JPH09113140A - Grain dryer - Google Patents
Grain dryerInfo
- Publication number
- JPH09113140A JPH09113140A JP29783295A JP29783295A JPH09113140A JP H09113140 A JPH09113140 A JP H09113140A JP 29783295 A JP29783295 A JP 29783295A JP 29783295 A JP29783295 A JP 29783295A JP H09113140 A JPH09113140 A JP H09113140A
- Authority
- JP
- Japan
- Prior art keywords
- grain
- chamber
- hot air
- air chamber
- burner
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
(57)【要約】
【課題】 穀粒を比較的短時間で、確実かつ均一に乾燥
することのできる穀粒乾燥機の加熱装置を提供する。
【解決手段】 外周に遠赤外線放射体を形成した放熱管
を熱風室、調質室または集穀室内に配備し、これらの放
熱管の一端にバーナを接続すると共に、放熱管の他端を
熱風室に接続し、遠赤外線による穀粒の加熱に加えて、
放熱管からの湿気のない乾いた熱風により穀粒の乾燥を
行う。これによりバーナの熱利用に無駄がなくなり熱効
率が向上する。
(57) Abstract: [PROBLEMS] To provide a heating device for a grain dryer capable of reliably and uniformly drying grains in a relatively short time. SOLUTION: A heat radiating pipe having a far infrared radiator formed on the outer periphery is provided in a hot air chamber, a tempering chamber or a grain collecting chamber, a burner is connected to one end of these radiating pipes, and the other end of the radiating pipe is hot air. In addition to heating the kernel with far infrared,
The grains are dried by dry, hot air from the radiant tube. As a result, the heat utilization of the burner is not wasted, and the thermal efficiency is improved.
Description
【0001】[0001]
【発明の属する技術分野】本発明は、機内を循環しなが
ら穀粒を乾燥させる穀粒乾燥機に関し、特にその加熱装
置の改良に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a grain dryer for drying grains while circulating them inside the machine, and more particularly to improvement of a heating device for the grain dryer.
【0002】[0002]
【従来の技術】従来、この種の穀粒乾燥機においては、
機体上部に穀粒の調質室を設け、その底部に通気構造の
穀粒流下通路を接続する。そして穀粒流下通路の下端の
落下口にロータリーバルブを設け、このロータリーバル
ブを介して穀粒流下通路の下端を機体底部の集穀室に接
続し、さらに穀粒流下通路を挟んで熱風室と排風室を隣
接し、熱風室にバーナを、排風室に吸引ファンをそれぞ
れ接続する。そしてロータリーバルブを回転し、調質室
の穀粒を穀粒流下通路を通して集穀室に落下し、これを
集穀ラセンと上昇エレベータおよび給穀ラセンにより再
び調質室に戻して機内を循環させ、同時に熱風室にバー
ナの熱風を送り、穀粒流下通路の穀粒の間を通過して、
穀粒を乾燥する。穀粒流下通路を通過後の湿気を含んだ
排熱風は、排風室の吸引ファンにより吸引し機外に排出
する。このように従来は、熱風を穀物に当てて伝熱だけ
で乾燥エネルギーを供給しているため、熱効率が十分で
はないという問題があった。2. Description of the Related Art Conventionally, in this type of grain dryer,
A grain refining chamber is provided at the top of the machine, and a grain-flowing passage with an aeration structure is connected to the bottom. A rotary valve is provided at the lower end of the grain flow passage, and the lower end of the grain flow passage is connected to the grain collection chamber at the bottom of the machine via this rotary valve. The exhaust chamber is adjacent to the burner and the suction fan is connected to the hot air chamber. Then, the rotary valve is rotated, and the grains in the tempering chamber are dropped into the grain collecting chamber through the grain flow passage, and are returned to the tempering chamber by the grain collecting spiral and the raising elevator and the grain feeding spiral to circulate in the machine. At the same time, the hot air of the burner is sent to the hot air chamber, passing between the grains in the grain flow passage,
Dry the grain. The exhaust hot air containing moisture after passing through the grain flow passage is sucked by the suction fan in the exhaust chamber and discharged to the outside of the machine. Thus, conventionally, there has been a problem that the thermal efficiency is not sufficient because the drying energy is supplied only by heat transfer by applying hot air to the grain.
【0003】[0003]
【発明が解決しようとする課題】本発明では、放射熱と
伝熱を併用して熱効率を上げ、穀粒を比較的短時間で、
ほぼ均一に乾燥することを目的とする。SUMMARY OF THE INVENTION In the present invention, radiant heat and heat transfer are used together to increase the thermal efficiency, and the grain can be removed in a relatively short time.
