JPH0528469Y2 - - Google Patents

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Publication number
JPH0528469Y2
JPH0528469Y2 JP1987012355U JP1235587U JPH0528469Y2 JP H0528469 Y2 JPH0528469 Y2 JP H0528469Y2 JP 1987012355 U JP1987012355 U JP 1987012355U JP 1235587 U JP1235587 U JP 1235587U JP H0528469 Y2 JPH0528469 Y2 JP H0528469Y2
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JP
Japan
Prior art keywords
chamber
hot air
dust
exhaust
chambers
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Expired - Lifetime
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JP1987012355U
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Japanese (ja)
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JPS63120086U (en
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Publication of JPS63120086U publication Critical patent/JPS63120086U/ja
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Description

【考案の詳細な説明】 産業上の利用分野 本考案は、穀物を循環流動させながら能率よく
乾燥させることができる穀物乾燥機に関する。
[Detailed Description of the Invention] Industrial Application Field The present invention relates to a grain dryer that can efficiently dry grain while circulating it.

従来の技術 従来、乾燥通路において、前後方向に分けられ
た穀物の流れを乾燥通路を通過したあと、左右方
向に流れが変わる所謂交差流下方式によつて高水
分穀物の流動性をより向上させ、高水分穀物とい
えども均一かつ品質よく仕上げ乾燥させることが
できる穀物乾燥機は本出願前例えば特公昭61−
55037号公報に記載されており、その内容を第4
図について説明する。
Conventional Technology Conventionally, in a drying passage, the flow of grains divided into front and back directions is changed from side to side after passing through the drying passage, which is the so-called cross-flow method, to further improve the fluidity of high-moisture grains. A grain dryer capable of finishing and drying even high-moisture grains evenly and with good quality was developed before this application was filed, for example, in
It is stated in Publication No. 55037, and its contents are
The diagram will be explained.

すなわち、前後方向に長い横長角筒状の乾燥機
本体1内の下半分左右両側に熱風送風室2と排塵
風室3とを対称的に設け、上記熱風送風室2と排
塵風室3との間には横長方向と直交する方向に向
け、熱風送風室2に通ずる複数の熱風室4と排塵
風室3に通ずる複数の排風室5とを両室4,5間
に巾狭の乾燥通路6が形成せられるよう交互に架
設し、前記複数の乾燥通路6の下端は乾燥通路
6、熱風室4及び排風室5の直下に横長方向に沿
い複数列に亘り配設した山形仕切壁7により形成
された複数の交差流下繰出し室8……へ夫々接続
せしめると共に夫々の交差流下繰出し室8の下部
に横長方向に沿い回転自在に軸架した繰出しロー
ル9……は周囲を熱風送風室2、排塵風室3及び
繰出し室8で囲まれた取出し室10にのぞませて
構成したものである。
That is, the hot air blowing chamber 2 and the dust exhausting air chamber 3 are symmetrically provided on both left and right sides of the lower half of the dryer main body 1, which is in the shape of a rectangular cylinder long in the front and back direction. A plurality of hot air chambers 4 communicating with the hot air blowing chamber 2 and a plurality of exhaust chambers 5 communicating with the dust removal chamber 3 are arranged in a narrow width direction between the two chambers 4 and 5 in a direction perpendicular to the horizontal direction. The lower ends of the plurality of drying passages 6 are arranged in multiple rows along the horizontal direction directly below the drying passages 6, the hot air chamber 4, and the exhaust chamber 5. The pay-out rolls 9 are connected to a plurality of cross-flow feed-out chambers 8 formed by the partition wall 7, and are rotatably mounted at the bottom of each cross-flow feed-out chamber 8 in the horizontal direction, and are surrounded by hot air. It is constructed so as to look into a take-out chamber 10 surrounded by a blowing chamber 2, a dust exhaust chamber 3, and a feeding chamber 8.

考案が解決しようとする問題点 ところで、従前のこの種、穀物乾燥機を使用し
て穀物の乾燥を行う場合にあつては被乾燥穀物中
には多くの塵埃が含まれており、これが塵埃を速
かに除去しない場合には塵埃の混入作用で被乾燥
穀物は正確な交差状態を営みながら流下しなくな
る許りか、流下ムラ現象を起し、高水分穀物を均
一かつ品質よく仕上げ乾燥をさせることができな
い。
Problems that the invention aims to solve By the way, when drying grain using a conventional grain dryer of this type, the grain to be dried contains a lot of dust, and this If it is not removed quickly, the grain to be dried will not flow down while maintaining a precise crossing state due to the contamination of dust, or it will cause an uneven flow phenomenon, making it difficult to finish and dry high moisture grains uniformly and with good quality. I can't.

