JP4261658B2 - Stir processing device - Google Patents

Stir processing device Download PDF

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Publication number
JP4261658B2
JP4261658B2 JP37543098A JP37543098A JP4261658B2 JP 4261658 B2 JP4261658 B2 JP 4261658B2 JP 37543098 A JP37543098 A JP 37543098A JP 37543098 A JP37543098 A JP 37543098A JP 4261658 B2 JP4261658 B2 JP 4261658B2
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gas
pipe
main body
processed
exhaust
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JP37543098A
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JP2000176271A (en
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和夫 大石
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Okawara Mfg Co Ltd
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Okawara Mfg Co Ltd
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【0001】
【発明の属する技術分野】
本発明は、被処理材を常圧若しくは真空で混合又は乾燥等の処理をする攪拌処理装置に関し、より詳細には、逆円錐形状の容器の内周壁近辺にガスを供給して被処理材の周壁への付着を防ぎながら効率よく混合又は乾燥等を行なう攪拌処理装置に関する。
【0002】
【従来の技術】
粉粒体の乾燥装置として、温度を上げられない場合や有機溶剤の除去等では、真空式の攪拌型乾燥装置、例えば特公平1−56808号公報、特公平2−31303号公報等に示されるような装置が用いられている。
この特公平1−56808号公報に示される装置は、縦なが型乾燥機内部に仕込まれた材料を攪拌する攪拌機を設け、必要により処理温度まで加熱するジャケットを外周に設け、縦なが型乾燥機内を減圧する減圧源を設け、不活性ガスを内部に導入するノズルを底部に設け、不活性ガスを加熱する加熱器を設けて構成している。そして、処理する粉粒体を縦なが型乾燥機に仕込み、攪拌機で攪拌しながら、ジャケットに温水又は水蒸気を循環させながら加熱すると共に、真空ポンプを作動させて乾燥機内部を減圧し、さらに加熱した温風、窒素ガス、炭酸ガス等を底部のノズルから導入しながら処理している。これにより、少量の残存有機溶剤を含む粉粒体の有機溶剤の残存量を、食品添加物等の規制値以下に除去することができる。
【0003】
また、後者の特公平2−31303号公報に示される装置は、装置の本体を竪型円錐形状とし、内部に容器の上ほど羽根の幅が広い攪拌翼を容器内壁に近接して設け、さらに熱媒体を流して容器内を加熱するジャケットを外周に設け、内部を減圧する真空発生源を設け、攪拌翼の位置を上下に変更可能に構成している。そして、乾燥機を所要の温度に加熱しておき、原料を投入した後、減圧して所定時間攪拌混合しながら乾燥する。これにより、加熱壁面への材料の付着防止が図れ、半径方向の混合が促進され、付着性の強いものでも処理できる。
【0004】
【発明が解決しようとする課題】
上述の特公平1−56808号公報に開示された装置は、攪拌機で粉粒体を攪拌するが、逆円錐形状に形成していることから、流動の悪い粉粒体では入替えが悪く、滞留する。また、攪拌により粉粒体に剪断力がかかり、形状変化等の物性が変化することがあった。また、特公平2−31303号公報に開示された装置でも、特公平1−56808号公報に示された装置と同様に、流動の悪い粉粒体では、滞留が生じ、材料に対して剪断力がかかって形状変化等の物性が変化することがあった。本発明者は上述した課題に対処して創案したものであって、種々逆円錐形状の攪拌しながら混合又は乾燥処理する装置について研究し、容器内の滞留し易いところにガスを噴出させることにより、粉粒体の内壁面での滞留を防ぎ、攪拌効果を高めると共に、材料に対する剪断力を最小限に抑えることができることを究明した。
【0005】
本発明の目的とする処は、粉粒体(被処理材ともいう)の容器内壁面への付着防止を図り、粉粒体の剪断による変形を最小限に抑え、混合または乾燥を効率よく行う攪拌処理装置を提供することにある。
【0006】
【課題を解決するための手段】
そして、上記目的を達成するための手段としての本発明の請求項1の攪拌処理装置は、被処理材を収容する容器本体と、該容器本体内に攪拌機構を設けて被処理材を攪拌し、該容器本体下部に取出機を設けて攪拌した被処理材を取り出し、該容器本体から排気する排気装置を設けてなる攪拌処理装置であって、前記容器本体にガスを供給するガス供給配管を設け、前記攪拌機構には中空のガス通路を設けてガス供給配管に接続するとともに、少なくとも前記容器本体の周壁近辺に位置する前記攪拌機構の半径方向に伸ばしたアーム先端又は該アーム先端に連結した連結アーム周面にガス噴射孔を設け、ガス通路を通してガスを前記ガス噴射孔から前記容器本体の周壁部に供給して被処理材を処理することを特徴とする。
【0007】
請求項2の攪拌処理装置は、請求項1の攪拌処理装置において、前記容器本体の下部にガス噴出孔を設けて構成した。請求項3の攪拌処理装置は、請求項1又は2の攪拌処理装置において、前記容器本体に熱媒体供給配管に接続してジャケットを設け、前記ガス供給配管を不活性ガス供給管に連通し、前記容器本体に前記取出機及び前記攪拌機構を気密に設け、被処理材を混合又は乾燥する。請求項4の攪拌処理装置は、請求項1〜3の攪拌処理装置において、前記排気装置を真空ポンプとして、真空で処理する構成とした。
【0008】
本発明における攪拌処理装置は、混合操作、乾燥操作の他、加熱、冷却、熱処理、殺菌、殺卵、反応、精製等の操作に使用することができる。本発明において処理される被処理材は、いわゆる粉粒体のみでなく、片状、葉状等各種の形状のものを含み、用途等から例示すれば、電子材料、セラミックス、磁性材料、炭化珪素、醗酵促進剤、漢方薬、調味料、飼料、樹脂パウダー、樹脂ペレット、医薬品、セルローズ、動植物性残渣、スターチ類、菓子原料、香辛料、わかめ、健康食品、無機系塩化物等があげられる。
