large. Therefore, the total amount of heat is given to the paddy rice in a total manner. The control is based on the temperature measurement value of the temperature sensor 20 ... of a temperature controller (not shown) arranged in the paddy rice passage 9 in FIG. The temperature of the paddy rice is adjusted to 1.0% / hour to 2.0% / hour by adjusting the electric current to the paddy rice.

【0013】 この装置においては吸気口21から冷たい外気が中空体7へ導入されるが、気 流は早いので、気流が放熱管群によって加熱されても高温の熱風となることはな い。これは、遠赤外線が籾米に照射されると内部発熱が生じて内部熱が外表へと 拡散するが、その場合、籾米の外層部が低温であるほど内部熱の外方への拡散が 早いことを利用して、内部熱の早い拡散とそれによる水分の発散を図ることを目 的としているものである。そのため籾米の表層温度が一定の方がむらが生じない 。前記風流は風下の方が中空体内で加熱を受けるため、風流が加熱されている分 だけ風下に位置する遠赤外線放熱管の籾米に対する遠赤外線の照射量を減らす方 が好ましいものである。In this device, cold outside air is introduced into the hollow body 7 through the intake port 21, but since the air flow is fast, even if the air flow is heated by the heat radiating tube group, it does not become hot hot air. This is because when far-infrared rays are applied to the paddy rice, internal heat is generated and the internal heat diffuses to the outer surface. In that case, the lower the temperature of the outer layer of the paddy rice, the faster the internal heat diffuses to the outside. The purpose of this is to promote the rapid diffusion of internal heat and the diffusion of water due to it. Therefore, unevenness does not occur when the surface temperature of paddy rice is constant. Since the leeward wind is heated in the hollow body, it is preferable to reduce the irradiation amount of far-infrared rays to the paddy rice in the far-infrared radiation pipe located leeward as much as the leeway is heated.

【0014】 上記のように構成されたこの装置において、生籾米5・・・を図示しない投入口 からエレベ−タ25の下部に投入すると、エレベ−タ25で上昇した籾米5・・・ はコンベア2によって受皿3上に降下し、回転翼4によって下方の収容部Rへ散 布される。収容部Rへ入った籾米5は籾米通路9を経てピット8Dに溜り、順次 収容部Rまで達する。そこで下方のコンベア24を稼働させれば、籾米は循環す ることになる。次いで、放熱管群12a・・・を作用させ、排気ファン23を稼働 させると、放熱管群12a・・・から放射される遠赤外線が籾米通路9を通過する 籾米5・・・に照射されて、籾米5の芯部の水分を外表部へと発散させる。また通 気口7B・・・,8B・・・を介して中空体7内部から有底内筒8外へ流通する気流に よって籾米5・・・の表面の水分を蒸発させる。この水分乾減率は1時間当り1.0% 〜2.0%に調節されるので、乾燥時間は短縮されるが、籾米の芯部から表層まで均 一的な乾燥なので胴割れが生じないし、籾米通路のどの位置を通過しても均一的 な加熱を受けるのでむらのない乾燥をさせることができる。前記中空体7の天井 部は閉鎖構造であるため放熱管群12a・・・によって温められた空気が上昇滞留 してファン23の吸引に対しても気流が少ないため傾斜上板7Aは加熱される。 この傾斜上板7Aの放熱作用で上部の籾米5・・・は加熱される。また有底筒体8 のテ−パ面8Aも、その下部のケ−シング1内の暖かい空気によって加熱される ため、その放熱作用で上部の籾米5・・・は加熱される。前記籾米通路9を通過す る籾米5・・・の速度は下部のコンベア24の排出速度で調節することができる。In this apparatus configured as described above, when raw rice 5 is charged into the lower part of the elevator 25 through a charging port (not shown), the rice 5 raised by the elevator 25 is conveyed by the conveyor. It is lowered onto the tray 3 by 2 and is scattered by the rotary vanes 4 to the lower housing portion R. The unhulled rice 5 that has entered the container R accumulates in the pit 8D through the unhulled rice passage 9 and sequentially reaches the container R. Therefore, if the lower conveyor 24 is operated, the paddy rice will circulate. Next, when the heat radiating tube group 12a ... Is operated to operate the exhaust fan 23, far infrared rays emitted from the heat radiating tube group 12a ... Are radiated to the unhulled rice 5 passing through the unhulled rice passage 9. , The moisture of the core of the paddy rice 5 is diffused to the outer surface. Further, the moisture on the surface of the paddy rice 5 ... Is evaporated by the air flow flowing from the inside of the hollow body 7 to the outside of the bottomed inner cylinder 8 through the ventilation ports 7B. The moisture loss rate is adjusted to 1.0% to 2.0% per hour, so the drying time is shortened, but since the rice is uniformly dried from the core to the surface layer, there is no cracking of the hull rice and Even if it passes through any position, it is uniformly heated so that uniform drying can be achieved. Since the ceiling of the hollow body 7 has a closed structure, the air warmed by the radiating tube groups 12a, ... Ascends and the airflow is small even when the fan 23 sucks the inclined upper plate 7A. . The upper paddy rice 5 ... Is heated by the heat radiation effect of the inclined upper plate 7A. Further, since the taper surface 8A of the bottomed cylindrical body 8 is also heated by the warm air in the casing 1 below it, the heat radiating action heats the paddy rice 5 above. The speed of the paddy rice 5 ... Which passes through the paddy rice passage 9 can be adjusted by the discharge speed of the lower conveyor 24.

