JP4283396B2 - Cleaning method, cleaning device and cleaning material for chemical reaction vessel - Google Patents
Cleaning method, cleaning device and cleaning material for chemical reaction vessel Download PDFInfo
- Publication number
- JP4283396B2 JP4283396B2 JP32374099A JP32374099A JP4283396B2 JP 4283396 B2 JP4283396 B2 JP 4283396B2 JP 32374099 A JP32374099 A JP 32374099A JP 32374099 A JP32374099 A JP 32374099A JP 4283396 B2 JP4283396 B2 JP 4283396B2
- Authority
- JP
- Japan
- Prior art keywords
- cleaning
- solvent
- resin
- adhesive resin
- reaction container
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Images
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
- Polymerisation Methods In General (AREA)
- Cleaning In General (AREA)
- Cleaning By Liquid Or Steam (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Detergent Compositions (AREA)
Description
【0001】
【発明の属する技術分野】
本発明は、洗浄技術、特に洗浄すべき表面に固着した付着性樹脂を短時間で除去できる化学反応容器の洗浄法及びその装置並びに洗浄材の分野に属する。
【0002】
【従来の技術】
従来、付着性の弱い付着性樹脂が固着した表面を洗浄する際に、付着性樹脂が可溶な溶媒の噴霧又は溶媒中に浸漬するディッピングによる洗浄法が用いられる。強固に付着する樹脂に対しては、剥離剤による接触剥離法、研磨剤配合のペーストによるワイピング法、付着性樹脂を削り取るサンドブラスティング、高圧水によるジェット法、酸若しくはアルカリによるケミカルエッチング、加水分解法又は人力による切削法が用いられる。これらの手法は、洗浄に長時間を要し、洗浄する表面の損傷を伴う。また、人体及び環境に悪影響を及ぼす溶媒を使用するため、洗浄後も溶媒の残留防止のため更に洗浄を必要とする。特に、化学反応を伴う製品を製造する際に使用する反応容器及び治具の洗浄は、溶媒の消費量が多いと共に洗浄に長時間要するため、製品価格に占める洗浄コストの割合が高いのが現状である。
【0003】
例えば、重縮合反応により、塗料、インキ、接着剤、合成樹脂等の製造に使用される反応装置は、反応生成物を反応容器から取り出した後、付着性樹脂が反応容器の内部表面に残留することは回避できない。残留した付着性樹脂は除去が困難であるが、完全に除去しなければその反応容器で別種の重合反応を行うとき、反応生成物と付着性樹脂とが混合して製品の品質低下を招く。また、重合反応で温度制御を行うコイル等に付着性樹脂が多量に固着すると、総括伝熱係数が低下して十分な温度制御が困難になる。
【0004】
このため、従来の標準的洗浄法は、付着性樹脂に対し可溶性の溶媒を使用して、重合反応終了1回毎に還流洗浄を行う。還流洗浄は、反応容器内に半分程度充填した溶媒を沸点付近の温度まで加熱し、溶媒を蒸発・凝縮させ内壁面を濡らして付着性樹脂を溶解して行う。蒸発した溶媒は、反応容器の上部に接続されたコンデンサ内で液化され捕集されて、反応容器内に戻される。この還流操作を60〜90分間繰り返す。還流洗浄で除去できない付着性樹脂は無視して次の重合反応を行う。繰り返し重合反応に使用した後、累積した樹脂の付着量に応じて重合反応数回毎に1回アルカリ溶液による洗浄を少なくとも16時間行う。更に作業員による人的操作で固着した樹脂の剥離作業を行う。
【0005】
樹脂の付着の程度は溶液重合、乳化重合法等の重合法で異なり、製造する樹脂の分子量の大きさ、粘着性、反応速度、急速高温熱源による加温の温度制御等でも異なる。樹脂の付着性防止のため、反応容器、取り扱い容器及び治具の表面処理による改善も行われているが、温度制御性及び耐久性の点で不完全である。
【0006】
また、前記の標準的洗浄法の洗浄コストは、5000Lの反応容器で500万円/年程度の額に達する。これは還流洗浄、アルカリ洗浄及び剥離作業に長時間要すると共に、還流洗浄に使用した溶媒は再生できず、燃焼廃棄、大気中へ排出等するためである。このことはコストばかりでなく環境汚染、資源の浪費及び作業者の健康阻害を引き起こす化学工業の本質的な問題点とされる。
【0007】
【発明が解決しようとする課題】
そこで本発明は、人力を必要としない合理的なクローズドシステムにより、物体の表面に固着した付着性樹脂を短時間で確実に除去する化学反応容器の洗浄法及びその装置並びに洗浄材を提供することを目的とする。
また、安全に且つ容易に付着性樹脂を除去する化学反応容器の洗浄法及びその装置並びに洗浄材を提供することを目的とする。
【0008】
【課題を解決するための手段】
前記課題を解決するための本発明の技術思想は、
[1] 従来の人力による機械的切削法に代わる手段として、洗浄すべき表面を損傷することなく物理的に付着性樹脂を攻撃できる固形物質を選択し、これを流動させて付着性樹脂を剥離させ、
[2] 従来から使用する溶媒を固形物質の分散媒として使用し、還流洗浄と併用し、溶解、膨潤及び剥離を円滑に行い、
[3] 本発明による洗浄材を使用した洗浄法が工業的に容易に且つ安全に、クローズドシステム化されることにある。
【0009】
即ち、本発明による化学反応容器の洗浄法は、洗浄すべき表面に固着した付着性樹脂を溶解及び膨潤させる良溶媒と膨潤した付着性樹脂を硬化させる貧溶媒とからなる混合溶媒(3)100重量部と、混合溶媒(3)に溶解しない最大長さ0.1〜50mmの固形物質10〜30重量部とからなる洗浄材を反応容器(1)に充填する工程と、洗浄材を反応容器(1)内で流動させる工程と、反応容器(1)の内壁面(1a)に固着する付着性樹脂(9)を混合溶媒(3)により溶解、浸透及び膨潤させ且つ混合溶媒(3)と共に流動する固形物質(4)を反応容器(1)の内壁面(1a)に衝突させて、膨潤した付着性樹脂(9)を物理的に剥離する工程と、洗浄材と共に、溶解及び剥離された付着性樹脂(9)を反応容器(1)から除去する工程とを含む。
【0010】
本発明による化学反応容器の洗浄装置は、化学反応により反応容器(1)の内壁面(1a)に固着した付着性樹脂(9)を内壁面(1a)から洗浄除去する。本発明では、付着性樹脂(9)を溶解及び膨潤させる良溶媒と膨潤した付着性樹脂を硬化させる貧溶媒とからなる混合溶媒(3)並びに付着性樹脂(9)を物理的に剥離させる固形物質(4)を反応容器(1)に供給する供給装置(23, 7)と、混合溶媒(3)及び固形物質(4)を含む洗浄材を流動させて、膨潤した付着性樹脂(9)に固形物質(4)を衝突させる撹拌機(2)と、洗浄に使用された洗浄材を混合溶媒(3)と固形物質(4)とに分離するセパレータ(22)と、分離された混合溶媒(3)から付着性樹脂(9)を除去して混合溶媒(3)を浄化するフィルタ(20)と、浄化された混合溶媒(3)及び分離された固形物質(4)を収容する収容槽(5, 6)とを備える。
【0011】
