JP3546840B2 - Filtration and drying equipment - Google Patents

Filtration and drying equipment Download PDF

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Publication number
JP3546840B2
JP3546840B2 JP2000396334A JP2000396334A JP3546840B2 JP 3546840 B2 JP3546840 B2 JP 3546840B2 JP 2000396334 A JP2000396334 A JP 2000396334A JP 2000396334 A JP2000396334 A JP 2000396334A JP 3546840 B2 JP3546840 B2 JP 3546840B2
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Prior art keywords
filtration
drying
chamber
container
cake
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JP2000396334A
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JP2002195747A (en
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賢一 日比
良二 山口
智史 山口
修二 岩崎
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Tsukishima Kikai Co Ltd
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Tsukishima Kikai Co Ltd
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  • Drying Of Solid Materials (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、スラリー状物質のろ過、乾燥を連続して行うことのできるろ過・乾燥装置に関するものであり、特に、ろ過板に付着したケーキの剥離を効率よく行なうことができるろ過・乾燥装置に関するものである。
【0002】
【従来の技術】
食品、化学品、医薬品等の広い産業分野では種々の物質の製造、生成等を行っている。特に、スラリー状物質の生成を行う場合には、ろ過機においてスラリーをろ過してケーキを形成し、多くの場合はケーキ洗浄を行い、不純物を除去後にケーキを乾燥して結晶や粉粒体を得ることが行われているが、各操作毎にろ過槽や乾燥機等を各別に設けることは設備費が嵩むものである。また、ろ過作業が終了した物質をろ過槽から乾燥機に移す場合には、その間に物質のロスを生ずることが多く、作業手間もかかるものであった。
【0003】
特に、高価な薬品の製造や空気に酸化されやすい結晶を扱う場合、上記のようにろ過作業や乾燥作業等を装置を異にして各別に行うことは製品全体の品質並びに収率が下がり、時には結晶が破壊されて品位が落ちる欠点を有していた。
そこで、特公昭46−22201号によって開示されるように一台のろ過兼乾燥装置でろ過、乾燥作業を連続して行うことのできる装置が提供されている。
【0004】
特公昭46−22201号で示されるろ過兼乾燥装置Aは、中部が円筒形、上下を円錐形とし、円筒部内の下端にはろ過板2を取り付けるとともに底部中央端にろ液排出口3を設ける。また、上面の開口1には処理液仕込管10、製品取出口および中央に洗浄水噴出管8を具えた蓋体9を取り付ける。そして、左右の管形機軸6、7によって回転可能に支持されている円筒部機体はジャケット5で取り巻かれて二重壁となっており、ジャケット5内には熱水が供給される。
【0005】
上記のろ過兼乾燥装置Aでろ過作業を行うには、ろ過すべき水溶液を処理液仕込管10から円筒部機内に送り、ろ過板2でろ過処理を行い、ろ液はろ液排出口3を通して外部に排出する。ある時間経過後、ろ過板2上にある程度の厚さのケーキ層が形成されると水溶液の供給を停止するとともに排出口3を閉じ、ジャケット5内に加熱用の熱媒体として熱水を循環させつつ円筒部を一定の方向に連続して回転させる。
【0006】
円筒部内を減圧した状態で円筒部を加熱しつつ管形機軸6、7を中心にして回転させれば、ろ過板2上に形成されたケーキ層は円筒部内を上下あるいは回転方向に循環移動し、ケーキは円筒部の内壁面にぶつかり、また、ケーキ相互の接触により徐々に乾燥されて最終的に結晶あるいは粉粒状物質等の乾燥物が生成される。必要な時間、乾燥処理を行った後、蓋体9を下向きにして開口し、乾燥物を取り出す。
【0007】
【発明が解決しようとする課題】
上記する従来のろ過・乾燥装置において、ろ過後にはろ過板2上にケーキ層が形成され、円筒部を一定の方向に連続して回転させれば、ケーキはろ過板2から振り落とされ、乾燥処理がなされる。
しかし、ろ過後のケーキには液分が残って粘着性を有しているので、円筒部を連続回転させても、ろ過板2に接触している薄い層のケーキはそのままろ過板2上に残り、乾燥してろ過板2に付着した状態となる。
その後に新たな原液スラリーを供給し、連続してろ過、乾燥作業を行なうと、ろ過板2に付着したケーキに更に他のケーキが薄く付着し、徐々にケーキ層が厚くなり、ろ過板2が目詰まり状態を生じて充分なろ過が行なえない事態を生じていた。
【0008】
本発明は、上記する従来技術の問題点に鑑み、ケーキの乾燥に先立ち、ろ過板に対してろ過面裏側からエアーのような圧力気体を供給するブローバック手段を設けることにより、ろ過板からケーキの剥離を行なうようにしたろ過・乾燥装置を提供することを目的とするものである。
【0009】
【課題を解決するための手段】
上記する目的を達成するために本発明装置は、加圧あるいは減圧可能な密閉型容器3の外周をジャケット4で被覆し、容器3内の下方にろ過板5を設置して容器3内をろ過室6と乾燥室7とに分離するとともにろ過室6は、格子状支持板13により複数室15に分割して各分割室15は連絡流路14により連絡可能としたろ過・乾燥槽1により原液スラリーをろ過し、ろ液は排出口11から排出するとともにろ過板5上に形成されたケーキはろ過室6から乾燥室7に向けて排出口11から噴射した圧力気体により剥離し、ろ過・乾燥槽1を回転あるいは反転させ、容器3を加熱しつつケーキを乾燥処理し、乾燥物を生成するようにしたものである。
【0010】
また、本発明装置は、加圧あるいは減圧可能な密閉型容器3の外周をジャケット4で被覆し、容器3内の下方にろ過板5を設置して容器3内をろ過室6と乾燥室7とに分離するとともにろ過室6は、格子状支持板13により独立した複数の分割室15を形成したろ過・乾燥槽1により原液スラリーをろ過し、ろ液は各分割室15に設けた排出口11から排出するとともにろ過板5上に形成されたケーキはろ過室6から乾燥室7に向けて各排出口11から噴射した圧力気体により剥離し、ろ過・乾燥槽1を回転あるいは反転させ、容器3を加熱しつつケーキを乾燥処理し、乾燥物を生成するようにしたものである。
【0011】
更に、本発明装置は、加圧あるいは減圧可能な密閉型容器3の外周をジャケット4で被覆し、容器3内の下方にろ過板5を設置して容器3内をろ過室6と乾燥室7とに分離するとともにろ過室6は、格子状支持板13により複数室15に分割して各分割室15は連絡流路14により連絡可能としたろ過・乾燥槽1により原液スラリーをろ過し、ろ液は排出口11から排出するとともにろ過板5上に形成されたケーキはろ過室6から乾燥室7に向けて排出口11から噴射した圧力気体により剥離し、上下反転させた容器3を加熱しつつ乾燥室7内に設置した攪拌機構25によりケーキを粉砕して乾燥物を生成するようにしたものである。
