JP2005249253A - Drier for sawdust - Google Patents

Drier for sawdust Download PDF

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JP2005249253A
JP2005249253A JP2004058296A JP2004058296A JP2005249253A JP 2005249253 A JP2005249253 A JP 2005249253A JP 2004058296 A JP2004058296 A JP 2004058296A JP 2004058296 A JP2004058296 A JP 2004058296A JP 2005249253 A JP2005249253 A JP 2005249253A
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sawdust
drying
air
dried
pressure
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JP4435605B2 (en
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Tsuneo Kaneko
常雄 金子
Yasuo Ishijima
康雄 石嶋
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Kaneko Agricultural Machinery Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a drier for sawdust formed so that the sawdust flowing down in a flow-down passage between an air supply shell and an air discharge shell installed in a drying tank oppositely to each other can flows down without being sucked by a ventilation hole in the air exhaust shell and well circulate in the drier in the drier for the sawdust for ventilatingly drying the sawdust while circulating. <P>SOLUTION: The amount of the air from a suction type blower connected to right and left hot air chambers on both sides of a collecting chamber collecting, at one end, the dried sawdust quantitatively discharged from a delivery roll in a collection part and the amount of the air from a suction type blower connected to an air discharge chamber are regulated to limit an air pressure (static pressure) in a flow-down passage in the drying tank within a specified range. Accordingly, since the sawdust is not sucked to the ventilation hole in the air discharge shell side face of the flow-down passage, the dried sawdust in the drying tank is allowed to flow down without accumulation. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は、被乾燥おが屑を循環しながら通風乾燥するおが屑の乾燥装置に間するものである。   The present invention is applied to a sawdust drying apparatus for drying by ventilation while circulating sawdust to be dried.

木材の加工、製材等によって発生するおが屑は、燃料、堆肥の原料、茸類の栽培基など、広範囲の利用が可能であるが、おが屑を燃料として利用する場合には十分乾燥していることが必要であり、また堆肥の原料としたり茸類の栽培基として利用する場合にも、その保管や運搬などのうえから十分乾燥すると共に、使用方法に応じた水分値への乾燥が重要である。   Sawdust generated by processing wood, sawing, etc. can be used in a wide range of sources, such as fuel, compost raw materials, and cultivation bases of potatoes. However, when sawdust is used as fuel, it must be sufficiently dry. In addition, when it is used as a raw material for compost or as a cultivation base for potatoes, it is important to dry it from its storage and transportation and to a moisture value according to the method of use.

一般に、丸太材などの製材に伴って発生するおが屑は、それ自体かなりの水分を含んでおり、また木材の加工や材木の切断によって発生するおが屑もその収集や保管の状態によるが、水分を多く含んだ状態で提供されるので、多くの場合、収集されたおが屑はそれを所定の水分まで乾燥しなければならないものである。   In general, sawdust generated by sawmills such as logs contains a lot of moisture, and sawdust generated by processing wood or cutting timber depends on the state of collection and storage, but it contains a lot of moisture. In many cases, the collected sawdust has to be dried to a predetermined moisture content because it is provided in a contained state.

また、ダム等に流れ着く流木は従来廃棄処分されていたが、資源の有効利用の観点から暖房機の燃料として利用されつつある。流木を暖房機の燃料に利用しやすくするため、近年ベレット化が行なわれていて、流木をペレットにするためには粉砕しておが屑にしてペレットにしやすい水分まで乾燥する必要がある。   In addition, the driftwood that reaches the dam has been disposed of in the past, but is being used as a fuel for heaters from the viewpoint of effective use of resources. In order to make it easy to use driftwood as fuel for heaters, in recent years, it has been converted to pellets. In order to make driftwood into pellets, it is necessary to pulverize them and dry them to moisture that can easily be turned into pellets.