本発明による洗浄材は、洗浄すべき表面(1a)に固着した付着性樹脂(9)を溶解及び膨潤させる良溶媒と、膨潤した付着性樹脂を硬化させる貧溶媒と、洗浄すべき表面(1a)に衝突して付着性樹脂(9)を物理的に剥離させる固形物質(4)とを含む。本明細書では、用語「良溶媒」は、溶質を溶かす能力の大きい溶媒をいう。また、用語「貧溶媒」は、溶質を溶かす能力の小さい溶媒をいう。良溶媒で付着性樹脂(9)を溶解させて除去すると共に、物体の表面に強固に付着した付着性樹脂(9)を膨潤させて固形物質(4)を衝突させて物理的に剥離するので、表面(1a)に固着した付着性樹脂(9)を確実に且つ自動的に除去することができる。従って、作業員が掻き取り作業を行わずに、良溶媒で除去できる溶解性の樹脂だけでなく、良溶媒に非溶解性の樹脂も除去可能である。
【0012】
【発明の実施の形態】
以下、本発明による化学反応容器の洗浄法及びその装置並びに洗浄材の実施の形態を図1〜図3により説明する。
【0013】
本発明による洗浄材は、洗浄すべき表面(1a)に固着した付着性樹脂(9)を溶解及び膨潤させる溶媒(3)と、洗浄すべき表面(1a)に衝突して付着性樹脂(9)を物理的に剥離させる固形物質(4)とを含む。溶媒(3)は良溶媒であり、酢酸エチル、酢酸ブチル等のエステル、アセトン、メチルエチルケトン、メチルイソブチルケトン等のケトン、トリクロロエチレン、四塩化炭素等のハロゲン化物、トルエン、キシレン等の芳香族炭化水素、イソプロピルアルコール等のアルコール、水酸化ナトリウム等のアルカリ及び水の1種又は2種以上である。必要に応じてジメチルアミノエタノール、ジエチルアミノエタノール、トリエチルアミン等の有機アミノ化合物、酢酸等の有機酸類、界面活性剤及びアンモニアも使用できる。更に、溶媒(3)粘度の調節及び付着性樹脂(9)の溶解促進のため、低分子量のアクリル樹脂、ポリエステル樹脂及び塩化ビニル樹脂を溶媒(3)に添加してもよい。
【0014】
固形物質(4)は、円柱形、球形、多面体形、金平糖形又はテトラポッド形の固体樹脂で最大長さが0.1〜50mmである。固形物質(4)の最大長さが0.1mm未満であると、溶媒(3)及び固形物質(4)を再利用するため剥離された付着性樹脂(9)を分離する際、固形物質(4)と付着性樹脂(9)とを完全に分離することが困難となる。固形物質(4)の最大長さが50mmを超えると、洗浄すべき表面(1a)である反応容器(1)及び配管の内壁面(1a)と固形物質(4)との衝突回数が減り、内壁面(1a)に固着した付着性樹脂(9)の剥離性が低下する。また、50mmを超えると、反応容器(1)内の凹凸部分、例えば、撹拌機(2)のシャフト(2a)と撹拌翼(2b)との接続箇所の図示しない凹凸部分の隙間に固形物質(4)が入り込まず、衝突できないデッドスペースが増える。
【0015】
固形物質(4)は、溶媒(3)に不溶で内壁面(1a)に比べて柔らかい材質であれば良く、内壁面(1a)に固着した付着性樹脂(9)に対し適度な衝撃を与えることができる20〜220J/mの衝撃強さを有する材質が好ましい。ポリオレフィン樹脂、ポリエステル樹脂、フェノール樹脂、メラミン樹脂、尿素樹脂、エポキシ樹脂、シリコン樹脂又はフッ素樹脂を使用でき、中でも高密度、高耐熱性、強い機械的強度を有するポリエチレン、ポリプロピレン、ポリエチレンテレフタレート又はポリテトラフルオロエチレン等のペレットが好ましい。前記固形物質(4)の単体の密度は、ポリエチレン製では0.92×103〜0.96×103kg/m3、ポリプロピレン製では0.85×103〜0.92×103kg/m3、ポリエチレンテレフタレート製では1.37×103〜1.38×103kg/m3及びポリテトラフルオロエチレン製では2.1〜2.3g/cm3であり、溶媒(3)中での分散性が良好で、流動による繰り返しのソフトアタックが効果的に行われる。固形物質(4)は樹脂以外にも安価で適度な硬度、比重、熱安定性及び耐磨耗性を有する材質であれば有機材料、無機材料、金属又はそれらの複合体を使用できるが、溶媒(3)に分散し得る比重を持つものが好ましい。
【0016】
溶媒(3)と固形物質(4)との関係は、50〜90重量部の溶媒(3)と10〜50重量部の固形物質(4)とを付着性樹脂(9)の性状に合わせて選択すればよい。溶媒(3)と固形物質(4)単体との密度の比は1:0.9〜1.4である。溶媒(3)1に対して固形物質(4)単体の密度の割合が0.9未満であると、固形物質(4)が溶媒(3)中に浮遊し、反応容器(1)の下部の内壁面(1a)を十分に洗浄できない。溶媒(3)1に対して固形物質(4)単体の密度の割合が1.4を超えると、固形物質(4)が溶媒(3)中で沈降して反応容器(1)の上部の内壁面(1a)を十分に洗浄できない。また、固形物質(4)の流動速度も遅くなり付着性樹脂(9)に対する衝撃力及び衝突回数が減少する。後述する混合溶媒(3)と固形物質(4)単体との密度の比も同様の理由で1:0.9〜1.4である。
【0017】
本発明による洗浄材で除去する付着性樹脂(9)は、固形物質(4)により物理的に剥離されるので、付着性樹脂(9)の種類は特に制約がない。有効な効果を発揮するのは、工業的に広く使用されるアクリル樹脂、ポリエステル樹脂、ウレタン樹脂、塩化ビニル樹脂、ポリスチレン若しくはABS樹脂の製造又はこれらの樹脂の組み合わせによる変性樹脂の製造により反応容器(1)及び配管内に固着した樹脂である。
【0018】
本発明の実施の形態では、浸透により膨潤した付着性樹脂(9)を硬化させる貧溶媒を含む。良溶媒と貧溶媒とを含む混合溶媒(3)を使用すると、更に洗浄力が強化される。即ち、付着性樹脂(9)がゲル分と分子量の小さいゾル分とから構成されるとき、ゾル分は良溶媒に良く溶けるが、ゲル分は多量の良溶媒を吸収し膨潤する。多量の良溶媒を吸収して膨潤したゲル分は、良溶媒から溶出せずに内壁面(1a)に付着した状態を維持して柔軟性が増すので、固形物質(4)や高圧水による物理的衝撃を緩和し、付着性樹脂(9)を内壁面(1a)から掻き取ることが困難となる。一方、溶質を溶かす能力の小さい貧溶媒は、ゲル分の良溶媒吸収量を制限して、膨潤したゲル分を硬化する。これにより、良溶媒でゾル分を溶解すると共にゲル分を膨潤させ、膨潤させたゲル分を貧溶媒で硬化した後、固形物質(4)で物理的に剥離する相乗効果により、付着性樹脂(9)を内壁面(1a)から完全に除去できる。図1に示すように撹拌機(2)で混合溶媒(3)を撹拌すると、図2に示すように固形物質(4)が付着性樹脂(9)に衝突して、付着性樹脂(9)を反応容器(1)の内壁面(1a)から完全に剥離できる。貧溶媒は、アルコール、石油エーテル、脂肪族炭化水素及び水の1種又は2種以上である。
【0019】
混合溶媒(3)である良溶媒及び貧溶媒の組み合わせは、付着性樹脂(9)により決定される。付着性樹脂(9)が、乳化重合、懸濁重合及び溶液重合可能なエチレン性不飽和二重結合を有する単量体、例えば塩化ビニル、酢酸ビニル、スチレン、メチルメタクリレート、ブチルアクリレート、イソオクチルアクリレート又はアクリロニトリルの重合反応により内壁面(1a)に付着するとき、エステル、ケトン、ハロゲン化アルキル及び芳香族炭化水素の1種又は2種以上の良溶媒と、アルコール、石油エーテル及び脂肪族炭化水素の1種又は2種以上の貧溶媒とを使用する。付着性樹脂(9)が、官能基を有するエチレン性不飽和二重結合を主成分とする単量体、例えばアクリル酸、メタクリル酸、2−ヒドロキシエチルアクリレート、アクリルアミド又はN−メチロールアクリルアミドの重合反応により内壁面(1a)に付着するとき、エステル、ケトン、ハロゲン化アルキル、芳香族炭化水素、アルコール及び水の1種又は2種以上の良溶媒と、石油エーテル及び脂肪族炭化水素の1種又は2種以上の貧溶媒とを使用する。前記のように、良溶媒及び貧溶媒は、付着性樹脂(9)の化学的成分により決定され、アルコールのように良溶媒又は貧溶媒のいずれにもなり得る溶媒がある。
【0020】
良溶媒、貧溶媒及び固形物質(4)の組み合わせは、例えば、良溶媒である分子量100以下のエステル20〜70重量%及び貧溶媒である炭素数1〜6のアルコール30〜80重量%の混合溶媒(3)100重量部と、最大長さが0.1〜50mmの固形物質(4)10〜30重量部である。良溶媒である分子量100以下のエステルが20重量%未満であると、付着性樹脂(9)に含まれるゾル分の溶解が不十分となり、70重量%を超えても溶解能は変わらない。また、貧溶媒である炭素数1〜6のアルコール30重量%未満であると、良溶媒により膨潤したゲル分を完全に硬化することができず、柔軟性を維持するので、固形物質(4)を衝突させることによる物理的剥離が困難となる。80重量%を超えてもそれ以上は硬化しない。混合溶媒(3)100重量部に対して0.1〜50mmの固形物質(4)が10重量部未満であると、反応容器(1)に含まれる固形物質(4)の含有量が少なく、固形物質(4)と反応容器(1)の内壁面(1a)との衝突回数が減り、付着性樹脂(9)の剥離性が低下する。30重量部を超えると、反応容器(1)に含まれる固形物質(4)含有量が多く且つ重く固形物質(4)の流動速度が遅くなり、固形物質(4)が激しく内壁面(1a)に衝突しないので剥離性が低下する。