【0009】
【発明の実施の形態】
以下、添付図面を参照しながら、本発明を具体化した実施の形態について説明する。ここに、図1〜図3は本発明の一実施態様を示し、図1は本発明に係る攪拌処理装置の要部の構成を示す模式図、図2は攪拌処理装置の後部の構成を示す模式図、図3、図4は攪拌機構を説明する図である。
【0010】
本実施態様の攪拌処理装置は、粉粒体等の被処理材を処理する逆円錐形状の容器本体1と、容器本体1内に設けられて被処理材を攪拌する攪拌機2と、攪拌機2を駆動する駆動モータ16と、処理した被処理材を取り出すための容器本体1の下部に設けられた取出機3と、容器本体1にガスを供給するガス供給配管4と、容器本体1から排気する排気装置5とを備える。容器本体1と排気装置5を排気管6で接続し、排気管6に排気から固体を除く分離装置7とさらに排気を処理する排気処理装置8を設け、容器本体1の外周に加熱又は冷却して処理するように熱媒体を流すジャケット9を設け、攪拌機2のアーム18の先端部には被処理材の滞留を防ぐようにガスを噴出するガス噴射孔10を設けている。
【0011】
容器本体1は逆円錐形状に配置され、下部の小径側に製品取出口を形成して取出機3を設け、上部は蓋で気密に閉鎖できるようにし、周囲にジャケット9を設けている。容器本体1の上部には密閉可能に材料投入口11を設け、材料を投入して密閉して処理できるようにしている。また上部に排気管6を接続して噴出ガスを排出したり雰囲気を排出して減圧するようにしている。さらに、容器本体1の上部にはバイパス配管12を設け、排気を排気処理装置8に直接送るようにしている。容器本体1の下部にガスを噴射するガス噴出孔13を設け、ガス噴出孔13とガス供給管4とをガス配管14により連通し、ガス配管14にバルブ15を設けて容器本体1内へのガスの供給を調節し、下部に溜まる材料をこのガスの供給で流動させるようにしている。取出機3は、容器本体1を真空にできるように気密にできる真空弁、ロータリバルブ、バタフライバルブ等を使用する。そして、容器本体1に供給した被処理材は攪拌機2により攪拌しながら処理する。
【0012】
攪拌機2は攪拌機構の従動部で、外部に設置された駆動モータ16に連結された取付軸17が容器本体1の中心部を垂下し、取付軸17から内壁に延びて放射状にアーム18が配置されている。図3に示すように、攪拌機2の取付軸17及びアーム18は中空に形成されて中空部が連通し、中空部にガスが流れるようにガス通路を形成している。アーム18は、その先端には中空部に連通してガス噴射孔10が設けられている。また、アーム18は上方から順次18a,18b,18c,18e,18fから構成され、その長さが容器本体1の内壁に近接するように上方に取り付けられたものほど長く形成されると共に、上下方向に隣接して取り付けられたアームの間隔は上方程大きくされている。さらに、アーム18の断面寸法も下方に配置されたものは小さく、18fは18aより小さい断面積に形成されている。このように構成することにより、被処理材の処理の効率を向上させ、剪断力の作用を軽減している。攪拌機2を回転駆動する駆動モータ16は、容器本体1の外部に設置され、変減速して速度調節可能にしている。取付軸17は気密を確保して蓋に取り付けられている。そして、取付軸17にガス供給配管4が接続し、中空のガス通路にガスが供給される。
【0013】
ガス供給配管4は、ガスの供給を調節する調節弁20が設けられ、図示しない不活性ガス供給源に連通した不活性ガス配管21、図示しないエアー供給源に連通したエアー配管22、真空ポンプ5に連通した循環配管23に接続している。各配管21、22、23にはそれぞれオンーオフする遮断弁24、25、26が設けられると共に、不活性ガス配管21及びエアー配管22にはそれぞれ調圧弁27、28が設けられており、各ガスは独立に又は混合されて容器本体1に供給される。各配管21、22、23には、必要ならば加熱装置、冷却装置等を設け、所要温度にしたガスを容器本体1に供給するようにしてもよい。被処理材は、容器本体1内で常圧又は真空で、攪拌機2のガス噴射孔10及び/又は容器本体1の下部に設けたガス噴出孔13から噴出されたガスと攪拌機2で攪拌流動されながら乾燥、混合等の処理がなされる。処理が終了したら、容器本体1の下部(円錐頂部)に設けられた取出機3を開口させて製品を取り出す。容器本体1の下部に設けられた取出機3の開閉は、エアーシリンダに圧縮エアーを流して行なうか、駆動モータにより行なうか、手動バルブによる行なう等適宜行なうことができる。
【0014】
容器本体1に設けられたジャケット9は上部連結管31及び下部連結管32に接続していると共に、蓋には蓋上部連結管33及び蓋下部連結管34が接続している。蓋上部連結管33は上部連結管31から分枝し、上部連結管31を介して蒸気配管35及び温水出口管36に連通し、蒸気配管35に安全弁37を設け、水蒸気圧力が過剰になるのを防止している。また、蓋下部連結管34は下部連結管32から分枝し、下部連結管32を介して温水配管38及び蒸気ドレン管39に連結している。容器本体1の処理温度はジャケット9に熱媒体を上部連結管31と蓋上部連結管33又は下部連結管32と蓋下部連結管34に流すことにより行なう。熱媒体として水蒸気を用いる場合は、水蒸気配管35から上部連結管31、蓋上部連結管33へ水蒸気を供給し、下部連結管32、蓋下部連結管34を経て蒸気ドレン管39から蒸気ドレンとして排出する。熱媒体として温水を用いる場合は、下部連結管32、蓋下部連結管34から温水を供給し、上部連結管31、蓋上部連結管33から排温水として排出する。また、上部連結管31は分離装置7の加熱装置の上部に連結した分離機上部連結管40と接続し、同様に、下部連結管32は分離装置7の加熱装置の下部に連結した分離機下部連結管41と接続している。容器本体1内で被処理材は、常圧又は真空で、ジャケット9、蓋に熱媒体を流して所定の温度に保持されて、攪拌機2のガス噴射孔10及び/又は容器本体1の下部に設けたガス噴出孔13から噴出されたガスと攪拌機2で攪拌流動されながら乾燥、混合等の処理がなされる。ガス供給配管4から供給され、容器本体1内に噴射されたガスは排気装置5に吸引されて上部の排気口から排気管6を通って排出される。
【0015】
