JP2008185311A5 - - Google Patents

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JP2008185311A5
JP2008185311A5 JP2007021357A JP2007021357A JP2008185311A5 JP 2008185311 A5 JP2008185311 A5 JP 2008185311A5 JP 2007021357 A JP2007021357 A JP 2007021357A JP 2007021357 A JP2007021357 A JP 2007021357A JP 2008185311 A5 JP2008185311 A5 JP 2008185311A5
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Description

穀粒乾燥機Grain dryer

本発明は穀粒乾燥機に関する。   The present invention relates to a grain dryer.

特許文献1には排風ファンから排出された排風を燃焼バーナ側に供給して再度熱風室に供給して乾燥作業に用いる技術が記載されている。
特開2007−10247号公報
Patent Document 1 describes a technique in which exhaust air discharged from an exhaust fan is supplied to a combustion burner side and supplied again to a hot air chamber for use in a drying operation.
JP 2007-10247 A

熱風を穀粒に晒して排風ファンで吸引されて機外に排出される排風内には異物や塵埃が多く含まれる。
本発明は排風ファンから排出された排風を再度熱風室に供給する穀粒乾燥機において、排風ファンから排出される排風に含まれる異物や塵埃をできるだけ熱風室に供給しないようにすることを課題とする。
A large amount of foreign matter and dust are contained in the exhaust air that is exposed to the grains and sucked by the exhaust fan and discharged to the outside of the machine.
The present invention provides a grain dryer for supplying exhaust air discharged from an exhaust fan to a hot air chamber again so that foreign matter and dust contained in the exhaust air discharged from the exhaust fan are not supplied to the hot air chamber as much as possible. This is the issue.

本発明は、上記課題を解決するために以下のような技術的手段を講じた。
すなわち、請求項1記載の発明は、燃焼バーナ(5)と、燃焼バーナ(5)で発生した熱風が通過する熱風室(11)と、熱風室(11)に隣接して設け穀粒が流下する穀粒流下通路(13)と、穀粒流下通路(13)を通過した熱風を吸引して排風として機外に排出する排風ファン(6)とを設けた穀粒乾燥機において、排風ファン(6)の排出側には排風ダクト(20)を設け、該排風ダクト(20)には排風ファン(6)で排出された排風を熱風室(11)に供給する排風循環通路を接続すると共に、排風ダクト(20)内には排風循環通路側と機外側とにそれぞれ排出する排風の割合を調節するよう回動軸(23a)を軸心に開閉動作する第一調節板(23)を設け、該第一調節板(23)が閉位置(fb)の時に排風ダクト(20)の内周面(20a)と第一調節板(23)との間に、排風に含まれる塵埃等の異物が通過できる隙間(Z)ができるよう第一調節板(23)の面積を排風ダクト(20)の開口面積より小さく構成したことを特徴とする穀粒乾燥機とする。
In order to solve the above problems, the present invention has taken the following technical means.
That is, the invention described in claim 1 includes a combustion burner (5), a hot air chamber (11) through which hot air generated by the combustion burner (5) passes, and a grain provided adjacent to the hot air chamber (11). A grain dryer provided with a grain downflow passage (13) and a wind exhaust fan (6) that sucks hot air that has passed through the grain downflow passage (13) and discharges it as exhaust air outside the machine. An exhaust duct (20) is provided on the exhaust side of the wind fan (6), and the exhaust duct (20) exhausts the exhaust air discharged from the exhaust fan (6) to the hot air chamber (11). While connecting the wind circulation passage, the exhaust duct (20) opens and closes around the pivot shaft (23a) so as to adjust the ratio of the exhaust air discharged to the exhaust air circulation passage side and the outside of the machine. The first adjusting plate (23) is provided, and when the first adjusting plate (23) is in the closed position (fb), the exhaust duct (20 Between the inner peripheral surface (20a) and the first adjusting plate (23) of the exhaust area of the gap (Z) first adjusting plate to allow (23) the foreign substances such as dust contained in the exhaust air can pass It is set as the grain dryer characterized by having comprised smaller than the opening area of a wind duct (20).

請求項2記載の発明は、排風循環通路内に排風ダクト(20)から排風循環通路内に供給される排風の量を調節する第二調節板(22)を設け、第一調節板(23)が開動作をするときには第二調節板(22)が閉動作をし、第一調節板(23)が閉動作をするときには第二調節板が開動作を行う調節弁駆動モータを制御する制御部を設けたことを特徴とする請求項1記載の穀粒乾燥機とする。 According to a second aspect of the present invention, the second adjustment plate (22) for adjusting the amount of the exhaust air supplied from the exhaust duct (20) into the exhaust air circulation passage is provided in the exhaust air circulation passage, and the first adjustment is performed. When the plate (23) opens, the second adjusting plate (22) closes, and when the first adjusting plate (23) closes, the second adjusting plate opens the adjusting valve drive motor. The grain dryer according to claim 1 , further comprising a control unit for controlling .

