JPS60159579A - Circulation type cereal drier - Google Patents

Circulation type cereal drier

Info

Publication number
JPS60159579A
JPS60159579A JP1316584A JP1316584A JPS60159579A JP S60159579 A JPS60159579 A JP S60159579A JP 1316584 A JP1316584 A JP 1316584A JP 1316584 A JP1316584 A JP 1316584A JP S60159579 A JPS60159579 A JP S60159579A
Authority
JP
Japan
Prior art keywords
ventilation
air
chamber
temperature
condenser
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
Application number
JP1316584A
Other languages
Japanese (ja)
Inventor
河田 憲文
牛木 良仁
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.)
KOURIYOU DENGIYOU KK
SHINOMIYA KK
Original Assignee
KOURIYOU DENGIYOU KK
SHINOMIYA KK
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 KOURIYOU DENGIYOU KK, SHINOMIYA KK filed Critical KOURIYOU DENGIYOU KK
Priority to JP1316584A priority Critical patent/JPS60159579A/en
Publication of JPS60159579A publication Critical patent/JPS60159579A/en
Pending legal-status Critical Current

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Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 従来の可燃油や可燃ガスを使用する循環式穀類乾燥機に
おいては、 (イ)乾燥風の温度が高いため、胴割れが発生し易い。
[Detailed Description of the Invention] In conventional circulation grain dryers that use combustible oil or gas, (a) shell cracking is likely to occur due to the high temperature of the drying air.

(ロ) 排気ガスが出るため、その排気ガスによる公害
がある上に、不完全燃焼時には燃料油の臭いが乾燥物に
耐着し、一方、燃焼音による運転時の騒音が高く、且つ
火災発生の危険性がある。
(b) Exhaust gas is emitted, which causes pollution, and when incomplete combustion occurs, the odor of fuel oil sticks to dry matter, and on the other hand, combustion noise causes high noise during operation, and fires occur. There is a risk of

(ハ)排気乾燥、または1部循環乾燥方式であるから、
熱を捨てながらの運転で、熱損失が大きい。
(c) Because it uses exhaust air drying or a partial circulation drying method,
There is a large amount of heat loss due to operation while discarding heat.

に)可燃油や可燃ガスの燃料保管設備、配管設備、附随
する安全設備等の設備が必要である上に、燃料の補給輸
送等に費用がかかる。
2) Facilities such as fuel storage equipment for flammable oil and combustible gas, piping equipment, and accompanying safety equipment are required, and costs are incurred for replenishing and transporting fuel.

等の欠点があった。There were other drawbacks.

そこで、本発明は上記欠陥を解消するため、ヒートポン
プ型の冷却装置を利用し、乾燥根本体の取出し室内に吹
込まれる含湿空気を蒸発器により冷却して結露させ水分
を機外に排出して脱湿乾燥した後、凝結器の放熱により
加温し、その脱湿乾燥して加温された乾燥空気を乾燥機
本体の通風乾燥室の乾燥空気室内に供給し、空気を循環
させて穀粒の水分を乾燥空気に吸収し、且つ乾燥空気の
温度が設定温度に達したときは、上記冷却装置に連結し
た通風冷却機の凝縮器により排熱して蒸発器による含湿
空気の脱湿乾燥のみを行い、燃料を使用することなく、
100〜40℃の低い温度の乾燥空気を循環させて胴割
れが発生することなく、乾燥を短時間で均一良好になし
得るようにしたことを特徴とする循環式穀類乾燥機に係
るものである。
Therefore, in order to eliminate the above-mentioned defects, the present invention utilizes a heat pump type cooling device, and uses an evaporator to cool the humid air blown into the drying base removal chamber, condenses it, and discharges the moisture outside the machine. After dehumidifying and drying the grain, it is heated by the heat radiation of the condenser, and the heated dry air is supplied to the dry air chamber of the ventilation drying chamber of the dryer main body, and the air is circulated to dry the grain. When the moisture of the grains is absorbed into the dry air and the temperature of the dry air reaches the set temperature, the heat is exhausted by the condenser of the ventilation cooler connected to the above cooling device, and the humid air is dehumidified and dried by the evaporator. without using fuel.
This relates to a circulation type grain dryer characterized by circulating dry air at a low temperature of 100 to 40°C, thereby achieving uniform and good drying in a short period of time without causing shell cracks. .