排気装置5は、容器本体1を常圧で操作するにはファンが用いられ、真空で処理する場合には真空ポンプ等を用いる。本実施例では、容器本体1内を真空に減圧できるように、真空ポンプを用いている。排気管6には、容器本体1から排気したガスを処理するように分離装置7、排気処理装置8を設けている。分離装置7は、排気に同伴してくる固体を除去する装置で、形式等は特に制限されず公知の分離装置を使用することができ、乾式ではサイクロン、バグフィルター等が排水処理等が不要なので好ましい。本実施例の分離装置7は、バグフィルターを用いて有機溶剤の凝縮を防ぐために加熱するように熱媒体として温水又は水蒸気を流せる構造にしている。分離装置7で固体分を除去された排気は、凝縮性の有機溶剤等を含む場合は排気処理装置8で凝縮成分を凝縮除去して清浄にされて排気装置5により放出される。または、不活性ガス等を使用している場合で、廃棄するのがコストアップになる場合などでは循環使用するように排気装置5の排出側の排気管6から循環配管23を分枝し、循環配管23を供給配管4に連結している。排気管6、循環配管23にはそれぞれ遮断弁44、45設けて、循環を調整できるようにしている。排気処理装置8は、コンデンサで構成し、排気中の有機溶剤等の凝縮性の成分を除去して清浄な排気を排出するようにしている。
【0016】
排気を処理する排気処理装置8は、冷却水配管46、冷却排水管47が連結され、冷却水配管46から冷却水を流して冷却し、凝縮成分を凝縮分離し、冷却に使用して温度上昇した冷却水は冷却排水管47から排出する。排気処理装置8で排気から凝縮分離された液体を溜めるドレンタンク48が設けられ、凝縮液を一時貯留するようにしている。ドレンタンク48は冷却水配管46から分枝した冷水配管46aが連結し、使用した冷却水を排水する排水管47aが連結している。排水管47aは冷却排水管47に連結し、冷却排水管47から排水する。冷却に使用した冷却水は、冷却排水管47に冷却装置を設け、冷却して再度使用してもよいし、廃棄してもよい。
【0017】
以下に、上記のように構成した攪拌処理装置を用いて水蒸気加熱で真空乾燥する運転方法について説明する。先ず、容器本体1、分離機7を加熱する水蒸気配管の弁を開き、水蒸気配管35から上部連結管31、蓋上部連結管33、分離機上部連結管40へ水蒸気を供給し、容器本体1内を所要の温度に予熱し、予熱に使用した水蒸気は下部連結管32を経て蒸気ドレンとして排出する。また、排気処理装置8では、その冷却水配管46に冷却水を供給して冷却を開始し、使用した冷却水は冷却排水管47から排出する。
【0018】
次いで、料供給口11から被処理材を材容器本体1内に導入して密閉した後、駆動モータ16を運転して攪拌機2を作動すると共に、ガス供給管4の弁20、不活性ガス配管21の弁24、ガス管14の弁15を開いて、ガスとして不活性の窒素ガスをガス噴射孔10、ガス噴出孔13から供給し、排気装置5を運転して容器本体1を減圧しながら処理する。排気装置5に吸引された排気は分離機7を通過するとき、粒状成分が除去される。さらに、排気は排気処理装置8でその凝縮成分が凝縮除去され、清浄にされて排気装置5を経て排出される。
【0019】
所定時間真空乾燥を行なうか、測定装置による測定値が所定の値に達したら、不活性ガスの供給を減らすか排気装置5の排気量を増やして、低圧で処理する。処理が終了したら、排気装置5を止め、容器本体1内を不活性ガスで充填して常圧にし、ガスの供給、水蒸気の供給、攪拌機2の運転、分離機7、排気処理装置8の運転を止め、冷却するか又は冷却せずに取出機3を運転して被処理材を乾燥処理して得た製品を取り出す。その後、前述のようにして次の被処理材を処理する操作を繰り返す。
【0020】
上記のように構成してなる攪拌処理装置によれば、攪拌機2のガス噴射孔10、容器本体1の下部のガス噴出孔13から不活性ガスを供給して、攪拌機2とこの供給ガスとで被処理材を攪拌するから、良く流動化でき、被処理材にかかる剪断力を減らすことができるという特有の効果が得られる。
【0021】
なお、本発明は、上述した実施態様に限定されるものでなく、本発明の主旨を変更しない範囲内で変形実施できるものを含む。因みに、上述においては、攪拌機を攪拌アームが半径方向に放射状に伸びた例で説明したが、図4に示すように、取付軸17から半径方向にアーム18a,18bを放射状に伸ばし、アーム18a,18bに中空の連結アーム50,50を取付け、これらの中空部を連通してガス流路を形成すると共に、連結アーム50の周面にガス流路に連通して複数個のガス噴孔51を設けるようにしてもよい。また、真空乾燥を不活性ガスとして窒素ガスを用いて、常時流している例で説明したが、被処理材への剪断力の影響が減った時点で止めたり、不活性ガスによる乾燥を断続的に行なうように止めたり、初めは空気を流し、仕上げ乾燥として不活性ガスを供給す等任意の工程で行なってよい。また、調節装置の説明を省略したが、所要の個所に測定装置、調節装置を設け、各種の量を調節できることは勿論である。さらに、排気処理の構成を乾式分離機とコンデンサの例で示したが、他の処理方法で構成してもよい。供給ジャケットに加熱媒体を供給する例で示したが、冷却を必要とする場合には冷却媒体を使用すればよい。
【0022】
【発明の効果】
逆円錐形状の容器本体内の攪拌機構から被処理材中にガスを噴出するので、容器本体の内壁面での被処理材の付着を防止することができ、被処理材の流動を良くすることができる結果、被処理材に作用する剪断力を減らすことができ、変形を防ぐことができ、よく混合することができる。混合が良くなることから、熱伝達率を大きくできる。さらに、ガスを供給することから、乾燥を良好にでき、溶媒を除去するものでは製品中に残る溶媒量も減らすことができる。
【0023】
請求項2の攪拌処理装置によれば、容器本体の下部にガス噴出孔を設けて混合するので、容器本体の下部に滞留する被処理材を一層よく流動させ、混合等の処理を効率良くすることができる。請求項3の攪拌処理装置によれば、溶剤の漏れ等をなくして被処理材を所要の雰囲気で処理でき、被処理材の品質の劣化を生じさせることなく、安全に処理することができる。請求項4の攪拌処理装置によれば、請求項4の攪拌処理装置は、真空で処理することができ、水分や有機溶剤の残存濃度を低濃度に効率よく除去することができる。
【図面の簡単な説明】
【0024】
【図1】 本発明に係る攪拌処理装置の要部の構成を示す模式図である。
【図2】 攪拌処理装置の後部の構成を示す模式図である。
【図3】 攪拌機を説明する図で、(a)は一部を破断した要部の正面図、(b)は(a)のB−B線断面図である。
【図4】 攪拌機の他の例を説明する図で、(a)は要部の正面図、(b)は下面図である。
【符号の説明】
【0025】
1:容器本体 2:攪拌機 3:取出機
4:ガス供給配管 5:排気装置 6:排気管
7:分離装置 8:排気処理装置 9:ジャケット
10:ガス噴射孔 11:材料投入口 12:バイパス配管
13:ガス噴出孔 14:ガス配管 15:バルブ
16:駆動モータ 17:取付軸 18:アーム