【0021】
前記洗浄材を用い反応容器(1)の洗浄を行う洗浄装置は、図3に示すように、付着性樹脂(9)を溶解及び膨潤させる溶媒(3)並びに付着性樹脂(9)を物理的に剥離させる固形物質(4)を反応容器(1)に供給する供給装置(23, 7)と、溶媒(3)及び固形物質(4)を含む洗浄材を図1に示すように流動させて、膨潤した付着性樹脂(9)に固形物質(4)を衝突させる撹拌機(2)と、洗浄に使用された洗浄材を溶媒(3)と固形物質(4)とに分離するセパレータ(22)と、分離された溶媒(3)から付着性樹脂(9)を除去して溶媒(3)を浄化するフィルタ(20)と、浄化された溶媒(3)及び分離された固形物質(4)を収容する収容槽(5, 6)とを備える。
【0022】
溶媒(3)の供給装置である溶媒ポンプ(23)は、溶媒(3)の収容槽である溶媒槽(5)と反応容器(1)との間に連結され、洗浄を開始するとき溶媒(3)を反応容器(1)に供給する。固形物質(4)の供給装置であるフィーダ(7)は、固形物質(4)の収容槽であるバケット槽(6)と反応容器(1)との間に連結され、洗浄を開始するとき固形物質(4)を反応容器(1)に供給する。図1に示すように、撹拌機(2)は、モータ(2c)から回転運動を与えられるシャフト(2a)と、シャフト(2a)に接続された撹拌翼(2b)とを備え、溶媒(3)及び固形物質(4)を流動させる。洗浄後の洗浄材は、バケット槽(6)に収容され、バケット槽(6)と珪藻土投入槽(10)との間に形成された平板状のセパレータ(22)で溶媒(3)と固形物質(4)とに分離される。セパレータ(22)は、固形物質(4)が通過できない程の開口部を全面に有するパンチングメタル又は金網により形成される。フィルタ(20)は、内部に形成された複数の濾板(20a)の外面又は内面に濾紙が配置され、その表面に粒子径3〜5μmの珪藻土が溶媒(3)の0.1重量%程度、濾過助剤としてプレコートされる。また、フィルタ(20)で浄化された溶媒(3)を反応容器(1)内に戻して、フィルタ(20)及び反応容器(1)間を循環させる循環ポンプ(24)を備える。更に、フィルタ(20)の濾過速度が早期に低下することを防ぐため、フィルタ(20)の前処理として、セパレータ(22)より分離精度が高くフィルタ(20)より濾過精度が低いストレーナ(21)を配置できる。
【0023】
前記洗浄材及び洗浄装置を用いた本発明による反応容器(1)の洗浄法は、溶媒(3)50〜90重量部と、溶媒(3)に溶解しない最大長さ0.1〜50mmの固形物質(4)10〜50重量部とからなる洗浄材を反応容器(1)に充填する。固形物質(4)が10重量部未満であると、固形物質(4)と反応容器(1)の内壁面(1a)との衝突回数が減り、付着性樹脂(9)の剥離性が低下する。固形物質(4)が50重量部を超えると、固形物質(4)の流動速度が遅くなり、固形物質(4)が激しく内壁面(1a)に衝突しないので剥離性が低下する。溶媒(3)は、有機溶媒の混合液、特に、洗浄力を強化するためメタノール等の貧溶媒を含む混合溶媒(3)を用いてもよい。
【0024】
次に、反応容器(1)に充填された洗浄材を図1に示すように撹拌機(2)で撹拌して流動させる。これにより、反応容器(1)の内壁面(1a)に固着する付着性樹脂(9)を溶媒(3)により溶解、浸透及び膨潤させ、溶媒(3)と共に流動する固形物質(4)を反応容器の内壁面(1a)に衝突させて、膨潤した付着性樹脂(9)を物理的に剥離する。撹拌終了後、洗浄材と共に、溶解及び剥離された付着性樹脂(9)を反応容器(1)から除去する。
【0025】
本発明では、洗浄に使用された洗浄材を反応容器(1)から回収する工程と、回収された洗浄材から固形物質(4)を分離する工程と、分離された固形物質(4)と溶媒(3)とを反応容器(1)に供給する工程と、反応容器(1)で洗浄材を流動させる工程とを含んでもよい。また、洗浄に使用された洗浄材を濾過して付着性樹脂(9)を除去する工程と、溶媒(3)及び固形物質(4)を混合して洗浄材を調整及び再生する工程と、再生された洗浄材を再使用する工程とを含んでもよい。
【0026】
【実施例】
溶剤型アクリル樹脂重合反応容器の洗浄に適用した本発明による洗浄材及び洗浄装置を用いた洗浄法の例を説明する。
【0027】
図3に示す反応容器(1)で重合されたアクリル樹脂を反応容器(1)から取り出した後、反応容器(1)の内壁面(1a)に付着したアクリル樹脂(9)を除去するため、前段階として良溶媒であるトルエンで還流洗浄を行った。還流洗浄の方法は前記の通りである。その後、混合溶媒(3)及び固形物質(4)を含む洗浄材を使用して、反応容器(1)の洗浄を行ったが、混合溶媒(3)5100kgの組成は、酢酸エチル50重量%、イソプロピルアルコール25重量%、メタノール25重量%であり、円柱形(直径3mm×高さ2mm)のポリエチレン樹脂を固形物質(4)として900kg使用した。
【0028】
前記混合溶媒(3)では、酢酸エチルが良溶媒であり、イソプロピルアルコール及びメタノールが貧溶媒である。円柱形の固形物質を使用するのは、長い棒状に射出成形されたポリエチレン樹脂を適度な大きさで切断するのみで使用でき、内壁面(1a)に付着したアクリル樹脂(9)の掻き取り性が良好だからである。本発明による洗浄材を用いて反応容器(1)を洗浄する頻度は、アクリル樹脂(9)の付着量により異なるが、本実施例では重合反応30回に1回行った。
【0029】
洗浄の際に、図3に示す6000Lの反応容器(1)へ5100kgの混合溶媒(3)を溶媒槽(5)から溶媒ポンプ(23)で供給すると同時に、900kgの固形物質(4)をバケット槽(6)からフィーダ(7)で反応容器(1)へ供給した。混合溶媒(3)は、反応容器(1)内の上部リング(8)のノズル(8a)から、シャワー状に噴射され反応容器(1)内に充填された。次に、充填された洗浄材の温度を50℃に保持し、図1に示すように洗浄材を撹拌機(2)で撹拌した。これにより、内壁面(1a)に付着したアクリル樹脂(9)を溶媒(3)で溶解除去すると同時に、溶解では除去されずに残存したアクリル樹脂(9)を固形物質(4)の衝突により内壁面(1a)から剥離させた。撹拌は、20〜80rpmの速度で5〜8時間行われ、固形物質(4)が効率よく内壁面(1a)に衝突するように、そのうち半分の時間は逆回転させた。撹拌終了前に温度を30℃、撹拌速度を20rpmにして撹拌を終了した。
【0030】
撹拌終了後、弁(11)を開き、固形物質(4)及び剥離されたアクリル樹脂(9)を含む混合溶媒(3)を反応容器(1)からバケット槽(6)に抜き取り、混合溶媒(3)は、セパレータ(22)開口部を通過して、バケット槽(6)と共に珪藻土投入槽(10)にも貯えらた。珪藻土投入槽(10)の混合溶媒(3)は、弁(15)及び(13)が開いた状態で循環ポンプ(24)により反応容器(1)に戻された。この循環を30〜40分間行い、反応容器(1)内の固形物質(4)がほぼ抜き取られた段階で、珪藻土投入槽(10)に珪藻土2kgを投入した。これと同時に、弁(11)及び(13)を閉じ、弁(14)を開いて珪藻土を循環ポンプ(24)でフィルタ(20)にプレコートした。珪藻土投入槽(10)に珪藻土を含む混合溶媒(3)がほぼ無くなったとき、更に4kgの珪藻土を図示しない投入口から反応容器(1)に投入して、弁(12)を開き、弁(15)を閉じて、フィルタ(20)にプレコートした。これにより、反応容器(1)、ストレーナ(21)、循環ポンプ(24)、フィルタ(20)及び反応容器(1)の経路で混合溶媒(3)を再び循環させた。このとき、混合溶媒(3)に含まれる粒径の大きなアクリル樹脂(9)はストレーナ(21)で分離され、粒径の小さなアクリル樹脂(9)はフィルタ(20)で濾過されるので、循環される混合溶媒(3)は常に、浄化された状態で反応容器(1)に供給できる。混合溶媒(3)による循環を90分間行った後、弁(16)を閉じ、弁(17)を開いて、混合溶媒(3)を溶媒槽(5)に戻した。混合溶媒(3)は、珪藻土がプレコートされたフィルタ(20)により高精度な濾過が行われるので、溶媒としての性能は劣化せず、不足分を補充する以外は、4〜5年に1回交換すればよい。また、固形物質(4)も再利用が可能であり、1年間に5%程度の補充量で足りる。最後にトルエンで反応容器(1)内を濯ぐことにより、反応容器(1)の洗浄が終了した。