しかしながら、上記公知の穀物乾燥機において
は、被乾燥穀物が乾燥機本体内を順次交差状態の
もとに乾燥されながら流下した後、取出し室に排
出される過程において塵埃を除去する手段が採用
されていないので、どうしても塵埃除去のために
数多くの部材が必要となるは勿論のこと構成も複
雑となる。
However, in the above-mentioned known grain dryer, a means is adopted to remove dust during the process of the grain being dried being sequentially passed through the main body of the dryer while being dried in an intersecting state and then being discharged into the unloading chamber. Therefore, not only a large number of members are required for removing dust, but also the structure becomes complicated.

その上、従前のこの種穀物乾燥機にあつては、
乾燥穀物を一時的に貯留しておくための調質槽
は、通常、乾燥熱風を流通させないで、穀物自体
の水分拡散移動作用のみを行わせていたので、穀
物の胴割れ発生を防止しながら乾燥の促進をより
向上させることができないという問題点を有して
いた。
Moreover, in the case of conventional grain dryers of this type,
Normally, tempering tanks for temporarily storing dried grains do not allow drying hot air to flow through them, but only allow moisture to diffuse and move within the grains themselves. This had the problem that the acceleration of drying could not be further improved.

本考案は従来の技術の有するこのような問題点
に鑑みてなされたものであり、その目的とすると
ころは、乾燥通路において前後方向に分けられた
穀物の流れを乾燥通路を通過したあと、左右方向
に流れが変わる所謂交差流下方式によつて高水分
穀物の流動性をより向上させて能率的な乾燥作業
を行わせるものであつても、穀物中に多く含まれ
た塵埃を熱風送風室から取出し室を経て集塵室に
向けて流通する乾燥熱風の風選作用で速かに選別
除去せしめると共に調質槽内を竪流下する穀物に
対して並行流する清浄乾燥熱風を積極的に浴びせ
て、より均一な乾燥作業を迅速に達成させること
ができる穀物乾燥機を提供しようとするものであ
る。
The present invention was devised in view of the above-mentioned problems of the conventional technology, and its purpose is to separate the grain flow, which is divided into front and back directions in the drying passage, after passing through the drying passage. Even if the so-called cross-flow method, in which the flow changes in one direction, improves the fluidity of high-moisture grains and performs efficient drying, the dust contained in the grains can be removed from the hot air blowing chamber. The grains are quickly sorted and removed by the wind selection action of the dry hot air that flows through the extraction chamber to the dust collection room, and the clean dry hot air that flows parallel to the grains flowing vertically in the tempering tank is actively sprayed. , it is an object of the present invention to provide a grain dryer that can quickly accomplish a more uniform drying operation.

問題点を解決するための手段 本考案は、前記問題点を解決するものであつ
て、以下にその内容を実施例に対応する第1図な
いし第3図を用いて説明する。
Means for Solving the Problems The present invention is intended to solve the above-mentioned problems, and its contents will be explained below using FIGS. 1 to 3, which correspond to embodiments.

乾燥機本体101を前後方向に長い横長角筒状
に形成する。そして前記乾燥機本体101内に、
横長方向と直交する方向に沿つて複数の熱風室1
05と排風室107とを両室105,107間に
巾狭の乾燥通路109が形成されるよう交互に架
設する。上記複数の乾燥通路109の上端は調質
槽110に、又下端は乾燥通路109、熱風室1
05及び排風室107の直下に横長方向に沿い複
数列に亘り配設した山形仕切壁111により形成
された複数の交差流下繰出し室112へ夫々接続
せしめてある。そして前記夫々の交差流下繰出し
室112の下端は取出し室119にのぞませてあ
る。
The dryer main body 101 is formed into a horizontally long rectangular tube shape that is long in the front-rear direction. And inside the dryer main body 101,
A plurality of hot air chambers 1 along the direction perpendicular to the horizontal direction
05 and exhaust chambers 107 are alternately constructed so that a narrow drying passage 109 is formed between both chambers 105 and 107. The upper ends of the plurality of drying passages 109 are connected to the tempering tank 110, and the lower ends thereof are connected to the drying passage 109 and the hot air chamber 1.
05 and the exhaust chamber 107 are respectively connected to a plurality of cross-flow downward feeding chambers 112 formed by chevron-shaped partition walls 111 arranged in a plurality of rows along the horizontal direction. The lower ends of each of the cross-flow downstream dispensing chambers 112 are exposed to a dispensing chamber 119.