It is intended to be dried almost uniformly.
【0004】[0004]
【課題を解決するための手段】上記目的を達成するため
本発明では、外周に遠赤外線放射体を形成した放熱管を
熱風室内に配備し、この放熱管の一端にバーナを接続す
ると共に、放熱管の他端を前記熱風室内に開口した。ま
た、調質室内に山型の流穀板を設置し、この流穀板の下
方に、外周に遠赤外線放射体を形成した放熱管を配備
し、この放熱管の一端にバーナを接続すると共に、放熱
管の他端を熱風室に連通した。さらに、外周に遠赤外線
放射体を形成した放熱管を集穀室内に配備し、この放熱
管の一端にバーナを接続すると共に、放熱管の他端を熱
風室に連通した。In order to achieve the above object, in the present invention, a heat radiation tube having a far-infrared radiator formed on the outer circumference is provided in a hot air chamber, and a burner is connected to one end of the heat radiation tube and heat radiation is performed. The other end of the tube was opened into the hot air chamber. In addition, a mountain-shaped grain plate is installed in the tempering chamber, and a radiator pipe having a far infrared radiator formed on the outer periphery is arranged below the grain plate, and a burner is connected to one end of this radiator pipe. The other end of the heat radiation pipe was connected to the hot air chamber. Further, a heat radiation tube having a far-infrared radiator formed on the outer circumference was provided in the grain collection chamber, a burner was connected to one end of the heat radiation tube, and the other end of the heat radiation tube was connected to the hot air chamber.
【0005】[0005]
【発明の実施の形態】本発明の実施の形態を図面に示し
て説明する。図1は本発明を実施した穀粒乾燥機の構成
を示す正面断面図、図2はその一部を断面で示す側面図
である。機体1の上部に調質室2を設ける。調質室2の
底部左右に2組の傾斜板をV字形に相対して流穀部4を
形成する。流穀部4の上方には前後方向に伸びる板材に
より山形に形成された一対の流動規制山形13をそれぞ
れ設ける。左右の流穀部4の下端に、多孔板16により
囲った穀粒流下通路3を形成し、その下端部を機体1の
下部に設けた集穀室5にのぞませるとともに、下端部に
ロータリーバルブ6を設ける。多孔板16には多数の小
孔を穿設し通気性を付与する。穀粒流下通路3を挟み内
側に熱風室7を、外側に排風室8をそれぞれ隣接して設
け、熱風室7から穀粒流下通路3を横断して排風室8に
通風自在に形成する。熱風室7にはバーナ9を、排風室
8には吸引ファン10を接続する。調質室2には、その
天井中央に前後方向に伸びる給穀ラセン11を設け、そ
の終端に電動機(図示せず)に連結した拡散板12を設
置する。集穀室5には、その底部中央に前後方向に伸び
る集穀ラセン14を設け、集穀ラセン14の後端を上昇
エレベータ15に接続し、上昇エレベータ15の上端は
調質室2の給穀ラセン11の始端に接続し、調質室2か
ら穀粒流下通路3を通り、集穀室5から集穀ラセン1
4、上昇エレベータ15、給穀ラセン11を経て、拡散
板12により調質室2の上部に拡散する穀粒の循環経路
を形成する。Embodiments of the present invention will be described with reference to the drawings. FIG. 1 is a front sectional view showing the structure of a grain dryer according to the present invention, and FIG. 2 is a side view showing a part thereof in section. A heat treatment room 2 is provided above the fuselage 1. Two sets of inclined plates are formed on the left and right sides of the bottom of the tempering chamber 2 so as to face each other in a V shape to form the grain portion 4. A pair of flow-regulating chevrons 13 each formed in a chevron shape by a plate material extending in the front-rear direction are provided above the grain portion 4. Grain flow-down passages 3 surrounded by a perforated plate 16 are formed at the lower ends of the left and right flown grain portions 4, and the lower end portion thereof can be seen in a grain collection chamber 5 provided at the lower portion of the machine body 1, and the rotary portion at the lower end portion A valve 6 is provided. A large number of small holes are formed in the perforated plate 16 to provide air permeability. A hot air chamber 7 is provided on the inner side of the grain flow passage 3 and an exhaust air chamber 8 is provided on the outer side thereof so as to cross the grain flow passage 3 and to be freely ventilated to the exhaust air chamber 8. . A burner 9 is connected to the hot air chamber 7 and a suction fan 10 is connected to the air exhaust chamber 8. In the tempering chamber 2, a grain feeding spiral 11 extending in the front-rear direction is provided at the center of the ceiling, and a diffusing plate 12 connected to an electric motor (not shown) is provided at the end thereof. The grain-collecting chamber 5 is provided with a grain-collecting helix 14 extending in the front-rear direction at the center of the bottom, and the rear end of the grain-collecting helix 14 is connected to a lifting elevator 15, and the upper end of the lifting elevator 15 feeds the grain in the tempering chamber 2. Connected to the starting end of the helix 11, passed through the grain flow passage 3 from the tempering chamber 2, and from the grain collecting chamber 5 to the grain collecting helix 1.