【0012】
更にまた本発明装置は、加圧あるいは減圧可能な密閉型容器3の外周をジャケット4で被覆し、容器3内の下方にろ過板5を設置して容器3内をろ過室6と乾燥室7とに分離するとともにろ過室6は、格子状支持板13により独立した複数の分割室15を形成したろ過・乾燥槽1により原液スラリーをろ過し、ろ液は各分割室15に設けた排出口11から排出するとともにろ過板5上に形成されたケーキはろ過室6から乾燥室7に向けて各排出口11から噴射した圧力気体により剥離し、上下反転させた容器3を加熱しつつ乾燥室7内に設置した攪拌機構25によりケーキを粉砕して乾燥物を生成するようにしたものである。
【0013】
【発明の実施の形態】
以下、図面に従って、本発明の実施の形態を詳細に説明する。
図1、図2は本発明ろ過・乾燥装置の第一の実施形態を示すものであり、ろ過・乾燥槽1は、円形胴部2の上下面を対称の湾曲面に形成した密閉可能な加圧あるいは減圧型の容器3の外周面をジャケット4で覆った二重壁構造とするとともに容器3内の下方にはろ過板5を設置し、容器3内はろ過室6と乾燥室7とに分離した構造となっている。
【0014】
常態では図1に示すように、ろ過室6は下方に位置し、乾燥室7は上方に位置しており、容器3の両側に突設した回転軸8を架台9上に設けた軸受に回転可能に軸支し、一方の回転軸8を図示しない逆転可能なモータにベルトやチェーン等を介して連結することにより、ろ過・乾燥槽1全体は一方向に連続回転するかあるいは反転可能となっている。
【0015】
図2に示すように容器3の上方位置には原液スラリーの供給口10を設けるとともに図1のように底部中央にはろ液の排出口11を形成し、この排出口11と図示しない吸引ポンプとを排出管12により連結し、ろ過板5でろ過されたろ液は真空吸引するか、または、容器3内を加圧状態に保つことにより排出するようになっている。
【0016】
供給口10は、図示しない原液スラリー槽に配管によって連結してあり、ポンプによって原液スラリーが供給口10を通して容器3内に送り込まれるようになっている。このため、ろ過・乾燥槽1は、常態では乾燥室7が上方に位置し、ろ過室6は下方に位置している。
【0017】
前記のろ過室6内には複数枚の支持板13が設置してある。この支持板13は、積層したケーキの加重に対してろ過板5を下方から支持するとともにブローバックの際に噴射した気体の圧力からろ過板5を保持し、かつ、気体の噴射方向の案内を兼ねている。
【0018】
図3は、ろ過室6の一例を示すものであり、格子状に組み合わせた支持板13の側面および底面をろ過室6内に溶接によって固定し、ろ過室6内を複数に分割する。そして、格子状支持板13の交差した下部は円形あるいは方形状に切り欠いて連絡流路14を形成し、この連絡流路14を通して各分割室15間にろ液や圧力気体等が流通可能となっている。
【0019】
前記したようにろ過室6の中央底部に設けた排出口11は、ろ液を排出するとともにブローバックのための圧力気体の圧入口を兼ねており、排出口11に面して上方に位置する支持板13の下端面には円形あるいは方形状の切り欠きを設けて拡散用空間16が形成してある。
【0020】
図4は、ろ過室6の他の例を示すものであり、格子状支持板13によって区画された各分割室15に面してろ過室6の底部には、前記のように圧力気体の圧入口を兼ねた排出口11をそれぞれ設け、各排出口11は分岐管17によって連結し、一本の排出管12に接続したものである。従って、格子状支持板13の下端面はろ過室6の底面に固定状態となっており、各分割室15は遮断されて独立した状態に形成してある。
【0021】
第一実施形態に示す構成は上記の通りであり、次に原液スラリーのろ過、乾燥作業について説明する。
ろ過・乾燥槽1の上方に向けたスラリー供給口10から容器3内に原液スラリーを供給し、容器3内を加圧あるいは減圧した状態でろ過処理を行い、ろ液はろ液排出口11から排出管12を通して外部に放出する。尚、ろ液は、排出管12に接続するバルブ18を開き、図示しない配管を通して放出するようにしてもよい。
【0022】
所定量の原液スラリーを供給した後、あるいは、所定の時間ろ過処理を行なった後、原液スラリーの供給を停止すればろ過板5上にはケーキ層が形成される。 その後、容器3とジャケット4との空間内に熱媒体を供給して容器3を加熱し、容器3内を加圧あるいは減圧した状態でろ過・乾燥槽1を一方向に回転させるか交互に往復反転させてケーキの乾燥処理を行なう。尚、熱水、熱風あるいは蒸気等の熱媒体は、図示しない供給装置に接続する供給管19を通し、供給口20から空間内に供給し、容器3を加熱するようになっている。
【0023】
ケーキの乾燥に先立って、ろ過・乾燥槽1を図1の状態から上下逆転させ、上方に位置するろ過室6から下方の乾燥室7に向けて下向きに圧力気体を噴射する。即ち、前記のろ液排出口11および排出管12を利用して気体を噴射させるものであり、排出管12は図示しない気体圧送装置に接続しておく。
【0024】
図3に示すろ過室6の場合、排出口(気体圧入口)11からろ過室6内に圧力気体を噴射させれば、気体は、拡散用空間16から連絡流路14を通して各室15内に分散し、ろ過板5の全面を通して乾燥室7内に噴射される。
図4に示すろ過室6の場合には、排出管12から分岐管17を通して各排出口11から気体を噴射すれば、各室15からろ過板5に対して気体が噴射されることになる。尚、気体の噴射に際して容器3内は減圧した状態となっている。
このようにろ過板5の裏面側(ケーキ付着面とは反対面)から圧力気体を噴射すれば、ろ過板5に付着しているケーキは剥離して落下することになる。
【0025】
圧力気体はバルブ18を通して圧入するようにしてもよい。即ち、バルブ18を配管を通して気体圧送装置に接続し、排出管12側のバルブ21を閉じ、バルブ18を開いて排出口11からろ過室6内に気体を噴射させればよい。
尚、ろ過室6と乾燥室7とを上下に逆転させて気体を噴射させる場合について説明したが、これに限定されるものではなく、図1の状態で下方のろ過室6かち上方の乾燥室7に向けて気体を噴射させるようにしてもよい。
【0026】
上記のようにしてろ過板5の上面(表面)からケーキを剥離した後、ろ過・乾燥槽1を回転または反転させればろ過板5上に形成されたケーキは、上下あるいは回転(反転)方向に循環移動し、ケーキは容器3の内壁面にぶつかり、また、ケーキ相互の接触により徐々に乾燥されて最終的に結晶あるいは粉粒状物質等の乾燥物が生成される。尚、熱媒体は連続して送り込まれているが、容器3の底部に設けた排出口22から排出管23を通して放出される。
【0027】
必要な時間、乾燥処理を行った後、乾燥室7の中央上面に設けた乾燥物排出用バルブ24が下向きとなるようろ過・乾燥槽1を回転して停止し、排出用バルブ24を開いて結晶あるいは粉粒状物質等の乾燥物を取り出す。尚、気体噴射および乾燥工程に先立ってスラリー供給口10から洗浄水を噴射してケーキの洗浄を行い、不純物を洗い流すようにしてもよい。
【0028】
容器3は回転あるいは反転するようにしてあるので、スラリー供給口10に接続するスラリー供給用の配管、ろ液の排出管12、熱媒体の供給管19あるいは熱媒体の排出管23等は図示しないロータリージョイントを介してスラリー槽や熱媒体供給装置、吸引ポンプ等と接続してあり、回転や反転等に支障を生ずることはない。ただし、ロータリージョイントを設けず、直接、人手あるいは特殊な装置により回転または反転可能に接続することもある。
【0029】
図5、図6は、本発明の第二の実施形態を示すものであり、前記の実施形態と同じ部分は同じ符号を使用している。