前記乾燥機本体101内に配設された調質槽、
熱風室105、排風室107、交差流下繰出し室
112及び取出し室119の左右両側には横長方
向に沿い排塵風室102及び熱風送風室103と
集塵室104とを対称的に設けて、排塵風室10
2と排風室107を、又熱風室105と集塵室1
04とを夫々接続し、熱風送風室102は通風路
128、取出し室119および通風路129を経
て集塵室104に接続せしめる。前述した調質槽
110内の上部位置には集塵室104に一端接続
されて除塵した清浄乾燥熱風を下段の排風室10
7に向け下向きに噴出流通せしめる複数列の噴出
体を横長方向と直交する方向に沿い並設して構成
したものである。
a tempering tank disposed within the dryer main body 101;
A dust removal chamber 102, a hot air blowing chamber 103, and a dust collecting chamber 104 are symmetrically provided along the horizontal direction on both the left and right sides of the hot air chamber 105, the exhaust chamber 107, the cross-flow downward feeding chamber 112, and the take-out chamber 119, Dust exhaust air chamber 10
2 and exhaust chamber 107, and hot air chamber 105 and dust collection chamber 1.
04, respectively, and the hot air blowing chamber 102 is connected to the dust collecting chamber 104 through a ventilation passage 128, a take-out chamber 119, and a ventilation passage 129. The upper part of the tempering tank 110 mentioned above is connected at one end to the dust collecting chamber 104, and the clean dry hot air from which dust is removed is sent to the lower ventilation chamber 10.
7, a plurality of rows of ejecting bodies are arranged in parallel in a direction orthogonal to the horizontal direction.

作 用 今、被乾燥穀物を、乾燥機本体101内に供給
すれば、該穀物は乾燥通路109及び交差流下繰
出し室112さらに乾燥通路109より上位の調
質槽110内に充填され、熱風室105、排風室
107及び噴出体130全体を穀物により閉塞状
態ならしめる。
Operation If the grains to be dried are now supplied into the dryer main body 101, the grains are filled into the drying passage 109, the cross-flow feed-out chamber 112, and the tempering tank 110 above the drying passage 109, and are filled into the hot air chamber 105. , the exhaust chamber 107 and the entire ejection body 130 are closed with grains.

以上のようにして所定量の穀物が乾燥機本体1
01内に充填されたら、その供給を停止し熱風室
103内において乾燥熱風を起成せしめると同時
に排塵風室102内を負圧状態ならしめる。
In the above manner, a predetermined amount of grain is delivered to the dryer body 1.
01 is filled, the supply is stopped, dry hot air is generated in the hot air chamber 103, and at the same time, the inside of the dust exhaust air chamber 102 is brought into a negative pressure state.

さすれば、熱風送風室103内において起成さ
れた乾燥熱風は排塵風室102における負圧作用
で、熱風送風室103、取出し室119、集塵室
104を通つて複数の熱風室105内に入り、次
いで熱風室105から出て乾燥通路109を横切
つて排風室107に入り、さらに排風室より排塵
風室103内に吸引された後、機外遠方へ集中排
風される一方、乾燥熱風の一部は集塵室104よ
り複数列の噴出体130……内に送風され、乾燥
熱風を下段の排風室107に向け下向きに流通せ
しめる。したがつて、穀物の繰出し作用で調質槽
110内を竪流下された穀物は複数列の噴出体1
30……より並行流する乾燥熱風を浴びて乾燥さ
れた後、熱風室105及び排風室107で分けら
れて前後方向の乾燥通路109に入つた後、乾燥
通路109中を順次竪流下される過程で流通する
乾燥熱風を浴び乾燥され、次いで乾燥通路109
を通過したあとの穀物は、今度は山形仕切壁11
1により左右方向に流れが変わる所謂交差流下状
態を呈しながら交差流下繰出し室112に流下堆
積された後、繰出し作用により取出し室119内
に順次排出される。
Then, the dry hot air generated in the hot air blowing chamber 103 passes through the hot air blowing chamber 103, the extraction chamber 119, and the dust collection chamber 104 into the plurality of hot air chambers 105 due to the negative pressure action in the dust exhausting chamber 102. The dust then exits from the hot air chamber 105, crosses the drying passage 109, enters the exhaust chamber 107, is further sucked into the dust exhaust chamber 103 from the exhaust chamber, and is then concentratedly exhausted to a far distance outside the machine. On the other hand, a part of the dry hot air is blown from the dust collection chamber 104 into the plurality of rows of blowing bodies 130 . Therefore, the grains that are vertically flowed down inside the tempering tank 110 by the grain feeding action are ejected from the plurality of rows of ejection bodies 1.
30... After being dried by being exposed to drying hot air flowing in parallel, it is divided into a hot air chamber 105 and an exhaust chamber 107, enters a front-back drying passage 109, and then is sequentially flowed down vertically in the drying passage 109. In the process, it is exposed to the circulating dry hot air and is then dried in the drying passage 109.
After passing through the grain, the grain passes through the chevron partition wall 11.
1, the particles are deposited in the cross-flow feed-out chamber 112 while exhibiting a so-called cross-flow state in which the flow changes in the left-right direction, and then sequentially discharged into the take-out chamber 119 by the feed-out action.