図面に示す本発明の1実施態様についてその構造を説明
すれば、(1)は循環式穀類乾燥機の乾燥機本体で、内
部には調質室(21、通風乾燥室(3)および取出し室
(4)を上方より順次立体的に構成し、その通風乾燥室
(3)内に通気網より成る乾燥空気室(5)を設け、底
面は通気網によってV字形に形成し、乾燥空気室(5)
と通風乾燥室(3)の底面の間に両側の穀粒流下路(6
)を設けてその底面下端の落下口にロータリーバルブ(
7)を装設する。
To explain the structure of one embodiment of the present invention shown in the drawings, (1) is a dryer main body of a circulating grain dryer, and the interior includes a conditioning chamber (21), a ventilation drying chamber (3), and a take-out chamber. (4) is constructed three-dimensionally from above, and a drying air chamber (5) made of a ventilation net is provided in the ventilation drying chamber (3), and the bottom surface is formed into a V shape by the ventilation net. 5)
and the bottom of the ventilation drying chamber (3), there are grain flow channels (6) on both sides.
) and a rotary valve (
7).

一方、取出し室(4)内の中間部に取出し用スクリュー
コンベヤ(8)を設け、1側壁の前部には開口(9)を
形成してその外側に排風機0αを連設する。
On the other hand, a take-out screw conveyor (8) is provided in the middle part of the take-out chamber (4), an opening (9) is formed in the front part of one side wall, and a blower 0α is connected to the outside of the opening (9).

(Illは本体(1)の上方に設けた供給用スクリュー
コンベヤで、スクリューコンベヤ(81の出口とスクリ
ューコンベヤαυの入口を本体(11の他側に附設した
昇降機α2により連結するときに、該昇降機α2の上端
出口に排出樋αJを連設し、図示してないが、スクリュ
ーコンベヤoDの入口と排出樋a3の上端入口の間には
、交互にそれらへ穀粒を供給可能の切替弁を設ける。I
は乾燥空気室(5)の他側壁に装設した乾燥空気入口、
(15)は取出し室(4)の他側壁後部に設けた含湿空
気出口、(161は昇降機Q21の下端前方の供給口に
附設した張込み漏斗である。
(Ill is a supply screw conveyor provided above the main body (1), and when the outlet of the screw conveyor (81) and the inlet of the screw conveyor A discharge gutter αJ is connected to the upper end outlet of α2, and although not shown, a switching valve is provided between the inlet of the screw conveyor oD and the upper end inlet of the discharge gutter a3, which can alternately supply grains thereto. .I
is the dry air inlet installed on the other side wall of the dry air chamber (5),
(15) is a moist air outlet provided at the rear of the other side wall of the take-out chamber (4), and (161 is a feeding funnel attached to the supply port in front of the lower end of the elevator Q21).

αnは本体(1)の他側後部に装設した乾燥空気発生機
の機体、轡は機体an内の1側部に形成した伏U字形の
通風路で、その下方風路a嘗の1端間口は蛇腹(2)に
よって含湿空気出口a9に、上方風路(211の1端間
口は蛇腹c2zによって乾燥空気人口−にそれぞれ連結
する。そして、下方風路■内の1側部に濾過器■を、中
間部に吸引送風機(2)をそれぞれ設けて上方風路(2
1+内の1側部には供給用送風機(至)を装設する。@
は下方風路仕り内に臨ませて設けた温度感知器、(27
1は通風路(119の他側に仕切って装設した空室、(
2)は空室鰭の上方前部に取付けた制御盤、e9は制御
盤(至)の温度調節用つまみである。
αn is the body of the dry air generator installed at the rear of the other side of the main body (1), and 轡 is an inverted U-shaped ventilation passage formed on one side of the body (an), and one end of the downward air passage a. The frontage is connected to the humid air outlet a9 by a bellows (2), and the opening at one end of the upper air passage (211) is connected to the dry air outlet by a bellows c2z.Then, a filter is connected to one side of the lower air passage (2). ■A suction blower (2) is installed in the middle part of the upper air passage (2).
A supply blower (to) is installed on one side of 1+. @
is a temperature sensor installed facing inside the lower air duct (27).
1 is a ventilation duct (a vacant room partitioned and installed on the other side of 119,
2) is a control panel attached to the upper front part of the cavity fin, and e9 is a temperature adjustment knob on the control panel (toward).