【0031】
洗浄終了後、反応容器(1)内の観察を行い、本発明による洗浄前の状態と比較した。洗浄前の肉眼及び指触による内壁面(1a)の状態は、全面に付着性樹脂(9)が0.1〜1.0mmの厚さで固着し、ザラザラ感があり、視感光沢状態はつや消し状態であったが、洗浄後の肉眼及び指触による内壁面(1a)の状態は、全面に付着性樹脂(9)の固着が無く、スベスベ感があり、視感光沢状態は金属鏡面光沢があった。本発明による洗浄後の内壁面(1a)は、全面に付着性樹脂(9)が無く、光沢を有する状態にまで洗浄されるので、本発明による洗浄材を使用して反応容器(1)の内壁面(1a)を洗浄することにより、付着性樹脂(9)を完全に除去できることが確認できた。
【0032】
本実施例では以下の作用効果が得られる。
[1] 良溶媒及び貧溶媒の混合溶媒(3)による溶解、浸透及び膨潤と、固形物質(4)による剥離との相乗効果で、反応容器(1)内の付着性樹脂(9)をほぼ完全に除去できる。
[2] 付着性樹脂(9)除去後の反応容器(1)の内壁面(1a)には、不純物が付着しないので、次の反応生成物の反応収率及び品質を向上できる。
[3] 反応容器(1)内で作業員が剥離作業を行う必要が無いので、作業環境が向上する。
[4] 従来2日間に亘る洗浄作業を12時間程度に短縮することができ、反応容器(1)の洗浄時間を短縮し、稼働率を向上できる。
[5] 溶媒代及び人件費を節約できるので、洗浄コストを大幅に低減できる。
【0033】
【発明の効果】
前記のように本発明では、付着性樹脂を短時間で確実に除去して、洗浄効率及び製品の品質を向上すると共に、洗浄コストの低減を図ることができる。
【図面の簡単な説明】
【図1】 本発明による洗浄材により反応容器内を洗浄する状態を示す概略図
【図2】 図1に示す反応容器の内壁面の拡大図
【図3】 本発明による洗浄材により反応容器内を洗浄するフロー図
【符号の説明】
(1)・・反応容器、 (1a)・・表面(内壁面)、 (2)・・撹拌機、 (2a)・・シャフト、 (2b)・・撹拌翼、 (2C)・・モータ、 (3)・・溶媒(混合溶媒)、 (4)・・固形物質、 (5)・・収容槽(溶媒槽)、 (6)・・収容槽(バケット槽)、 (7)・・フィーダ、 (8)・・上部リング、 (8a)・・ノズル、 (9)・・付着性樹脂(アクリル樹脂)、 (10)・・珪藻土投入槽、 (11)〜(17)・・弁、 (20)・・フィルタ、 (20a)・・濾板、 (21)・・ストレーナ、 (22)・・セパレータ、 (23)・・溶媒ポンプ、 (24)・・循環ポンプ、[0001]
BACKGROUND OF THE INVENTION
The present invention belongs to the field of cleaning techniques, in particular, a method and apparatus for cleaning a chemical reaction vessel and a cleaning material capable of removing adhesive resin adhered to the surface to be cleaned in a short time.
[0002]
[Prior art]
Conventionally, when cleaning a surface to which an adhesive resin having low adhesiveness is fixed, a cleaning method by spraying a solvent in which the adhesive resin is soluble or dipping in a solvent is used. For resins that adhere strongly, contact peeling method with a release agent, wiping method with a paste containing an abrasive, sand blasting to remove the adhesive resin, jet method with high pressure water, chemical etching with acid or alkali, hydrolysis Or a manual cutting method is used. These techniques require a long time for cleaning and involve damage to the surface to be cleaned. In addition, since a solvent that adversely affects the human body and the environment is used, further washing is required to prevent the solvent from remaining after washing. In particular, cleaning of reaction vessels and jigs used when manufacturing products with chemical reactions consumes a large amount of solvent and requires a long time for cleaning, so the ratio of cleaning costs to the product price is high. It is.
[0003]
For example, in a reactor used for the production of paints, inks, adhesives, synthetic resins, etc. by polycondensation reaction, the adhesive resin remains on the inner surface of the reaction vessel after the reaction product is taken out from the reaction vessel. That cannot be avoided. The remaining adhesive resin is difficult to remove, but if it is not completely removed, when another type of polymerization reaction is carried out in the reaction vessel, the reaction product and the adhesive resin are mixed, leading to a reduction in product quality. In addition, if a large amount of adhesive resin adheres to a coil or the like that performs temperature control by a polymerization reaction, the overall heat transfer coefficient decreases, and sufficient temperature control becomes difficult.