この実施形態においては、ろ過・乾燥槽1自体の構造は前記の実施形態と同じであるが、容器3の乾燥室7内において湾曲上面にそって攪拌機構25を設置し、ケーキの乾燥時に攪拌機構25を回転させてケーキを粉砕するようにしたことに特徴を有している。このため、容器3の中央上面に減速機付きのモータ26を設置し、攪拌機構25を一方向に回転するようにしてある。そして、モータ26に近接して湾曲上面には乾燥物の排出口27を設置し、開閉用シリンダー28で開閉するようになっている。
【0030】
前記の実施形態の場合と同じく、原液スラリーのろ過が終了し、ろ過板5上に積層したケーキの乾燥処理するために図1の状態からろ過・乾燥槽1を上下逆転する。従って、この実施形態の場合、ろ過・乾燥槽1は回転運動あるいは反転運動はせず、上下を逆転させた状態で停止する。
【0031】
ろ過・乾燥槽1を逆転させればケーキは自重により落下するが、前記の場合と同じくろ過室6から乾燥室7に向けて圧力気体を噴射させてろ過板5に付着しているケーキを剥離し、落下させる。落下したケーキは、回転する攪拌機構25の攪拌羽根29によって粉砕される。所定の時間、攪拌作業を行なった後、下向きの状態となっている排出口27をシリンダー28で開き、乾燥物を排出する。
【0032】
上記する各実施形態において、ろ過板5には圧力気体の噴射圧がかかるので、ろ過板5を堅牢なものとする必要がある。
図7は、堅牢性を有するろ過板5の一例を示すものであり、多数の細孔を設けた金属製のろ過用支持板30の上面にろ布31を設けたものであり、ろ過室6と乾燥室7との間に設置する。図7においてろ過室6の下方から圧力気体を噴射すれば、気体は支持板30およびろ布31を通して乾燥室7内に圧入されるが、ろ布31は支持板30で支持されているので噴射圧によって持ち上げられることがなく、安定状態を維持することができる。
【0033】
上記する各実施形態において、容器3には洗浄パイプ32が付設してある。この洗浄パイプ32から容器3内に洗浄水が噴射可能となっており、乾燥処理する前のケーキを洗浄したり、あるいは、乾燥物を排出した後、ろ過・乾燥槽1を図1の常態位置に復帰し、容器3内面や攪拌機構25およびろ過板5等の洗浄を行なう。尚、洗浄後の水は排出口11から排出すればよい。
【0034】
ケーキの乾燥処理のためにろ過・乾燥槽1を上下反転させて停止するが、そのために検出アーム33とセンサー34を使用することができる。検出アーム33は回転軸8に垂直上方に向けて突設してあり、センサー34は架台9の側面に設置してある。
【0035】
図1の常態位置からろ過・乾燥槽1を一方向に回転させれば、検出アーム33も同時に回転し、センサー34が検出アーム33を検知するとろ過・乾燥槽1の回転駆動モータに停止信号を送り、ろ過・乾燥槽1が上下に反転した位置で停止させることができる。そして、検出アーム33とは反対側に検出アーム35を突設しておけば、乾燥物を排出した後、モータによってろ過・乾燥槽1を復帰方向に回転させることによりセンサー34が検出アーム35を検知し、ろ過・乾燥槽1は図1の状態で停止することになる。
【0036】
前記した各実施形態において、ジャケット4は容器3の全面を覆う場合について説明したが、ろ過・乾燥槽1は、ろ過板5を境として上下に分割可能としたものがある。これは、ろ過室6や乾燥室7内の保守点検、ろ過板5の洗浄、交換等のためである。このため、容器2は、ろ過板5の部分を境として上下に分離し、かつ、密に連結するようにしてある。
【0037】
従って、ジャケット4も連結部を境界として上下に分離してあり、乾燥室7およびろ過室6を囲むジャケット4にもそれぞれ供給管19、供給口20および排出口22が独立して設けてある。そして、各排出口22は一本の排出管23に接続しておく。
【0038】
【発明の効果】
以上、説明した本発明によれば、原液スラリーをろ過後、ろ過・乾燥槽1を回転あるいは反転させつつろ過板5上に形成されたケーキを乾燥処理するに際し、ろ過室6から乾燥室7に向けて圧力気体を噴射させれば、ろ過板5に付着しているケーキを剥離することができる。その後、容器3を加熱しつつろ過・乾燥槽1を回転あるいは反転させれば、ケーキは乾燥して粉砕され、結晶や粉粒状物質としての乾燥物が生成されることになる。
【0039】
特に、ろ過室6は、格子状支持板13により複数室15に分割し、各分割室15を通して乾燥室7に圧力気体を噴射するようにしてあるので、ろ過板5全面から圧力を噴射することができる。また、乾燥室7内に攪拌機構25を設置し、ろ過後のケーキを乾燥する際、ろ過・乾燥槽1を上下逆転して攪拌機構25を回転させれば、ケーキは乾燥しつつ粉砕され、短時間で効率よく乾燥物を生成することができる。
【図面の簡単な説明】
【図1】本発明ろ過・乾燥装置の第一の実施形態を示す一部を断面とした正面図である。
【図2】本発明ろ過・乾燥装置の第一の実施形態を示す側面図である。
【図3】本発明ろ過・乾燥装置で使用するろ過室の一例を示す斜視図である。
【図4】本発明ろ過・乾燥装置で使用するろ過室の他の例を示す斜視図である。
【図5】本発明ろ過・乾燥装置の第二の実施形態を示す一部を断面とした正面図である。
【図6】本発明ろ過・乾燥装置の第にの実施形態を示す側面図である。
【図7】堅牢性を有するろ過板の一例を示す断面図である。
【符号の説明】
1 ろ過・乾燥槽
2 円形胴部
3 容器
4 ジャケット
5 ろ過板
6 ろ過室
7 乾燥室
8 回転軸
9 架台
10 スラリー供給口
11 ろ液排出口
12 ろ液排出管
13 支持板
14 連絡流路
15 分割室
16 拡散用空間
17 分岐管
18 バルブ
19 熱媒体供給管
20 熱媒体供給口
21 バルブ
22 熱媒体排出口
23 熱媒体排出管
24 乾燥物排出用バルブ
25 攪拌機構
26 減速機付きモータ
27 乾燥物排出口
28 開閉用シリンダー
29 攪拌羽根
30 ろ過用支持板
31 ろ布
32 洗浄パイプ
33 検出アーム
34 センサー
35 検出アーム
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a filtration / drying apparatus capable of continuously performing filtration and drying of a slurry-like substance, and particularly to a filtration / drying apparatus capable of efficiently removing a cake attached to a filter plate. Things.
[0002]
[Prior art]
In a wide range of industrial fields such as foods, chemicals, and pharmaceuticals, various substances are manufactured and produced. In particular, when producing a slurry-like substance, the slurry is filtered in a filter to form a cake, and in many cases, the cake is washed, and after removing impurities, the cake is dried to remove crystals and powder. However, providing separate filtration tanks and dryers for each operation increases the equipment cost. In addition, when the material after the filtration operation is transferred from the filtration tank to the dryer, the loss of the material often occurs during that time, and the operation is troublesome.