20:調節弁 21:不活性ガス配管
22:エアー配管 23:循環配管 24,25,26:遮断弁
27,28:調節弁 31:上部連結管 32:下部連結管
33:蓋上部連結管 34:蓋下部連結管 35:蒸気配管
36:温水出口 37:安全弁 38:温水配管
39:蒸気ドレン 40:分離機上部連結管 41:分離機下部連結管
44,45:遮断弁 46:冷却水配管 47:冷却排水管
48:ドレンタンク
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an agitation processing apparatus that performs processing such as mixing or drying of a material to be processed at normal pressure or vacuum, and more specifically, supplying a gas to the vicinity of an inner peripheral wall of an inverted conical container. The present invention relates to an agitation processing apparatus that performs efficient mixing or drying while preventing adhesion to a peripheral wall.
[0002]
[Prior art]
In the case where the temperature cannot be increased or the organic solvent is removed as a drying apparatus for the powder and granular material, a vacuum type stirring type drying apparatus, for example, Japanese Patent Publication No. 1-56808, Japanese Patent Publication No. 2-331303, etc. Such a device is used.
The apparatus disclosed in Japanese Patent Publication No. 1-56808 is provided with a stirrer that stirs the material charged in the vertical mold dryer and, if necessary, a jacket that heats up to the processing temperature, on the outer periphery. A decompression source for decompressing the inside of the dryer is provided, a nozzle for introducing an inert gas into the interior is provided at the bottom, and a heater for heating the inert gas is provided. Then, the powder particles to be treated are charged into a vertical mold dryer, heated while circulating hot water or water vapor in the jacket while stirring with a stirrer, and the inside of the dryer is depressurized by operating a vacuum pump, Heated hot air, nitrogen gas, carbon dioxide gas, etc. are treated while being introduced from the bottom nozzle. Thereby, the residual quantity of the organic solvent of the granular material containing a small amount of residual organic solvent can be removed below the regulation value of food additives and the like.
[0003]
Further, the apparatus shown in the latter Japanese Examined Patent Publication No. 2-331303 has a main body of a bowl-shaped conical shape, and a stirring blade whose blade width is wider toward the top of the container is provided close to the inner wall of the container. A jacket for flowing a heat medium to heat the inside of the container is provided on the outer periphery, a vacuum generation source for reducing the pressure inside is provided, and the position of the stirring blade can be changed up and down. Then, the dryer is heated to a required temperature, and after the raw materials are charged, the pressure is reduced and drying is performed while stirring and mixing for a predetermined time. Thereby, the adhesion of the material to the heating wall surface can be prevented, the mixing in the radial direction is promoted, and even a highly adherent material can be processed.