それ故、調質槽110内において並行流する乾
燥熱風で幾分乾燥された穀物が乾燥通路109を
流下した時の穀物の流れ方向は交差流下繰出し室
112に落入する時には直交する方向に変向され
るため初期含水分値の異なる穀物は交差流下繰出
し室112に落入する際、効果的に攪拌混合さ
れ、初期含水分値の異なる穀物といえども複数回
の循環流動作動で乾燥熱風により乾燥ムラを起す
ことなく均一に乾燥されると同時に、交差流下状
態によつて穀物の流動性も向上され、流下ムラを
起すことなく均等に流下される。そして取出し室
119内に散乱状態のもとに排出された塵埃を多
く含んだ乾燥穀物は、熱風送風室103より通風
路128を経て取出し室119内を横切り、さら
に通風路129を経て集塵室104に向け流通す
る乾燥熱風を浴びて乾燥穀物より塵埃のみを風選
別し、これが塵埃を流通する乾燥熱風で集塵室1
04に運びこれが塵埃を集塵せしめ除塵作業を行
う。
Therefore, the flow direction of the grains, which have been somewhat dried by the dry hot air flowing in parallel in the tempering tank 110, when they flow down the drying passage 109 changes to a direction perpendicular when they fall into the cross-flow feed-out chamber 112. Therefore, grains with different initial moisture contents are effectively stirred and mixed when they fall into the cross-flow feed-out chamber 112, and even grains with different initial moisture contents can be mixed by drying hot air by multiple circulation flow operations. The grains are dried uniformly without uneven drying, and at the same time, the fluidity of the grains is improved due to the cross-flow condition, and the grains are evenly flowed down without uneven drying. The dried grains containing a large amount of dust discharged in a scattered state into the take-out chamber 119 pass from the hot air blowing chamber 103 through the ventilation passage 128, cross the inside of the take-out chamber 119, and further pass through the ventilation passage 129 to the dust collection chamber. The dust is separated from the dried grains by being exposed to the dry hot air flowing towards the dust collection chamber 104.
04, where it collects dust and performs dust removal work.

それ故、取出し室119内に排出された乾燥穀
物は塵埃の混入が少ない許りか、噴出体130…
…より下向きに噴出する乾燥熱風も清浄化される
は勿論のこと、横切るように流通する乾燥熱風で
さらに乾燥が促進されるので、これが乾燥穀物を
複数回に亘り循環返流させれば、穀物は所要の含
水率に乾燥されるものである。
Therefore, the dried grains discharged into the take-out chamber 119 contain less dust, and the ejector 130...
...Not only is the drying hot air blowing downwards cleaned, but the drying hot air flowing across the area further accelerates drying, so if the dried grains are circulated and returned several times, is dried to the required moisture content.

実施例 本考案に係る穀物乾燥機の一実施例を図面につ
いて説明する。
Embodiment An embodiment of the grain dryer according to the present invention will be described with reference to the drawings.

図面において、101は、前後方向に長い横長
角筒状を呈する乾燥機本体であつて、該乾燥機本
体101内の左右上下両側には横長方向に沿い排
塵風室102及び熱風送風室103と集塵室10
4とを対称的に設けてある。
In the drawings, reference numeral 101 denotes a dryer main body that has a rectangular cylindrical shape that is long in the front and back direction, and a dust exhaust air chamber 102 and a hot air blower chamber 103 are provided along the horizontal direction on both left and right upper and lower sides of the dryer main body 101. Dust collection room 10
4 are provided symmetrically.