[0003]
In particular, when manufacturing expensive chemicals or handling crystals that are easily oxidized by air, performing the filtration work and drying work etc. separately with different apparatuses as described above lowers the quality and yield of the entire product, and sometimes There was a disadvantage that the crystal was destroyed and the quality was lowered.
Therefore, as disclosed in Japanese Patent Publication No. 46-22201, there is provided an apparatus capable of continuously performing filtration and drying operations with one filtration and drying apparatus.
[0004]
The filtration and drying apparatus A shown in Japanese Patent Publication No. 46-22201 has a cylindrical shape at the center and a conical shape at the top and bottom, a filter plate 2 is attached to the lower end in the cylindrical portion, and a filtrate outlet 3 is provided at the center of the bottom. . Further, a lid 9 having a processing liquid charging pipe 10, a product outlet, and a washing water jetting pipe 8 at the center is attached to the opening 1 on the upper surface. The cylindrical body that is rotatably supported by the left and right tubular machine shafts 6 and 7 is surrounded by a jacket 5 to form a double wall, and hot water is supplied into the jacket 5.
[0005]
In order to carry out the filtration operation with the above-mentioned filtration and drying apparatus A, the aqueous solution to be filtered is sent from the treatment liquid charging pipe 10 into the cylindrical unit, the filtration treatment is carried out by the filtration plate 2, and the filtrate is passed through the filtrate discharge port 3 to the outside. To be discharged. After a certain period of time, when a cake layer having a certain thickness is formed on the filter plate 2, the supply of the aqueous solution is stopped, the outlet 3 is closed, and hot water is circulated in the jacket 5 as a heating medium for heating. While rotating the cylindrical portion continuously in a certain direction.
[0006]
When the cylindrical portion is heated and rotated about the tubular machine shafts 6 and 7 while the inside of the cylindrical portion is decompressed, the cake layer formed on the filter plate 2 circulates in the cylindrical portion up and down or in the rotating direction. The cake collides with the inner wall surface of the cylindrical portion, and is gradually dried by the mutual contact of the cake to finally produce a dried product such as a crystal or a granular material. After performing a drying process for a necessary time, the lid 9 is opened with the downward facing, and the dried product is taken out.
[0007]
[Problems to be solved by the invention]
In the above-mentioned conventional filtration / drying device, a cake layer is formed on the filter plate 2 after filtration, and the cake is shaken off from the filter plate 2 by rotating the cylindrical portion continuously in a certain direction, and the cake is dried. Processing is performed.
However, since the liquid remains on the cake after filtration and has stickiness, even when the cylindrical portion is continuously rotated, the thin layer cake in contact with the filter plate 2 remains on the filter plate 2 as it is. It is dried and adheres to the filter plate 2.