[0004]
[Problems to be solved by the invention]
The apparatus disclosed in the above Japanese Patent Publication No. 1-56808 stirs the powder with a stirrer, but since it is formed in an inverted cone shape, the powder with poor flow is poorly replaced and stays. . In addition, a shearing force is applied to the granular material by stirring, and physical properties such as a shape change sometimes change. Further, even in the apparatus disclosed in Japanese Patent Publication No. 2-331303, in the same manner as the apparatus disclosed in Japanese Patent Publication No. 1-56808, in a granular material having poor flow, stagnation occurs and shear force is applied to the material. In some cases, the physical properties such as the shape change may change due to the deformation. The inventor of the present invention has been devised to cope with the above-described problems, and has studied a device for mixing or drying while stirring various inverted conical shapes, and by ejecting gas to a place where it tends to stay in a container. The inventors have found that it is possible to prevent the particles from staying on the inner wall surface, to increase the stirring effect, and to minimize the shearing force on the material.
[0005]
The object of the present invention is to prevent adhesion of powder particles (also called materials to be treated) to the inner wall surface of the container, minimize deformation due to shearing of the powder particles, and perform mixing or drying efficiently. The object is to provide an agitation processing apparatus.
[0006]
[Means for Solving the Problems]
The stirrer according to claim 1 of the present invention as means for achieving the above object comprises a container main body for storing the material to be processed, and an agitating mechanism provided in the container main body for stirring the material to be processed. An agitation processing apparatus provided with an exhaust device for taking out a material to be agitated by providing a take-out device at the lower part of the container body and exhausting the material from the container body, wherein a gas supply pipe for supplying gas to the container body is provided. The stirring mechanism is provided with a hollow gas passage and connected to the gas supply pipe, and at least the arm tip extended in the radial direction of the stirring mechanism located in the vicinity of the peripheral wall of the container body or connected to the arm tip A gas injection hole is provided in the peripheral surface of the connecting arm, and a material to be processed is processed by supplying gas through the gas passage from the gas injection hole to the peripheral wall portion of the container body.
[0007]
According to a second aspect of the present invention, there is provided the agitation processing apparatus according to the first aspect, wherein a gas ejection hole is provided in a lower portion of the container body. The stirring treatment apparatus according to claim 3 is the stirring treatment apparatus according to claim 1 or 2, wherein the container body is provided with a jacket connected to a heat medium supply pipe, and the gas supply pipe communicates with an inert gas supply pipe. The unloader and the stirring mechanism are provided in an airtight manner in the container body, and the material to be treated is mixed or dried. According to a fourth aspect of the present invention, there is provided the agitation processing apparatus according to the first to third aspects, wherein the evacuation device is a vacuum pump for processing in vacuum.
[0008]
The stirrer in the present invention can be used for operations such as heating, cooling, heat treatment, sterilization, egg killing, reaction, purification, etc. in addition to mixing operation and drying operation. The material to be processed in the present invention includes not only so-called powder particles but also various shapes such as flakes and leaves, and examples of applications include electronic materials, ceramics, magnetic materials, silicon carbide, Examples include fermentation promoters, traditional Chinese medicines, seasonings, feeds, resin powders, resin pellets, pharmaceuticals, cellulose, animal and vegetable residues, starches, confectionery ingredients, spices, wakame, health foods, and inorganic chlorides.
[0009]
DETAILED DESCRIPTION OF THE INVENTION
DESCRIPTION OF EMBODIMENTS Hereinafter, embodiments of the present invention will be described with reference to the accompanying drawings. 1 to 3 show one embodiment of the present invention, FIG. 1 is a schematic diagram showing the configuration of the main part of the stirring treatment apparatus according to the present invention, and FIG. 2 shows the configuration of the rear part of the stirring processing apparatus. FIG. 3 and FIG. 4 are diagrams for explaining the stirring mechanism.
[0010]
An agitation processing apparatus according to this embodiment includes an inverted conical container body 1 for processing a material to be processed such as a granular material, an agitator 2 provided in the container body 1 for agitating the material to be processed, and an agitator 2. A drive motor 16 for driving, an unloader 3 provided at the lower part of the container body 1 for taking out the processed material, a gas supply pipe 4 for supplying gas to the container body 1, and exhausting from the container body 1 and an exhaust system 5. The container body 1 and the exhaust device 5 are connected by an exhaust pipe 6, and a separation device 7 that removes solids from the exhaust gas and an exhaust treatment device 8 that processes the exhaust gas are provided in the exhaust pipe 6, and the outer periphery of the container body 1 is heated or cooled. A jacket 9 through which a heat medium flows is provided so as to process the gas, and a gas injection hole 10 for jetting gas is provided at the tip of the arm 18 of the stirrer 2 so as to prevent the material to be processed from staying.