(alは機体αη上に設けた通風冷却機を示し、(至)
は冷却機(alの胴体で、その1側端上に外気人口C3
1)を、他側に排気口3′IJをそれぞれ形成し、該胴
体(至)内の他側部に送風機(至)を設ける。
(al indicates the ventilation cooler installed on the aircraft αη, (to)
is the fuselage of the cooler (al), with outside air population C3 on one side end of it.
1), an exhaust port 3'IJ is formed on the other side, and a blower is provided on the other side of the body.

(b)はヒートボング型の冷却装置を示し、04)はそ
の圧縮機で、空室回内に設置する。命圓翰は再熱用凝縮
器、冷却除湿用蒸発器、排熱用凝縮器で、その再熱用凝
縮器(至)は上方風路(211内の他側部に、冷却除湿
用蒸発器(至)は通風路a8の他側壁と再熱用凝縮器C
9の間に、排熱用凝縮器C371は胴体(至)内の1側
部にそれぞれ設置する。
(b) shows a heat bong type cooling device, and 04) is its compressor, which is installed in the empty chamber. The life condenser has a reheating condenser, a cooling dehumidifying evaporator, and a waste heat condenser. (To) is the other side wall of ventilation passage a8 and reheat condenser C
9, the exhaust heat condensers C371 are each installed on one side of the fuselage.

而して、第7図に示すように、圧縮機C34)の冷媒押
出口と再熱用凝縮器6■の入口を電磁3方弁■付きパイ
プ田により、再熱用凝縮器(ハ)の出口と冷却除湿用蒸
発器伽)の入口を膨張弁(41J付きパイプ卿により、
冷却除湿用蒸発益田の出口と圧縮機ぷ)の冷媒入口をパ
イプ(4zによりそれぞれ連通し、その電磁3方弁(至
)と排熱用凝縮器G′71の入口をパイプ(431によ
り、排熱用凝縮器4371の出口と冷却除湿用蒸発器(
至)の入口を膨張弁(441付きパイプ(49によりそ
れぞれ連通する。
As shown in Fig. 7, the refrigerant extrusion port of the compressor C34) and the inlet of the reheat condenser 6 are connected to the reheat condenser (c) by a pipe equipped with an electromagnetic three-way valve. Connect the outlet and the inlet of the cooling and dehumidifying evaporator with an expansion valve (41J pipe).
The outlet of the evaporator Masuda for cooling and dehumidification and the refrigerant inlet of the compressor P) are connected through a pipe (4z), and the solenoid three-way valve (to) and the inlet of the exhaust heat condenser G'71 are connected through a pipe (431). The outlet of the heat condenser 4371 and the cooling and dehumidifying evaporator (
The inlets of the expansion valves (441 and 49) are connected to each other by pipes (49).

また、図示してないが、送風機241.(5)、(至)
、温度感知器(至)、制御盤(2)、圧縮機(Aおよび
電磁3方弁(至)の間には、制御盤(2)のスイッチを
入れれば、送風機(財)(至)および圧縮機(至)が運
転を開始し、本体(1)および通風室ae内の乾燥空気
の温度が設定温度に達したとき、温度感知器(イ)の感
知により自動的に電磁3方弁(至)がパイプG9側から
パイプ03側に切替わると共に、送風機@が運転を開始
する電気回路を構成する。
Although not shown, a blower 241. (5), (to)
, temperature sensor (To), control panel (2), compressor (A and solenoid 3-way valve (To)). When the compressor (to) starts operating and the temperature of the dry air in the main body (1) and ventilation chamber ae reaches the set temperature, the electromagnetic three-way valve ( (to) is switched from the pipe G9 side to the pipe 03 side, and constitutes an electric circuit in which the blower @ starts operating.