このため、従来から、おが屑の乾燥手段が種々提案されている。それを機能別に概ね分類すれば、被乾燥おが屑の静止堆積層に熱風を浴びせて乾燥するもの(特開昭48−2436号公報参照)、被乾燥おが屑を回転ドラムで撹拌しながら加熱乾燥するもの(特開昭60−2868号公報参照)、被乾燥おが屑をサイクロンで旋回させながら熱風を浴びせるもの(実願昭55−167157号(実開昭57−89196号)のマイクロフィルム参照)、被乾燥おが屑を乾燥ドラム内で撹拌体で撹拌しながら熱風で乾燥するもの(実願平2−41864号(実開平4−1394号)のマイクロフィルムがある。   For this reason, conventionally, various means for drying sawdust have been proposed. If it is roughly classified by function, it is dried by applying hot air to a stationary layer of sawdust to be dried (see Japanese Patent Laid-Open No. 48-2436), and dried by stirring the sawdust to be dried with a rotating drum. (See Japanese Laid-Open Patent Publication No. 60-2868), which is subjected to hot air while rotating dried sawdust with a cyclone (see microfilm of Japanese Utility Model Application No. 55-167157 (Japanese Utility Model Publication No. 57-89196)), There is a microfilm of sawdust that is dried with hot air while stirring with a stirring body in a drying drum (Japanese Utility Model Application No. 2-41864 (Japanese Utility Model Application No. 4-1394)).

また、おが屑を循環させながら通風乾燥するおが屑乾燥方法とその装置も平成15年5月26日(特願2003−148074号)を本特許請求人が出願を行なっている。   Further, this patent applicant has filed an application for a sawdust drying method and apparatus for drying by ventilation while circulating sawdust on May 26, 2003 (Japanese Patent Application No. 2003-148074).

特開昭48−2436号公報Japanese Patent Laid-Open No. 48-2436 特開昭60−2868号公報JP-A-60-2868 実開昭57−89196号公報Japanese Utility Model Publication No. 57-89196 実開平4−1394号公報Japanese Utility Model Publication No. 4-1394

一般に、おが屑は水分を含むと団子状にかたまった態様を呈するので、それを堆積したままで熱風を浴びせても、乾燥効率が甚だ低く、表面だけは乾燥しても全体を均等に乾燥することが出来ないものである。また、おが屑を乾燥し易いように回転ドラムや撹拌体によって撹拌しても、おが屑のかたまりがやや小さくなるだけであってけして散粒状に解かれた状態とはならず、やはり効率よく均等に乾燥することが出来ないのが実状である。   In general, sawdust appears in the form of dumplings when it contains moisture, so even if it is deposited with hot air, the drying efficiency is very low, and even if only the surface is dried, the whole is evenly dried. Is not possible. In addition, even if the sawdust is agitated with a rotating drum or stirring body so that it can be easily dried, the mass of sawdust is only slightly reduced and it does not become a state of being broken up into particles, and it is also efficient and even. The reality is that it cannot be dried.

そこで本特許出願人は平成15年5月26日(特願2003−148074号)に出願した、被乾燥おが屑を循環しながら通風乾燥するおが屑乾燥方法とその装置の発明を行ない、おが屑を効率よく均等に乾燥できるようにしているものである。   Therefore, the present applicant filed on May 26, 2003 (Japanese Patent Application No. 2003-148074), invented a sawdust drying method and apparatus for drying by drying while circulating the sawdust to be dried, and efficiently sawdust. It is designed to be able to dry evenly.

しかし、本特許請求人が出願した、乾燥槽内に前回の乾燥済みおが屑を適量残留させておくか、あるいは乾燥済みおが屑を適量投入して、乾燥済みおが屑の循環を繰り返しながら未乾燥のおが屑を投入して、未乾燥おが屑に乾燥済みおが屑が混合されて流動性を良好にし、乾燥機内におが屑の滞留を防止する乾燥方法と、さらに吸引風または圧送風の通風、あるいはそれらの交互流通を用いても、乾燥槽内に対向して設けられた給風胴と排風胴の間の流下路を流下するおが屑は、給風胴付近のおが屑が良好に流下するのに対し、排風胴付近のおが屑は排風胴の通気孔に吸着され、均等に流下していない事が実験で判明した。   However, an appropriate amount of the previous dried sawdust is left in the drying tank, or an appropriate amount of dried sawdust is put into the drying tank, and the dry sawdust is removed while repeating the circulation of the dried sawdust. The drying method that mixes the dried sawdust with the dried sawdust to improve fluidity and prevent the sawdust from staying in the dryer, and the suction or pressure ventilation or alternate flow of them is used. However, sawdust that flows down the flow path between the air supply drum and the exhaust drum provided opposite to the drying tank is good for the sawdust in the vicinity of the air supply drum. Experiments have shown that sawdust is adsorbed by the vents of the wind tunnel and does not flow evenly.

