JP4724674B2 - Continuous dryer - Google Patents

Continuous dryer Download PDF

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JP4724674B2
JP4724674B2 JP2007034368A JP2007034368A JP4724674B2 JP 4724674 B2 JP4724674 B2 JP 4724674B2 JP 2007034368 A JP2007034368 A JP 2007034368A JP 2007034368 A JP2007034368 A JP 2007034368A JP 4724674 B2 JP4724674 B2 JP 4724674B2
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covering member
trough
stirring
stirring blades
liquid
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JP2008196818A (en
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和典 福本
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Kurimoto Ltd
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Description

本発明は、合成樹脂の重合処理等の後における溶剤等の液体成分の除去や、処理廃液からの溶剤等の液体成分の回収、化学原料や各種無機物からの水分の除去等に用いられる連続式乾燥機に関する。   The present invention is a continuous type used for removal of liquid components such as solvents after polymerization treatment of synthetic resin, recovery of liquid components such as solvents from processing waste liquid, removal of moisture from chemical raw materials and various inorganic substances, etc. It relates to the dryer.

合成樹脂を有機溶剤中で重合等の処理をする場合には、その後工程で溶剤等の液体成分を除去する乾燥処理を行う必要がある。また、処理廃液から溶剤等の液体成分を回収するために乾燥処理を行うことも必要になる。さらに、化学原料や各種無機物から水分を除去するために乾燥処理が必要になる場合もある。   When the synthetic resin is subjected to a treatment such as polymerization in an organic solvent, it is necessary to perform a drying treatment to remove a liquid component such as a solvent in a subsequent step. In addition, it is necessary to perform a drying process in order to recover a liquid component such as a solvent from the processing waste liquid. Furthermore, a drying process may be required to remove moisture from chemical raw materials and various inorganic substances.

このような乾燥処理を連続的に行う連続式乾燥機として、図4および図5に示すように、一端側に被処理物の投入口1aを、他端側にその排出口1bを設けた横型トラフ1内に、互いに逆向きに回転する撹拌羽根2が設けられた一対の回転軸2aを横架して、投入口1aから投入される被処理物を、中空の回転軸2a内やトラフ1の外側のジャケット3内に通される熱媒体で間接加熱しながら、撹拌羽根2で撹拌しつつ排出口1bへ移送し、この移送中に被処理物に含まれる液体成分を蒸発させるようにしたものがある(例えば、特許文献1参照)。   As a continuous dryer for continuously performing such a drying process, as shown in FIGS. 4 and 5, a horizontal type in which an input port 1a for an object to be processed is provided on one end side and an outlet port 1b is provided on the other end side. A pair of rotating shafts 2 a provided with stirring blades 2 that rotate in opposite directions in the trough 1 are horizontally mounted, and an object to be processed that is input from the input port 1 a is placed in the hollow rotating shaft 2 a or the trough 1. While being indirectly heated with a heat medium passed through the outer jacket 3, it is transferred to the discharge port 1 b while being stirred by the stirring blade 2, and the liquid component contained in the object to be processed is evaporated during this transfer. There are some (see, for example, Patent Document 1).

特許文献1に記載されたものでは、トラフ1内を移送中の被処理物から蒸発する液体成分を除去しやすくするためにトラフ1の上部を開放し、開放した上部を天井7aと側壁7bおよび端壁7cで囲って蒸気室7に形成し、天井7aに長さ方向で間隔を開けて複数の排気口8を設けて、各排気口8を真空ポンプ等の減圧装置に接続するとともに、トラフ1の投入口1a側端部から液体成分の蒸発活性域の全域またはその大半を含む範囲で、一対の各撹拌羽根2に接近させてこれらの上側を覆う覆い部材9を配設している。   In the one described in Patent Document 1, the upper portion of the trough 1 is opened in order to easily remove the liquid component that evaporates from the processing object being transferred through the trough 1, and the opened upper portion has a ceiling 7a and a side wall 7b. Formed in the steam chamber 7 by being surrounded by the end wall 7c, provided with a plurality of exhaust ports 8 at intervals in the length direction on the ceiling 7a, and connecting each exhaust port 8 to a decompression device such as a vacuum pump, A covering member 9 is provided so as to approach the pair of stirring blades 2 and cover the upper side thereof in a range including the whole or most of the evaporation active region of the liquid component from the end portion on the side of the one inlet 1a.