After that, when a new stock solution slurry is supplied and filtration and drying operations are continuously performed, another cake is further thinly adhered to the cake adhered to the filter plate 2, and the cake layer gradually becomes thicker. The situation where clogging occurred and sufficient filtration could not be performed occurred.
[0008]
The present invention has been made in view of the above-mentioned problems of the prior art, and prior to drying of the cake, by providing blowback means for supplying a pressure gas such as air from the back side of the filtration surface to the filtration plate, the cake from the filtration plate It is an object of the present invention to provide a filtration / drying device for stripping off.
[0009]
[Means for Solving the Problems]
In order to achieve the above object, the apparatus of the present invention covers the outer periphery of a pressurized or depressurized sealed container 3 with a jacket 4 and installs a filter plate 5 below the container 3 to filter the inside of the container 3. The filtration chamber 6 is separated into a chamber 6 and a drying chamber 7, and the filtration chamber 6 is divided into a plurality of chambers 15 by a grid-like support plate 13. The slurry is filtered, the filtrate is discharged from the discharge port 11, and the cake formed on the filter plate 5 is separated from the filtration chamber 6 toward the drying chamber 7 by the pressure gas injected from the discharge port 11, and filtered and dried. The tank 1 is rotated or inverted, and the cake is dried while heating the container 3 to produce a dried product.
[0010]
Further, in the apparatus of the present invention, the outer periphery of the closed type container 3 which can be pressurized or depressurized is covered with a jacket 4, and a filter plate 5 is installed below the container 3, and the inside of the container 3 is provided with a filtration chamber 6 and a drying chamber 7. The filtration chamber 6 is provided with a filtration / drying tank 1 in which a plurality of separate chambers 15 are formed by a grid-like support plate 13, and the filtrate is discharged through a discharge port provided in each of the chambers 15. The cake discharged on the filter plate 5 and formed on the filter plate 5 is peeled off from the filtration chamber 6 toward the drying chamber 7 by the pressurized gas jetted from each discharge port 11, and the filtration / drying tank 1 is rotated or inverted, and The cake is dried while heating 3 to produce a dried product.
[0011]
Further, in the apparatus of the present invention, the outer periphery of the closed or pressurized closed container 3 is covered with a jacket 4, a filter plate 5 is provided below the container 3, and the inside of the container 3 is provided with a filtration chamber 6 and a drying chamber 7. The filtration chamber 6 is divided into a plurality of chambers 15 by a grid-like support plate 13, and each of the divided chambers 15 filters the undiluted slurry by the filtration / drying tank 1, which can be connected by a communication channel 14. The liquid is discharged from the discharge port 11 and the cake formed on the filter plate 5 is separated from the filtration chamber 6 toward the drying chamber 7 by the pressurized gas injected from the discharge port 11, and the inverted container 3 is heated. While the cake is crushed by the stirring mechanism 25 installed in the drying chamber 7, a dried product is generated.
[0012]
Furthermore, in the apparatus of the present invention, the outer periphery of the closed container 3 which can be pressurized or depressurized is covered with a jacket 4, and a filter plate 5 is installed below the container 3, and the inside of the container 3 is provided with a filtration chamber 6 and a drying chamber 7. The filtration chamber 6 is provided with a filtration / drying tank 1 in which a plurality of separate chambers 15 are formed by a grid-like support plate 13, and the filtrate is discharged through a discharge port provided in each of the chambers 15. The cake discharged on the filter plate 5 and formed on the filter plate 5 is separated from the filtration chamber 6 toward the drying chamber 7 by the pressurized gas jetted from each of the outlets 11, and the container 3 is turned upside down while being heated upside down. The cake is pulverized by a stirring mechanism 25 installed in the chamber 7 to produce a dried product.
[0013]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.
FIGS. 1 and 2 show a first embodiment of the filtration / drying apparatus of the present invention. The filtration / drying tank 1 has a circular body 2 having upper and lower surfaces formed into symmetrical curved surfaces and capable of being sealed. A pressure or pressure reducing container 3 has a double wall structure in which the outer peripheral surface is covered with a jacket 4, and a filter plate 5 is provided below the container 3, and a filter chamber 6 and a drying chamber 7 are provided in the container 3. It has a separate structure.
[0014]
In a normal state, as shown in FIG. 1, the filtration chamber 6 is located below and the drying chamber 7 is located above, and rotating shafts 8 protruding on both sides of the container 3 are rotated by bearings provided on a gantry 9. By supporting one of the rotating shafts 8 to a reversible motor (not shown) via a belt, a chain, or the like, the entire filtration / drying tank 1 can be continuously rotated in one direction or can be inverted. ing.
[0015]
As shown in FIG. 2, a supply port 10 for the undiluted slurry is provided above the container 3 and a discharge port 11 for the filtrate is formed in the center of the bottom as shown in FIG. Are connected by a discharge pipe 12, and the filtrate filtered by the filter plate 5 is discharged by vacuum suction or by keeping the inside of the container 3 in a pressurized state.
[0016]
The supply port 10 is connected to a stock slurry tank (not shown) by a pipe, and the stock slurry is fed into the container 3 through the supply port 10 by a pump. For this reason, in the filtration / drying tank 1, the drying chamber 7 is normally located above, and the filtration chamber 6 is normally located below.
[0017]
A plurality of support plates 13 are provided in the filtration chamber 6. The support plate 13 supports the filter plate 5 from below with respect to the weight of the laminated cake, holds the filter plate 5 from the pressure of the gas injected at the time of blowback, and guides the gas injection direction. Also serves as.
[0018]
FIG. 3 shows an example of the filtration chamber 6, in which the side and bottom surfaces of the support plates 13 combined in a lattice are fixed in the filtration chamber 6 by welding, and the inside of the filtration chamber 6 is divided into a plurality. The crossed lower portion of the grid-like support plate 13 is cut out in a circular or square shape to form a communication channel 14, and a filtrate, a pressurized gas, and the like can flow between the divided chambers 15 through the communication channel 14. Has become.
[0019]
As described above, the discharge port 11 provided at the central bottom of the filtration chamber 6 serves as a pressure inlet for the pressurized gas for discharging the filtrate and for blowback, and is located above the discharge port 11. A circular or square notch is provided in the lower end surface of the support plate 13 to form a diffusion space 16.