[0011]
The container body 1 is arranged in an inverted conical shape, a product outlet is formed on the lower diameter side of the lower portion, the take-out machine 3 is provided, the upper portion can be hermetically closed with a lid, and a jacket 9 is provided around. A material charging port 11 is provided at the upper part of the container body 1 so as to be able to be sealed, and the material is charged so as to be sealed. Further, an exhaust pipe 6 is connected to the upper part to discharge the jet gas or discharge the atmosphere to reduce the pressure. Further, a bypass pipe 12 is provided in the upper part of the container body 1 so that the exhaust gas is sent directly to the exhaust treatment device 8. A gas ejection hole 13 for injecting gas is provided at the lower part of the container body 1, the gas ejection hole 13 and the gas supply pipe 4 are communicated with each other by a gas pipe 14, and a valve 15 is provided in the gas pipe 14 to supply the gas into the container body 1. The gas supply is adjusted, and the material accumulated in the lower part is caused to flow by this gas supply. The unloader 3 uses a vacuum valve, a rotary valve, a butterfly valve or the like that can be hermetically sealed so that the container body 1 can be evacuated. And the to-be-processed material supplied to the container main body 1 processes, stirring with the stirrer 2. FIG.
[0012]
The stirrer 2 is a follower of a stirring mechanism, and an attachment shaft 17 connected to a drive motor 16 installed outside hangs down from the central portion of the container body 1 and extends radially from the attachment shaft 17 to the inner wall. Has been. As shown in FIG. 3, the mounting shaft 17 and the arm 18 of the stirrer 2 are formed in a hollow shape so that the hollow portion communicates with each other and a gas passage is formed so that gas flows through the hollow portion. The arm 18 is provided with a gas injection hole 10 at the tip thereof so as to communicate with the hollow portion. The arm 18 is composed of 18a, 18b, 18c, 18e, and 18f sequentially from above, and the longer the arm 18 is attached so as to be close to the inner wall of the container body 1, the longer the upper and lower directions. The distance between the arms attached adjacent to each other is increased upward. Further, the cross-sectional dimension of the arm 18 is small, and 18f is formed to have a smaller cross-sectional area than 18a. By comprising in this way, the efficiency of the process of a to-be-processed material is improved and the effect | action of a shear force is reduced. A drive motor 16 that rotationally drives the stirrer 2 is installed outside the container body 1 and is variable in speed so that the speed can be adjusted. The mounting shaft 17 is attached to the lid while ensuring airtightness. The gas supply pipe 4 is connected to the mounting shaft 17 and gas is supplied to the hollow gas passage.
[0013]
The gas supply pipe 4 is provided with a control valve 20 that regulates the supply of gas, an inert gas pipe 21 that communicates with an inert gas supply source (not shown), an air pipe 22 that communicates with an air supply source (not shown), and a vacuum pump 5. It connects to the circulation piping 23 connected to. The pipes 21, 22 and 23 are provided with shut-off valves 24, 25 and 26 which are turned on and off, respectively, and the inert gas pipe 21 and the air pipe 22 are provided with pressure regulating valves 27 and 28, respectively. The container body 1 is supplied independently or mixed. Each pipe 21, 22, 23 may be provided with a heating device, a cooling device, or the like, if necessary, so that a gas having a required temperature is supplied to the container body 1. The material to be treated is stirred and flowed by the stirrer 2 with the gas ejected from the gas injection hole 10 of the stirrer 2 and / or the gas ejection hole 13 provided in the lower part of the container main body 1 at normal pressure or vacuum in the container main body 1. However, drying, mixing, etc. are performed. When the processing is completed, the unloader 3 provided at the lower part (conical top) of the container body 1 is opened to take out the product. The unloader 3 provided at the lower part of the container body 1 can be appropriately opened and closed by flowing compressed air through an air cylinder, by a drive motor, or by a manual valve.
[0014]
The jacket 9 provided in the container body 1 is connected to the upper connecting pipe 31 and the lower connecting pipe 32, and the lid upper connecting pipe 33 and the lid lower connecting pipe 34 are connected to the lid. The lid upper connecting pipe 33 branches off from the upper connecting pipe 31, communicates with the steam pipe 35 and the hot water outlet pipe 36 via the upper connecting pipe 31, and a safety valve 37 is provided in the steam pipe 35, so that the water vapor pressure becomes excessive. Is preventing. The lid lower connecting pipe 34 branches from the lower connecting pipe 32 and is connected to the hot water pipe 38 and the steam drain pipe 39 through the lower connecting pipe 32. The processing temperature of the container body 1 is determined by flowing a heat medium through the upper connection pipe 31 and the upper lid connection pipe 33 or the lower connection pipe 32 and the lower lid connection pipe 34 in the jacket 9. When water vapor is used as the heat medium, water vapor is supplied from the water vapor pipe 35 to the upper connecting pipe 31 and the lid upper connecting pipe 33, and is discharged from the steam drain pipe 39 through the lower connecting pipe 32 and the lid lower connecting pipe 34 as steam drain. To do. When hot water is used as the heat medium, hot water is supplied from the lower connecting pipe 32 and the lid lower connecting pipe 34 and discharged from the upper connecting pipe 31 and the lid upper connecting pipe 33 as exhaust hot water. Further, the upper connecting pipe 31 is connected to the separator upper connecting pipe 40 connected to the upper part of the heating device of the separator 7. Similarly, the lower connecting pipe 32 is connected to the lower part of the heating device of the separator 7. The connecting pipe 41 is connected. In the container main body 1, the material to be treated is maintained at a predetermined temperature by flowing a heat medium through the jacket 9 and the lid at normal pressure or vacuum, and the gas injection hole 10 of the stirrer 2 and / or the lower part of the container main body 1. Processing such as drying and mixing is performed while stirring and flowing with the gas ejected from the gas ejection hole 13 provided and the agitator 2. The gas supplied from the gas supply pipe 4 and injected into the container body 1 is sucked into the exhaust device 5 and discharged from the upper exhaust port through the exhaust pipe 6.