請求項1記載の発明においては、第一調節弁(23)がもっとも排風の量を排風循環通路側に排風を排出する閉位置(fb)にあるときにも、排風ダクト(20)の内周面(20a)と第一調節板(23)との間に隙間(Z)ができるよう第一調節板(23)の面積を排風ダクト(20)の開口面積より小さく構成したことで、隙間(Z)から多くの塵埃を機外に排出しやすくすることができ、排風循環通路内に供給される塵埃を減らすことができる。また、第一調節板(23)を小さくすることができるためその分排風ダクト(20)の長さを短くすることができる。従って排風を循環させる量を調節できるものでありながら、穀粒乾燥機の前後長をコンパクトにすることができる。   In the first aspect of the present invention, even when the first control valve (23) is in the closed position (fb) for exhausting the exhaust air to the exhaust air circulation passage side, the exhaust air duct (20). The area of the first adjustment plate (23) is smaller than the opening area of the exhaust duct (20) so that a gap (Z) is formed between the inner peripheral surface (20a) of the first adjustment plate (23). Thus, a large amount of dust can be easily discharged from the gap (Z), and dust supplied into the exhaust air circulation passage can be reduced. Further, since the first adjustment plate (23) can be made smaller, the length of the exhaust duct (20) can be shortened accordingly. Therefore, the front and rear length of the grain dryer can be made compact while the amount of circulating exhaust air can be adjusted.

請求項2記載の発明においては、機体外に排出する排風と排風循環通路内に供給する排風の割合を調節しやすくすることができる。   In the second aspect of the invention, it is possible to easily adjust the ratio of the exhaust air discharged outside the machine body and the exhaust air supplied into the exhaust air circulation passage.

発明を実施するための最良の形態としての穀粒が循環する穀粒乾燥機について説明する。
図1は穀粒乾燥機の内部を説明する斜視図で、直方体形状の箱体1の内部に上部から穀粒を貯留する貯留部2、貯留部2で貯留した穀粒を乾燥する乾燥部3、乾燥部3で乾燥した穀粒が集まる集穀部4とを設ける。なお、本実施の形態では箱体1の長手方向sを前後方向、短手方向tを左右方向と呼ぶ。
The grain dryer in which the grain circulates as the best mode for carrying out the invention will be described.
FIG. 1 is a perspective view illustrating the inside of a grain dryer, a storage unit 2 that stores grains from above in a rectangular box 1, and a drying unit 3 that dries the grains stored in the storage unit 2. And a cereal collection unit 4 where the grains dried by the drying unit 3 gather. In the present embodiment, the longitudinal direction s of the box 1 is referred to as the front-rear direction, and the lateral direction t is referred to as the left-right direction.

箱体1の長手方向sすなわち前後方向の一端でかつ乾燥部3に対向する左右中央位置にスリット状の外気取り入れ口50を正面側に多数形成したバーナケース40に収容された燃焼バーナ5を、他端には乾燥部3に対向する左右中央位置に排風ファン6をそれぞれ設ける。また、箱体1の前後方向の一端にあってかつバーナケース40に隣接する位置には穀粒を揚穀する昇降機7を設け、箱体1の上部には昇降機7で揚穀した穀粒を貯留部2に搬送する上部搬送装置8及び上部搬送装置8で搬送中の穀粒に混合する藁屑等の夾雑物を吸引除去する吸塵ファン9を設けている。   Combustion burner 5 accommodated in a burner case 40 in which a large number of slit-like outside air intake ports 50 are formed on the front side at one end in the longitudinal direction s of the box 1, that is, in the front-rear direction and opposite to the drying unit 3, At the other end, an exhaust fan 6 is provided at each of the left and right central positions facing the drying unit 3. Moreover, the elevator 7 which raises a grain is provided in the position which exists in the front-back direction of the box 1 and adjoins the burner case 40, and the grain which was grained by the elevator 7 is provided in the upper part of the box 1 An upper conveyance device 8 that conveys to the storage unit 2 and a dust suction fan 9 that sucks and removes foreign matters such as scum mixed with the grains being conveyed by the upper conveyance device 8 are provided.

10は穀粒の水分を検出する水分計で昇降機7に取り付け揚穀中の穀粒からサンプル穀粒を取り込み水分を検出する。
乾燥部3は箱体1の左右両端部に燃焼バーナ5で発生した熱風が通過する熱風室11を設け、箱体1の左右中央部に排風ファン6と連通する排風室12を設け、熱風室11と排風室12との間には貯留室2の穀粒が順次通過する穀粒流下通路13を設け、穀粒流下通路13の下端部には穀粒を集穀部4に繰り出すロータリバルブ14を設けている。
Reference numeral 10 denotes a moisture meter that detects the moisture of the grain. The moisture meter 10 is attached to the elevator 7 and takes in the sample grain from the grain that is being fried and detects the moisture.
The drying unit 3 is provided with hot air chambers 11 through which hot air generated by the combustion burner 5 passes at both left and right ends of the box 1, and an exhaust air chamber 12 that communicates with the exhaust fan 6 at the left and right center of the box 1. Between the hot air chamber 11 and the exhaust air chamber 12, a grain flow passage 13 through which the grains of the storage chamber 2 sequentially pass is provided, and the grain is fed to the cereal collection section 4 at the lower end of the grain flow passage 13. A rotary valve 14 is provided.