[0020]
FIG. 4 shows another example of the filtration chamber 6, in which the pressure of the pressurized gas is applied to the bottom of the filtration chamber 6 facing each of the divided chambers 15 divided by the grid-like support plate 13 as described above. Discharge ports 11 also serving as inlets are provided, and each discharge port 11 is connected by a branch pipe 17 and connected to one discharge pipe 12. Therefore, the lower end surface of the grid-like support plate 13 is fixed to the bottom surface of the filtration chamber 6, and each of the divided chambers 15 is cut off and formed independently.
[0021]
The configuration shown in the first embodiment is as described above. Next, the filtration and drying operations of the stock slurry will be described.
The undiluted solution slurry is supplied into the container 3 from the slurry supply port 10 directed upward of the filtration / drying tank 1, and filtration is performed while the pressure in the container 3 is increased or reduced, and the filtrate is discharged from the filtrate outlet 11. Discharge to the outside through tube 12. The filtrate may be discharged through a pipe (not shown) by opening a valve 18 connected to the discharge pipe 12.
[0022]
After the supply of the undiluted slurry after the supply of the undiluted slurry of a predetermined amount or the filtration treatment for a predetermined time, a cake layer is formed on the filter plate 5. Thereafter, a heating medium is supplied into the space between the container 3 and the jacket 4 to heat the container 3, and the filtration / drying tank 1 is rotated in one direction or alternately reciprocated while the pressure in the container 3 is increased or reduced. The cake is dried upside down. A heat medium such as hot water, hot air or steam is supplied into the space from a supply port 20 through a supply pipe 19 connected to a supply device (not shown) to heat the container 3.
[0023]
Prior to drying of the cake, the filtration / drying tank 1 is turned upside down from the state shown in FIG. 1 and a pressurized gas is jetted downward from the filtration chamber 6 located above toward the drying chamber 7 below. That is, gas is injected by using the filtrate outlet 11 and the discharge pipe 12 described above, and the discharge pipe 12 is connected to a gas pumping device (not shown).
[0024]
In the case of the filtration chamber 6 shown in FIG. 3, if a pressurized gas is injected from the discharge port (gas pressure inlet) 11 into the filtration chamber 6, the gas flows into the respective chambers 15 from the diffusion space 16 through the communication flow path 14. It is dispersed and injected into the drying chamber 7 through the entire surface of the filter plate 5.
In the case of the filtration chamber 6 shown in FIG. 4, if gas is ejected from each outlet 11 through the discharge pipe 12 through the branch pipe 17, gas is ejected from each chamber 15 to the filter plate 5. The inside of the container 3 is in a depressurized state when the gas is injected.
By injecting the pressurized gas from the back surface of the filter plate 5 (the surface opposite to the cake attachment surface), the cake attached to the filter plate 5 is peeled off and falls.
[0025]
The pressurized gas may be injected through the valve 18. That is, the valve 18 may be connected to a gas pumping device through a pipe, the valve 21 on the discharge pipe 12 side may be closed, the valve 18 may be opened, and gas may be injected from the discharge port 11 into the filtration chamber 6.
In addition, the case where the gas is injected by inverting the filtration chamber 6 and the drying chamber 7 up and down has been described. However, the present invention is not limited to this, and in the state of FIG. Alternatively, the gas may be injected toward 7.
[0026]
After peeling the cake from the upper surface (front surface) of the filter plate 5 as described above, if the filtration / drying tank 1 is rotated or inverted, the cake formed on the filter plate 5 will be vertically or rotationally (inverted) direction. The cake circulates, and the cake hits the inner wall surface of the container 3 and is gradually dried by the mutual contact of the cake to finally produce a dried product such as a crystal or a granular material. Although the heating medium is continuously fed, it is discharged from a discharge port 22 provided at the bottom of the container 3 through a discharge pipe 23.
[0027]
After performing the drying process for a necessary time, the filtration / drying tank 1 is rotated and stopped so that the dry matter discharging valve 24 provided on the upper central surface of the drying chamber 7 faces downward, and the discharging valve 24 is opened. Take out the dried material such as crystals or granular material. Prior to the gas injection and drying steps, the cake may be washed by injecting washing water from the slurry supply port 10 to wash out the impurities.
[0028]
Since the container 3 is rotated or inverted, a slurry supply pipe connected to the slurry supply port 10, a filtrate discharge pipe 12, a heat medium supply pipe 19, a heat medium discharge pipe 23, and the like are not shown. It is connected to a slurry tank, heat medium supply device, suction pump, etc. via a rotary joint, and does not hinder rotation or inversion. However, there is also a case where a rotary joint is directly or rotatably or reversibly connected by a manual device or a special device without providing a rotary joint.
[0029]
FIG. 5 and FIG. 6 show a second embodiment of the present invention, and the same parts as those in the above-described embodiment use the same reference numerals.
In this embodiment, the structure of the filtration / drying tank 1 itself is the same as that of the above-described embodiment, but a stirring mechanism 25 is installed along a curved upper surface in the drying chamber 7 of the container 3 to stir when drying the cake. The feature is that the cake is pulverized by rotating the mechanism 25. For this purpose, a motor 26 with a speed reducer is installed on the upper surface of the center of the container 3 so that the stirring mechanism 25 rotates in one direction. An outlet 27 for dried matter is provided on the curved upper surface in the vicinity of the motor 26, and is opened and closed by an opening / closing cylinder 28.
[0030]
As in the case of the above embodiment, the filtration of the undiluted slurry is completed, and the filtration / drying tank 1 is turned upside down from the state of FIG. 1 to dry the cake laminated on the filter plate 5. Therefore, in the case of this embodiment, the filtration / drying tank 1 does not rotate or invert, but stops in a state where the tank is turned upside down.
[0031]
If the filtration / drying tank 1 is reversed, the cake falls under its own weight. However, similarly to the above case, the pressure gas is injected from the filtration chamber 6 toward the drying chamber 7 to peel off the cake adhering to the filter plate 5. And let it fall. The cake that has fallen is crushed by the stirring blades 29 of the rotating stirring mechanism 25. After performing the stirring operation for a predetermined time, the discharge port 27 in the downward state is opened by the cylinder 28 to discharge the dried product.