そして、上記排塵風室102と集塵室104と
の間の空間上方位置には横長方向と直交する方向
に向け、一側が集塵室104と送風窓106を介
し接続した先止め状の複数からなる熱風室105
と、一側が排塵風室102と排風窓108を介し
て接続した先止め状の複数からなる排風室107
を、熱風室105と排風室107との間に乾燥通
路109が形成せられるよう交互に架設して、前
記乾燥通路109の上端側は熱風室105及び排
風室107の上部に形成した調質槽110に接続
せしめると共に、その下端側は熱風室105及び
排風室107の直下に横長方向に沿い複数列に亘
り配設した山形仕切壁111により形成された複
数の交差流下繰出し室112に接続せしめてあ
る。上記熱風室105及び排風室107は乾燥通
路114に形成すると共に下部を開放115及び
116して、熱風室104及び排風室107内部
を交差流下繰出し室112と接続せしめてある。
したがつて、熱風室105、排風室107及び乾
燥通路109の長さが短かく形成できると同時に
その数を多くして、調質槽110内に充填された
穀物の堆積圧が大きくても、熱風室105及び排
風室107が彎曲することなく、その耐久性を大
きくできる許りか、送風窓106及び排風窓10
8の数も増加させて熱風送風室103より送風さ
れる乾燥熱風の送風抵抗を減少させ、熱風送風室
103よりの送風量を多くできる。
At a position above the space between the dust exhaust air chamber 102 and the dust collection chamber 104, a plurality of end-stopped holes are connected at one side to the dust collection chamber 104 through a ventilation window 106, facing in a direction perpendicular to the horizontal direction. Hot air chamber 105 consisting of
and a plurality of air exhaust chambers 107 connected on one side to the dust exhaust air chamber 102 through an air exhaust window 108.
are installed alternately so that a drying passage 109 is formed between the hot air chamber 105 and the exhaust air chamber 107, and the upper end side of the drying passage 109 is connected to the air conditioner formed above the hot air chamber 105 and the exhaust air chamber 107. In addition to being connected to the pawn tank 110, the lower end thereof is connected to a plurality of cross-flow downstream feeding chambers 112 formed by chevron-shaped partition walls 111 arranged in a plurality of rows along the horizontal direction directly below the hot air chamber 105 and the exhaust chamber 107. It is connected. The hot air chamber 105 and the exhaust chamber 107 are formed in a drying passage 114 and have open lower portions 115 and 116 to connect the insides of the hot air chamber 104 and the exhaust chamber 107 to the cross-flow downward delivery chamber 112.
Therefore, the lengths of the hot air chamber 105, the exhaust chamber 107, and the drying passage 109 can be made short, and at the same time, the number of them can be increased, so that even if the deposition pressure of the grains filled in the tempering tank 110 is high, , the ventilation window 106 and the ventilation window 10 may be able to increase their durability without causing the hot air chamber 105 and the ventilation chamber 107 to curve.
8 is also increased, the blowing resistance of the dry hot air blown from the hot air blowing chamber 103 can be reduced, and the amount of air blown from the hot air blowing chamber 103 can be increased.

又、熱風室105と排風室107の下部を開放
115及び116したことにより、乾燥通路10
9が流下する穀物中に混入した塵埃等の一部が通
風路113及び114より熱風室105及び排風
室107内に進入しても、該塵埃等が熱風室10
5及び排風室107内底部に堆積されることな
く、総て円滑に下部の交差流下繰出し室112へ
流下させ、堆積塵埃等の引火燃焼による穀物乾燥
機の火災事故を防止できる。
In addition, by opening the lower portions 115 and 116 of the hot air chamber 105 and the exhaust chamber 107, the drying passage 10
Even if part of the dust mixed into the grains 9 flows down enters the hot air chamber 105 and the exhaust chamber 107 from the ventilation passages 113 and 114, the dust and the like enters the hot air chamber 10
5 and the inner bottom of the exhaust chamber 107, and all of the dust flows smoothly down to the lower cross-flow dispensing chamber 112, thereby preventing fire accidents in the grain dryer due to ignition and combustion of accumulated dust and the like.

その上、さらに熱風室105及び排風室107
の直下に複数の山形仕切壁111により複数の交
差流下繰出し室112が形成されているため、乾
燥通路109において前後方向に分けられた穀物
の流れを乾燥通路109を通過したあと、今度は
左右方向に流れを変えて交差流下せしめ、初期含
水分値の異なる穀物を効率よく攪拌混合せしめる
と同時に穀物の流動性を向上させて、穀物の乾燥
ムラ及び流下ムラを無くして均一に乾燥させこと
ができる。
Furthermore, a hot air chamber 105 and an exhaust chamber 107
A plurality of cross-flow downward feeding chambers 112 are formed by a plurality of chevron-shaped partition walls 111 directly under the drying passage 109, so that after passing through the drying passage 109, the grain flow divided in the front-rear direction in the drying passage 109 is then transferred in the left-right direction. By changing the flow to cross flow, it is possible to efficiently stir and mix grains with different initial moisture contents, and at the same time improve the fluidity of grains, eliminating uneven drying and uneven flow of grains and drying them uniformly. .

なお上記交差流下繰出し室112内には、乾燥
通路109を経て流下した穀物が常に充満してい
るので、熱風や排塵風の漏出を未然に防止でき
る。
Note that, since the cross-flow down-feeding chamber 112 is always filled with grains that have flowed down through the drying passage 109, leakage of hot air and dust air can be prevented.