すなわち、前記投入口1aから投入された直後の被処理物には蒸発しやすい液体成分が多く含まれているので、トラフ1の投入口1a側の所定の領域は、これらの液体成分が活発に蒸発する蒸発活性域となる。このような蒸発活性域では、蒸気室7が減圧装置で減圧されると、これらの液体成分が一気に蒸発して多量の蒸気が発生する突沸現象が生じやすくなり、この突沸現象に伴う蒸気流によって、被処理物中の固形物や蒸発し難い液状物が上方へ飛散して、蒸気室7を形成する天井7aや壁7b、7cに付着する。このように天井7aや壁7b、7cに付着した固形物や液状物は、時間の経過とともに蒸気室7内の熱による熱劣化等によって変質し、異物となって被処理物に混入する恐れがある。また、天井7aに付着するものは排気口8を閉塞する恐れもある。このような突沸現象による固形物や液状物の天井7aや壁7b、7cへの付着を防止するために、特許文献1に記載されたものでは、蒸発活性域で一対の各撹拌羽根2の上側を覆う覆い部材9を配設し、突沸現象に伴う蒸気流を、覆い部材9のない蒸発活性域の下流側へ迂回させて排気口8へ導くようにしている。   That is, since the object to be processed immediately after being introduced from the inlet 1a contains a lot of liquid components that easily evaporate, the liquid components are actively present in a predetermined region of the trough 1 on the inlet 1a side. It becomes the evaporation active area to evaporate. In such an evaporation active region, when the vapor chamber 7 is depressurized by a decompression device, a bumping phenomenon in which these liquid components evaporate all at once and a large amount of vapor is generated easily occurs. The solid matter or the liquid matter that is difficult to evaporate is scattered upward and adheres to the ceiling 7a and the walls 7b, 7c forming the vapor chamber 7. As described above, the solid matter or liquid matter adhering to the ceiling 7a or the walls 7b and 7c may be changed by heat deterioration due to heat in the steam chamber 7 with the passage of time, and may be mixed into the object to be processed as foreign matter. is there. Moreover, what adheres to the ceiling 7a may block the exhaust port 8. In order to prevent the solid matter or the liquid matter from adhering to the ceiling 7a or the walls 7b, 7c due to such a bumping phenomenon, the one described in Patent Document 1 has an upper side of each pair of stirring blades 2 in the evaporation active region A covering member 9 is provided so that the vapor flow accompanying the bumping phenomenon is diverted to the downstream side of the evaporation active region without the covering member 9 and led to the exhaust port 8.

特開2001−280844号公報Japanese Patent Laid-Open No. 2001-280844

特許文献1に記載されたように蒸発活性域に覆い部材を配設した連続式乾燥機は、突沸現象による固形物や液状物の蒸気室の天井や壁への付着は防止できるが、蒸発活性域から覆い部材を迂回して排気口に導かれる蒸気流や、蒸発活性域の下流側で発生して覆い部材の上側から排気口に導かれる蒸気流に混入する固形粉体や飛沫液体が、覆い部材の上面に降下して、徐々に堆積する。このように覆い部材の上面に堆積した堆積物は、蒸気の通路となる覆い部材の上側を塞いだり、長時間の加熱で変質して発火したりする恐れがある。   As described in Patent Document 1, the continuous dryer having a covering member disposed in the evaporation active region can prevent the solid or liquid material from adhering to the ceiling or wall of the vapor chamber due to bumping phenomenon, but the evaporation activity The vapor flow that is led from the area around the covering member to the exhaust port, or the solid powder or splash liquid that is generated downstream of the evaporation active area and mixed into the vapor flow that is led from the upper side of the covering member to the exhaust port, It descends to the upper surface of the covering member and gradually accumulates. Thus, the deposit deposited on the upper surface of the covering member may block the upper side of the covering member serving as a vapor passage, or may change in quality and ignite due to long-time heating.