[0004]
For this reason, the conventional standard washing method uses a solvent that is soluble in the adhesive resin and performs reflux washing every time the polymerization reaction is completed. The reflux washing is performed by heating the solvent filled in the reaction vessel about half to a temperature near the boiling point, evaporating and condensing the solvent to wet the inner wall surface and dissolving the adhesive resin. The evaporated solvent is liquefied and collected in a condenser connected to the upper part of the reaction vessel, and returned to the reaction vessel. This reflux operation is repeated for 60 to 90 minutes. Adhesive resin that cannot be removed by reflux washing is ignored and the next polymerization reaction is performed. After repeated use in the polymerization reaction, washing with an alkaline solution is carried out for at least 16 hours, once every several polymerization reactions, depending on the amount of accumulated resin. Further, the resin is fixed by a human operation by a worker.
[0005]
The degree of resin adhesion varies depending on the polymerization method such as solution polymerization and emulsion polymerization, and also varies depending on the molecular weight of the resin to be produced, the tackiness, the reaction rate, the temperature control of heating by a rapid high-temperature heat source, and the like. In order to prevent resin adhesion, improvements have been made by surface treatment of reaction vessels, handling vessels and jigs, but they are incomplete in terms of temperature controllability and durability.
[0006]
The cleaning cost of the standard cleaning method reaches about 5 million yen / year in a 5000 L reaction vessel. This is because reflux cleaning, alkali cleaning, and stripping work take a long time, and the solvent used for the reflux cleaning cannot be regenerated and is discarded by combustion or discharged into the atmosphere. This is an essential problem in the chemical industry that causes not only costs but also environmental pollution, waste of resources and health hazards to workers.
[0007]
[Problems to be solved by the invention]
Accordingly, the present invention provides a cleaning method for a chemical reaction vessel, an apparatus therefor, and a cleaning material that can reliably remove the adhesive resin fixed to the surface of an object in a short time with a rational closed system that does not require human power. With the goal.
It is another object of the present invention to provide a chemical reaction vessel cleaning method and apparatus and a cleaning material for removing an adhesive resin safely and easily.
[0008]
[Means for Solving the Problems]
The technical idea of the present invention for solving the above problems is as follows:
[1] As an alternative to the conventional mechanical cutting method by human power, a solid substance that can physically attack the adhesive resin without damaging the surface to be cleaned is selected, and this is flowed to peel the adhesive resin. Let
[2] A conventional solvent is used as a dispersion medium for a solid substance, and is used in combination with reflux cleaning to smoothly dissolve, swell, and peel off.
[3] The cleaning method using the cleaning material according to the present invention is industrially easily and safely formed into a closed system.
[0009]
That is, the chemical reaction vessel cleaning method according to the present invention is a mixed solvent (3) 100 comprising a good solvent for dissolving and swelling the adhesive resin fixed to the surface to be cleaned and a poor solvent for curing the swollen adhesive resin. A step of filling the reaction vessel (1) with a cleaning material comprising 10 parts by weight of a solid substance having a maximum length of 0.1 to 50 mm that does not dissolve in the mixed solvent (3); (1) The step of flowing in and the adhesive resin (9) fixed to the inner wall surface (1a) of the reaction vessel (1) is dissolved, infiltrated and swollen with the mixed solvent (3) and together with the mixed solvent (3) The flowing solid substance (4) collided with the inner wall surface (1a) of the reaction vessel (1) to physically peel the swollen adhesive resin (9), and the dissolved and peeled together with the cleaning material. Removing the adhesive resin (9) from the reaction vessel (1).
[0010]
The chemical reaction container cleaning apparatus according to the present invention cleans and removes the adhesive resin (9) fixed to the inner wall surface (1a) of the reaction container (1) from the inner wall surface (1a) by a chemical reaction. In the present invention, a mixed solvent (3) composed of a good solvent for dissolving and swelling the adhesive resin (9) and a poor solvent for curing the swollen adhesive resin, and a solid that physically separates the adhesive resin (9). Adhesive resin (9) swollen by supplying a supply device (23, 7) for supplying the substance (4) to the reaction vessel (1) and a cleaning material containing the mixed solvent (3) and the solid substance (4). A stirrer (2) for causing the solid substance (4) to collide with the separator, a separator (22) for separating the cleaning material used for washing into the mixed solvent (3) and the solid substance (4), and the separated mixed solvent A filter (20) for removing the adhesive resin (9) from (3) to purify the mixed solvent (3), and a storage tank for storing the purified mixed solvent (3) and the separated solid substance (4) (5, 6).
[0011]
The cleaning material according to the present invention comprises a good solvent for dissolving and swelling the adhesive resin (9) fixed to the surface (1a) to be cleaned, a poor solvent for curing the swollen adhesive resin, and the surface (1a) to be cleaned. ) And a solid substance (4) that physically peels off the adhesive resin (9). As used herein, the term “good solvent” refers to a solvent that has a high ability to dissolve solutes. The term “poor solvent” refers to a solvent having a small ability to dissolve a solute. Since the adhesive resin (9) is dissolved and removed with a good solvent, the adhesive resin (9) firmly adhered to the surface of the object is swollen and collided with the solid substance (4) to physically peel off. The adhesive resin (9) fixed to the surface (1a) can be reliably and automatically removed. Therefore, it is possible to remove not only a soluble resin that can be removed with a good solvent but also a resin that is insoluble in a good solvent without the operator performing scraping work.
[0012]
DETAILED DESCRIPTION OF THE INVENTION
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of a chemical reaction vessel cleaning method and apparatus and cleaning material according to the present invention will be described below with reference to FIGS.
[0013]
The cleaning material according to the present invention comprises a solvent (3) that dissolves and swells the adhesive resin (9) fixed to the surface (1a) to be cleaned, and the adhesive resin (9) that collides with the surface (1a) to be cleaned. And a solid substance (4) that physically exfoliates. Solvent (3) is a good solvent, esters such as ethyl acetate and butyl acetate, ketones such as acetone, methyl ethyl ketone and methyl isobutyl ketone, halides such as trichloroethylene and carbon tetrachloride, aromatic hydrocarbons such as toluene and xylene, One or more of alcohols such as isopropyl alcohol, alkalis such as sodium hydroxide, and water. If necessary, organic amino compounds such as dimethylaminoethanol, diethylaminoethanol and triethylamine, organic acids such as acetic acid, surfactants and ammonia can also be used. Furthermore, a low molecular weight acrylic resin, polyester resin and vinyl chloride resin may be added to the solvent (3) in order to adjust the viscosity of the solvent (3) and promote dissolution of the adhesive resin (9).
[0014]
The solid substance (4) is a solid resin having a cylindrical shape, a spherical shape, a polyhedral shape, a confetti shape or a tetrapod shape, and has a maximum length of 0.1 to 50 mm. When the maximum length of the solid substance (4) is less than 0.1 mm, the solid substance (9) is separated when the separated adhesive resin (9) is separated to reuse the solvent (3) and the solid substance (4). It becomes difficult to completely separate 4) and the adhesive resin (9). If the maximum length of the solid substance (4) exceeds 50 mm, the number of collisions between the reaction container (1), which is the surface (1a) to be cleaned, and the inner wall surface (1a) of the pipe, and the solid substance (4) decreases. The peelability of the adhesive resin (9) fixed to the inner wall surface (1a) is lowered. If the thickness exceeds 50 mm, solid substances (not shown) in the concavo-convex portions in the reaction vessel (1), for example, the gaps between the concavo-convex portions (not shown) at the connection point between the shaft (2a) of the stirrer (2) and the stirring blade (2b). 4) will not enter and dead space that cannot collide will increase.