山形仕切壁111の各谷部には横長方向に沿つ
て繰出し口117が開口されており、この繰出し
口117位置には間欠回転される繰出しロール1
18が回転自在に軸架されている。交差流下繰出
し室112の下部には周囲を熱風送風室103、
集塵室104、繰出し室112及び乾燥機本体1
01の前後壁板により囲まれた取出し室119を
配設すると共に、熱風送風室103と集塵室10
4の下部間隔には排出樋120を横長方向に沿つ
て配設して、これが搬出樋120を取出し室11
9と接続せしめる。なお搬出樋120の内部には
搬出スクリユー121が回転自在に横架されてお
り、前記搬出樋120の一端は乾燥機本体101
の一側に付設した循環昇降機122の下部に接続
せしめると共に循環昇降機122の上部は乾燥機
本体101の頂部に横長方向に沿い横設した搬入
樋123の供給側へ接続せしめる。
A feed-out port 117 is opened along the horizontal direction in each valley of the chevron-shaped partition wall 111, and a feed-out roll 1 that is intermittently rotated is located at the position of the feed-out port 117.
18 is rotatably mounted on a shaft. A hot air blowing chamber 103 surrounds the lower part of the cross-flow downward feeding chamber 112,
Dust collection chamber 104, feeding chamber 112, and dryer main body 1
A take-out chamber 119 surrounded by the front and rear wall plates of 01 is provided, as well as a hot air blowing chamber 103 and a dust collection chamber 10.
4, a discharge gutter 120 is arranged along the horizontal direction, and this drains the discharge gutter 120 into the extraction chamber 11.
Connect it to 9. Note that a carry-out screw 121 is rotatably horizontally suspended inside the carry-out gutter 120, and one end of the carry-out gutter 120 is connected to the dryer main body 101.
It is connected to the lower part of a circulation elevator 122 attached to one side, and the upper part of the circulation elevator 122 is connected to the supply side of a carry-in gutter 123 installed horizontally along the horizontal direction at the top of the dryer main body 101.

熱風送風室103の前面側及び排塵風室102
の後面側には内部にバーナ125を収蔵したバー
ナ装置124と内部に吸引排風機127を回転自
在に収蔵した吸引排風装置126を夫々装着せし
めて、バーナ装着124と熱風送風室103を、
又吸引排風装置126と排塵風室102とを接続
せしめる。
Front side of hot air blowing room 103 and dust exhaust air room 102
On the rear side, a burner device 124 housing a burner 125 therein and a suction/exhaust device 126 housing a suction/exhaust fan 127 rotatably inside are installed, respectively, to connect the burner attachment 124 and the hot air blowing chamber 103.
Also, the suction/exhaust device 126 and the dust exhaust/air chamber 102 are connected.

前述した取出し室119はその左右両側に隣設
された熱風送風室103及び集塵室104と通風
路128,129を介して接続され、熱風送風室
103内において起風された乾燥熱風を排塵風室
102において生じた負圧作用で熱風送風室10
3より通風路128を経て取出し室119内を横
切り、さらに通風路129を通り集塵室104を
経て熱風室105に向け流通せしめたことで、取
出し室119内に散粒状態をもつて排出された乾
燥穀物中に含まれた多くの塵埃を風選別して集塵
室104内へ除去して集塵せしめると同時に排出
された乾燥穀物に乾燥熱風を直接浴びせて穀物の
乾燥をさらに促進せしめるように図つている。な
お集塵室104内に集塵された塵埃は適宜の手段
を用いて外部に排出させればよい。又、通風路1
28は多孔板としてもよい。
The above-mentioned extraction chamber 119 is connected to the hot air blowing chamber 103 and the dust collection chamber 104 installed on the left and right sides thereof via ventilation passages 128 and 129, and removes dust from the dry hot air generated in the hot air blowing chamber 103. The hot air blowing chamber 10 is heated by the negative pressure generated in the wind chamber 102.
3, passes through the ventilation passage 128, crosses the interior of the extraction chamber 119, further passes through the ventilation passage 129, passes through the dust collection chamber 104, and flows toward the hot air chamber 105, thereby being discharged into the extraction chamber 119 in the form of particles. A large amount of dust contained in the dried grains is air sorted and removed into the dust collection chamber 104 for dust collection, and at the same time, drying hot air is directly applied to the discharged dried grains to further accelerate the drying of the grains. I'm planning on it. Note that the dust collected in the dust collection chamber 104 may be discharged to the outside using an appropriate means. Also, ventilation duct 1
28 may be a perforated plate.