そこで、本発明は被乾燥おが屑を循環させながら通風乾燥するおが屑の乾燥装置において、乾燥槽内に対向して設けられた給風胴と排風胴の間の流下路を流下するおが屑が、排風胴の通気孔に吸着されずに流下し良好に乾燥機内を循環するように、収集部の内部の繰出しロールから定量的に繰出される被乾燥おが屑を一端に収集する収集室を挟んで左右の熱風室に接続された圧送送風機と排風室に接続された吸引送風機の風量を調節して、乾燥槽内の流下路の空気圧(静圧)を一定の範囲に限定することで、流下路の排風胴側面の通気孔におが屑が吸着せず、乾燥槽の被乾燥おが屑を滞りなく流下させるように構成したおが屑の乾燥装置を提供することを目的とする。   Therefore, the present invention provides a sawdust drying apparatus that circulates and drys the sawdust to be dried, and the sawdust flowing down the flow path between the air supply drum and the exhaust drum provided in the drying tank is discharged. Left and right across the collection chamber that collects dried sawdust quantitatively fed from the feed roll inside the collection unit at one end so that it flows down without being adsorbed by the vents of the wind tunnel and circulates well inside the dryer. By adjusting the air volume of the suction blower connected to the hot air chamber and the suction blower connected to the exhaust air chamber, the air pressure (static pressure) of the flow channel in the drying tank is limited to a certain range, and the flow channel An object of the present invention is to provide a sawdust drying device configured such that sawdust is not adsorbed to the vent holes on the side surface of the exhaust wind tunnel, and the to-be-dried sawdust in the drying tank flows down without delay.

上記目的を達成するために、本発明は請求項1又は請求項2に係るおが屑の乾燥装置を提供する。   In order to achieve the above object, the present invention provides a sawdust drying apparatus according to claim 1 or claim 2.

即ち、請求項1に係るおが屑の乾燥装置は、被乾燥おが屑を循環させながら通風乾燥するおが屑の乾燥装置であって、被乾燥おが屑を収容し循環させながら通風乾燥する乾燥槽と、この乾燥槽に被乾燥おが屑を投入して循環させるおが屑揚送機とを備えて構成され、乾燥槽の内部には、給風胴と排風胴とを対向させてそれらの間を被乾燥おが屑の流下路と成した通風乾燥部と、おが屑貯留部と繰出し規制体と、その下方には繰出しロールを設けていて、繰出しロールから定量的に繰出される被乾燥おが屑を一端に収集するおが屑収集部の収集室を挟んで左右に圧送送風機に接続された熱風室と、吸引送風機に接続された排風室を備えたおが屑の乾燥装置において、乾燥槽の内部の流下路内の空気圧(静圧)が通風温度20℃から80℃の範囲であるときに0Paから−30Paであって、流下路の側面の給風胴と排風胴の通気孔におが屑が吸着せず、乾燥槽の被乾燥おが屑を滞りなく流下させるように構成したことを特徴とするものである。   That is, the sawdust drying apparatus according to claim 1 is a sawdust drying apparatus that ventilates air while circulating the sawdust to be dried, and a drying tank that ventilates and drys the sawdust to be dried and the drying tank. A sawdust pump that feeds and circulates dried sawdust to the inside of the drying tank. Collecting of the sawdust collection unit that collects the dried sawdust that is quantitatively fed from the feed roll at one end, provided with a ventilation drying unit, sawdust storage unit and feed regulating body, and a feed roll below it Air pressure (static pressure) in the downflow path inside the drying tank is ventilated in a sawdust drying device with a hot air chamber connected to the pressure blower on the left and right across the chamber and an exhaust air chamber connected to the suction fan Temperature range from 20 ℃ to 80 ℃ In some cases, it is 0 Pa to -30 Pa, and sawdust is not adsorbed to the air supply and exhaust vents on the side of the downflow passage, and the dried sawdust in the drying tank is allowed to flow without any delay. It is a feature.

請求項2に係るおが屑の乾燥装置は、請求項1のおが屑の乾燥装置において、乾燥槽の内部の流下路内の空気圧(静圧)が通風温度20℃から80℃の範囲であるときに0Paから−30Paになるように、圧送送風機と吸引送風機の一方若しくはその両方の風量を制御可能としたことを特徴とするものである。   The sawdust drying apparatus according to claim 2 is the Padding sawdust drying apparatus according to claim 1, wherein the air pressure (static pressure) in the flow path inside the drying tank is 0 Pa when the airflow temperature is in the range of 20 ° C to 80 ° C. The air volume of one or both of the pressure blower and the suction blower can be controlled so that the pressure becomes -30 Pa.