集穀部4には穀粒を昇降機7に搬送する下部ラセン15を設けている。
排風ファン6は円形のファン胴6a内部に軸流遠心式のファン羽根6bと、ファン羽根6bで発生させる排風に圧力を与える固定板6cとを内装し、排風ファン6の排風排出側には円形の排風ダクト20を連結している。
The grain collecting unit 4 is provided with a lower spiral 15 for conveying the grains to the elevator 7.
The exhaust fan 6 includes an axial centrifugal fan blade 6b and a fixed plate 6c that applies pressure to the exhaust generated by the fan blade 6b inside the circular fan body 6a. A circular exhaust duct 20 is connected to the side.

排風ダクト20の上部には排風を箱体1内側に供給するための方形の排風供給ダクト21を設け、排風供給ダクト21の排風入口には排風供給ダクト21内に供給される排風の量を調節する第二調節弁22を設けている。   A square exhaust air supply duct 21 for supplying exhaust air to the inside of the box 1 is provided at the upper part of the exhaust air duct 20, and the exhaust air inlet of the exhaust air supply duct 21 is supplied into the exhaust air supply duct 21. A second control valve 22 is provided for adjusting the amount of exhausted air.

排風ダクト20内には排風を排風ダクト20外と排風供給ダクト21に排出する量の割合を調節する第一調節弁23を設けている。
第一調節弁23と第二調節弁22は横軸心の回動軸23a及び回動軸22aでそれぞれ回動する構成とし、第一調節弁23と第二調節弁22とは連結ロッド24で連結し、第一調節弁23と第二調節弁22との回動動作を調節弁駆動モータ25で連動する構成としている。第二調節弁22が全閉位置gaにあって排風が排風供給ダクト21内に排出されない時には、第一調節弁23が全開位置faにあって排風を全て機外に排出される。
In the exhaust duct 20, a first control valve 23 that adjusts the ratio of the amount of exhaust air discharged to the outside of the exhaust duct 20 and the exhaust air supply duct 21 is provided.
The 1st control valve 23 and the 2nd control valve 22 are set as the structure rotated by the rotating shaft 23a and the rotating shaft 22a of a horizontal axis, respectively, and the 1st control valve 23 and the 2nd control valve 22 are connected by the connecting rod 24. The first control valve 23 and the second control valve 22 are connected to each other so as to be linked by a control valve drive motor 25. When the second control valve 22 is in the fully closed position ga and exhaust air is not discharged into the exhaust air supply duct 21, the first control valve 23 is in the fully open position fa and all exhaust air is discharged outside the machine.

反対に第二調節弁22が全開位置gbにあって、排風が最も排風供給ダクト21内に最も多くの排風が排出される時には、第一調節弁23が最も排風の量を排風供給ダクト21側に排風を排出する閉位置fbに位置する。なお、第一調節弁23と第二調節弁22はそれぞれ無段階に開閉調節できる構成とし、排風供給ダクト21に排出する排風量を制御部(図示せず)で適宜調節している。   On the other hand, when the second control valve 22 is in the fully open position gb and the exhaust air is discharged most into the exhaust air supply duct 21, the first control valve 23 exhausts the most exhaust air. It is located at the closed position fb for discharging the exhaust air to the wind supply duct 21 side. In addition, the 1st control valve 23 and the 2nd control valve 22 are set as the structure which can be opened / closed steplessly, respectively, and the exhaust_gas | exhaustion amount discharged | emitted to the exhaust_gas | exhaustion supply duct 21 is adjusted suitably by the control part (not shown).

第一調節弁23が最も排風の量を排風供給ダクト21側に排風を排出する閉位置fbにあるときに、排風ダクト20の内周面20aと第一調節板23の端部23aとの間に設定間隔の隙間zができるよう第一調節弁23の回動軸23aから端部までの長bを排風ダクト20の中心から内周面20aまでの長さより短くし、第一調節弁23の面積を排風ダクトの開口面積より小さく構成している。jは第一調節弁23の回動軌跡である。   When the first control valve 23 is in the closed position fb that discharges the exhaust air to the exhaust air supply duct 21 side most, the inner peripheral surface 20a of the exhaust air duct 20 and the end of the first adjustment plate 23 The length b from the rotation shaft 23a to the end of the first control valve 23 is shorter than the length from the center of the exhaust duct 20 to the inner peripheral surface 20a so that a gap z with a set interval is formed between the first control valve 23 and The area of one control valve 23 is configured to be smaller than the opening area of the exhaust duct. j is a turning locus of the first control valve 23;

また、第一調節弁23がもっとも排風の量を排風供給ダクト21側に排風を排出する閉位置fbは、図4に示すように後ろ下がり傾斜に位置する構成とし、第二調節弁22は前下がり傾斜に位置する構成とすることで、排風を排風供給ダクト21内に案内し易くしている。   In addition, the closed position fb where the first control valve 23 discharges the most exhausted air to the exhaust air supply duct 21 side is located at a rearward downward slope as shown in FIG. 22 is configured so as to be inclined forward and downward so that the exhausted air can be easily guided into the exhausted air supply duct 21.