前述した調質槽110の上位置には、下部を開
放した断面傘状を呈する複数列の噴出体130が
等間隔をおいて水平に並設されており、該複数列
の噴出体130……の一端を通風口131を介し
集塵室104に接続せしめて、乾燥熱風の一部を
噴出体130……から調質槽110内を竪流下す
る穀物に対して並行流するように噴出せしめて、
調質槽110内においても穀物の乾燥作業を達成
させ、乾燥の促進と均一乾燥化を図るようにして
ある。したがつて調質槽110は排塵風室102
と集塵室104で囲まれて2重構成となつている
ことで結露発生を未然に防止できる。
Above the aforementioned conditioning tank 110, a plurality of rows of ejection bodies 130, each having an umbrella-like cross section with an open bottom, are arranged horizontally at equal intervals, one end of each of the rows of ejection bodies 130 is connected to the dust collection chamber 104 via a ventilation port 131, and a portion of the dry hot air is ejected from the ejection bodies 130 so as to flow in parallel with the grains flowing vertically downward within the conditioning tank 110,
The grains are dried in the conditioning tank 110 as well, to promote drying and ensure uniform drying.
The dust collecting chamber 104 is surrounded by a double structure, so that the occurrence of condensation can be prevented.

考案の効果 要するに本考案は前述したような技術的手段を
有するので、乾燥通路109の面積を極力広くし
て、発生熱風量が同一であつても熱風室105内
に多量の熱風を送風損失が少ないもとに供給して
乾燥能力の向上を果すことができる許りか初期含
水分値の異なる高含水分値の穀物であつても、乾
燥通路109において前後方向に分けられた穀物
の流れを乾燥通路109を通過したあと、左右方
向に流れが変るよう交差状に流下せしめて攪拌混
合し総ての穀物を乾燥ムラを発生させることなく
均一乾燥することができる穀物乾燥機であつて
も、熱風送風室103、取出し室119及び集塵
室104とが互いに接続されるように構成したこ
とにより、熱風送風室103より取出し室119
内を横切つて集塵室104に向かつて流通する乾
燥熱風により取出し室119内に散乱状態のもと
に排出された乾燥穀物中に含まれた多くの塵埃を
高率的に除去し、これが分離された塵埃を自動的
に集塵室104へ集塵させることができるは勿論
のこと、取出し室119内における乾燥熱風の再
度吹き当て作用で乾燥の促進をより一層図ること
ができる外、調質槽110内においても、竪流下
する穀物に対して複数列の噴出体130……より
集塵室104において除塵され清浄化された乾燥
熱風を並行流せしめて乾燥させたことで塵埃の混
入を極力防止して流下ムラをなくし、乾燥の均一
化と乾燥の促進をより向上させることができると
同時に調質槽110の周囲を排塵風室102およ
び集塵室104で囲むことで2重構成として、結
露発生を未然に防止しより一層流下ムラを皆無な
らしめる等の効果を奏する。
Effects of the invention In short, the present invention has the above-mentioned technical means, so that the area of the drying passage 109 is made as wide as possible, and even if the amount of hot air generated is the same, a large amount of hot air can be delivered into the hot air chamber 105 without blowing loss. It is possible to improve the drying capacity by supplying a small amount of grain to each other, even if the grain has a high moisture content and has a different initial moisture content. Even if the grain dryer is capable of uniformly drying all grains without causing drying unevenness by flowing down in a crosswise manner so that the flow changes from side to side after passing through the passage 109 and agitating and mixing the grains, the hot air By configuring the ventilation chamber 103, the extraction chamber 119, and the dust collection chamber 104 to be connected to each other, the extraction chamber 119 is connected to the hot air ventilation chamber 103.
A large amount of dust contained in the dried grains discharged in a scattered state into the take-out chamber 119 is removed with high efficiency by the dry hot air flowing across the inside and toward the dust collection chamber 104. Not only can the separated dust be automatically collected in the dust collection chamber 104, but also drying can be further promoted by blowing dry hot air again in the extraction chamber 119. Also in the grain tank 110, dry hot air that has been removed and cleaned in the dust collection chamber 104 is made to flow in parallel against the vertically flowing grains from multiple rows of jetting bodies 130... to prevent dust from entering. It is possible to prevent uneven flow as much as possible, improve uniformity of drying and promotion of drying, and at the same time surround the tempering tank 110 with a dust exhaust air chamber 102 and a dust collection chamber 104 to create a double structure. This has the effect of preventing dew condensation and further eliminating uneven flow.