そこで、本発明の課題は、連続式乾燥機の蒸発活性域に配設した覆い部材の上面に、蒸気流に混入する固形粉体や飛沫液体が堆積しないようにすることである。   Therefore, an object of the present invention is to prevent the solid powder and the splash liquid mixed in the vapor flow from accumulating on the upper surface of the covering member disposed in the evaporation active region of the continuous dryer.

上記の課題を解決するために、本発明は、一端側に被処理物の投入口を、他端側にその排出口を設けた横型トラフ内に、互いに逆向きに回転する撹拌羽根が設けられた一対の回転軸を横架して、これらの撹拌羽根の上方の前記トラフ内を蒸気室に形成し、この蒸気室を形成する天井に長さ方向で間隔を開けて複数の排気口を設けて、前記投入口から投入される被処理物を加熱しながら、前記撹拌羽根で撹拌しつつ前記排出口へ移送し、この移送中に前記被処理物に含まれる液体成分を蒸発させて、その蒸気を前記排気口から排気するようにし、前記トラフの投入口側端部から前記液体成分の蒸発活性域の全域またはその大半を含む範囲で、前記各撹拌羽根に近接させてこれらの上側を覆う覆い部材を配設した連続式乾燥機において、前記覆い部材に、前記各撹拌羽根がその回転軸に対して下向きに回転移動する側で、回転軸の軸方向に延びる開口を設け、前記覆い部材の上面に前記開口に向かって下降傾斜する傾斜面を設けた構成を採用した。   In order to solve the above-mentioned problems, the present invention is provided with stirring blades rotating in opposite directions in a horizontal trough provided with a workpiece inlet on one end and a discharge outlet on the other end. A pair of rotating shafts are horizontally mounted, the inside of the trough above the stirring blades is formed in a steam chamber, and a plurality of exhaust ports are provided at intervals in the length direction on the ceiling forming the steam chamber. Then, while heating the object to be processed which is input from the input port, it is transferred to the discharge port while being stirred by the stirring blade, and during this transfer, the liquid component contained in the object to be processed is evaporated, The steam is exhausted from the exhaust port, and covers the upper side of each of the stirring blades close to each other within the range including the whole or most of the evaporation active region of the liquid component from the end portion on the trough inlet side. In a continuous dryer provided with a covering member, the covering The material is provided with an opening extending in the axial direction of the rotating shaft on the side where each of the stirring blades rotates downward with respect to the rotating shaft, and an inclined surface inclined downward toward the opening is provided on the upper surface of the covering member. The provided configuration was adopted.

すなわち、覆い部材に、各撹拌羽根がその回転軸に対して下向きに回転移動する側で、回転軸の軸方向に延びる開口を設け、覆い部材の上面に開口に向かって下降傾斜する傾斜面を設けることにより、蒸気流に混入して覆い部材の上面に降下する固形粉体や飛沫液体を、覆い部材の上面の傾斜面に沿わせて開口へ落下させ、下向きに回転移動する撹拌羽根に巻き込まれる被処理物に付着させて、被処理物と一緒に移送するようにし、固形粉体や飛沫液体が覆い部材の上面に堆積しないようにした。   That is, the cover member is provided with an opening extending in the axial direction of the rotation shaft on the side where each stirring blade rotates downward with respect to the rotation shaft, and an inclined surface that is inclined downward toward the opening on the upper surface of the cover member. By providing, solid powder and splash liquid mixed in the vapor flow and descending to the upper surface of the covering member are dropped along the inclined surface of the upper surface of the covering member into the opening, and are caught in the stirring blade that rotates downward. It was made to adhere to the to-be-processed object and to be transferred together with the to-be-processed object so that the solid powder and the splash liquid were not deposited on the upper surface of the covering member.