本発明によれば、被乾燥おが屑を循環させながら通風乾燥するにあたって、乾燥槽内の通風乾燥部に対向して設けられた給風胴と排風胴の間の流下路を流下するおが屑が、排風胴の通気孔に吸着されずに良好に乾燥装置内を循環するように、収集部の内部の繰出しロールから定量的に繰出される被乾燥おが屑を一端に収集する収集室を挟んで左右の熱風室に接続された圧送送風機と排風室に接続された吸引送風機の風量を調節して、乾燥槽内の流下路の空気圧(静圧)を一定の範囲に限定したので、流下路の排風胴側面の通気孔におが屑が吸着せず、乾燥槽の被乾燥おが屑を滞りなく流下出来るようになった。   According to the present invention, when air-drying while circulating the sawdust to be dried, sawdust flowing down the flow path between the air supply drum and the exhaust drum provided facing the air-drying unit in the drying tank, Left and right across the collection chamber that collects dried sawdust quantitatively fed from the feed roll inside the collection unit at one end so that it can be circulated in the drying device without being adsorbed by the ventilation holes of the exhaust duct Since the air flow (static pressure) in the drying tank in the drying tank was limited to a certain range by adjusting the air volume of the pressure blower connected to the hot air chamber and the suction fan connected to the exhaust chamber, Sawdust is not adsorbed in the vent holes on the side of the exhaust wind tunnel, and the dried sawdust in the drying tank can flow down without delay.

更に、吸引送風機と圧送送風機は、通風乾燥部の流下路の空気圧(静圧)が常に定められた範囲内になるようそれぞれの風量を変更することができるので、被乾燥おが屑の水分の差による流下路の空気圧に変化が生じても、直ちに設定範囲内になるように調節できるので高水分のおが屑から、乾燥終了間近のおが屑に至って乾燥層内の排風胴の通気孔におが屑が吸着されずに流動性を良好にして、効率よく全体を均一に乾燥することができる効果を得られるものである。   Furthermore, the suction air blower and the pressure blower can change the air volume so that the air pressure (static pressure) of the flow path of the ventilation drying unit is always within a predetermined range. Even if there is a change in the air pressure in the downflow, it can be adjusted so that it immediately falls within the set range, so that high-moisture sawdust reaches the sawdust near the end of drying, and the sawdust is adsorbed to the vent holes in the exhaust drum in the drying layer. In addition, the fluidity is improved, and the effect of being able to efficiently and uniformly dry the whole can be obtained.

図1には本発明の実施の形態に係るおが屑の乾燥装置の外観斜視略図、図2には図1図と対象方向から示した一部を破断して示す斜視図、図3には本発明の実施の形態の正面断面図、図4には本発明の実施の形態の平面断面図である。   FIG. 1 is a schematic external perspective view of a sawdust drying apparatus according to an embodiment of the present invention, FIG. 2 is a perspective view showing a part cut away from FIG. 1 and the target direction, and FIG. FIG. 4 is a plan sectional view of the embodiment of the present invention.

図1ないし図2、図3に示す本発明に係るおが屑の乾燥装置1は、乾燥槽2とおが屑の投入口を備えたおが屑揚送機3とで構成されている。乾燥槽2はその上部から順におが屑収容部4、通風乾燥部5、おが屑滞留部6、おが屑収集部10を成しており、おが屑収集部10の上端には、複数の繰出しロール7によるおが屑繰出し部8を成している。9はその山形の繰出し規制体である。おが屑収集部10の下端部にはおが屑排出スクリューコンベア11が設けられている。また、おが屑収容部4の上部、即ち乾燥槽2の天面には、おが屑を均等分散させるための均分スクリューコンベア12が設けられている。乾燥槽2の上記おが屑排出スクリューコンベア11の搬送終端とおが屑揚送機3の下端側、そして均分スクリューコンベア12の搬送始端とおが屑揚送機3の上端側は接続されていて、おが屑の循環を円滑に行う事が出来る。   The sawdust drying apparatus 1 according to the present invention shown in FIGS. 1 to 2 and 3 includes a drying tank 2 and a sawdust feeder 3 having a sawdust inlet. The drying tank 2 includes a sawdust storage unit 4, a ventilation drying unit 5, a sawdust retention unit 6, and a sawdust collection unit 10 in that order from the top, and sawdust is delivered by a plurality of feeding rolls 7 at the upper end of the sawdust collection unit 10. Part 8 is formed. 9 is the Yamagata pay-out restricting body. A sawdust discharge screw conveyor 11 is provided at the lower end of the sawdust collection unit 10. Further, an equalizing screw conveyor 12 for evenly dispersing sawdust is provided at the upper portion of the sawdust accommodating portion 4, that is, the top surface of the drying tank 2. The transport end of the sawdust discharge screw conveyor 11 in the drying tank 2 and the lower end side of the sawdust lifter 3, and the transfer start end of the leveling screw conveyor 12 and the upper end side of the sawdust lifter 3 are connected to circulate sawdust. Can be performed smoothly.