4, through the ascending elevator 15 and the grain feeding helix 11, a diffusion plate 12 forms a circulation route for grains that diffuse to the upper part of the tempering chamber 2.
【0006】図2に示すように、熱風室7の正面には機
体1の外にバーナ9を設け、熱風室7内でバーナ9に連
結して後方に伸びる放熱管17をほぼ水平に配設し、熱
風室7の後部で上方にU字状に折返して、先端17aを
バーナ9側に戻して熱風室7内に開放する。放熱管17
は、バーナ9との接続部から所定の範囲を外管により覆
って二重管構造とし、二重管部18の外周に遠赤外線放
射体を形成する遠赤外線塗料(例えばオキツモ株式会社
製B−600)を塗装する。排風室8の背面に吸引ファ
ン10を機体1の外に設ける。As shown in FIG. 2, a burner 9 is provided outside the machine body 1 in the front of the hot air chamber 7, and a heat radiating pipe 17 connected to the burner 9 and extending rearward is disposed substantially horizontally in the hot air chamber 7. Then, at the rear of the hot air chamber 7, it is folded back upward in a U shape, and the tip 17a is returned to the burner 9 side and opened into the hot air chamber 7. Radiator tube 17
Is a far-infrared paint that forms a far-infrared radiator on the outer periphery of the double-tube portion 18 by covering a predetermined range from the connection portion with the burner 9 with an outer tube (for example, B- manufactured by Okitsumo Co., Ltd. 600) is painted. A suction fan 10 is provided outside the machine body 1 on the back surface of the exhaust chamber 8.
【0007】以上のように構成された穀粒乾燥機につい
て、その作用を説明する。調質室2に、収穫された穀粒
を上昇エレベータ15と給穀ラセン11により供給し、
穀粒を拡散板12の上に落下して拡散板12の回転によ
り、穀粒を調質室2内に広く均一に散布する。この時、
穀粒は穀粒流下通路3を埋めてロータリーバルブ6まで
到達する。この状態で、バーナ9により熱風を熱風室7
の放熱管17に送り、放熱管17の二重管部18をバー
ナ9からの熱風により直接加熱し、外周に塗装した遠赤
外線塗料から遠赤外線を放射する。ここで、二重管部1
8により管壁の過熱を防止する。二重管部18を加熱し
た熱風は、放熱管17の先端17aから熱風室7内に供
給する。そして熱風室7から穀粒流下通路3の穀粒の間
を通り、穀粒の含有水分を蒸発させ、湿った排熱風とな
って排風室8の吸引ファン10により吸引排気し、機外
に排出する。二重管部18の外周から放射された遠赤外
線は穀粒流下通路3の内壁を照射して加熱するととも
に、その多数の小孔を通して穀粒流下通路3内の穀粒を
直射する。遠赤外線の浸透により穀粒流下通路3内の穀
粒が均一に加熱され、穀粒内の含有水分の表面への移動
を促進し、穀粒の乾燥を早めるとともに、収縮、胴割
れ、かびの発生や変質等の欠陥を防止する。The operation of the grain dryer configured as described above will be described. The harvested grain is supplied to the tempering chamber 2 by the ascending elevator 15 and the grain feeding helix 11,
The grains are dropped onto the diffusion plate 12 and the diffusion plate 12 is rotated so that the grains are widely and uniformly dispersed in the tempering chamber 2. At this time,
The grain fills the grain flow path 3 and reaches the rotary valve 6. In this state, hot air is blown into the hot air chamber 7 by the burner 9.
The double pipe portion 18 of the heat radiating pipe 17 is directly heated by the hot air from the burner 9, and far infrared rays are radiated from the far infrared paint coated on the outer periphery. Here, double pipe section 1
8 prevents the tube wall from overheating. The hot air that has heated the double pipe portion 18 is supplied into the hot air chamber 7 from the tip 17 a of the heat dissipation pipe 17. Then, it passes between the grains in the grain flow passage 3 from the hot air chamber 7 to evaporate the moisture content of the grains to form moist exhaust hot air, which is sucked and exhausted by the suction fan 10 in the exhaust chamber 8 and then out of the machine. Discharge. Far-infrared rays emitted from the outer periphery of the double pipe section 18 irradiate and heat the inner wall of the grain flow-down passage 3, and directly irradiate the grain in the grain flow-down passage 3 through the numerous small holes. By the penetration of far infrared rays, the grains in the grain flow path 3 are heated uniformly, promoting the movement of the moisture content in the grains to the surface, speeding the drying of the grains, and shrinking, cracking, and mold Prevent defects such as generation and alteration.