排風供給ダクト21と箱体1との間には排風供給ダクト21内を通過した排風を左右両側に分散する排風分散通路26であるケースを排風ファン6の左右両側に亘って設ける。排風分散通路26の左右両端部と後述する熱風室内貫通通路27の後端部とを第一排風開口部mで連通する構成としている。   Between the exhaust air supply duct 21 and the box 1, a case that is an exhaust air distribution passage 26 that distributes the exhaust air that has passed through the exhaust air supply duct 21 to the left and right sides extends over both the left and right sides of the exhaust fan 6. Provide. The left and right ends of the exhaust air distribution passage 26 and the rear end portion of the hot air indoor through passage 27 described later are configured to communicate with each other through a first exhaust air opening m.

熱風室内貫通通路27は左右の熱風室11内前後方向に沿って備える筒形状の通路で、本実施の形態では断面形状で上部が尖った台形状に形成している。箱体1とバーナケース40の間には箱体1内を循環して還元された排風が通過する第一還元通路41と燃焼バーナ5で発生した熱風が通過する熱風通路42を内部に形成する熱排風通過ケース43を備えている。そして、熱風室内貫通通路27の前端部と第一還元通路41とを第二排風開口部pで連通する構成とすると共に、第一還元通路41とバーナケース40の左右両側に形成する第二還元通路44とを第三排風開口部rで連通する構成としている。バーナケース40の下方には第三還元通路45を形成しており、第二還元通路44と第三還元通路45とを第四排風開口部dで連通する構成としている。   The hot-air chamber through passage 27 is a cylindrical passage provided along the front-rear direction in the left and right hot-air chambers 11 and is formed in a trapezoidal shape with a cross-sectional shape and a sharp upper portion in this embodiment. Between the box 1 and the burner case 40, there are formed a first reduction passage 41 through which exhausted air reduced through circulation in the box 1 passes and a hot air passage 42 through which hot air generated in the combustion burner 5 passes. A heat exhaust passage case 43 is provided. The second end formed on the left and right sides of the first reduction passage 41 and the burner case 40 is configured so that the front end portion of the hot air chamber through passage 27 and the first reduction passage 41 communicate with each other through the second exhaust opening p. The reduction passage 44 is configured to communicate with the third exhaust opening r. A third reduction passage 45 is formed below the burner case 40, and the second reduction passage 44 and the third reduction passage 45 are communicated with each other through a fourth exhaust opening d.

熱排風通過ケース43内の熱風通路42は第三還元通路45と、第五排風開口部eを介して連通すると共にバーナケース40と第一熱風開口部cで連通する熱排風混合通路46と、熱排風混合通路46を通過した熱風を第二熱風開口部vから第三熱風開口部wを経て熱風室11に供給する熱風供給通路47とを設けている。   The hot air passage 42 in the hot exhaust passage case 43 communicates with the third reduction passage 45 via the fifth exhaust passage opening e and communicates with the burner case 40 and the first hot air opening portion c. 46 and a hot air supply passage 47 for supplying the hot air having passed through the hot exhaust air mixing passage 46 from the second hot air opening v to the hot air chamber 11 through the third hot air opening w.

熱排風通過ケース43の構成について詳述する。
第一還元通路41と熱風供給通路47とは箱体1の正面左右両側にあって上下二段に形成し、熱排風混合通路46は左右中央側にあってバーナケース40に対向する位置に設けている。第一熱風開口部cは熱排風混合通路46及びバーナケース40の中央部に、第五熱風開口部eは熱排風混合通路46の下部にそれぞれ形成している。
The configuration of the heat exhaust air passage case 43 will be described in detail.
The first reduction passage 41 and the hot air supply passage 47 are formed on the front left and right sides of the box 1 and are formed in two upper and lower stages, and the heat exhaust air mixing passage 46 is on the left and right center side at a position facing the burner case 40. Provided. The first hot air opening c is formed at the center of the hot exhaust air mixing passage 46 and the burner case 40, and the fifth hot air opening e is formed at the lower portion of the hot exhaust air mixing passage 46.

なお、本実施の形態では排風供給ダクト21から第三還元通路45に至るまでの排風が通過する経路を総称して排風循環通路と呼ぶ。また第一還元通路41と第二還元通路44と第三還元通路45の部分については還元通路と呼ぶ。   In the present embodiment, a path through which the exhaust air from the exhaust air supply duct 21 to the third reduction passage 45 passes is generically called an exhaust air circulation passage. The portions of the first reduction passage 41, the second reduction passage 44, and the third reduction passage 45 are called reduction passages.