[0015]
The solid material (4) may be any material that is insoluble in the solvent (3) and softer than the inner wall surface (1a), and gives an appropriate impact to the adhesive resin (9) fixed to the inner wall surface (1a). A material having an impact strength of 20 to 220 J / m is preferable. Polyolefin resin, polyester resin, phenol resin, melamine resin, urea resin, epoxy resin, silicone resin or fluororesin can be used, among which polyethylene, polypropylene, polyethylene terephthalate or polytetra- mer having high density, high heat resistance and strong mechanical strength Pellets such as fluoroethylene are preferred. The density of the solid substance (4) is 0.92 × 10 3 to 0.96 × 10 3 kg / m 3 for polyethylene and 0.85 × 10 3 to 0.92 × 10 3 kg for polypropylene. / m 3, in 1.37 × 10 3 ~1.38 × 10 3 kg /
[0016]
The relationship between the solvent (3) and the solid substance (4) is that 50 to 90 parts by weight of the solvent (3) and 10 to 50 parts by weight of the solid substance (4) are matched to the properties of the adhesive resin (9). Just choose. The density ratio of the solvent (3) and the solid substance (4) alone is 1: 0.9 to 1.4. If the density ratio of the solid substance (4) alone to the solvent (3) 1 is less than 0.9, the solid substance (4) floats in the solvent (3), and the lower part of the reaction vessel (1) The inner wall (1a) cannot be cleaned sufficiently. When the ratio of the density of the solid substance (4) alone to the solvent (3) 1 exceeds 1.4, the solid substance (4) settles in the solvent (3) and stays in the upper part of the reaction vessel (1). The wall (1a) cannot be cleaned sufficiently. In addition, the flow rate of the solid substance (4) becomes slow, and the impact force and the number of collisions with respect to the adhesive resin (9) are reduced. For the same reason, the density ratio of the mixed solvent (3) and the solid substance (4), which will be described later, is 1: 0.9 to 1.4.
[0017]
Since the adhesive resin (9) to be removed by the cleaning material according to the present invention is physically peeled off by the solid substance (4), the type of the adhesive resin (9) is not particularly limited. An effective effect is achieved by the production of acrylic resin, polyester resin, urethane resin, vinyl chloride resin, polystyrene or ABS resin widely used in the industry or the production of modified resin by a combination of these resins (reaction vessel ( 1) Resin fixed inside the pipe.
[0018]
In the embodiment of the present invention, a poor solvent for curing the adhesive resin (9) swollen by permeation is included. When the mixed solvent (3) containing a good solvent and a poor solvent is used, the detergency is further enhanced. That is, when the adhesive resin (9) is composed of a gel component and a sol component having a low molecular weight, the sol component dissolves well in a good solvent, but the gel component absorbs a large amount of good solvent and swells. The gel that swells after absorbing a large amount of good solvent maintains its state of adhering to the inner wall surface (1a) without eluting from the good solvent, increasing flexibility. It is difficult to mitigate the mechanical impact and scrape off the adhesive resin (9) from the inner wall surface (1a). On the other hand, a poor solvent having a small ability to dissolve a solute limits the amount of good solvent absorbed by the gel and hardens the swollen gel. As a result, the sol content is dissolved with a good solvent and the gel content is swollen, and after the swollen gel content is cured with a poor solvent, the adhesive resin ( 9) can be completely removed from the inner wall surface (1a). When the mixed solvent (3) is stirred with the stirrer (2) as shown in FIG. 1, the solid substance (4) collides with the adhesive resin (9) as shown in FIG. 2, and the adhesive resin (9) Can be completely peeled from the inner wall surface (1a) of the reaction vessel (1). The poor solvent is one or more of alcohol, petroleum ether, aliphatic hydrocarbon, and water.
[0019]
The combination of the good solvent and the poor solvent that are the mixed solvent (3) is determined by the adhesive resin (9). Adhesive resin (9) is a monomer having an ethylenically unsaturated double bond capable of emulsion polymerization, suspension polymerization and solution polymerization, such as vinyl chloride, vinyl acetate, styrene, methyl methacrylate, butyl acrylate, isooctyl acrylate Or when adhering to the inner wall surface (1a) by the polymerization reaction of acrylonitrile, one or more good solvents of ester, ketone, alkyl halide and aromatic hydrocarbon, alcohol, petroleum ether and aliphatic hydrocarbon One or more poor solvents are used. Polymerization reaction of a monomer whose adhesive resin (9) has a functional group having an ethylenically unsaturated double bond as a main component, for example, acrylic acid, methacrylic acid, 2-hydroxyethyl acrylate, acrylamide or N-methylolacrylamide When adhering to the inner wall surface (1a), one or more good solvents such as esters, ketones, alkyl halides, aromatic hydrocarbons, alcohols and water and petroleum ethers and aliphatic hydrocarbons or Two or more poor solvents are used. As described above, the good solvent and the poor solvent are determined by the chemical components of the adhesive resin (9), and there are solvents that can be either a good solvent or a poor solvent such as alcohol.
[0020]
The combination of the good solvent, the poor solvent and the solid substance (4) is, for example, a mixture of 20 to 70% by weight of an ester having a molecular weight of 100 or less which is a good solvent and 30 to 80% by weight of an alcohol having 1 to 6 carbon atoms which is a poor solvent. 100 parts by weight of the solvent (3) and 10 to 30 parts by weight of the solid substance (4) having a maximum length of 0.1 to 50 mm. If the ester having a molecular weight of 100 or less, which is a good solvent, is less than 20% by weight, dissolution of the sol contained in the adhesive resin (9) becomes insufficient, and the solubility does not change even if it exceeds 70% by weight. Further, if the alcohol having 1 to 6 carbon atoms, which is a poor solvent, is less than 30% by weight, the gel component swollen by the good solvent cannot be completely cured and the flexibility is maintained, so that the solid substance (4) It becomes difficult to physically peel off by colliding. Even if it exceeds 80% by weight, no further curing occurs. When the solid substance (4) of 0.1 to 50 mm is less than 10 parts by weight with respect to 100 parts by weight of the mixed solvent (3), the content of the solid substance (4) contained in the reaction vessel (1) is small, The number of collisions between the solid substance (4) and the inner wall surface (1a) of the reaction vessel (1) decreases, and the peelability of the adhesive resin (9) decreases. If it exceeds 30 parts by weight, the content of the solid substance (4) contained in the reaction vessel (1) is large and heavy, the flow rate of the solid substance (4) becomes slow, and the solid substance (4) becomes intense and the inner wall (1a) Since it does not collide with the film, the peelability is reduced.
[0021]
As shown in FIG. 3, the cleaning apparatus for cleaning the reaction vessel (1) using the cleaning material physically removes the solvent (3) and the adhesive resin (9) for dissolving and swelling the adhesive resin (9). The supply device (23, 7) for supplying the solid material (4) to be separated into the reaction vessel (1) and the cleaning material containing the solvent (3) and the solid material (4) are flowed as shown in FIG. A stirrer (2) for causing the solid substance (4) to collide with the swollen adhesive resin (9), and a separator (22) for separating the cleaning material used for washing into the solvent (3) and the solid substance (4). ), A filter (20) that purifies the solvent (3) by removing the adhesive resin (9) from the separated solvent (3), and the purified solvent (3) and the separated solid substance (4) Storage tanks (5, 6).
[0022]
The solvent pump (23), which is a supply device for the solvent (3), is connected between the solvent tank (5), which is a storage tank for the solvent (3), and the reaction vessel (1). 3) is supplied to the reaction vessel (1). The feeder (7), which is a supply device for the solid substance (4), is connected between the bucket tank (6), which is a storage tank for the solid substance (4), and the reaction vessel (1). Material (4) is fed to the reaction vessel (1). As shown in FIG. 1, the stirrer (2) includes a shaft (2a) to which a rotational motion is given from a motor (2c), a stirring blade (2b) connected to the shaft (2a), and a solvent (3 ) And solid material (4). The cleaning material after cleaning is accommodated in the bucket tank (6), and the solvent (3) and the solid substance are separated by a flat separator (22) formed between the bucket tank (6) and the diatomaceous earth charging tank (10). (4). The separator (22) is formed of a punching metal or a metal net having an opening on the entire surface so that the solid substance (4) cannot pass through. In the filter (20), filter paper is arranged on the outer surface or inner surface of a plurality of filter plates (20a) formed inside, and diatomaceous earth having a particle diameter of 3 to 5 μm is about 0.1% by weight of the solvent (3). Pre-coated as a filter aid. In addition, a circulation pump (24) for returning the solvent (3) purified by the filter (20) into the reaction vessel (1) and circulating between the filter (20) and the reaction vessel (1) is provided. Furthermore, in order to prevent the filtration rate of the filter (20) from decreasing early, as a pretreatment of the filter (20), the strainer (21) has higher separation accuracy than the separator (22) and lower filtration accuracy than the filter (20). Can be placed.