【0008】ついで、ロータリーバルブ6により穀粒流
下通路3内の穀粒は、順次集穀室5に落下する。穀粒流
下通路3を下降する穀粒は、放熱管17の外周から放射
された遠赤外線により加熱され、同時に放熱管17の先
端17aからの熱風により乾燥する。集穀室5に落下し
た穀粒は集穀ラセン14により送られ、上昇エレベータ
15に移載して上昇し、上昇エレベータ15の上端で給
穀ラセン11に移り、拡散板12により調質室2の上部
に戻される。以後、穀粒が所定の水分率(例えば13〜14
%)になるまで繰り返し機内を循環する。このように図
1、2の例では、従来の循環型乾燥機の熱風室に放熱管
17を収容するため、従来の乾燥機をそのまま利用でき
経済的であり、乾燥能力も従来技術が利用でき把握しや
すいという利点がある。Then, the rotary valve 6 causes the grains in the grain flow-down passage 3 to sequentially fall into the grain collecting chamber 5. The grain descending through the grain flow-down passage 3 is heated by far infrared rays radiated from the outer periphery of the heat radiating pipe 17, and is simultaneously dried by hot air from the tip 17 a of the heat radiating pipe 17. Grains that have fallen into the grain collecting chamber 5 are sent by the grain collecting helix 14 and transferred to the ascending elevator 15 to ascend, move to the grain supplying helix 11 at the upper end of the ascending elevator 15, and the tempering chamber 2 is provided by the diffusion plate 12. Returned to the top of. After that, the grain has a predetermined moisture content (for example, 13 to 14).
%) Repeatedly circulating in the machine. As described above, in the example of FIGS. 1 and 2, since the radiation pipe 17 is housed in the hot air chamber of the conventional circulation type dryer, the conventional dryer can be used as it is, which is economical, and the conventional technology can be used for the drying capacity. It has the advantage of being easy to grasp.
【0009】図3は本発明の放熱管を調質室に設けた穀
粒乾燥機の構成を示す正面断面図、図4はその側面図、
図5はその正面図である。以下、図1および図2に示す
穀粒乾燥機と異なる部分について、その構造と作用を説
明する。調質室2には、中央に前後方向に伸びる2枚の
板を山形に取付けて流穀板23を形成し、その下に前後
方向に伸びる放熱管17を配置し、放熱管17の上方に
前後方向に伸びる断面円弧状の反射板19を設けて放熱
部20を形成する。放熱部20の後方に、機体1から外
側に突出してバーナ9を取付け、図6に示すように、後
方のバーナ9に二重管部18を先にして放熱管17を接
続し、放熱部20の前部で放熱管17を接続ブロック2
1を介して折り返し、その先端17aをバーナ9側に戻
して機体1の外側に突出する。放熱管17の二重管部1
8の外周には前述と同様に遠赤外線塗料を塗装する。放
熱管17の先端17aを、機体1に沿って下方に伸びる
連結管22に接続し、連結管22の下端を熱風室7に連
通する。調質室2の中央で放熱部20に対向する位置
に、2枚の流動規制板27の上端を内側面に取付け、下
方に向ってその間隔が狭まるように固定し、山形の放熱
部20との間にで穀粒の流路を形成して穀粒の流れを規
制する。以上のように構成することにより、バーナ9か
ら熱風を放熱管17に送り、二重管部18を加熱し、連
結管22を経由して熱風室7に送り、熱風室7から穀粒
流下通路3を通して排風室8に入り、機体1の前面に突
出して設けた吸引ファン10により機外に排出する。バ
ーナ9の熱風により放熱管17の二重管部18を加熱
し、二重管部18の外周に塗装した遠赤外線塗料から、
流穀板23の下方に形成された穀粒の空洞部の底部に露
出する穀粒に直射して、調質室2の穀粒をほぼ均一に加
熱する。このように、図3〜6の例では、調質室の穀粒
に遠赤外線を直接照射するので、穀粒は乾燥しないで温
度だけ上昇し、穀粒内部の水分分布がほぼ均一になる。
この穀粒が穀粒流下通路3を流下する際、放熱管17の
先端17aより供給される熱風にさらされるので、乾燥
が迅速に進行するという利点がある。FIG. 3 is a front sectional view showing the structure of a grain dryer in which the heat dissipation pipe of the present invention is provided in a tempering chamber, and FIG. 4 is a side view thereof.