次に燃焼バーナ5で発生した熱風が排風となって排風循環通路を経て再度熱風室11に供給されるまでの過程について説明する。
燃焼バーナ5で発生した熱風はバーナケース40から第一熱風開口部cを通過し、熱排風混合通路46から第二熱風開口部v、熱風供給通路47、第三熱風開口部wを通過して熱風室11に供給される。
Next, a process until hot air generated in the combustion burner 5 is exhausted and supplied to the hot air chamber 11 again through the exhaust air circulation passage will be described.
Hot air generated in the combustion burner 5 passes from the burner case 40 through the first hot air opening c, and from the hot exhaust air mixing passage 46 through the second hot air opening v, the hot air supply passage 47, and the third hot air opening w. And supplied to the hot air chamber 11.

熱風室11内の熱風は多数のスリット(図示省略)を形成する穀粒流下通路13を流下する穀粒内を通過し、穀粒から水分を奪って排風室12に供給され、排風ファン6で吸引されて排風ダクト20に排風として排出される。   The hot air in the hot air chamber 11 passes through the grain flowing down the grain flow passage 13 that forms a large number of slits (not shown), deprives the grain of moisture and is supplied to the exhaust air chamber 12, and the exhaust fan 6 and is discharged as exhaust air to the exhaust duct 20.

排風ダクト20内の排風は第一調節弁23及び第二調節弁22の開度の制御により適宜必要な排風量を排風循環通路を経て再度熱風室11側に循環すべく排風供給ダクト21に供給される。   Exhaust air in the exhaust duct 20 is supplied to exhaust the necessary amount of exhaust air through the exhaust air circulation passage to the hot air chamber 11 again by controlling the opening degree of the first control valve 23 and the second control valve 22. It is supplied to the duct 21.

排風供給ダクト21に供給された排風は排風分散通路26で左右に分散され、第一排風開口部mから熱風室内貫通通路27に供給される。そして、熱風室内貫通通路27内の排風は第二排風開口部pから第一還元通路41、第三排風開口部r、第二還元通路44、第四排風開口部d、第三還元通路45、第五排風開口部eを経て熱排風混合通路46に供給される。そこで熱風と混合されて熱風供給通路47を経て熱風室11に供給される。   The exhaust air supplied to the exhaust air supply duct 21 is dispersed left and right in the exhaust air distribution passage 26 and supplied to the hot air indoor through passage 27 from the first exhaust air opening m. And, the exhaust air in the hot air indoor through passage 27 is discharged from the second exhaust opening p to the first reduction passage 41, the third exhaust opening r, the second reduction passage 44, the fourth exhaust opening d, the third. It is supplied to the heat exhaust air mixing passage 46 through the reduction passage 45 and the fifth exhaust air opening e. Therefore, it is mixed with hot air and supplied to the hot air chamber 11 through the hot air supply passage 47.

熱風室11に供給された排風と熱風の混合空気は熱風に排風に含まれる熱と水分が加わることから高温でかつ湿度の高い状態であり、これを穀粒に晒すと、混合空気の高熱の作用により穀温を早く上昇させながら、穀温上昇により穀粒の内部から急激に気化されようとする水分を混合空気中の湿気で抑えながら気化させることで、穀粒中における水分の急激な移動すなわち気化による穀粒の胴割れを防止しながら効率よく穀粒中の水分を除去して乾燥作業を行なうことができる。   The mixed air of exhaust air and hot air supplied to the hot air chamber 11 is in a high temperature and high humidity state because the heat and moisture contained in the exhaust air are added to the hot air, and when this is exposed to the grain, While rapidly raising the grain temperature by the action of high heat, the moisture that is about to be vaporized rapidly from the inside of the grain due to the rise in grain temperature is vaporized while being suppressed by the moisture in the mixed air, thereby rapidly increasing the moisture content in the grain. It is possible to efficiently remove the moisture in the grain and prevent the grain from being cracked due to slow movement, that is, vaporization.

次に本実施の形態の構成から発生する効果について説明する。
第一調節弁23が最も排風の量を排風供給ダクト21側に排風を排出する閉位置fbにあるときに、排風ダクト20の内周面20aと第一調節板23の端部23bとの間に隙間zができるよう第一調節板23の面積を排風ダクト20の開口面積より小さく構成することで、排風に含まれる比較的大きな塵埃が排風ダクト20から隙間zから機外に排出され易くなり、排風供給ダクト21から第三還元通路45に至るまでの排風循環通路内に塵埃が堆積し難くする事ができ、排風の通過を円滑にすることができる。また、排風供給ダクト21を排風ダクト20の上方にあるため、大きな塵埃が排風供給ダクト21に入り難くして機外に排出し易くすることができる。
Next, effects generated from the configuration of the present embodiment will be described.
When the first control valve 23 is in the closed position fb that discharges the exhaust air to the exhaust air supply duct 21 side most, the inner peripheral surface 20a of the exhaust air duct 20 and the end of the first adjustment plate 23 By configuring the area of the first adjusting plate 23 to be smaller than the opening area of the exhaust duct 20 so that a gap z is formed between the exhaust duct 20 and the air gap 23b, relatively large dust contained in the exhaust air is removed from the exhaust duct 20 from the gap z. It becomes easy to be discharged outside the machine, dust can be made difficult to accumulate in the exhaust air circulation passage from the exhaust air supply duct 21 to the third reduction passage 45, and the exhaust air can be passed smoothly. . Further, since the exhaust air supply duct 21 is located above the exhaust air duct 20, it is difficult for large dust to enter the exhaust air supply duct 21 and to be easily discharged outside the apparatus.