次にその作用を説明する。最初乾燥機の運転を開始した
後、穀粒な漏斗a(へ)内に投入し昇降機Q21および
スクリューコンベヤaυを経て本体+11内に供給し、
その本体(1)内の乾燥室(3)から調質室(2)内に
わたって所定量部ったとき漏斗αeへの穀粒の投入を止
めれば、乾燥室(3)および調質室(2)内の穀粒は、
ロータリーバルブ(7)の回転により順次徐々に調質室
(2(内から乾燥室(31の流下路(6)内を下降して
乾燥室(3)の下端落下口より取出し室(4)内に落下
し、スクリューコンベヤ(8)、昇降機Q3、スクリュ
ーコンベヤ(111を介し本体(1)内に還元されて本
体(11内を循環する。
Next, its effect will be explained. After starting the operation of the dryer, the grains are put into a funnel a and fed into the main body +11 via an elevator Q21 and a screw conveyor aυ.
If the grains are stopped from being fed into the funnel αe when a predetermined amount has passed from the drying chamber (3) to the tempering chamber (2) in the main body (1), then the drying chamber (3) and the tempering chamber (2) can be stopped. ) The grains in
As the rotary valve (7) rotates, it gradually descends from the inside of the conditioning chamber (2) through the flow path (6) of the drying chamber (31) and enters the take-out chamber (4) from the lower end of the drying chamber (3). , and is returned to the main body (1) via the screw conveyor (8), elevator Q3, and screw conveyor (111), and circulates within the main body (11).

一方、制御盤(2)のスイッチを入れて乾燥空気発生機
の運転を開始し、その後、つまみ(至)を回転して穀粒
に応じた10°−40℃内の所定温度に設定すると、 (5)初期には圧縮機(2)の運転により、冷媒が第7
図に実線矢印で示すように、圧縮機(財)から電磁3方
弁(2)、パイプC39を通り凝縮器(ハ)内に圧入さ
れて該凝縮器−から放熱され、次いで、パイプ(4]l
、膨張弁(4υを通って蒸発器夏向に至り蒸発して該蒸
発器□□□を冷却し、その後パイプ(42)を通って圧
縮機(2)に戻る。
On the other hand, turn on the control panel (2) to start operating the dry air generator, and then turn the knob (to) to set the predetermined temperature within 10°-40°C depending on the grain. (5) Initially, due to the operation of the compressor (2), the refrigerant is
As shown by the solid line arrow in the figure, the compressor passes through the electromagnetic three-way valve (2) and pipe C39, is press-fitted into the condenser (c), and is radiated from the condenser. ]l
, through the expansion valve (4υ) to reach the evaporator, evaporate and cool the evaporator, and then return to the compressor (2) through the pipe (42).

一方、送風機(241四の運転によって本体(11およ
び機体aD内の空気は第3図に矢印で示すように乾燥室
(3)、取出し室(4)および通風路Q8内を循環する
から、空気室(5)より流下路(6)内の順次下降する
穀粒中を通過して取出し室(4)内に至った含湿空気は
、出口(151から濾過器■を通過し除塵されて下方風
路a9内に吸入される。
On the other hand, when the blower (2414) is operated, the air inside the main body (11) and the airframe aD is circulated through the drying chamber (3), the take-out chamber (4), and the ventilation passage Q8 as shown by the arrow in FIG. The humid air that has passed through the grains that descend sequentially in the flow path (6) from the chamber (5) and reached the take-out chamber (4) passes through the outlet (151) and the filter ■, where it is dust-removed and sent downward. It is sucked into the air passage a9.

而して、上記吸入風は、通風路α稀の他側壁と蒸発器(
3)間、蒸発器■と凝縮器−間の両空間内に分岐して進
行し、その通風路Q8の他側壁と蒸発器(ト)間の空間
内に進行した風は蒸発器(ト)を通過し、該蒸発益田の
通過時に冷却されて結露し、水分は機体αη外に排出さ
れ、空気は大気中における相対湿度が20チ〜25チま
で脱湿乾燥されて蒸発益田と凝縮器(ト)間の空間内に
至り、該空間内に直接進行してくる含湿空気と合する。
Therefore, the above-mentioned intake air flows through the ventilation passage α and the other side wall of the evaporator (
3) The air branches off into the space between the evaporator (■) and the condenser (2), and the air that advances into the space between the other side wall of the ventilation passage Q8 and the evaporator (G) flows through the evaporator (G). The air is cooled and condensed as it passes through the evaporator, and the moisture is discharged outside the aircraft αη, and the air is dehumidified and dried until the relative humidity in the atmosphere reaches 20 to 25 cm, and then passes through the evaporator and condenser ( g), and is combined with the humid air that advances directly into the space.