FIG. 5 is a front view thereof. The structure and operation of the parts different from the grain dryer shown in FIGS. 1 and 2 will be described below. In the tempering chamber 2, two plates extending in the front-rear direction are attached in the center in a mountain shape to form a grain plate 23, and a heat radiating pipe 17 extending in the front-rear direction is disposed below the grain plate 23, and above the heat radiating pipe 17. A heat dissipation portion 20 is formed by providing a reflection plate 19 having an arcuate cross section that extends in the front-rear direction. The burner 9 is attached to the rear of the heat radiating portion 20 so as to project outward from the machine body 1. As shown in FIG. 6, the double pipe portion 18 is connected first to the heat radiating pipe 17 of the rear burner 9, and the heat radiating portion 20 is connected. Connect the heat dissipation pipe 17 at the front of the block 2
1, and the tip 17a thereof is returned to the burner 9 side and protrudes to the outside of the machine body 1. Double pipe part 1 of heat dissipation pipe 17
Far-infrared paint is applied to the outer periphery of 8 as described above. The tip 17a of the heat dissipation pipe 17 is connected to the connecting pipe 22 extending downward along the machine body 1, and the lower end of the connecting pipe 22 is communicated with the hot air chamber 7. The upper ends of the two flow regulating plates 27 are attached to the inner side surfaces at positions facing the heat radiating portion 20 in the center of the tempering chamber 2, and are fixed so that the distance between the flow regulating plates 27 is narrowed downward. A grain flow path is formed between them to regulate the grain flow. With the above configuration, the hot air is sent from the burner 9 to the radiating pipe 17, the double pipe portion 18 is heated, and sent to the hot air chamber 7 via the connecting pipe 22, and the hot air chamber 7 transfers the grain downflow passage. The air enters into the exhaust chamber 8 through 3, and is exhausted to the outside of the machine by a suction fan 10 provided so as to project on the front surface of the machine body 1. The double pipe portion 18 of the radiating pipe 17 is heated by the hot air of the burner 9, and the far-infrared paint applied to the outer periphery of the double pipe portion 18
The grains in the tempering chamber 2 are heated almost uniformly by directly irradiating the grains exposed at the bottom of the hollow portion of the grains formed below the shed plate 23. As described above, in the examples of FIGS. 3 to 6, since the grains in the tempering chamber are directly irradiated with far-infrared rays, the grains do not dry but rise in temperature and the moisture distribution inside the grains becomes substantially uniform.
When this grain flows down the grain flow path 3, it is exposed to the hot air supplied from the tip 17a of the heat radiating pipe 17, so that there is an advantage that the drying progresses quickly.
【0010】図7は本発明の放熱管を集穀室に設けた穀
粒乾燥機の構成を示す正面断面図、図8はその側面図で
ある。以下、図1および図2に示す穀粒乾燥機と異なる
部分について、その構造と作用を説明する。集穀室5の
上部中央に、熱風室7との間を仕切り左右に庇状の突出
片24を設けた仕切り板25を設け、仕切り板25の下
方に前後方向に平行して放熱管17を設ける。集穀室5
の前面に機体1から突出してバーナ9を取付け、バーナ
9に放熱管17の二重管部18を接続し、集穀室5の前
方で上方にU字状に折り返してバーナ9側に戻し、バー
ナ9側で連結U字管26により、その先端17aを熱風
室7にのぞませる。以上のように構成することにより、
バーナ9から熱風を放熱管17に送り、二重管部18を
加熱し、二重管部18の外周に塗装した遠赤外線塗料か
ら、集穀室5の穀粒に直射して加熱する。加熱された穀
粒は、集穀ラセン14、上昇エレベータ15、給穀ラセ
ン11、及び拡散板12により調質室2の上部に戻され
る。そして穀粒流下通路3を通過する際に、放熱管17
の先端17aより供給される熱風により加熱乾燥して、
湿った排熱風を排風室8から吸引ファン10により機外
に排出する。このように、図7、8の例では、バーナ9
の熱風を放熱管17を経てその先端17aより熱風室7
に供給して穀粒を乾燥する。この穀粒は穀粒流下通路3
より集穀室5を連続して流れる際、放熱管17の遠赤外
線照射を受ける。このため、熱風を浴びて表層部と中心
部の水分分布に格差を生じた穀粒が、遠赤外線照射によ
り内部まで加熱され水分分布が平均化し、調質室2での