熱風室内貫通通路27を熱風室11内に設けることで、熱風室内貫通通路27内部の温度も高くなり、塵埃を含む高湿度の排風が熱風室内貫通通路27内部で結露して塵埃が付着したりするのを防止することができる。また、排風室12内に排風を通過する通路を設けると排風室12の空間が小さくなり排風ファン6の吸引力が低下するという欠点が生じるが、熱風室11内に備えることで本実施の形態によりそれを防止することができる。   By providing the hot air chamber through passage 27 in the hot air chamber 11, the temperature inside the hot air chamber through passage 27 is also increased, and high-humidity exhaust air containing dust is condensed inside the hot air chamber through passage 27 and dust is deposited. Can be prevented. In addition, if a passage for passing the exhaust air is provided in the exhaust air chamber 12, the space of the exhaust air chamber 12 is reduced and the suction force of the exhaust air fan 6 is reduced. However, by providing it in the hot air chamber 11. This can be prevented by this embodiment.

熱風室11を箱体1の左右両側に設け、排風室12を箱体1の中央部に設けたことで、外気温度が低い場合において、排風と熱風が混合した高温高湿度の混合気体が排風として通過する排風室12内を結露し難くすることができる。   By providing the hot air chamber 11 on both the left and right sides of the box 1 and the exhaust air chamber 12 at the center of the box 1, a high temperature and high humidity mixed gas in which the exhaust air and hot air are mixed when the outside air temperature is low. Can be prevented from condensing in the exhaust chamber 12 through which the exhaust passes.

熱風室内貫通通路27から熱排風混合通路46に排風を供給するまでにバーナケース40に隣接する第一還元通路41から第三還元通路45までの還元通路を経て燃焼バーナ5の燃焼面に対向する熱排風混合通路46に供給することで排風を燃焼バーナ5に直接晒すことによる燃焼バーナ5の劣化を防止することができる。また、還元通路中に熱排風混合通路46より低い位置に第三還元通路45を設けることで、第一還元通路41から排風を第三還元通路45に向かって落下させてから熱排風混合通路46に向かって上昇するため、第三還元通路45に排風中の塵埃を多く堆積することが可能になり、熱排風混合通路46及び熱風室11に供給される塵埃の量を減少させることができる。還元通路をバーナケース40に隣接して設けることで、排風の保温性を向上させることができる。   Before the exhaust air is supplied to the hot exhaust air mixing passage 46 from the hot air interior passage 27, the combustion surface of the combustion burner 5 passes through the reduction passage from the first reduction passage 41 adjacent to the burner case 40 to the third reduction passage 45. By supplying to the opposing heat exhaust air mixing passage 46, deterioration of the combustion burner 5 due to direct exposure of exhaust air to the combustion burner 5 can be prevented. Further, by providing the third reduction passage 45 at a position lower than the heat exhaust air mixing passage 46 in the reduction passage, the exhaust air is dropped from the first reduction passage 41 toward the third reduction passage 45 and then the heat exhaust air. Since it rises toward the mixing passage 46, it becomes possible to accumulate a large amount of dust being exhausted in the third reduction passage 45, and the amount of dust supplied to the hot exhaust air mixing passage 46 and the hot air chamber 11 is reduced. Can be made. By providing the reduction passage adjacent to the burner case 40, the heat retention of the exhaust air can be improved.

次に第一調節弁23及び第二調節弁22の開度の制御方法について説明する。
外気温度センサ(図示せず)で検出された外気温が20℃で外気湿度センサ(図示せず)で検出された外気湿度が70%で制御部(図示せず)で演算された絶対湿度(Z)が13g/m3とする。そして、制御目標とする排風(Y)を例えば排風温度が30℃で排風湿度が70%、そして絶対湿度(U)を25g/m3とした場合とする。そして、本実施例の排風ファン7の風量を1900kg/hで、穀粒乾燥機に供給された穀粒(籾)量を800kg、乾減率(一時間あたりに乾燥される水分の割合)を1.2%/hとした場合、どの程度の割合の排風を熱風室13に還元するかを以下の式より求める。
Next, the control method of the opening degree of the 1st control valve 23 and the 2nd control valve 22 is demonstrated.
Absolute humidity calculated by a control unit (not shown) when the outside air temperature detected by an outside air temperature sensor (not shown) is 20 ° C. and the outside air humidity detected by an outside air humidity sensor (not shown) is 70%. Z) is 13 g / m3. The exhaust air (Y) as a control target is, for example, a case where the exhaust air temperature is 30 ° C., the exhaust air humidity is 70%, and the absolute humidity (U) is 25 g / m 3. And the air volume of the exhaust fan 7 of a present Example is 1900 kg / h, the quantity of the grain (rice cake) supplied to the grain dryer is 800 kg, and a drying rate (ratio of the moisture dried per hour) Is 1.2% / h, the rate of exhaust air to be reduced to the hot air chamber 13 is obtained from the following equation.