その適度に脱湿乾燥された空気は、凝縮器間を通過して
該凝縮器(至)の通過時に加温され、温度を高められた
乾燥空気は上方風路c!Dを通って入口圓がら空気室(
5)内に供給され、流下路(6)内の穀粒中を通過する
どき穀粒の脱湿乾燥をなし、以下順次上記作用が繰返さ
れながら空気は循環して穀粒の循環乾燥作業が行われる
。一方、時間の経過に伴って循環乾燥空気の温度は次第
に上昇する。
The air, which has been appropriately dehumidified and dried, passes between the condensers and is warmed as it passes through the condensers, and the heated dry air passes through the upper air passage c! Through D, enter the air chamber (
5) The grains are dehumidified and dried as they pass through the grains in the flow path (6), and the above actions are repeated sequentially while the air is circulated and the grains are circulated and dried. It will be done. On the other hand, the temperature of the circulating dry air gradually increases as time passes.

なお、作業開始当初においては、排風機aαを運転すれ
ば、穀粒中に混入していて取出し室(4)内に吹込まれ
る塵埃を順次排風機0Qにより吸引し本体(1)外に排
出しで本体(1)内の除塵を行うことができる。その後
、排風機00)の運転を停止すると、上記循環乾燥作業
が行われる。
In addition, at the beginning of the work, if the exhaust fan aα is operated, the dust mixed in the grains and blown into the extraction chamber (4) will be suctioned by the exhaust fan 0Q and discharged to the outside of the main body (1). It is possible to remove dust from inside the main body (1). Thereafter, when the operation of the exhaust fan 00) is stopped, the circulation drying operation described above is performed.

(B) 而して、上記循環空気の温度が設定温度に達す
ると、温度感知器Qθの感知によって自動的に電磁3方
弁(至)がパイプ(43側に切替わると共に、送風機(
至)が運転を開始する。
(B) When the temperature of the circulating air reaches the set temperature, the temperature sensor Qθ automatically switches the electromagnetic three-way valve (to) to the pipe (43 side) and the blower (
) starts operation.

従って、冷媒が第7図に点線矢印で示すように、圧縮機
(財)から電磁3方弁(至)、パイプ(113を通り凝
縮器(3p内に圧入されて#凝縮器Gnから放熱され、
次いでパイプ(ハ)、膨張弁(転)を通って蒸発器製内
に至り蒸発して該蒸発器■を冷却し、その後パイプ(4
2を通って圧縮機(財)に戻る。
Therefore, as shown by the dotted line arrow in Fig. 7, the refrigerant passes from the compressor, through the electromagnetic three-way valve (to), to the pipe (113), and is pressurized into the condenser (3p), where the heat is radiated from the condenser Gn. ,
Next, it passes through the pipe (c) and the expansion valve (converter) into the evaporator, where it evaporates and cools the evaporator (2).
2 and returns to the compressor (goods).

一方、送風機(至)の運転によって外気が入口(31)
から胴体(至)内に吸入されて凝縮器C371を通過し
、該凝縮器Gnの通過時に凝縮器C371の冷却を行い
、その冷却を行って温まった排気は出口G2から胴体(
3o)外に放出される。
On the other hand, the outside air is inlet (31) by the operation of the blower (to).
The exhaust gas is sucked into the fuselage (to) and passes through the condenser C371, and as it passes through the condenser Gn, the condenser C371 is cooled, and the heated exhaust gas is passed through the outlet G2 to the fuselage (
3o) Released outside.