乾燥槽2には、通風乾燥部5とおが屑滞留部6およびおが屑収集部10が、おが屑収集部10の収集室13によって左右に2分されていて、その一方が熱風室19、他方が排風室20となっている。   In the drying tank 2, the ventilation drying unit 5, the sawdust retention unit 6 and the sawdust collection unit 10 are divided into right and left by the collection chamber 13 of the sawdust collection unit 10, one of which is a hot air chamber 19 and the other is exhausted. It becomes the room 20.

熱風室19には乾燥風送風部21が設けられていて、この乾燥風送風部21はバーナ22の燃焼を燃焼管23内で行ない、圧送送風機24からの圧送風を燃焼管23の付近を通過した乾燥風を乾燥室19に強制的に送りこむようになっている。図4でバーナ22の燃焼風を燃焼管23から機外に排出しているが、バーナ22の燃焼風を乾燥風送風部21の圧送送風機24で外気と混合して乾燥室19内に送り込んでもよい。また、図4では乾燥風送風部21が熱風室19の外部に設置されているが、熱風室19内に乾燥風送風部21が内蔵されていてもよい(図示せず)。   The hot air chamber 19 is provided with a dry air blower 21, which burns the burner 22 in the combustion pipe 23 and passes the pressure blown air from the pressure blower 24 near the combustion pipe 23. The dried air is forcibly sent to the drying chamber 19. In FIG. 4, the combustion air of the burner 22 is discharged from the combustion pipe 23 to the outside of the machine. However, even if the combustion air of the burner 22 is mixed with the outside air by the pressure blower 24 of the drying air blowing unit 21 and sent into the drying chamber 19. Good. In FIG. 4, the dry air blowing unit 21 is installed outside the hot air chamber 19, but the dry air blowing unit 21 may be built in the hot air chamber 19 (not shown).

排風室20には吸引送風機25が機外に装備されていて圧送送風機24から熱風室19、そして通風乾燥部5を介して排風室20から吸引送風機25に通風するようになっている。なお、吸引送風機25も排風室20内に内蔵されていてもよい(図示せず)。   The exhaust fan 20 is equipped with a suction blower 25 outside the apparatus so as to pass air from the pressure blower 24 to the hot air chamber 19 and from the exhaust fan 20 to the suction fan 25 via the ventilation drying unit 5. The suction blower 25 may also be built in the exhaust air chamber 20 (not shown).

乾燥槽2の天面には、おが屑収容部4の上部空間から吸引排気する吸引排気ファン26を設けると共に、乾燥槽2内の平面方向の四隅には、熱風室19からおが屑収容部4まで乾燥風の一部を導く吸気ダクト27と、おが屑収容部4内の空気を排気室20まで導く排気ダクト28で繋がれていて、乾燥風の一部をおが屑収容部4に通気することによって、おが屑収容部4内の湿気を持った空気をいち早く機外に排出するので、天面及びおが屑収容部4内部の結露を防止している。   The top surface of the drying tank 2 is provided with suction / exhaust fans 26 for sucking and exhausting air from the upper space of the sawdust storage unit 4, and drying from the hot air chamber 19 to the sawdust storage unit 4 is performed at four corners in the plane of the drying tank 2. An air duct 27 that guides a part of the wind is connected to an exhaust duct 28 that guides the air in the sawdust accommodating portion 4 to the exhaust chamber 20, and a part of the dry air is vented to the sawdust accommodating portion 4, thereby sawdust. Moist air in the housing part 4 is quickly discharged out of the machine, so that condensation on the top surface and sawdust housing part 4 is prevented.