【0015】[0015]

【考案の効果】[Effect of device]

以上説明したように、この考案は次のようなすぐれた効果を有している。 As described above, the present invention has the following excellent effects.

【0016】 (1) 乾燥装置において籾米通路を通過する籾米に対して遠赤外線を照射し、か つ通風によって乾燥させるので、籾米の芯部の水分と表層部の水分とを効率よく 短時間で乾燥させることができ、表層部だけ過乾燥とならないため籾米に胴割れ が生じない。(1) In the drying device, since the far-infrared rays are irradiated to the paddy rice passing through the paddy-rice passage and the paddy rice is dried by ventilation, the moisture of the core portion of the paddy rice and the moisture of the surface layer portion are efficiently and quickly. Since it can be dried and only the surface layer is not overdried, no cracking occurs in the paddy rice.

【0017】 (2) 籾米の水分乾減率を1.0%/時〜2.0%/時に調節しているため、乾燥処理時 間を短縮することができ、米の風味を損なわない。(2) Since the moisture loss rate of paddy rice is adjusted to 1.0% / hour to 2.0% / hour, the drying treatment time can be shortened and the flavor of rice is not impaired.

【0018】 (3) 通風経路の位置差によって、籾米に対する加熱温度が変化することに対し 放熱管群の放熱量を風上の方は多く、風下の方は少なくする構成としたので籾米 を均一的に乾燥させることができる。(3) The heating temperature of the paddy rice changes due to the difference in the position of the ventilation path, whereas the radiation amount of the radiant tube group is set to be larger on the windward side and smaller on the leeward side. Can be dried.

【0019】 (4) 乾燥装置において、放熱管群を通風経路の風上から風下にかけて順次放熱 量が大,中,小となるように配設し、籾米通路に複数配設された測温子によって 温度管理ができるため、籾米通路を通過する籾米に対して均一的に加熱させて、 むらのない乾燥をさせることができる。(4) In the drying device, the heat radiation pipes are arranged so that the heat radiation amount becomes large, medium, and small in order from the windward to the lee of the ventilation path, and a plurality of temperature measuring elements are provided in the paddy rice passage. Since the temperature can be controlled, it is possible to uniformly heat the unhulled rice that passes through the unhulled rice passage so as to achieve uniform drying.

【0020】 (5) 放熱管群の後方に反射板を設けたので遠赤外線を籾米通路方向へむらがな いように照射させることができる。(5) Since the reflecting plate is provided at the rear of the heat radiating tube group, it is possible to irradiate far infrared rays in the rice grain passage direction without unevenness.

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

【図1】乾燥装置の縦断面図である。FIG. 1 is a vertical sectional view of a drying device.

【図2】回転翼の平面図である。FIG. 2 is a plan view of a rotary blade.

【図3】図1におけるX−X線断面図である。3 is a cross-sectional view taken along line XX in FIG.

【図4】乾燥装置の横断平面図である。FIG. 4 is a cross-sectional plan view of the drying device.

【図5】放熱管の発熱体の巻密度の差を示す断面図であ
る。A,B,Cはカ−トリッジタイプを示し、D,E,
Fはシ−スタイプを示す。
FIG. 5 is a cross-sectional view showing a difference in winding density of heat generating elements of a heat radiation tube. A, B, C indicate cartridge type, D, E,
F indicates a sheath type.

【図6】面発熱体の斜視図である。FIG. 6 is a perspective view of a surface heating element.

【図7】面発熱体の変形例を示す斜視図であるFIG. 7 is a perspective view showing a modified example of the surface heating element.