それ故、凝縮器(ト)は閉じられてこれを冷媒が通らな
く、本体(1)と機体aη内を循環する空気は蒸発器(
至)の通過時に冷却されて結露するだけで加温されない
から、その循環空気の温度は次第に下降する。
Therefore, the condenser (g) is closed so that no refrigerant passes through it, and the air circulating inside the main body (1) and the aircraft body aη is kept in the evaporator (g).
The temperature of the circulating air gradually decreases because it is only cooled and condensed as it passes through the air and is not heated.

(Q 而して、上記循環空気の温度が設定温度まで下降
すると、温度感知器(至)の感知により自動的に電磁3
方弁□□□がパイプC31側に切替わって上記(5)の
作用が行われる。
(Q) When the temperature of the circulating air drops to the set temperature, the electromagnetic 3
The direction valve □□□ is switched to the pipe C31 side, and the above operation (5) is performed.

以下、順次上記作用が自動的に繰返され、流下路(6)
には均一な温度の脱湿乾燥空気が定速で通過して乾燥作
用が行われる。
Thereafter, the above actions are automatically repeated one after another, and the flow path (6)
The drying effect is performed by passing dehumidified dry air of uniform temperature at a constant speed.

その際、つまみ(至)を回動操作することにより、本体
(11と機体(17)内の循環空気温度を106〜40
℃の範囲内で自由に調節して設定することができる。
At that time, by rotating the knob (to), the circulating air temperature in the main body (11 and fuselage (17)) can be adjusted to 106 to 40.
It can be freely adjusted and set within the range of °C.

本発明は循環式穀類乾燥機を上記のように構成したから
、 (イ)乾燥空気の温度が106〜40℃の範囲で低いた
め、急激な温度変化がなくて胴割れの発生が少ない。
Since the circulation type grain dryer of the present invention is configured as described above, (a) the temperature of the drying air is low in the range of 106 to 40°C, so there is no sudden temperature change and there is little occurrence of shell cracking.

(ロ)乾燥空気の脱湿効率が良い上に、その乾燥空気の
加温が相俟つヤ乾燥時間を大幅に短縮でき、且つ乾燥空
気の温度が設定温度に達すると、自動的に冷媒を通風冷
却機の凝縮器に切替え機外に排熱して乾燥空気は蒸発器
による冷却と結露のみがなされるから、終始均一な適当
温度の脱湿乾燥空気で乾燥を行って作業能率を向上する
(b) In addition to the high dehumidification efficiency of dry air, the drying time can be significantly shortened by heating the dry air, and when the temperature of the dry air reaches the set temperature, the refrigerant is automatically turned on. Switching to the condenser of the ventilation cooler, the heat is exhausted outside the machine, and the dry air is only cooled and condensed by the evaporator, so drying is performed with dehumidified dry air at a uniform and appropriate temperature throughout, improving work efficiency.

e] 可燃油、可燃ガスを全く使用しないから、排気ガ
スによる公害がない上に、燃焼音がなくて運転時の音が
低く、且つ運転時の温度は最高40℃と低(て火災発生
の危険性は極めて少なく、安心して運転を放置しておく
ことができる。
e] Since no flammable oil or gas is used, there is no pollution caused by exhaust gas, there is no combustion noise, the noise during operation is low, and the operating temperature is low (maximum 40 degrees Celsius) (and there is no risk of fire occurring). There is very little danger, and you can leave the car running with confidence.

に)乾燥空気を常時循環させて運転するため、熱損失は
極めて少ない上に、熱源は電気のみであるから、燃料保
管設備、配管設備、燃料の補給輸送、附随する安全設備
等の費用を節減できる。
2) Since dry air is constantly circulated during operation, heat loss is extremely low, and the only heat source is electricity, reducing costs for fuel storage equipment, piping equipment, fuel supply and transportation, and associated safety equipment. can.

(ホ)温度設定とスイッチを入れる操作だけで連続運転
をなし得る上に、乾燥空気の温度を穀粒の乾燥に適した
温度に任意に設定することができ、且つ脱湿による排出
水量で乾燥度の検知をなし得られ、運転管理が容易で取
扱い易い。
(e) Not only can continuous operation be achieved by simply setting the temperature and turning on the switch, the temperature of the drying air can be arbitrarily set to a temperature suitable for drying the grains, and the amount of water discharged from dehumidification can be used to dry the grains. It is easy to operate, manage and handle.