[0032]
In each of the embodiments described above, since the injection pressure of the pressurized gas is applied to the filter plate 5, it is necessary to make the filter plate 5 robust.
FIG. 7 shows an example of a filter plate 5 having robustness, in which a filter cloth 31 is provided on the upper surface of a metal support plate 30 having a large number of pores. And the drying room 7. In FIG. 7, when a pressurized gas is injected from below the filtration chamber 6, the gas is pressed into the drying chamber 7 through the support plate 30 and the filter cloth 31, but is injected because the filter cloth 31 is supported by the support plate 30. A stable state can be maintained without being lifted by pressure.
[0033]
In each of the above-described embodiments, the washing pipe 32 is attached to the container 3. Washing water can be sprayed from the washing pipe 32 into the container 3 to wash the cake before the drying process or to discharge the dried product, and then place the filtration / drying tank 1 in the normal position in FIG. To wash the inner surface of the container 3, the stirring mechanism 25, the filter plate 5, and the like. Note that the water after washing may be discharged from the outlet 11.
[0034]
In order to dry the cake, the filtration / drying tank 1 is turned upside down and stopped. For this purpose, the detection arm 33 and the sensor 34 can be used. The detection arm 33 protrudes vertically upward from the rotation shaft 8, and the sensor 34 is installed on a side surface of the gantry 9.
[0035]
When the filtration / drying tank 1 is rotated in one direction from the normal position in FIG. 1, the detection arm 33 is simultaneously rotated. When the sensor 34 detects the detection arm 33, a stop signal is sent to the rotation drive motor of the filtration / drying tank 1. The feed and filtration / drying tank 1 can be stopped at a position where the tank is turned upside down. If the detection arm 35 is protrudingly provided on the opposite side to the detection arm 33, after the dried matter is discharged, the filtration / drying tank 1 is rotated by the motor in the return direction, so that the sensor 34 causes the detection arm 35 to rotate. Upon detection, the filtration / drying tank 1 stops in the state shown in FIG.
[0036]
In each of the embodiments described above, the case in which the jacket 4 covers the entire surface of the container 3 has been described. However, the filtration / drying tank 1 may be divided vertically with the filter plate 5 as a boundary. This is for maintenance and inspection in the filtration chamber 6 and the drying chamber 7, cleaning and replacement of the filtration plate 5, and the like. For this reason, the container 2 is vertically separated from the filter plate 5 as a boundary and is closely connected.
[0037]
Therefore, the jacket 4 is also vertically separated by the connecting portion as a boundary, and the jacket 4 surrounding the drying chamber 7 and the filtration chamber 6 is also provided with a supply pipe 19, a supply port 20 and a discharge port 22, respectively. Each discharge port 22 is connected to one discharge pipe 23.
[0038]
【The invention's effect】
According to the present invention described above, after the undiluted slurry is filtered, the cake formed on the filter plate 5 is dried while rotating or reversing the filtration / drying tank 1, from the filtration chamber 6 to the drying chamber 7. If the pressurized gas is injected toward the filter plate, the cake adhering to the filter plate 5 can be peeled off. Thereafter, if the filtration / drying tank 1 is rotated or inverted while the container 3 is heated, the cake is dried and pulverized, and a dried product as a crystal or a granular material is generated.
[0039]
In particular, since the filtration chamber 6 is divided into a plurality of chambers 15 by the grid-like support plate 13 and the pressurized gas is injected into the drying chamber 7 through each of the division chambers 15, pressure is injected from the entire surface of the filtration plate 5. Can be. In addition, when the stirring mechanism 25 is installed in the drying chamber 7 and the cake after filtration is dried, if the filtration and drying tank 1 is turned upside down and the stirring mechanism 25 is rotated, the cake is pulverized while drying, A dried product can be efficiently produced in a short time.
[Brief description of the drawings]
FIG. 1 is a partially sectional front view showing a first embodiment of a filtration / drying apparatus of the present invention.
FIG. 2 is a side view showing a first embodiment of the filtration / drying device of the present invention.
FIG. 3 is a perspective view showing an example of a filtration chamber used in the filtration / drying apparatus of the present invention.
FIG. 4 is a perspective view showing another example of the filtration chamber used in the filtration / drying apparatus of the present invention.
FIG. 5 is a partially sectional front view showing a second embodiment of the filtration / drying apparatus of the present invention.
FIG. 6 is a side view showing a filtration and drying apparatus according to a second embodiment of the present invention.