おが屑揚送機3には、揚送中に飛散する被乾燥おが屑を採取してその水分を計測する水分計測手段29を備えていて、本発明に係るおが屑乾燥装置1にあっては、この水分計測手段29により、循環乾燥中のおが屑の水分が所定値になったことを検出された時点で、乾燥を終了するように構成してある。   The sawdust lifting machine 3 is provided with a moisture measuring means 29 for collecting dried sawdust scattered during the feeding and measuring the moisture, and the sawdust drying device 1 according to the present invention has this moisture. When the measuring means 29 detects that the moisture content of the sawdust being circulated and dried reaches a predetermined value, the drying is terminated.

乾燥槽2の通風乾燥部5は、頂部が山形で多孔状の給風胴30と同様の排風胴31を交互に配設していて、それらの間におが屑の流下路32を形成して成るものであり、給風胴30は熱風室19に、排風胴31は排風室20にそれぞれ連通させてあって、熱風室19から乾燥風が給風胴30、おが屑の流下路32を横切って排風胴31に流入したうえ排風室20に排出されるように成っている。   The ventilation drying section 5 of the drying tank 2 is provided with alternately arranged exhaust wind drums 31 similar to the air supply drum 30 having a mountain shape at the top and a sawdust downflow path 32 formed between them. The air supply drum 30 communicates with the hot air chamber 19 and the air exhaust drum 31 communicates with the air exhaust chamber 20, respectively. The dry air is supplied from the hot air chamber 19 through the air supply drum 30 and the sawdust flow path 32. It crosses into the wind exhaust drum 31 and is discharged into the wind exhaust chamber 20.

おが屑の流下路32にはその部分の空気圧(静圧)を測定するセンサーを設けているものである。なお、収集室13、熱風室19、排風室20のどれか若しくはそれぞれにも空気圧(静圧)を測定するセンサーが設けられていればよく、それぞれのセンサーはおが屑の乾燥装置の制御部に繋がれている(図示せず)。   The sawdust flow path 32 is provided with a sensor for measuring the air pressure (static pressure) at that portion. Any one of the collection chamber 13, the hot air chamber 19, and the exhaust chamber 20 may be provided with a sensor for measuring air pressure (static pressure), and each sensor is provided in the control unit of the sawdust drying device. It is connected (not shown).

おが屑揚送機3のおが屑の投入口から投入された被乾燥おが屑は、内部に通風乾燥部5を設けた乾燥槽2の上部から被乾燥おが屑が投入され、流下路32を流下し、繰出しロール7から定量に繰り出され、収集室13の底部のおが屑排出スクリューコンベア11からおが屑揚送機3にいたる循環工程を乾燥終了まで繰り返す。   Dried sawdust introduced from the sawdust feeding port of sawdust lifter 3 is fed into the desiccated sawdust from the upper part of the drying tank 2 provided with the ventilation drying section 5 inside, and flows down the downflow path 32 and is fed out. 7, the circulation process from the sawdust discharging screw conveyor 11 at the bottom of the collection chamber 13 to the sawdust lifter 3 is repeated until the drying is completed.

この工程の途中、通風乾燥部5の流下路32において、この流下路32の空気圧(静圧)が0Paに近づくほど給風胴30から排風胴31へ通過する乾燥風があっても流下路32の排風胴31側面の通気孔におが屑が張り付く現象が起きないことが実験から解った。特に乾燥風が20℃から80℃の範囲において、流下路32の空気圧(静圧)が0Paから−30Paで特におが屑の吸着現象の発生を抑えることがことが判明した。そこで乾燥風が20℃から80℃の範囲に、圧送送風機24と吸引送風機25のそれぞれの風量を調整し、流下路32の空気圧(静圧)を0Paから−30Paになるように調節することによって流下路32の排風胴31側面の通気孔におが屑が吸着されないので、流下路32をおが屑が滞りなく流下するものである。   In the middle of this process, in the downstream channel 32 of the ventilation drying unit 5, even if there is dry wind passing from the air supply drum 30 to the exhaust drum 31 as the air pressure (static pressure) of the downstream channel 32 approaches 0 Pa, the downstream channel is present. It has been found from experiments that the phenomenon of sawdust sticking to the vent holes on the side surface of the 32 exhaust cylinders 31 does not occur. In particular, it has been found that when the drying air is in the range of 20 ° C. to 80 ° C., the air pressure (static pressure) of the downflow passage 32 is 0 Pa to −30 Pa, and particularly the occurrence of the sawdust adsorption phenomenon is suppressed. Therefore, by adjusting the air flow rate of the pressure blower 24 and the suction blower 25 so that the drying air is in the range of 20 ° C. to 80 ° C., and adjusting the air pressure (static pressure) of the flow down passage 32 from 0 Pa to −30 Pa. Since sawdust is not adsorbed in the vent holes on the side surface of the exhaust duct 31 of the downflow path 32, the sawdust flows down the downflow path 32 without stagnation.