調質作用が円滑に行われるという利点がある。FIG. 7 is a front sectional view showing the construction of a grain dryer in which the heat radiation tube of the present invention is provided in the grain collection chamber, and FIG. 8 is a side view thereof. The structure and operation of the parts different from the grain dryer shown in FIGS. 1 and 2 will be described below. At the center of the upper part of the grain collecting chamber 5, a partition plate 25 is provided which partitions the space between the hot air chamber 7 and the eaves-like projecting pieces 24 on the right and left sides, and below the partition plate 25, the radiating pipe 17 is arranged in parallel with the front-rear direction. Set up. Grain collection room 5
The burner 9 is attached to the front of the machine so as to project from the machine body 1, the double pipe portion 18 of the heat radiating pipe 17 is connected to the burner 9, and it is folded back upward in a U-shape in front of the grain collection chamber 5 and returned to the burner 9 side. At the burner 9 side, the tip 17a of the connecting U-shaped tube 26 is looked into the hot air chamber 7. By configuring as above,
Hot air is sent from the burner 9 to the heat radiating pipe 17 to heat the double pipe portion 18, and the far infrared coating material applied to the outer periphery of the double pipe portion 18 is directly radiated to the grains in the grain collecting chamber 5 for heating. The heated grain is returned to the upper portion of the tempering chamber 2 by the grain collecting helix 14, the raising elevator 15, the grain feeding helix 11, and the diffusion plate 12. When passing through the grain flow-down passage 3, the heat dissipation pipe 17
By heating and drying with hot air supplied from the tip 17a of
The moist exhaust hot air is discharged from the exhaust chamber 8 to the outside of the machine by the suction fan 10. Thus, in the example of FIGS. 7 and 8, the burner 9
Hot air from the hot air chamber 7 through the radiating pipe 17 from the tip 17a.
To dry the grain. This grain is the grain flow path 3
When continuously flowing through the grain collection chamber 5, the radiation pipe 17 receives far infrared radiation. Therefore, the grains that have been exposed to the hot air and have a difference in water distribution between the surface layer portion and the center portion are heated to the inside by far-infrared irradiation and the water distribution is averaged, so that the tempering action in the tempering chamber 2 is smoothly performed. It has the advantage of being done.
【0011】[0011]
【発明の効果】本発明では、バーナに接続する放熱管の
外周に遠赤外線放射体を形成し、バーナの熱風により放
熱管を加熱して遠赤外線を放射し、乾燥機内を循環する
穀粒を遠赤外線により加熱するとともに、放熱管を通過
した熱風を熱風室に還流して、穀粒流下通路3を流下す
る穀粒を通風加熱する。放熱管より出る熱風は湿気を含
まないから、穀粒流下通路3の穀粒を充分乾燥する能力
がある。従って、本発明によれば、遠赤外線による加熱
と湿気のない熱風による乾燥とが並行して進行し、穀粒
を効率良く乾燥でき、乾燥時間の短縮と消費熱量の削減
が達成できる。INDUSTRIAL APPLICABILITY In the present invention, a far-infrared radiator is formed on the outer periphery of a heat-radiating pipe connected to a burner, the heat-radiating pipe is heated by the hot air of the burner to radiate far-infrared light, and grains circulating in a dryer are collected. While heating with far infrared rays, the hot air that has passed through the heat radiation pipe is returned to the hot air chamber, and the grains that flow down through the grain downflow passage 3 are heated by ventilation. Since the hot air discharged from the heat radiation pipe does not contain moisture, it has the ability to sufficiently dry the grains in the grain flow passage 3. Therefore, according to the present invention, heating by far infrared rays and drying by hot air having no moisture proceed in parallel, grain can be efficiently dried, and shortening of drying time and reduction of heat consumption can be achieved.
【図1】本発明の穀粒乾燥機の構成を示す正面断面図で
ある。FIG. 1 is a front sectional view showing the configuration of a grain dryer of the present invention.
【図2】同上側面図である。FIG. 2 is a side view of the same.
【図3】本発明の放熱管を調質室に設けた穀粒乾燥機の
構成を示す正面断面図である。FIG. 3 is a front cross-sectional view showing the configuration of a grain dryer in which a heat dissipation pipe of the present invention is provided in a tempering chamber.
【図4】同上穀粒乾燥機の側面図である。FIG. 4 is a side view of the same grain dryer.
【図5】同上穀粒乾燥機の背面図てある。FIG. 5 is a rear view of the same grain dryer.
【図6】同上穀粒乾燥機の放熱管の構成を示す平面図で
ある。FIG. 6 is a plan view showing a configuration of a heat radiating tube of the same grain dryer.