絶対湿度(U)−絶対湿度(Z)=12(g/m3) …(イ)
外気が吸水できる最大吸水量は
12×1900/1000≒23(kg) …(ロ)
そして、一時間あたりに乾燥機から除去される水分量は
800(kg)×1.2(%/h)=9.6(kg/h) …(ハ)
(ロ)の式と(ハ)の式より
23/9.6+23≒0.71 →71%…(二)
すなわち、排風ファン7から排出される排風量の71%を熱風室11に還元すべく第一調節弁23及び第二調節弁22を調節する。
Absolute humidity (U)-Absolute humidity (Z) = 12 (g / m3) (a)
The maximum amount of water that can be absorbed by outside air is 12 x 1900/1000 ≒ 23 (kg) (B)
The amount of water removed from the dryer per hour is 800 (kg) × 1.2 (% / h) = 9.6 (kg / h) (C)
From the formulas (b) and (c), 23 / 9.6 + 23≈0.71 → 71% (2)
That is, the first control valve 23 and the second control valve 22 are adjusted so that 71% of the exhausted air amount discharged from the exhaust air fan 7 is reduced to the hot air chamber 11.

なお、第一調節弁23及び第二調節弁22が排風量の71%より多くの量を熱風室11に還元するよう調節された場合には、多くなればなるほど還元される水分量が多くなるため、穀粒から新たに水分を除去し難くなる。また、第一調節弁23及び第二調節弁22が排風量の71%より少ない量を熱風室11に還元した場合には熱風室11に還元される熱量が少なくなるため、穀粒の温度の上昇がし難くなり乾燥速度が遅くなる。   In addition, when the 1st control valve 23 and the 2nd control valve 22 are adjusted so that more than 71% of exhaust air volume may be returned to the hot air chamber 11, the amount of water | moisture content reduce | restored increases, so that it increases. For this reason, it becomes difficult to remove moisture from the grain. Further, when the first control valve 23 and the second control valve 22 reduce an amount less than 71% of the exhausted air amount to the hot air chamber 11, the amount of heat reduced to the hot air chamber 11 decreases, so that the temperature of the grain is reduced. It is difficult to rise and the drying speed is slow.

本実施の形態の式1に還元する割合を調節することで、排風ファン6から排出された排風が帯びる熱、すなわち吸水力をできる限り適正に利用することで燃焼効率の良い乾燥作業を行うことができる。   By adjusting the ratio of reduction to Equation 1 of the present embodiment, the heat generated by the exhaust air discharged from the exhaust air fan 6, that is, the drying operation with good combustion efficiency can be performed by using the water absorption force as appropriately as possible. It can be carried out.

本実施の形態の乾燥制御についてさらに詳述すると、前記外気温度センサと前記外気湿度センサで外気の温度と湿度とを検出し、制御部で外気の絶対湿度を演算し、外気の絶対湿度と穀物水分や外気絶対湿度の条件から予め設定する排風の絶対湿度とを比較する温度及び相対湿度時の排風の絶対湿度とを比較して、その差異(増加水量)を外気が吸収できる最大の吸水量として演算する。そして、一方では乾燥作業により乾燥機から蒸発する蒸発水量(本実施の形態では前述の一時間あたりに乾燥機から除去される水分量)を求め、増加水量が乾燥作業による蒸発水量と合算された値に対する割合が、排風を還元できる割合と考えるものである。すなわち、前記(ニ)の式は
増加水量/増加水量+蒸発水量
を示している。
The drying control according to the present embodiment will be described in more detail. The outside air temperature sensor and the outside air humidity sensor detect the outside air temperature and humidity, the control unit calculates the outside air absolute humidity, and the outside air absolute humidity and the grain. Comparing the absolute humidity of the exhaust air at the relative humidity and the temperature to compare with the absolute humidity of the exhaust air set in advance from the conditions of moisture and the absolute humidity of the outside air Calculated as water absorption. On the other hand, the amount of water evaporated from the dryer by the drying operation (in this embodiment, the amount of water removed from the dryer per one hour as described above) was obtained, and the increased amount of water was added to the amount of water evaporated by the drying operation. The ratio to the value is considered as the ratio that can reduce the exhaust air. That is, the above formula (d) is the amount of increased water / increasing water amount + evaporated water amount.
Is shown.