[0023]
The method of cleaning the reaction vessel (1) according to the present invention using the cleaning material and the cleaning apparatus is composed of 50 to 90 parts by weight of the solvent (3) and a solid having a maximum length of 0.1 to 50 mm that does not dissolve in the solvent (3). The reaction container (1) is filled with a cleaning material consisting of 10 to 50 parts by weight of the substance (4). When the solid substance (4) is less than 10 parts by weight, the number of collisions between the solid substance (4) and the inner wall surface (1a) of the reaction vessel (1) is reduced, and the peelability of the adhesive resin (9) is lowered. . When the solid substance (4) exceeds 50 parts by weight, the flow rate of the solid substance (4) becomes slow, and the solid substance (4) does not collide with the inner wall surface (1a) violently, so that the peelability is lowered. As the solvent (3), a mixed solution of an organic solvent, particularly a mixed solvent (3) containing a poor solvent such as methanol may be used in order to enhance the detergency.
[0024]
Next, the cleaning material filled in the reaction vessel (1) is stirred and fluidized with a stirrer (2) as shown in FIG. As a result, the adhesive resin (9) adhering to the inner wall surface (1a) of the reaction vessel (1) is dissolved, infiltrated and swelled by the solvent (3), and the solid substance (4) flowing together with the solvent (3) is reacted. The swollen adhesive resin (9) is physically peeled by colliding with the inner wall surface (1a) of the container. After completion of the stirring, the adhesive resin (9) dissolved and peeled off together with the cleaning material is removed from the reaction vessel (1).
[0025]
In the present invention, the step of recovering the cleaning material used for cleaning from the reaction vessel (1), the step of separating the solid material (4) from the recovered cleaning material, the separated solid material (4) and the solvent (3) may be supplied to the reaction vessel (1), and a step of flowing the cleaning material in the reaction vessel (1) may be included. In addition, the cleaning material used for cleaning is filtered to remove the adhesive resin (9), the solvent (3) and the solid substance (4) are mixed to adjust and regenerate the cleaning material, and the regeneration Reusing the cleaned cleaning material.
[0026]
【Example】
An example of the cleaning method using the cleaning material and the cleaning apparatus according to the present invention applied to the cleaning of the solvent type acrylic resin polymerization reaction vessel will be described.
[0027]
After removing the acrylic resin polymerized in the reaction vessel (1) shown in FIG. 3 from the reaction vessel (1), the acrylic resin (9) adhering to the inner wall surface (1a) of the reaction vessel (1) is removed. As a previous step, reflux washing was performed with toluene as a good solvent. The method of reflux cleaning is as described above. Thereafter, the reaction vessel (1) was cleaned using a cleaning material containing the mixed solvent (3) and the solid substance (4). The composition of the mixed solvent (3) 5100 kg was 50% by weight of ethyl acetate, 900 kg of a solid (4) polyethylene resin having 25% by weight of isopropyl alcohol and 25% by weight of methanol and having a cylindrical shape (
[0028]
In the mixed solvent (3), ethyl acetate is a good solvent, and isopropyl alcohol and methanol are poor solvents. The cylindrical solid material can be used by simply cutting polyethylene resin that has been injection-molded into a long rod shape with an appropriate size, and scraping properties of acrylic resin (9) attached to the inner wall surface (1a) Is good. The frequency of washing the reaction vessel (1) with the cleaning material according to the present invention varies depending on the amount of the acrylic resin (9) attached, but in this example, it was carried out once every 30 polymerization reactions.
[0029]
At the time of washing, 5100 kg of the mixed solvent (3) is supplied from the solvent tank (5) by the solvent pump (23) to the 6000 L reaction vessel (1) shown in FIG. The reaction vessel (1) was supplied from the tank (6) by the feeder (7). The mixed solvent (3) was sprayed in a shower from the nozzle (8a) of the upper ring (8) in the reaction vessel (1) and filled into the reaction vessel (1). Next, the temperature of the filled cleaning material was maintained at 50 ° C., and the cleaning material was stirred with a stirrer (2) as shown in FIG. As a result, the acrylic resin (9) adhering to the inner wall surface (1a) is dissolved and removed by the solvent (3), and at the same time, the remaining acrylic resin (9) that has not been removed by dissolution is collided with the solid substance (4). It peeled from the wall surface (1a). Stirring was performed at a speed of 20 to 80 rpm for 5 to 8 hours, and half of the time was reversed so that the solid substance (4) collided with the inner wall surface (1a) efficiently. Stirring was completed by setting the temperature to 30 ° C. and the stirring speed to 20 rpm before the stirring was completed.
[0030]
After the stirring, the valve (11) is opened, the mixed solvent (3) containing the solid substance (4) and the peeled acrylic resin (9) is extracted from the reaction vessel (1) into the bucket tank (6), and the mixed solvent ( 3) passed through the opening of the separator (22) and was stored in the diatomaceous earth charging tank (10) together with the bucket tank (6). The mixed solvent (3) in the diatomite charging tank (10) was returned to the reaction vessel (1) by the circulation pump (24) with the valves (15) and (13) opened. This circulation was performed for 30 to 40 minutes, and 2 kg of diatomaceous earth was charged into the diatomaceous earth charging tank (10) when the solid substance (4) in the reaction vessel (1) was almost extracted. At the same time, the valves (11) and (13) were closed, the valve (14) was opened, and diatomaceous earth was precoated on the filter (20) with the circulation pump (24). When the mixed solvent (3) containing diatomaceous earth almost disappeared in the diatomaceous earth charging tank (10), 4 kg of diatomaceous earth was further introduced into the reaction vessel (1) from the inlet (not shown), the valve (12) was opened, the valve ( 15) was closed and the filter (20) was precoated. Thereby, the mixed solvent (3) was circulated again through the paths of the reaction vessel (1), the strainer (21), the circulation pump (24), the filter (20), and the reaction vessel (1). At this time, the acrylic resin (9) having a large particle size contained in the mixed solvent (3) is separated by the strainer (21), and the acrylic resin (9) having a small particle size is filtered by the filter (20). The mixed solvent (3) can always be supplied to the reaction vessel (1) in a purified state. After circulating with the mixed solvent (3) for 90 minutes, the valve (16) was closed, the valve (17) was opened, and the mixed solvent (3) was returned to the solvent tank (5). The mixed solvent (3) is filtered with high accuracy by the filter (20) pre-coated with diatomaceous earth, so the performance as a solvent does not deteriorate, and every 4 to 5 years, except for replenishing the shortage. Replace it. The solid material (4) can also be reused, and a replenishment amount of about 5% per year is sufficient. Finally, the inside of the reaction vessel (1) was rinsed with toluene to complete the washing of the reaction vessel (1).
[0031]
After the completion of washing, the inside of the reaction vessel (1) was observed and compared with the state before washing according to the present invention. The state of the inner wall (1a) by the naked eye and finger touch before washing is that the adhesive resin (9) is fixed to the entire surface with a thickness of 0.1 to 1.0 mm, has a rough feeling, and the visual glossy state is Although it was in a frosted state, the state of the inner wall surface (1a) by the naked eye and the finger touch after washing has no sticking of the adhesive resin (9) on the entire surface, there is a smooth feeling, and the visual glossy state is a metallic mirror gloss was there. Since the inner wall surface (1a) after washing according to the present invention has no adhesive resin (9) on the entire surface and is washed to a glossy state, the cleaning material according to the present invention is used to clean the reaction vessel (1). It was confirmed that the adhesive resin (9) could be completely removed by washing the inner wall surface (1a).
[0032]
In this embodiment, the following effects can be obtained.