前記各撹拌羽根を前記一対の回転軸間の中央側で下向きに回転移動するものとし、前記覆い部材の前記各撹拌羽根が下向きに回転移動する側で設けられる開口を、前記回転軸間の中央側で一つの共通のものとすることにより、開口を一箇所にまとめて形成することができる。   Each of the stirring blades is rotated downward on the center side between the pair of rotation shafts, and an opening provided on the side of the cover member on which the stirring blades rotate downward is provided at the center between the rotation shafts. By making one common on the side, the openings can be formed in one place.

本発明の連続式乾燥機は、蒸発活性域に配設した覆い部材に、各撹拌羽根がその回転軸に対して下向きに回転移動する側で、回転軸の軸方向に延びる開口を設け、覆い部材の上面に開口に向かって下降傾斜する傾斜面を設けることにより、蒸気流に混入して覆い部材の上面に降下する固形粉体や飛沫液体を、覆い部材の上面の傾斜面に沿わせて開口へ落下させ、下向きに回転移動する撹拌羽根に巻き込まれる被処理物に付着させて、被処理物と一緒に移送するようにしたので、固形粉体や飛沫液体が覆い部材の上面に堆積しないようにすることができる。   In the continuous dryer according to the present invention, an opening extending in the axial direction of the rotary shaft is provided on the cover member disposed in the evaporation active region on the side where each stirring blade rotates downward with respect to the rotary shaft. By providing an inclined surface that is inclined downward toward the opening on the upper surface of the member, solid powder and droplet liquid mixed in the vapor flow and descending on the upper surface of the covering member are caused to follow the inclined surface of the upper surface of the covering member. Since it is dropped into the opening and attached to the object to be wound around the stirring blade that rotates downward, it is transferred together with the object to be processed, so that solid powder and splash liquid do not accumulate on the upper surface of the covering member. Can be.

前記各撹拌羽根を一対の回転軸間の中央側で下向きに回転移動するものとし、覆い部材の各撹拌羽根が下向きに回転移動する側で設けられる開口を、回転軸間の中央側で一つの共通のものとすることにより、開口を一箇所にまとめて形成することができる。   Each of the stirring blades is rotationally moved downward on the center side between the pair of rotating shafts, and an opening provided on the side where each of the stirring blades of the covering member is rotated downward is provided on the central side between the rotating shafts. By using a common one, the openings can be formed in one place.

以下、図面に基づき、本発明の実施形態を説明する。図1および図2は、第1の実施形態を示す。この連続式乾燥機は、一端側に被処理物の投入口1aを、他端側にその排出口1bを設けた横型トラフ1内に、互いに逆向きに中央の内側で下向きに回転する撹拌羽根2が設けられた一対の回転軸2aを横架して、投入口1aから投入される被処理物を、中空の回転軸2a内とトラフ1の外側のジャケット3内に通される熱媒体で間接加熱しながら、撹拌羽根2で撹拌しつつ排出口1bへ移送し、移送中に被処理物に含まれる液体成分を蒸発させるようにしたものである。   Hereinafter, embodiments of the present invention will be described with reference to the drawings. 1 and 2 show a first embodiment. This continuous dryer is a stirring blade that rotates downward in the center in the opposite direction in a horizontal trough 1 having an inlet 1a for a workpiece on one end and an outlet 1b on the other end. 2 is a heating medium that passes through a pair of rotating shafts 2 a provided with 2 and passes through a hollow rotating shaft 2 a and a jacket 3 outside the trough 1, to be processed. The liquid component contained in the object to be processed is evaporated during the transfer while being indirectly heated and transferred to the discharge port 1b while being stirred by the stirring blade 2.