従来の熱風乾燥においては、穀粒の表面の水分を除去する毎に穀粒内部の水分が熱伝導を利用した水分移動で穀粒の表面に順次出てくる性質を利用して乾燥するため、高速乾燥を行なうために急激に高温で乾燥を行なうと穀粒表面と内部との水分差が大きくなり、胴割れを起こし易いという欠点があるのに対し、本実施の形態の排風乾燥においては、排風中に含まれる熱と水分を同時に熱風室(11)に還元することで、穀粒表面から除去されようとする水分を排風中に含まれる水分で抑止して穀粒内部の水分勾配を一定にすることで穀粒を割れ難くすると共に、排風中の熱を余分に与えることで穀温を短時間で上昇させることで、高速な乾燥を可能にするものである。   In conventional hot air drying, every time the moisture on the surface of the grain is removed, the moisture inside the grain is dried by utilizing the property that the water moves using heat conduction to sequentially appear on the surface of the grain. In the exhaust air drying according to the present embodiment, the moisture difference between the grain surface and the inside increases when the drying is rapidly performed at a high temperature in order to perform high-speed drying. By simultaneously reducing the heat and moisture contained in the exhaust air to the hot air chamber (11), the moisture to be removed from the grain surface is suppressed by the moisture contained in the exhaust air, and the moisture inside the kernel While making the grain difficult to break by making the gradient constant, the grain temperature is raised in a short time by giving extra heat during exhaust air, thereby enabling high-speed drying.

穀粒乾燥機の内部を説明する斜視図The perspective view explaining the inside of a grain dryer 乾燥部と集穀部の構成を説明する斜視図The perspective view explaining the structure of a drying part and a grain collection part 乾燥部と集穀部の構成を説明する正面図Front view illustrating the configuration of the drying unit and the cereal collecting unit 第一調節弁と第二調節弁の連動構成を説明する側面図Side view explaining the interlocking configuration of the first control valve and the second control valve 排風供給ダクトと排風分散通路と排風ファンを示した斜視図A perspective view showing an exhaust air supply duct, an exhaust air dispersion passage, and an exhaust fan バーナケース及び熱排風通過ケースの内部を説明する斜視図The perspective view explaining the inside of a burner case and a heat exhaust air passage case

5 燃焼バーナ
6 排風ファン
11 熱風室
13 穀粒流下通路
20 排風ダクト
22 第二調節板
23 第一調節板
23a回動軸
24 ロッド
5 Combustion Burner 6 Exhaust Fan 11 Hot Air Chamber 13 Grain Flow Down Passage 20 Exhaust Duct 22 Second Adjustment Plate 23 First Adjustment Plate 23a Rotating Shaft 24 Rod

Claims (2)

燃焼バーナ(5)と、燃焼バーナ(5)で発生した熱風が通過する熱風室(11)と、熱風室(11)に隣接して設け穀粒が流下する穀粒流下通路(13)と、穀粒流下通路(13)を通過した熱風を吸引して排風として機外に排出する排風ファン(6)とを設けた穀粒乾燥機において、
排風ファン(6)の排出側には排風ダクト(20)を設け、該排風ダクト(20)には排風ファン(6)で排出された排風を熱風室(11)に供給する排風循環通路を接続すると共に、排風ダクト(20)内には排風循環通路側と機外側とにそれぞれ排出する排風の割合を調節するよう回動軸(23a)を軸心に開閉動作する第一調節板(23)を設け、
該第一調節板(23)が閉位置(fb)の時に排風ダクト(20)の内周面(20a)と第一調節板(23)との間に、排風に含まれる塵埃等の異物が通過できる隙間(Z)ができるよう第一調節板(23)の面積を排風ダクト(20)の開口面積より小さく構成したことを特徴とする穀粒乾燥機。
A combustion burner (5), a hot air chamber (11) through which hot air generated in the combustion burner (5) passes, a kernel flow passage (13) provided adjacent to the hot air chamber (11) and through which the kernel flows down, In a grain dryer provided with an exhaust fan (6) that sucks hot air that has passed through the grain flow passage (13) and exhausts it as exhaust air to the outside of the machine,
An exhaust duct (20) is provided on the exhaust side of the exhaust fan (6), and exhaust air exhausted by the exhaust fan (6) is supplied to the exhaust duct (20) to the hot air chamber (11). The exhaust air circulation passage is connected, and the rotation shaft (23a) is opened and closed about the center of the exhaust air duct (20) so as to adjust the ratio of the exhaust air discharged to the exhaust air circulation passage side and the outside of the machine. A first adjusting plate (23) that operates,
When the first adjustment plate (23) is in the closed position (fb), dust or the like contained in the exhaust air is placed between the inner peripheral surface (20a) of the exhaust duct (20) and the first adjustment plate (23) . A grain dryer characterized in that the area of the first adjustment plate (23) is smaller than the opening area of the exhaust duct (20) so that a gap (Z) through which foreign matter can pass is formed.
排風循環通路内に排風ダクト(20)から排風循環通路内に供給される排風の量を調節する第二調節板(22)を設け、第一調節板(23)が開動作をするときには第二調節板(22)が閉動作をし、第一調節板(23)が閉動作をするときには第二調節板が開動作を行う調節弁駆動モータを制御する制御部を設けたことを特徴とする請求項1記載の穀粒乾燥機。 A second adjusting plate (22) for adjusting the amount of exhaust air supplied from the exhaust duct (20) into the exhaust air circulation passage is provided in the exhaust air circulation passage, and the first adjusting plate (23) opens. A control unit is provided for controlling the control valve drive motor that performs the closing operation of the second adjusting plate (22) when opening, and the second adjusting plate (23) opening when the first adjusting plate (23) is closed. The grain dryer according to claim 1.
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