しかしながら被乾燥物の水分値によって、通風乾燥部5内の流下路32の空気抵抗に変化が生じ、乾燥機内の空気圧が変動することは知られている所である。そこで本発明に係る実施においては、流下路32内に空気圧(静圧)を測定するセンサーを設けているのでセンサーからの信号を制御盤で判断し、圧送送風機24と吸引送風機25のどちらかまたはその両方の風量を変化させて常に流下路32の空気圧(静圧)を0Paから−30Paにすることによって、おが屑の良好な流動性を維持できるものである。このため、水分を多く含んだ被乾燥おが屑であっても効率よく全体を均等に乾燥できるものである。   However, it is known that the air resistance of the downflow path 32 in the ventilation drying unit 5 varies depending on the moisture value of the material to be dried, and the air pressure in the dryer fluctuates. Therefore, in the implementation according to the present invention, since a sensor for measuring the air pressure (static pressure) is provided in the downflow passage 32, a signal from the sensor is judged by the control panel, and either the pressure blower 24 or the suction blower 25 or By changing both of the air volumes so that the air pressure (static pressure) of the flow path 32 is always changed from 0 Pa to −30 Pa, the good flowability of sawdust can be maintained. For this reason, even if it is to-be-dried sawdust containing much moisture, the whole can be dried efficiently and uniformly.

流下路32内に空気圧(静圧)を測定するセンサーを設ける場所によっては、流下路32内におが屑の流下の障害物を設けてしまう可能性がある。そこで本発明では、被乾燥おが屑の乾燥中の流下路32内の空気圧(静圧)を0Paから−30Paにすると、排風室20の空気圧(静圧)が−300Paから−350Pa、熱風室19の空気圧(静圧)は0Paから−10Pa、収集室13の空気圧(静圧)は−30Paから−100Paの付近になることも実験より判明し、排風室20、熱風室19、収集室13のどれか若しくはその複数に空気圧測定センサーを設け、それぞれの設定値内の空気圧(静圧)になるよう常に圧送送風機24と吸引送風機25のどちらか若しくはその両方を制御することで、おが屑を効率よく全体を均等に乾燥できる。   Depending on where the sensor for measuring the air pressure (static pressure) is provided in the downflow path 32, there is a possibility that an obstacle for the flow of sawdust will be provided in the downflow path 32. Therefore, in the present invention, when the air pressure (static pressure) in the flow path 32 during drying of the sawdust to be dried is changed from 0 Pa to −30 Pa, the air pressure (static pressure) of the exhaust chamber 20 is −300 Pa to −350 Pa, the hot air chamber 19. It has also been found from experiments that the air pressure (static pressure) of air is 0 Pa to −10 Pa, and the air pressure (static pressure) of the collection chamber 13 is in the vicinity of −30 Pa to −100 Pa. Efficient sawdust by providing air pressure measurement sensors on one or more of them, and controlling either one or both of the pressure blower 24 and suction blower 25 so that the air pressure (static pressure) is within the set value. The whole can be dried evenly.

本発明のおが屑の乾燥装置においては、おが屑のみならず質量の軽い粉粒物であっても循環通風乾燥が可能となるので、農業用の穀物乾燥装置から、食品加工物の乾燥又は産業廃棄物のチップの乾燥等幅広い乾燥装置として使用可能となる。   In the sawdust drying device of the present invention, circulation ventilation drying is possible not only for sawdust but also for a light-weight powdered granule, so that it is possible to dry food processed products or industrial waste from an agricultural grain drying device. It can be used as a wide range of drying equipment such as drying chips.

本発明の実施の形態に係るおが屑の乾燥装置の外観斜視略図。1 is a schematic external perspective view of a sawdust drying apparatus according to an embodiment of the present invention. 図1図と対象方向から示した一部を破断して示す斜視図。The perspective view which fractures | ruptures and shows a part shown from FIG. 1 and an object direction. 本発明の実施の形態の正面断面図。The front sectional view of an embodiment of the invention. 本発明の実施の形態の平面断面図。The top sectional view of an embodiment of the invention.