【図7】本発明の放熱管を集穀室に設けた穀粒乾燥機の
構成を示す正面断面図である。FIG. 7 is a front cross-sectional view showing the configuration of a grain dryer in which the heat radiation tube of the present invention is provided in the grain collection chamber.
【図8】同上穀粒乾燥機の側面図である。FIG. 8 is a side view of the same grain dryer.
1 機体 2 調質室 3 穀粒流下通路 4 流穀部 5 集穀室 6 ロータリーバルブ 7 熱風室 8 排風室 9 バーナ 10 吸引ファン 11 給穀ラセン 12 拡散板 13 流動規制山形 14 集穀ラセン 15 上昇エレベータ 16 多孔板 17 放熱管 18 二重管部 19 反射板 20 放熱部 21 接続ブロック 22 連結管 23 流穀板 24 突出片 25 仕切り板 26 連結U字管 27 流動規制板 1 Airframe 2 Conditioning room 3 Grain flow path 4 Grain flow section 5 Grain collecting room 6 Rotary valve 7 Hot air chamber 8 Exhaust air chamber 9 Burner 10 Suction fan 11 Grain feeding spiral 12 Diffusion plate 13 Flow control Yamagata 14 Grain collecting helix 15 Lifting elevator 16 Perforated plate 17 Radiating pipe 18 Double pipe part 19 Reflecting plate 20 Radiating part 21 Connection block 22 Connecting pipe 23 Grains board 24 Projecting piece 25 Partition plate 26 Connecting U-shaped pipe 27 Flow regulating plate
───────────────────────────────────────────────────── フロントページの続き (71)出願人 000197344 静岡製機株式会社 静岡県袋井市山名町4番地の1 (71)出願人 000144898 株式会社山本製作所 山形県天童市大字老野森404番地 (72)発明者 久保田 興太郎 埼玉県大宮市日進町1丁目40番地2号 生 物系特定産業技術研究推進機構内 (72)発明者 柏嵜 勝 埼玉県大宮市日進町1丁目40番地2号 生 物系特定産業技術研究推進機構内 (72)発明者 市川 友彦 埼玉県大宮市日進町1丁目40番地2号 生 物系特定産業技術研究推進機構内 (72)発明者 上谷 弘践 愛媛県伊予郡砥部町八倉1番地 井関農機 株式会社技術部内 (72)発明者 小條 ▲れい▼二 愛媛県伊予郡砥部町八倉1番地 井関農機 株式会社技術部内 (72)発明者 土門 正幸 埼玉県羽生市西2丁目21番10号 金子農機 株式会社内 (72)発明者 池田 智 埼玉県羽生市西2丁目21番10号 金子農機 株式会社内 (72)発明者 造賀 和成 広島県東広島市八本松町原6981番2号 (72)発明者 宮武 義邦 静岡県袋井市久能1232番5号 (72)発明者 武田 俊広 山形県天童市大字老野森404番地 株式会 社山本製作所内 ─────────────────────────────────────────────────── ─── Continuation of the front page (71) Applicant 000197344 Shizuoka Machinery Co., Ltd. 1-4 Yamana-cho, Fukuroi-shi, Shizuoka Prefecture (71) Applicant 000144898 Yamamoto Manufacturing Co., Ltd. 404 Noomori, Tendo-shi, Yamagata Prefecture (72) Invention Kotaro Kubota 1-40-2 Nisshin-cho, Omiya-shi, Saitama Biotechnology-Specific Industrial Technology Research Organization (72) Inventor Katsuo Katsuzaki 1-40-2 Nisshin-cho, Omiya-shi, Saitama Bio-specific industries Within the Technical Research Promotion Organization (72) Inventor Tomohiko Ichikawa 1-40-2 Nisshin-cho, Omiya City, Saitama Prefecture Within the Research Promotion Organization for Specific Industrial Technology for Biotechnology (72) Inventor Hironori Uetani 1 Yakura, Tobe Town, Iyo-gun, Ehime Prefecture Address: Iseki Agricultural Machinery Co., Ltd. Technical Department (72) Inventor Kojo ▲ Rei ▼ No. 1, Yakura, Tobe-cho, Iyo-gun, Ehime Prefecture Iseki Agricultural Machinery Co., Ltd. (72) Inventor Masayuki Domon 2-21-10 West, Hanyu-shi, Saitama Prefecture Kaneko Agricultural Machinery Co., Ltd. (72) Inventor Satoshi Ikeda 2--21-10 West, Hanyu City, Saitama Prefecture Kaneko Agricultural Machinery Co., Ltd. (72) Inventor Zoka Waseri 6981-2, Hachihonmatsuchohara, Higashihiroshima City, Hiroshima Prefecture (72) Inventor Yoshikuni Miyatake 1232-5 Kuno, Fukuroi City, Shizuoka Prefecture (72) Inventor Toshihiro Takeda 404, Oonomori, Tendo City, Yamagata Corporation Yamamoto Manufacturing Co., Ltd. Within
Claims (3)
すると共に、該穀粒流下通路下端を集穀室に接続し、 穀粒流下通路を挟んで熱風室と排風室を設け、 外周に遠赤外線放射体を形成した放熱管を前記熱風室内
に配備し、この放熱管の一端に前記バーナを接続すると
共に、放熱管の他端を前記熱風室内に開口して成る穀粒
乾燥機。1. A grain-flowing passage having a ventilation structure is connected to the tempering chamber, a lower end of the grain-flowing passage is connected to a grain-collecting chamber, and a hot air chamber and an exhaust air chamber are provided with the grain-flowing passage sandwiched therebetween. , A heat radiating tube having a far infrared radiator formed on the outer periphery is provided in the hot air chamber, the burner is connected to one end of the heat radiating tube, and the other end of the heat radiating tube is opened in the hot air chamber to dry the grain. Machine.