前記各撹拌羽根2は、トラフ1の投入口1a側端部から排出口1bに至る範囲は順送りスクリュ2bとされ、排出口1bから排出口1b側端部までの範囲は、行き過ぎた被処理物を排出口1bに戻すため、逆送りスクリュ2cとされている。順送りスクリュ2bは、被処理物の撹拌作用を高めるために、回転軸2aを挟んで対向する位置でスクリュ外周部の一部を切り取った切り取り部4が設けられ、各切り取り部4の一端側にはスクレーパ5が取り付けられている。また、排出口1bの上方には、被処理物を排出しやすくするために、各撹拌羽根2の上部に近接するフード6が設けられている。   Each stirring blade 2 has a progressive feed screw 2b in the range from the end of the trough 1 on the inlet 1a side to the outlet 1b, and the range from the outlet 1b to the end of the outlet 1b is excessive. Is returned to the discharge port 1b as a reverse feed screw 2c. In order to enhance the stirring action of the workpiece, the progressive feed screw 2b is provided with a cutout portion 4 in which a part of the outer peripheral portion of the screw is cut off at a position facing the rotation shaft 2a, and one end side of each cutout portion 4 is provided. A scraper 5 is attached. Further, a hood 6 adjacent to the upper part of each stirring blade 2 is provided above the discharge port 1b in order to facilitate discharge of the workpiece.

前記トラフ1の上部は開放されて、開放された上部が天井7aと側壁7bおよび端壁7cで囲われて蒸気室7に形成され、天井7aに長さ方向で間隔を開けて複数の排気口8が設けられており、蒸気室7を減圧するために、各排気口8が真空ポンプ(図示省略)に接続されている。また、後述する蒸発活性域となるトラフ1の投入口1a側端部から全長の約50%の範囲では、一対の各撹拌羽根2に近接させてこれらの上側を覆う覆い部材9が配設されている。覆い部材9は、互いに内側へ逆向きに回転する各撹拌羽根2が下向きに回転移動するトラフ1の中央で、回転軸2aの軸方向に延びる開口10が設けられ、その両側の上面に開口10に向かって下降傾斜する傾斜面9aが設けられている。   The upper part of the trough 1 is opened, and the opened upper part is surrounded by a ceiling 7a, a side wall 7b, and an end wall 7c to be formed in a steam chamber 7, and a plurality of exhaust ports are provided at intervals in the length direction on the ceiling 7a. 8 is provided, and each exhaust port 8 is connected to a vacuum pump (not shown) in order to depressurize the steam chamber 7. Further, in the range of about 50% of the total length from the end portion of the trough 1 serving as an evaporation active region to be described later, the covering member 9 is disposed so as to be close to the pair of stirring blades 2 and to cover the upper side thereof. ing. The covering member 9 is provided with an opening 10 extending in the axial direction of the rotating shaft 2a at the center of the trough 1 in which the respective stirring blades 2 rotating in the opposite directions to each other rotate downward. An inclined surface 9a that is inclined downward is provided.

以下に、上述した連続式乾燥機の作用を説明する。前記トラフ1内の被処理物は、熱媒体で間接加熱されながら撹拌羽根2で撹拌されて乾燥されるが、投入口1aから投入された直後の被処理物は蒸発しやすい液体成分を多く含むので、前記覆い部材9で覆われた投入口1a側の領域は、液体成分が活発に蒸発する蒸発活性域となる。   Below, the effect | action of the continuous dryer mentioned above is demonstrated. The object to be processed in the trough 1 is dried by being stirred by the stirring blade 2 while being indirectly heated by the heat medium, but the object to be processed immediately after being charged from the charging port 1a contains a lot of liquid components that easily evaporate. Therefore, the region on the inlet 1a side covered with the covering member 9 is an evaporation active region where the liquid component is actively evaporated.