[0015]
The exhaust device 5 uses a fan to operate the container body 1 at normal pressure, and uses a vacuum pump or the like when processing in vacuum. In this embodiment, a vacuum pump is used so that the inside of the container body 1 can be decompressed to a vacuum. The exhaust pipe 6 is provided with a separation device 7 and an exhaust treatment device 8 so as to process the gas exhausted from the container body 1. Separation device 7 is a device that removes solids accompanying the exhaust gas, and the type and the like are not particularly limited, and a known separation device can be used. In a dry type, a cyclone, bag filter, etc. do not require wastewater treatment. preferable. The separation device 7 of the present embodiment has a structure in which warm water or water vapor can flow as a heat medium so as to heat the organic solvent using a bag filter in order to prevent condensation. When the exhaust gas from which the solid content has been removed by the separation device 7 contains a condensable organic solvent or the like, the exhaust gas is condensed and removed by the exhaust treatment device 8 and discharged by the exhaust device 5. Alternatively, when an inert gas or the like is used and the cost increases when it is discarded, the circulation pipe 23 is branched from the exhaust pipe 6 on the discharge side of the exhaust device 5 so as to be circulated. The pipe 23 is connected to the supply pipe 4. The exhaust pipe 6 and the circulation pipe 23 are provided with shut-off valves 44 and 45, respectively, so that the circulation can be adjusted. The exhaust treatment device 8 is composed of a condenser, and removes a condensable component such as an organic solvent in the exhaust to discharge clean exhaust.
[0016]
The exhaust gas treatment device 8 for treating the exhaust gas is connected to a cooling water pipe 46 and a cooling drain pipe 47, is cooled by flowing cooling water from the cooling water pipe 46, condenses and separates condensed components, and is used for cooling to increase the temperature. The cooled water is discharged from the cooling drain pipe 47. A drain tank 48 for storing the liquid condensed and separated from the exhaust gas in the exhaust treatment device 8 is provided to temporarily store the condensate. The drain tank 48 is connected to a cold water pipe 46a branched from the cooling water pipe 46, and a drain pipe 47a for draining the used cooling water. The drain pipe 47 a is connected to the cooling drain pipe 47 and drains from the cooling drain pipe 47. The cooling water used for cooling may be used again after cooling by providing a cooling device in the cooling drain pipe 47 or may be discarded.
[0017]
Below, the driving | running method which vacuum-drys by steam heating using the stirring processing apparatus comprised as mentioned above is demonstrated. First, the valve of the steam pipe for heating the container main body 1 and the separator 7 is opened, and water vapor is supplied from the steam pipe 35 to the upper connecting pipe 31, the lid upper connecting pipe 33, and the separator upper connecting pipe 40. Is preheated to a required temperature, and the steam used for the preheating is discharged through the lower connecting pipe 32 as a steam drain. In the exhaust treatment device 8, cooling water is supplied to the cooling water pipe 46 to start cooling, and the used cooling water is discharged from the cooling drain pipe 47.
[0018]
Next, after the material to be treated is introduced into the material container body 1 from the material supply port 11 and sealed, the drive motor 16 is operated to operate the stirrer 2, and the valve 20 of the gas supply pipe 4, the inert gas pipe. 21 and the valve 15 of the gas pipe 14 are opened, inert nitrogen gas is supplied as gas from the gas injection hole 10 and the gas injection hole 13, and the exhaust device 5 is operated to decompress the container body 1. To process. When the exhaust gas sucked into the exhaust device 5 passes through the separator 7, particulate components are removed. Further, the exhaust component is condensed and removed by the exhaust treatment device 8, cleaned, and exhausted through the exhaust device 5.
[0019]
When the vacuum drying is performed for a predetermined time or when the measurement value by the measuring device reaches a predetermined value, the supply of the inert gas is reduced or the exhaust amount of the exhaust device 5 is increased, and processing is performed at a low pressure. When the treatment is completed, the exhaust device 5 is stopped, the inside of the container body 1 is filled with an inert gas to normal pressure, the gas is supplied, the water vapor is supplied, the stirrer 2 is operated, the separator 7 and the exhaust treatment device 8 are operated. The product obtained by drying the material to be treated by operating the unloader 3 with or without cooling, and taking out the product. Thereafter, the operation for processing the next material to be processed is repeated as described above.
[0020]
According to the agitation processing apparatus configured as described above, an inert gas is supplied from the gas injection hole 10 of the agitator 2 and the gas injection hole 13 at the lower part of the container body 1, and the agitator 2 and the supply gas are used. Since the material to be treated is agitated, a specific effect can be obtained that the material can be fluidized well and the shearing force applied to the material to be treated can be reduced.
[0021]
In addition, this invention is not limited to the embodiment mentioned above, The thing which can be deform | transformed within the range which does not change the main point of this invention is included. Incidentally, in the above description, the stirrer has been described as an example in which the stirring arm radially extends in the radial direction. However, as shown in FIG. 4, the arms 18a and 18b are radially extended from the mounting shaft 17 in the radial direction. The hollow connecting arms 50 and 50 are attached to 18b, and these hollow portions are connected to form a gas flow path, and the peripheral surface of the connecting arm 50 is connected to the gas flow path to form a plurality of gas injection holes 51. You may make it provide. In addition, although vacuum drying is described as an example in which nitrogen gas is always used as an inert gas, it has been explained, but when the influence of shearing force on the material to be processed is reduced, drying by an inert gas is intermittently performed. It may be carried out in an arbitrary process such as stopping in the first step, or initially flowing air and supplying an inert gas as finish drying. Moreover, although explanation of the adjusting device is omitted, it is needless to say that various amounts can be adjusted by providing a measuring device and adjusting device at a required place. Furthermore, although the configuration of the exhaust treatment is shown as an example of the dry separator and the condenser, other treatment methods may be used. Although an example in which a heating medium is supplied to the supply jacket is shown, a cooling medium may be used when cooling is required.