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

図面は本考案に係る穀物乾燥機の一実施例を示
すものであつて、第1図は縦断正面図、第2図は
要部の一部を破断した側面図、第3図は第1図に
おける横断平面図、第4図は従来例の縦断正面図
である。 101……乾燥機本体、102……排塵風室、
103……熱風送風室、104……集塵室、10
5……熱風室、107……排風室、109……乾
燥通路、111……山形仕切壁、112……交差
流下繰出し室、119……取出し室、128,1
29……通風路、130……噴出体。
The drawings show one embodiment of the grain dryer according to the present invention, in which Fig. 1 is a longitudinal sectional front view, Fig. 2 is a side view with a part of the main part cut away, and Fig. 3 is a view similar to Fig. 1. FIG. 4 is a longitudinal sectional front view of the conventional example. 101...Dryer main body, 102...Dust exhaust air chamber,
103... Hot air blowing room, 104... Dust collection room, 10
5...Hot air chamber, 107...Exhaust air chamber, 109...Drying passage, 111...Chevron partition wall, 112...Cross flow downward delivery chamber, 119...Takeout chamber, 128,1
29... Ventilation passage, 130... Ejector.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 前後方向に長い乾燥機本体内に、横長方向と直
交する方向に沿つて複数の熱風室と排風室とを両
室間に巾狭の乾燥通路が形成されるよう交互に架
設し、上記複数の乾燥通路の上端は調質槽に、又
下端は乾燥通路、熱風室及び排風室の直下に横長
方向に沿い複数列に亘り配設した山形仕切壁によ
り形成された複数の交差流下繰出し室へ夫々接続
せしめると共に前記夫々の交差流下繰出し室の下
端は取出し室にのぞませたものにおいて、前記乾
燥機本体内に配設された調質槽、熱風室、排風
室、交差流下繰出し室及び取出し室の左右両側に
は横長方向に沿い排塵風室及び熱風送風室と集塵
室とを対称的に設けて、排塵風室と排風室を、又
熱風室と集塵室とを夫々接続し、熱風送風室は通
風路、取出し室および通風路を経て集塵室に接続
せしめると共に調質槽内の上部位置には一端が集
塵室に接続されて除塵された清浄乾燥熱風を下段
の排風室に向け下向きに噴出流通せしめる複数列
の噴出体を横長方向と直交する方向に並設したこ
とを特徴とする穀物乾燥機。
A plurality of hot air chambers and a plurality of exhaust ventilation chambers are constructed alternately along a direction orthogonal to the horizontal direction within a long dryer main body in the longitudinal direction so that a narrow drying passage is formed between the two chambers. The upper end of the drying passage is connected to the tempering tank, and the lower end is connected to the drying passage, a plurality of cross-flow discharge chambers formed by chevron-shaped partition walls arranged in multiple rows along the horizontal direction directly below the hot air chamber, and the exhaust chamber. and the lower ends of the respective cross-flow dispensing chambers are connected to the dispensing chamber, and the lower ends of the respective cross-flow dispensing chambers are connected to the dispensing chamber, and the tempering tank, the hot air chamber, the exhaust chamber, and the cross-current dispensing chamber are arranged in the dryer main body. A dust exhaust air chamber, a hot air blower chamber, and a dust collection chamber are installed symmetrically along the horizontal direction on both the left and right sides of the extraction chamber. The hot air blowing chamber is connected to the dust collection chamber through a ventilation passage, a take-out chamber, and a ventilation passage, and one end of the hot air blowing chamber is connected to the dust collection chamber at the upper part of the tempering tank to receive clean, dry hot air from which dust has been removed. A grain dryer characterized in that a plurality of rows of ejecting bodies are arranged in parallel in a direction orthogonal to a horizontal direction, for distributing ejected grains downward toward a lower ventilation chamber.
JP1987012355U 1987-01-30 1987-01-30 Expired - Lifetime JPH0528469Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1987012355U JPH0528469Y2 (en) 1987-01-30 1987-01-30

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1987012355U JPH0528469Y2 (en) 1987-01-30 1987-01-30

Publications (2)

Publication Number Publication Date
JPS63120086U JPS63120086U (en) 1988-08-03
JPH0528469Y2 true JPH0528469Y2 (en) 1993-07-21

Family

ID=30800410

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1987012355U Expired - Lifetime JPH0528469Y2 (en) 1987-01-30 1987-01-30

Country Status (1)

Country Link
JP (1) JPH0528469Y2 (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55105182A (en) * 1979-02-06 1980-08-12 Iseki Agricult Mach Humidity control type cereal drier
JPS5627595B2 (en) * 1973-12-13 1981-06-25
JPS5728064U (en) * 1980-07-25 1982-02-13

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5627595U (en) * 1979-08-08 1981-03-14
JPS60170693U (en) * 1983-09-19 1985-11-12 金子農機株式会社 Dust accumulation prevention device in the dust exhaust air chamber of a grain dryer

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5627595B2 (en) * 1973-12-13 1981-06-25
JPS55105182A (en) * 1979-02-06 1980-08-12 Iseki Agricult Mach Humidity control type cereal drier
JPS5728064U (en) * 1980-07-25 1982-02-13

Also Published As

Publication number Publication date
JPS63120086U (en) 1988-08-03

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