前記蒸発活性域では、蒸気室7が減圧装置で減圧されるので、これらの液体成分が一気に蒸発して多量の蒸気が発生する突沸現象が生じることがある。しかしながら、覆い部材9が設けられた蒸発活性域は、覆い部材9の下方に被処理物が充満していることと、大半が覆い部材9で覆われていることから、突沸現象が生じてもその勢いが弱まり、その蒸気流に含まれる固形物や液状物が覆い部材9の開口10を通過して上方へ飛散する恐れは殆どない。また、これらが上方へ飛散しても、その勢いが弱いため蒸気室7の天井7aまで到達することはなく、覆い部材9の上面に降下して、その傾斜面9aに沿って滑落または流下し、開口10内に落下する。開口10内に落下した固形物や液状物は、中央の内側で下向きに回転移動する各撹拌羽根2に巻き込まれる被処理物に付着して、被処理物と一緒に下流側へ移送される。   In the evaporation active region, the vapor chamber 7 is depressurized by the decompression device, so that a bumping phenomenon may occur in which these liquid components evaporate all at once and a large amount of vapor is generated. However, the evaporation active area provided with the cover member 9 is filled with the object to be processed under the cover member 9 and is mostly covered with the cover member 9, so that even if bumping phenomenon occurs. The momentum is weakened, and there is almost no risk that the solid or liquid contained in the vapor flow will scatter upward through the opening 10 of the covering member 9. Even if they are scattered upward, they do not reach the ceiling 7a of the steam chamber 7 because of their weak momentum, and descend to the upper surface of the covering member 9 and slide down or flow down along the inclined surface 9a. , Falls into the opening 10. The solid matter or liquid matter that has fallen into the opening 10 adheres to the workpiece to be wound around each stirring blade 2 that rotates downward inside the center, and is transferred to the downstream side together with the workpiece.

また、前記蒸発活性域で発生した蒸気の大半は、覆い部材9の下流側へ迂回して、天井7aの各排気口8へ向かう。覆い部材9のない蒸発活性域より下流側で発生した蒸気も各排気口8へ向かう。これらの蒸気には細かい固形粉体や飛沫液体が含まれ、覆い部材9の上方の排気口8へ向かう蒸気に含まれるものは、自重で覆い部材9の上面に降下するが、これらの固形粉体や飛沫液体も上面の傾斜面9aに沿って滑落または流下し、開口10内に落下する。したがって、覆い部材9の上面に固形粉体や飛沫液体が堆積することはない。なお、揮発しやすい液体成分を除去されて排出口1bへ移送された被処理物は、粉状やペースト状の乾燥処理物として排出口1bから押し出される。   Further, most of the steam generated in the evaporating active area is detoured to the downstream side of the covering member 9 and goes to each exhaust port 8 of the ceiling 7a. Vapor generated downstream from the evaporation active region without the covering member 9 also travels toward the exhaust ports 8. These vapors contain fine solid powder and liquid droplets, and what is contained in the vapor directed to the exhaust port 8 above the covering member 9 falls to the upper surface of the covering member 9 by its own weight. The body and the splash liquid also slide down or flow down along the inclined surface 9 a on the upper surface and fall into the opening 10. Therefore, no solid powder or splash liquid is deposited on the upper surface of the covering member 9. In addition, the to-be-processed object which removed the liquid component which is easy to volatilize, and was transferred to the discharge port 1b is extruded from the discharge port 1b as a powdery or paste-like dry processed material.

上述した連続式乾燥機(実施例)と図4に示した従来の連続式乾燥機(比較例)を用いて、溶剤75質量%を含む樹脂溶液の被処理物の乾燥処理を行った。これらの連続式乾燥機の諸元と運転条件は以下の通りである。
・撹拌羽根の外径 :100mm
・撹拌羽根の回転数 :30〜60rpm
・覆い部材の配設範囲:トラフの全長の約50%
・トラフ内の加熱温度:200℃
・蒸気室の減圧圧力 :50〜100torr
・被処理物の投入量 :24kg/hr
・運転時間 :5時間
Using the above-described continuous dryer (Example) and the conventional continuous dryer shown in FIG. 4 (Comparative Example), the treatment object of the resin solution containing 75% by mass of the solvent was dried. The specifications and operating conditions of these continuous dryers are as follows.
・ Outer diameter of stirring blade: 100 mm
・ Rotation speed of stirring blade: 30-60rpm
-Covering range of cover member: about 50% of the total length of trough
-Heating temperature in the trough: 200 ° C
・ Vacuum chamber pressure reduction: 50-100 torr
-Input amount of workpiece: 24 kg / hr
・ Operating time: 5 hours

上記乾燥処理を行ったのち、実施例と比較例の連続式乾燥機における覆い部材の上面の堆積物の量を測定した。比較例のものは、覆い部材の上面に堆積物が約5mm堆積していたのに対して、実施例のものでは殆ど堆積物が認められなかった。   After performing the above-mentioned drying treatment, the amount of deposits on the upper surface of the covering member in the continuous dryers of Examples and Comparative Examples was measured. In the comparative example, about 5 mm of deposit was deposited on the upper surface of the covering member, whereas in the example, almost no deposit was observed.