すると共に、該穀粒流下通路下端を集穀室に接続し、 穀粒流下通路を挟んで熱風室と排風室を設け、 前記調質室内に山型の流穀板を設置し、この流穀板の下
方に、外周に遠赤外線放射体を形成した放熱管を配備
し、この放熱管の一端にバーナを接続すると共に、放熱
管の他端を前記熱風室に連通して成る穀粒乾燥機。2. A tempering chamber is connected to a grain flow-down passage having a ventilation structure, a lower end of the grain flow-down passage is connected to a grain collecting chamber, and a hot air chamber and an exhaust air chamber are provided across the grain flow-down passage. , A mountain-shaped grain plate is installed in the tempering chamber, a radiation pipe having a far infrared radiator formed on the outer periphery is arranged below the grain plate, and a burner is connected to one end of the radiation pipe. , A grain dryer in which the other end of the heat radiation pipe is connected to the hot air chamber.
すると共に、該穀粒流下通路下端を集穀室に接続し、 穀粒流下通路を挟んで熱風室と排風室を隣接し、 外周に遠赤外線放射体を形成した放熱管を前記集穀室内
に配備し、この放熱管の一端にバーナを接続すると共
に、放熱管の他端を前記熱風室に連通して成る穀粒乾燥
機。3. The tempering chamber is connected to a grain flow-down passage having a ventilation structure, the lower end of the grain flow-down passage is connected to a grain collecting chamber, and the hot air chamber and the exhaust air chamber are adjacent to each other with the grain flow-down passage interposed therebetween. Then, a heat radiating tube having a far infrared radiator formed on the outer periphery is arranged in the grain collecting chamber, a burner is connected to one end of the heat radiating tube, and the other end of the heat radiating tube is connected to the hot air chamber. Dryer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP29783295A JPH09113140A (en) | 1995-10-20 | 1995-10-20 | Grain dryer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP29783295A JPH09113140A (en) | 1995-10-20 | 1995-10-20 | Grain dryer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH09113140A true JPH09113140A (en) | 1997-05-02 |
Family
ID=17851738
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP29783295A Pending JPH09113140A (en) | 1995-10-20 | 1995-10-20 | Grain dryer |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH09113140A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH1114259A (en) * | 1997-06-25 | 1999-01-22 | Seibutsukei Tokutei Sangyo Gijutsu Kenkyu Suishin Kiko | Grain drying method in far infrared dryer |
| KR100430446B1 (en) * | 1999-08-24 | 2004-05-10 | 가부시끼가이샤 사따께 | Circulating type grain drying machine |
| JP2008051491A (en) * | 2006-08-21 | 2008-03-06 | Shin Hung Industry Co Ltd | Supersized far-infrared circulation type grain drier, and grain drying method for reducing water content deviation between grain layers in storage chamber |
-
1995
- 1995-10-20 JP JP29783295A patent/JPH09113140A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH1114259A (en) * | 1997-06-25 | 1999-01-22 | Seibutsukei Tokutei Sangyo Gijutsu Kenkyu Suishin Kiko | Grain drying method in far infrared dryer |
| KR100430446B1 (en) * | 1999-08-24 | 2004-05-10 | 가부시끼가이샤 사따께 | Circulating type grain drying machine |
| JP2008051491A (en) * | 2006-08-21 | 2008-03-06 | Shin Hung Industry Co Ltd | Supersized far-infrared circulation type grain drier, and grain drying method for reducing water content deviation between grain layers in storage chamber |
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