[0022]
【The invention's effect】
Since gas is jetted into the material to be treated from the stirring mechanism in the inverted conical container body, the adhesion of the material to be treated on the inner wall surface of the container body can be prevented, and the flow of the material to be treated is improved. As a result, the shearing force acting on the material to be treated can be reduced, deformation can be prevented, and mixing can be performed well. Since mixing is improved, the heat transfer coefficient can be increased. Further, since the gas is supplied, the drying can be satisfactorily performed, and in the case of removing the solvent, the amount of the solvent remaining in the product can be reduced.
[0023]
According to the agitation processing apparatus of the second aspect, since the gas ejection holes are provided in the lower part of the container main body and mixed, the material to be treated staying in the lower part of the container main body is made to flow more efficiently and the processing such as mixing is made efficient. be able to. According to the agitation processing apparatus of the third aspect, it is possible to process the material to be processed in a required atmosphere without leaking of the solvent and the like, and it is possible to safely process the material without deteriorating the quality of the material to be processed. According to the stirring processing apparatus of claim 4, the stirring processing apparatus of claim 4 can process in vacuum, and can efficiently remove the residual concentration of moisture and organic solvent to a low concentration.
[Brief description of the drawings]
[0024]
FIG. 1 is a schematic diagram showing a configuration of a main part of a stirring treatment apparatus according to the present invention.
FIG. 2 is a schematic view showing a configuration of a rear portion of the stirring processing apparatus.
FIGS. 3A and 3B are diagrams illustrating a stirrer, in which FIG. 3A is a front view of a main part with a part broken away, and FIG. 3B is a cross-sectional view taken along line BB in FIG.
4A and 4B are diagrams for explaining another example of a stirrer, in which FIG. 4A is a front view of a main part, and FIG. 4B is a bottom view.
[Explanation of symbols]
[0025]
1: Container body 2: Stirrer 3: Unloader 4: Gas supply piping 5: Exhaust device 6: Exhaust tube 7: Separation device 8: Exhaust treatment device 9: Jacket 10: Gas injection hole 11: Material inlet 12: Bypass piping 13: Gas ejection hole 14: Gas piping 15: Valve 16: Drive motor 17: Mounting shaft 18: Arm 20: Control valve 21: Inert gas piping 22: Air piping 23: Circulation piping 24, 25, 26: Shut-off valve 27 28: Control valve 31: Upper connecting pipe 32: Lower connecting pipe 33: Upper lid connecting pipe 34: Lower lid connecting pipe 35: Steam pipe 36: Hot water outlet 37: Safety valve 38: Hot water pipe 39: Steam drain 40: Separator Upper connecting pipe 41: Separator lower connecting pipe 44, 45: Shut-off valve 46: Cooling water pipe 47: Cooling drain pipe 48: Drain tank

Claims (4)

被処理材を収容する容器本体と、該容器本体内に攪拌機構を設けて被処理材を攪拌し、該容器本体下部に取出機を設けて攪拌した被処理材を取り出し、該容器本体から排気する排気装置を設けてなる攪拌処理装置であって、前記容器本体にガスを供給するガス供給配管を設け、前記攪拌機構には中空のガス通路を設けてガス供給配管に接続するとともに、少なくとも前記容器本体の周壁近辺に位置する前記攪拌機構の半径方向に伸ばしたアーム先端又は該アーム先端に連結した連結アーム周面にガス噴射孔を設け、ガス通路を通してガスを前記ガス噴射孔から前記容器本体の周壁部に供給して被処理材を処理することを特徴とする攪拌処理装置。A container main body for storing the material to be processed, and a stirring mechanism provided in the container main body to stir the material to be processed, and a take-out processing material was taken out by providing a take-out device at the bottom of the container main body, and exhausted from the container main body a stirring apparatus comprising an exhaust system provided for the gas supply pipe for supplying gas provided in the container main body, as well as connected to a gas supply pipe provided with a hollow gas passage to the stirring mechanism, at least the A gas injection hole is provided in the distal end of the stirring mechanism located in the vicinity of the peripheral wall of the container main body in the radial direction or in the peripheral surface of the connecting arm connected to the front end of the arm , and gas is passed through the gas passage from the gas injection hole to the container main body. An agitation processing apparatus, wherein the material to be processed is processed by being supplied to the peripheral wall portion. 前記容器本体の下部にガス噴出孔を設けた請求項1に記載の攪拌処理装置。 The agitation processing apparatus according to claim 1, wherein a gas ejection hole is provided in a lower portion of the container body. 前記容器本体に熱媒体供給配管に接続してジャケットを設け、前記ガス供給配管を不活性ガス供給管に連通し、前記容器本体に前記取出機及び前記攪拌機構を気密に設け、被処理材を混合又は乾燥する請求項1又は2に記載の攪拌処理装置。The container body is connected to a heat medium supply pipe, a jacket is provided, the gas supply pipe is communicated with an inert gas supply pipe, the unloader and the stirring mechanism are provided in the container body in an airtight manner, and a material to be processed is provided. The agitation processing apparatus according to claim 1 or 2, which is mixed or dried. 前記排気装置を真空ポンプとした請求項1〜3のいずれかに記載の攪拌処理装置。 The stirring treatment apparatus according to claim 1, wherein the exhaust device is a vacuum pump.
JP37543098A 1998-12-14 1998-12-14 Stir processing device Expired - Lifetime JP4261658B2 (en)

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