図3は、第2の実施形態を示す。この連続式乾燥機は、基本的な構成は第1の実施形態のものと同じであり、前記一対の撹拌羽根2が互いに逆向きに外側で下向きに回転するものとされ、前記蒸発活性域を覆う覆い部材9の開口10が、各撹拌羽根2が下向きに回転移動するトラフ1の両サイドに設けられ、覆い部材9の上面が中央から両側の開口10に向かって下降傾斜する傾斜面9aとされている点が異なる。したがって、この実施形態では、覆い部材9の上面に降下する前記固形物や液状物および固形粉体や飛沫液体が、トラフ1の両サイドの各開口10に分かれて落下し、下向きに回転移動する各撹拌羽根2に巻き込まれる被処理物に付着して、被処理物と一緒に下流側へ移送される。   FIG. 3 shows a second embodiment. This continuous dryer has the same basic configuration as that of the first embodiment, and the pair of stirring blades 2 rotate outwardly in opposite directions to each other. An opening 10 of the covering member 9 is provided on both sides of the trough 1 where each stirring blade 2 rotates downward, and an inclined surface 9a in which the upper surface of the covering member 9 is inclined downward from the center toward the openings 10 on both sides; Is different. Therefore, in this embodiment, the solid material, liquid material, solid powder, and splash liquid falling on the upper surface of the covering member 9 fall into the openings 10 on both sides of the trough 1 and rotate downward. It adheres to the workpiece to be wound around each stirring blade 2 and is transferred to the downstream side together with the workpiece.

上述した各実施形態では、蒸発活性域を覆う覆い部材の配設範囲をトラフの全長の約50%としたが、蒸発活性域は被処理物の揮発性液体成分の含有量や加熱条件等によって異なるので、覆い部材の配設範囲は、蒸発活性域の長さに応じてトラフの全長の20〜50%程度の範囲で変更するとよい。また、覆い部材は、必ずしも蒸発活性域の全域を覆う必要はなく、全域の70%以上、好ましくは90%以上を覆うようにするとよい。なお、覆い部材は、軸方向に分割したユニットから成るものとし、所望の配設範囲に応じて、ユニット単位で取り付け、取り外しするようにしてもよい。
部材とし、
In each of the above-described embodiments, the covering member covering range of the evaporation active region is set to about 50% of the total length of the trough. Since it differs, the arrangement | positioning range of a covering member is good to change in the range of about 20 to 50% of the full length of a trough according to the length of an evaporation active region. Further, the covering member does not necessarily need to cover the entire area of the evaporation active region, and may cover 70% or more, preferably 90% or more of the entire region. The cover member is composed of units divided in the axial direction, and may be attached and detached in units according to a desired arrangement range.
As a member,

また、上述した各実施形態では、被処理物の投入口と排出口をトラフの下側に設けたが、これらの投入口や排出口はトラフの横側に設けることもでき、投入口は覆い部材を貫通させてトラフの上側に設けることもできる。   In each of the above-described embodiments, the workpiece inlet and outlet are provided on the lower side of the trough. However, these inlet and outlet can be provided on the side of the trough, and the inlet is covered. A member can be passed through and provided on the upper side of the trough.

第1の実施形態の連続式乾燥機を示す縦断面図The longitudinal cross-sectional view which shows the continuous-type dryer of 1st Embodiment 図1のII−II線に沿った横断面図Cross-sectional view along line II-II in FIG. 第2の実施形態の連続式乾燥機を示す横断面図Cross-sectional view showing a continuous dryer according to the second embodiment 従来の連続式乾燥機を示す縦断面図Longitudinal sectional view showing a conventional continuous dryer 図4のV−V線に沿った横断面図Cross-sectional view along line VV in FIG.