FIG. 7 is a cross-sectional view showing an example of a filter plate having robustness.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Filtration / drying tank 2 Circular trunk 3 Container 4 Jacket 5 Filtration plate 6 Filtration chamber 7 Drying chamber 8 Rotating shaft 9 Stand 10 Slurry supply port 11 Filtrate discharge port 12 Filtrate discharge pipe 13 Support plate 14 Communication channel 15 Division Chamber 16 Diffusion space 17 Branch pipe 18 Valve 19 Heat medium supply pipe 20 Heat medium supply port 21 Valve 22 Heat medium discharge port 23 Heat medium discharge pipe 24 Dry matter discharge valve 25 Stirring mechanism 26 Motor with reduction gear 27 Dry matter discharge Outlet 28 Opening / closing cylinder 29 Stirrer blade 30 Filtration support plate 31 Filter cloth 32 Cleaning pipe 33 Detection arm 34 Sensor 35 Detection arm

Claims (4)

加圧あるいは減圧可能な密閉型容器3の外周をジャケット4で被覆し、容器3内の下方にろ過板5を設置して容器3内をろ過室6と乾燥室7とに分離するとともにろ過室6は、格子状支持板13により複数室15に分割して各分割室15は連絡流路14により連絡可能としたろ過・乾燥槽1により原液スラリーをろ過し、ろ液は排出口11から排出するとともにろ過板5上に形成されたケーキはろ過室6から乾燥室7に向けて排出口11から噴射した圧力気体により剥離し、ろ過・乾燥槽1を回転あるいは反転させ、容器3を加熱しつつケーキを乾燥処理し、乾燥物を生成するようにしたことを特徴とするろ過・乾燥装置。The outer periphery of the pressurized or depressurized sealed container 3 is covered with a jacket 4, and a filter plate 5 is provided below the container 3 to separate the inside of the container 3 into a filtration chamber 6 and a drying chamber 7. 6 is divided into a plurality of chambers 15 by a grid-like support plate 13, and each of the divided chambers 15 filters the stock solution slurry by the filtration / drying tank 1 communicable by a communication channel 14, and the filtrate is discharged from the discharge port 11. At the same time, the cake formed on the filter plate 5 is separated from the filtration chamber 6 toward the drying chamber 7 by the pressurized gas jetted from the discharge port 11, and the filtration / drying tank 1 is rotated or inverted to heat the container 3. A filtration / drying apparatus characterized in that a cake is dried while drying to produce a dried product. 加圧あるいは減圧可能な密閉型容器3の外周をジャケット4で被覆し、容器3内の下方にろ過板5を設置して容器3内をろ過室6と乾燥室7とに分離するとともにろ過室6は、格子状支持板13により独立した複数の分割室15を形成したろ過・乾燥槽1により原液スラリーをろ過し、ろ液は各分割室15に設けた排出口11から排出するとともにろ過板5上に形成されたケーキはろ過室6から乾燥室7に向けて各排出口11から噴射した圧力気体により剥離し、ろ過・乾燥槽1を回転あるいは反転させ、容器3を加熱しつつケーキを乾燥処理し、乾燥物を生成するようにしたことを特徴とするろ過・乾燥装置。The outer periphery of the pressurized or depressurized sealed container 3 is covered with a jacket 4, and a filter plate 5 is provided below the container 3 to separate the inside of the container 3 into a filtration chamber 6 and a drying chamber 7. 6 filters the undiluted slurry by the filtration / drying tank 1 in which a plurality of independent divided chambers 15 are formed by the grid-like support plate 13, and the filtrate is discharged from the outlets 11 provided in each divided chamber 15 and the filtration plate is filtered. The cake formed on 5 is separated from the filtration chamber 6 toward the drying chamber 7 by the pressurized gas injected from each outlet 11, and the filtration / drying tank 1 is rotated or inverted, and the cake is heated while the container 3 is heated. A filtration / drying apparatus characterized in that a drying process is performed to produce a dried product. 加圧あるいは減圧可能な密閉型容器3の外周をジャケット4で被覆し、容器3内の下方にろ過板5を設置して容器3内をろ過室6と乾燥室7とに分離するとともにろ過室6は、格子状支持板13により複数室15に分割して各分割室15は連絡流路14により連絡可能としたろ過・乾燥槽1により原液スラリーをろ過し、ろ液は排出口11から排出するとともにろ過板5上に形成されたケーキはろ過室6から乾燥室7に向けて排出口11から噴射した圧力気体により剥離し、上下反転させた容器3を加熱しつつ乾燥室7内に設置した攪拌機構25によりケーキを粉砕して乾燥物を生成するようにしたことを特徴とするろ過・乾燥装置。The outer periphery of the pressurized or depressurized sealed container 3 is covered with a jacket 4, and a filter plate 5 is provided below the container 3 to separate the inside of the container 3 into a filtration chamber 6 and a drying chamber 7. 6 is divided into a plurality of chambers 15 by a grid-like support plate 13, and each of the divided chambers 15 filters the stock solution slurry by the filtration / drying tank 1 communicable by a communication channel 14, and the filtrate is discharged from the discharge port 11. At the same time, the cake formed on the filter plate 5 is separated from the filtration chamber 6 toward the drying chamber 7 by the pressurized gas injected from the discharge port 11, and is placed in the drying chamber 7 while heating the container 3 which is turned upside down. A filter and drying device, wherein the cake is pulverized by the stirring mechanism 25 to produce a dried product. 加圧あるいは減圧可能な密閉型容器3の外周をジャケット4で被覆し、容器3内の下方にろ過板5を設置して容器3内をろ過室6と乾燥室7とに分離するとともにろ過室6は、格子状支持板13により独立した複数の分割室15を形成したろ過・乾燥槽1により原液スラリーをろ過し、ろ液は各分割室15に設けた排出口11から排出するとともにろ過板5上に形成されたケーキはろ過室6から乾燥室7に向けて各排出口11から噴射した圧力気体により剥離し、上下反転させた容器3を加熱しつつ乾燥室7内に設置した攪拌機構25によりケーキを粉砕して乾燥物を生成するようにしたことを特徴とするろ過・乾燥装置。The outer periphery of the pressurized or depressurized sealed container 3 is covered with a jacket 4, and a filter plate 5 is provided below the container 3 to separate the inside of the container 3 into a filtration chamber 6 and a drying chamber 7. 6 filters the undiluted slurry by the filtration / drying tank 1 in which a plurality of independent divided chambers 15 are formed by the grid-like support plate 13, and the filtrate is discharged from the outlets 11 provided in each divided chamber 15 and the filtration plate is filtered. The cake formed on 5 is separated from the filtration chamber 6 toward the drying chamber 7 by the pressurized gas injected from each outlet 11, and a stirring mechanism installed in the drying chamber 7 while heating the container 3 which has been turned upside down. 25. A filtration / drying device, wherein the cake is crushed by 25 to produce a dried product.
JP2000396334A 2000-12-27 2000-12-27 Filtration and drying equipment Expired - Lifetime JP3546840B2 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109621540A (en) * 2019-01-08 2019-04-16 莱芜职业技术学院 A kind of bio-pharmaceuticals solid-liquid separating equipment

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA2578020A1 (en) * 2004-08-31 2006-03-09 Kakuno Seisakusho Co., Ltd. Depressurization type drying machine and method for drying lumber using the same
CN112807827A (en) * 2020-12-01 2021-05-18 飞潮(无锡)过滤技术有限公司 Full-automatic cleaning and filtering system
CN115871127B (en) * 2023-02-14 2023-05-05 汕头市三润机电科技有限公司 Raw material pretreatment equipment

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109621540A (en) * 2019-01-08 2019-04-16 莱芜职业技术学院 A kind of bio-pharmaceuticals solid-liquid separating equipment
CN109621540B (en) * 2019-01-08 2021-07-20 莱芜职业技术学院 Solid-liquid separation equipment for bio-pharmaceuticals

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