【符号の説明】[Explanation of symbols]

1 ケ−シング 2,24 スクリュ−コンベア 3 受皿 4 回転翼 5 籾米 6 支持杆 7 中空体 7A 傾斜上板 7B 側壁 8 有底内筒 8A テ−パ面 8B 側壁 8D ピット 8E 底部 9 籾米通路 10,11 通気孔 12a〜12c,12a’〜12c’ 放熱管群 13 放熱管(カ−トリッジタイプ) 13’ 放熱管(シ−スタイプ) 14 発熱体(ニクロム線) 15 焼結棒 16 金属管(表面に遠赤外線放射塗料塗工) 17 面発熱体 18 反射板 19 支持杆 20 測温子 21 吸気口 22 排気口 23 排気ファン 25 エレベ−タ 1 Casing 2,24 Screw Conveyor 3 Sauce 4 Rotating Blade 5 Paddy Rice 6 Support Rod 7 Hollow Body 7A Inclined Upper Plate 7B Sidewall 8 Bottomed Inner Cylinder 8A Tapered Surface 8B Sidewall 8D Pit 8E Bottom 9 Rice Paddy Path 10, 11 Vents 12a to 12c, 12a 'to 12c' Radiating tube group 13 Radiating tube (Cartridge type) 13 'Radiating tube (Cee type) 14 Heating element (Nichrome wire) 15 Sintered rod 16 Metal tube (on surface) Far-infrared radiation paint coating) 17 Surface heating element 18 Reflector 19 Support rod 20 Thermometer 21 Intake port 22 Exhaust port 23 Exhaust fan 25 Elevator

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 ケ−シング内に有底ホッパ状内筒を、そ
の上開口端周部をケ−シング内壁に接続して配設し、該
内筒の中心部に、中央部の高い中空体を配設して中空体
外周面と内筒側壁間に上下に連通する籾米通路を形成
し、該籾米通路の各対向壁にはそれぞれ籾米の通過し得
ない無数の通気孔を貫通形成し、前記中空体内には、反
射面を通気孔に対面させて反射板を立設し、該反射板と
通気孔間に遠赤外線放熱管群を区分的に立設し、該遠赤
外線放熱管群は区分毎にそれぞれ通風の流路上流側から
下流側へ順次高温放熱、中温放熱、低温放熱となるよう
放熱管を配列し、前記ケ−シングの天井部内には投入用
スクリュ−コンベアを架設し、前記籾米通路には温度調
節器の測温子を配設し、ケ−シングには排気ファンを有
する風胴を前記中空体の気流と連通状に設けたことを特
徴とする胴割れのない籾米の乾燥装置。
1. A hopper-shaped inner cylinder having a bottom is provided in the casing, the upper opening end peripheral portion of which is connected to the inner wall of the casing, and the central portion of the inner cylinder has a high hollow center. A body is provided to form a paddy rice passage that communicates vertically between the outer peripheral surface of the hollow body and the inner cylinder side wall, and innumerable vent holes through which the paddy rice cannot pass are formed in the respective opposing walls of the paddy rice passage. In the hollow body, a reflection plate is erected with the reflection surface facing the ventilation hole, and a far infrared radiation pipe group is erected in a segmented manner between the reflection plate and the ventilation hole. For each section, heat radiation pipes are arranged so that high-temperature heat radiation, medium-temperature heat radiation, and low-temperature heat radiation are sequentially arranged from the upstream side to the downstream side of the ventilation passage, and a charging screw conveyor is installed in the ceiling of the casing. A temperature sensor of a temperature controller is provided in the paddy rice passage, and a wind tunnel having an exhaust fan is provided in the casing as the hollow body. An apparatus for drying unhulled rice without cracks in the barrel, which is provided in communication with the air flow of
JP1992063120U 1992-08-18 1992-08-18 Dryer for paddy rice without cracks Expired - Lifetime JP2513078Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1992063120U JP2513078Y2 (en) 1992-08-18 1992-08-18 Dryer for paddy rice without cracks

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1992063120U JP2513078Y2 (en) 1992-08-18 1992-08-18 Dryer for paddy rice without cracks

Publications (2)

Publication Number Publication Date
JPH0622890U true JPH0622890U (en) 1994-03-25
JP2513078Y2 JP2513078Y2 (en) 1996-10-02

Family

ID=13220113

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2513078Y2 (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5657001A (en) * 1979-10-15 1981-05-19 Seiko Epson Corp Reflection preventing film
JPS60155882A (en) * 1983-12-29 1985-08-15 株式会社同和 Method and device for drying cereal

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5657001A (en) * 1979-10-15 1981-05-19 Seiko Epson Corp Reflection preventing film
JPS60155882A (en) * 1983-12-29 1985-08-15 株式会社同和 Method and device for drying cereal

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