符号の説明Explanation of symbols

1 おが屑乾燥装置
2 乾燥槽
3 おが屑揚送機
4 おが屑収容部
5 通風乾燥部
6 おが屑滞留部
7 繰出しロール
8 おが屑繰出し部
9 繰出し規制体
10 おが屑収集部
11 おが屑排出スクリューコンベア
12 均分スクリューコンベア
13 収集室
19 熱風室
20 排風室
21 乾燥風送風部
22 バーナ
23 燃焼管
24 圧送送風機
25 吸引送風機
26 吸引排気ファン
27 吸気ダクト
28 排気ダクト
29 水分計測手段
30 給風胴
31 排風胴
32 流下路
DESCRIPTION OF SYMBOLS 1 Sawdust drying apparatus 2 Drying tank 3 Sawdust transporter 4 Sawdust accommodating part 5 Ventilation drying part 6 Sawdust retention part 7 Feeding roll 8 Sawdust delivery part 9 Feeding regulation body 10 Sawdust collection part 11 Sawdust discharge screw conveyor 12 Uniform screw conveyor 13 Collection chamber 19 Hot air chamber 20 Ventilation chamber 21 Dry air blower 22 Burner 23 Combustion tube 24 Pressure blower 25 Suction blower 26 Suction exhaust fan 27 Intake duct 28 Exhaust duct 29 Moisture measuring means 30 Air supply drum 31 Exhaust drum 32 Downstream

Claims (2)

被乾燥おが屑を循環させながら通風乾燥するおが屑の乾燥装置であって、
被乾燥おが屑を収容し循環させながら通風乾燥する乾燥槽と、この乾燥槽に被乾燥おが屑を投入して循環させるおが屑揚送機とを備えて構成され、
乾燥槽の内部には、給風胴と排風胴とを対向させてそれらの間を被乾燥おが屑の流下路と成した通風乾燥部と、
おが屑滞留部と繰出し規制体と、その下方には繰出しロールを設けていて、
繰出しロールから定量的に繰出される被乾燥おが屑を一端に収集するおが屑収集部の収集室を挟んで左右に圧送送風機に接続された熱風室と、吸引送風機に接続された排風室を備えたおが屑の乾燥装置において、
乾燥槽の内部の流下路内の空気圧(静圧)が通風温度20℃から80℃の範囲であるときに0Paから−30Paであって、流下路の側面の給風胴と排風胴の通気孔におが屑が吸着せず、乾燥槽の被乾燥おが屑を滞りなく流下させるように構成したことを特徴とする
おが屑の乾燥装置。
A sawdust drying device for drying by ventilation while circulating dried sawdust,
It comprises a drying tank that stores and circulates dried sawdust, and a sawdust lifter that feeds and circulates dried sawdust into the drying tank.
In the inside of the drying tank, a ventilation drying section formed by facing the air supply drum and the exhaust drum and the flow of dried sawdust between them,
A sawdust retention part, a feeding regulation body, and a lowering roll are provided below,
A hot air chamber connected to a pressure blower on both sides across a collection chamber of a sawdust collection unit that collects dry sawdust quantitatively fed from a feed roll at one end, and an exhaust chamber connected to a suction blower In sawdust drying equipment,
When the air pressure (static pressure) in the downflow channel inside the drying tank is in the range of 20 ° C to 80 ° C in the ventilation temperature range of 0 ° C to -30Pa, A sawdust drying apparatus, wherein sawdust is not adsorbed in the pores, and the dried sawdust in the drying tank is allowed to flow smoothly.
乾燥槽の内部の流下路内の空気圧(静圧)が通風温度20℃から80℃の範囲であるときに0Paから−30Paになるように、圧送送風機と吸引送風機の一方若しくはその両方の風量を制御可能としたことを特徴とする請求項1に記載のおが屑の乾燥装置。
When the air pressure (static pressure) in the flow path inside the drying tank is in the range of 20 ° C. to 80 ° C., the air volume of one or both of the pressure blower and the suction blower is adjusted so as to be 0 Pa to −30 Pa. The sawdust drying apparatus according to claim 1, wherein the sawdust drying apparatus is controllable.
JP2004058296A 2004-03-03 2004-03-03 Sawdust drying equipment Expired - Lifetime JP4435605B2 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112503913A (en) * 2020-11-05 2021-03-16 合肥三伍机械有限公司 Grain drying structure

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112503913A (en) * 2020-11-05 2021-03-16 合肥三伍机械有限公司 Grain drying structure

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