(へ) 1台のビートポンプ型の冷却装置で乾燥空気の
冷却と加温の両件用を行うので、簡単に構成できる。
(f) One beat pump type cooling device performs both cooling and heating of dry air, so it can be configured easily.

等の効果がある。There are other effects.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の1実施態様を示す循環式穀類乾燥機の
正面図、第2図は同上側面図、第3図は第2図の1−1
線断面図、第4図は第3図の1m−II線断面図、第5
図は第3図の■−■線断面図、第6図は第3図のI’V
−IV線断面図、第7図はそのビートポンプ型冷却装置
の配管図である。
Fig. 1 is a front view of a circulating grain dryer showing one embodiment of the present invention, Fig. 2 is a side view of the same, and Fig. 3 is 1-1 in Fig. 2.
Line sectional view, Figure 4 is a 1m-II line sectional view of Figure 3, Figure 5
The figure is a sectional view taken along the ■-■ line in Figure 3, and Figure 6 is a cross-sectional view of I'V in Figure 3.
-IV line sectional view and FIG. 7 are piping diagrams of the beat pump type cooling device.

Claims (1)

【特許請求の範囲】[Claims] 調質室、通風乾燥室および取出し室を上方より順次立体
的に構成して穀粒が循環する乾燥機本体の側壁には、そ
の通風乾燥室内に装設した乾燥空気室に臨む空気入口、
および取出し室に臨む空気出口を設け、上記空気出口と
空気入口を通風路により連通して該通風路内には送風機
を設けると共に、ヒートポンプ型冷却装置の蒸発器およ
び凝縮器を適当間隔に並設し、機体外の通風冷却機内に
設けた凝縮器と上記冷却装置を電磁3方弁を介装したパ
イプ回路により連結し、その通風路付き乾燥機本体内の
適当箇所に臨ませた温度感知器と上記電磁3方弁と温度
調節用制御盤の間には、乾燥空気の温度が所定温度に達
したとき、温度感知器の感知により電磁3方弁が上記の
通風路内の凝縮器側から通風冷却機の凝縮器側へ切替わ
る電気回路を形成したことを特徴とする循環式穀類乾燥
機。
The side wall of the main body of the dryer, which has a conditioning chamber, a ventilation drying chamber, and a take-out chamber arranged three-dimensionally from above to circulate grain, has an air inlet facing a drying air chamber installed in the ventilation drying chamber.
and an air outlet facing the extraction chamber, the air outlet and the air inlet are communicated through a ventilation passage, and a blower is provided in the ventilation passage, and an evaporator and a condenser of a heat pump type cooling device are installed in parallel at appropriate intervals. The condenser installed in the ventilation cooler outside the machine and the above cooling device are connected by a pipe circuit with a three-way electromagnetic valve, and a temperature sensor is installed at an appropriate location inside the dryer body with ventilation ducts. Between the above electromagnetic 3-way valve and the temperature control control panel, when the temperature of the dry air reaches a predetermined temperature, the electromagnetic 3-way valve operates from the condenser side in the above ventilation path when the temperature sensor detects the temperature. A circulating grain dryer characterized by forming an electric circuit that switches to the condenser side of the ventilation cooler.
JP1316584A 1984-01-26 1984-01-26 Circulation type cereal drier Pending JPS60159579A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1316584A JPS60159579A (en) 1984-01-26 1984-01-26 Circulation type cereal drier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1316584A JPS60159579A (en) 1984-01-26 1984-01-26 Circulation type cereal drier

Publications (1)

Publication Number Publication Date
JPS60159579A true JPS60159579A (en) 1985-08-21

Family

ID=11825557

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1316584A Pending JPS60159579A (en) 1984-01-26 1984-01-26 Circulation type cereal drier

Country Status (1)

Country Link
JP (1) JPS60159579A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0493587A (en) * 1990-08-06 1992-03-26 Kubota Corp Dehumidifying and drying machine

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0493587A (en) * 1990-08-06 1992-03-26 Kubota Corp Dehumidifying and drying machine

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