符号の説明Explanation of symbols

1 トラフ
1a 投入口
1b 排出口
2 撹拌羽根
2a 回転軸
2b 順送りスクリュ
2c 逆送りスクリュ
3 ジャケット
4 切り取り部
5 スクレーパ
6 フード
7 蒸気室
7a 天井
7b 側壁
7c 端壁
8 排気口
9 覆い部材
9a 傾斜面
10 開口
DESCRIPTION OF SYMBOLS 1 Trough 1a Input port 1b Discharge port 2 Stirring blade 2a Rotating shaft 2b Forward feed screw 2c Reverse feed screw 3 Jacket 4 Cutout part 5 Scraper 6 Hood 7 Steam chamber 7a Ceiling 7b Side wall 7c End wall 8 Exhaust port 9 Cover member 9a Inclined surface 10 Opening

Claims (2)

一端側に被処理物の投入口を、他端側にその排出口を設けた横型トラフ内に、互いに逆向きに回転する撹拌羽根が設けられた一対の回転軸を横架して、これらの撹拌羽根の上方の前記トラフ内を蒸気室に形成し、この蒸気室を形成する天井に長さ方向で間隔を開けて複数の排気口を設けて、前記投入口から投入される被処理物を加熱しながら、前記撹拌羽根で撹拌しつつ前記排出口へ移送し、この移送中に前記被処理物に含まれる液体成分を蒸発させて、その蒸気を前記排気口から排気するようにし、前記トラフの投入口側端部から前記液体成分の蒸発活性域の全域またはその大半を含む範囲で、前記各撹拌羽根に近接させてこれらの上側を覆う覆い部材を配設した連続式乾燥機において、前記覆い部材に、前記各撹拌羽根がその回転軸に対して下向きに回転移動する側で、回転軸の軸方向に延びる開口を設け、前記覆い部材の上面に前記開口に向かって下降傾斜する傾斜面を設けたことを特徴とする連続式乾燥機。   A horizontal trough having a workpiece inlet on one end and a discharge outlet on the other end is provided with a pair of rotating shafts provided with stirring blades rotating in opposite directions. The inside of the trough above the stirring blade is formed in a steam chamber, a plurality of exhaust ports are provided at intervals in the length direction on the ceiling forming the steam chamber, and an object to be processed that is input from the input port While heating, stirring with the stirring blade, the liquid is transferred to the discharge port, the liquid component contained in the object to be processed is evaporated during the transfer, and the vapor is exhausted from the exhaust port. In the continuous drier in which a covering member is provided in the range including the whole or most of the evaporation active region of the liquid component from the inlet side end portion thereof and covering the upper side in the vicinity of the stirring blades. Each stirring blade is opposed to its rotating shaft on the cover member. Te on the side where the rotating movement downwards, the opening extending in the axial direction of the rotary shaft is provided, a continuous dryer, characterized by comprising an inclined surface inclined downward toward the opening on the upper surface of the cover member. 前記各撹拌羽根を前記一対の回転軸間の中央側で下向きに回転移動するものとし、前記覆い部材の前記各撹拌羽根が下向きに回転移動する側で設けられる開口を、前記回転軸間の中央側で一つの共通のものとした請求項1に記載の連続式乾燥機。   Each of the stirring blades is rotated downward on the center side between the pair of rotation shafts, and an opening provided on the side of the cover member on which the stirring blades rotate downward is provided at the center between the rotation shafts. The continuous dryer according to claim 1, wherein one is common on the side.
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CN104603565A (en) * 2012-09-11 2015-05-06 月岛机械株式会社 Indirect heating-type rotary drier

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JP5696948B2 (en) * 2012-02-21 2015-04-08 株式会社栗本鐵工所 Conductive heat transfer dryer
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FI124272B (en) * 2012-06-06 2014-05-30 Ccm Power Oy DRYING AND PROCEDURE FOR DRYING MATERIALS

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CN104603565A (en) * 2012-09-11 2015-05-06 月岛机械株式会社 Indirect heating-type rotary drier
CN104603565B (en) * 2012-09-11 2017-05-10 月岛机械株式会社 Indirect heating-type rotary drier

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