[1] Due to the synergistic effect of dissolution, permeation and swelling with the mixed solvent (3) of the good and poor solvents, and peeling with the solid substance (4), the adhesive resin (9) in the reaction vessel (1) is almost eliminated. Can be completely removed.
[2] Since impurities do not adhere to the inner wall surface (1a) of the reaction vessel (1) after removal of the adhesive resin (9), the reaction yield and quality of the next reaction product can be improved.
[3] Since the worker does not need to perform the peeling work in the reaction vessel (1), the working environment is improved.
[4] The conventional two-day cleaning operation can be shortened to about 12 hours, the cleaning time of the reaction vessel (1) can be shortened, and the operating rate can be improved.
[5] Since the solvent cost and labor cost can be saved, the cleaning cost can be greatly reduced.
[0033]
【The invention's effect】
As described above, in the present invention, the adhesive resin can be reliably removed in a short time to improve the cleaning efficiency and product quality, and to reduce the cleaning cost.
[Brief description of the drawings]
FIG. 1 is a schematic view showing a state in which a reaction vessel is cleaned with a cleaning material according to the present invention. FIG. 2 is an enlarged view of an inner wall surface of the reaction vessel shown in FIG. Flow diagram for cleaning [Explanation of symbols]
(1) ・ ・ Reaction vessel, (1a) ・ ・ Surface (inner wall surface), (2) ・ ・ Agitator, (2a) ・ ・ Shaft, (2b) ・ ・ Agitator blade, (2C) ・ ・ Motor, ( 3) ・ ・ Solvent (mixed solvent), (4) ・ ・ Solid material, (5) ・ ・ Container tank (solvent tank), (6) ・ ・ Container tank (bucket tank), (7) ・ ・ Feeder, ( 8) ・ ・ Upper ring, (8a) ・ ・ Nozzle, (9) ・ ・ Adhesive resin (acrylic resin), (10) ・ ・ Diatomite filling tank, (11) to (17) ・ ・ Valve, (20)・ ・ Filter, (20a) ・ ・ Filter plate, (21) ・ ・ Strainer, (22) ・ ・ Separator, (23) ・ ・ Solvent pump, (24) ・ ・ Circulating pump,
Claims (19)
洗浄材を反応容器内で流動させる工程と、
反応容器の内壁面に固着する付着性樹脂を混合溶媒により溶解、浸透及び膨潤させ且つ混合溶媒と共に流動する固形物質を反応容器の内壁面に衝突させて、膨潤した付着性樹脂を物理的に剥離する工程と、
洗浄材と共に、溶解及び剥離された付着性樹脂を反応容器から除去する工程とを含むことを特徴とする化学反応容器の洗浄法。100 parts by weight of a mixed solvent composed of a good solvent for dissolving and swelling the adhesive resin fixed to the surface to be cleaned and a poor solvent for curing the swollen adhesive resin, and a maximum length of 0.1 to 0.1 not dissolved in the mixed solvent Filling a reaction vessel with a cleaning material consisting of 10 to 30 parts by weight of a 50 mm solid substance;
Flowing the cleaning material in the reaction vessel;
Dissolve, permeate, and swell the adhesive resin that adheres to the inner wall surface of the reaction vessel with a mixed solvent, and collide the solid substance that flows with the mixed solvent against the inner wall surface of the reaction vessel to physically peel the swollen adhesive resin. And a process of
A method for cleaning a chemical reaction container, comprising a step of removing the dissolved and peeled adhesive resin from the reaction container together with the cleaning material.
回収された洗浄材から固形物質を分離する工程と、
分離された固形物質と混合溶媒とを反応容器に供給する工程と、
反応容器で洗浄材を流動させる工程とを含む請求項1に記載の化学反応容器の洗浄法。Recovering the cleaning material used for cleaning from the reaction vessel;
Separating the solid material from the recovered cleaning material;
Supplying the separated solid substance and the mixed solvent to the reaction vessel;
The method for cleaning a chemical reaction container according to claim 1, further comprising a step of flowing a cleaning material in the reaction container.
混合溶媒及び固形物質を混合して洗浄材を調整及び再生する工程と、
再生された洗浄材を再使用する工程とを含む請求項1に記載の化学反応容器の洗浄法。Filtering the cleaning material used for cleaning to remove the adhesive resin;
Adjusting and regenerating the cleaning material by mixing the mixed solvent and the solid substance;
The method for cleaning a chemical reaction container according to claim 1, further comprising a step of reusing the regenerated cleaning material.
付着性樹脂を溶解及び膨潤させる良溶媒と膨潤した付着性樹脂を硬化させる貧溶媒とからなる混合溶媒並びに付着性樹脂を物理的に剥離させる固形物質を反応容器に供給する供給装置と、
混合溶媒及び固形物質を含む洗浄材を流動させて、膨潤した付着性樹脂に固形物質を衝突させる撹拌機と、
洗浄に使用された洗浄材を混合溶媒と固形物質とに分離するセパレータと、
分離された混合溶媒から付着性樹脂を除去して混合溶媒を浄化するフィルタと、
浄化された混合溶媒及び分離された固形物質を収容する収容槽とを備えることを特徴とする化学反応容器の洗浄装置。In the chemical reaction container cleaning apparatus for cleaning and removing the adhesive resin fixed to the inner wall surface of the reaction container from the inner wall surface by a chemical reaction,
A supply device for supplying a reaction vessel with a mixed solvent composed of a good solvent for dissolving and swelling the adhesive resin and a poor solvent for curing the swollen adhesive resin, and a solid substance for physically peeling the adhesive resin;
A stirrer that causes a cleaning material containing a mixed solvent and a solid substance to flow and collides the solid substance with the swollen adhesive resin;
A separator that separates the cleaning material used for cleaning into a mixed solvent and a solid substance;
A filter that purifies the mixed solvent by removing the adhesive resin from the separated mixed solvent;
A cleaning apparatus for a chemical reaction container, comprising: a purified mixed solvent and a storage tank for storing a separated solid substance.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32374099A JP4283396B2 (en) | 1999-11-15 | 1999-11-15 | Cleaning method, cleaning device and cleaning material for chemical reaction vessel |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32374099A JP4283396B2 (en) | 1999-11-15 | 1999-11-15 | Cleaning method, cleaning device and cleaning material for chemical reaction vessel |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2001139604A JP2001139604A (en) | 2001-05-22 |
JP4283396B2 true JP4283396B2 (en) | 2009-06-24 |
Family
ID=18158096
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP32374099A Expired - Lifetime JP4283396B2 (en) | 1999-11-15 | 1999-11-15 | Cleaning method, cleaning device and cleaning material for chemical reaction vessel |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP4283396B2 (en) |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4702080B2 (en) * | 2005-03-29 | 2011-06-15 | 住友化学株式会社 | Cleaning method for equipment members |
US7253253B2 (en) * | 2005-04-01 | 2007-08-07 | Honeywell Federal Manufacturing & Technology, Llc | Method of removing contaminants from plastic resins |
JP4956086B2 (en) * | 2006-08-07 | 2012-06-20 | 三菱レイヨン株式会社 | Method for producing polymer and method for producing resist composition |
JP5037874B2 (en) * | 2006-08-07 | 2012-10-03 | 三菱レイヨン株式会社 | Method for producing resist polymer and method for producing resist composition |
JP5503835B2 (en) * | 2006-11-15 | 2014-05-28 | 東洋インキScホールディングス株式会社 | Cleaning liquid for pigment dispersion type colored resin composition |
JP5490774B2 (en) * | 2011-12-02 | 2014-05-14 | 花王株式会社 | Cleaning method for water-based pigment dispersion manufacturing apparatus |
CN106269735A (en) * | 2016-07-30 | 2017-01-04 | 淄博德信联邦化学工业有限公司 | The method for cleaning of reactor fouling |
CN110327859A (en) * | 2019-04-22 | 2019-10-15 | 广州市中潭空气净化科技有限公司 | It is a kind of for producing the reaction kettle with cleaning function of Corvic |
CN115069646B (en) * | 2022-07-21 | 2023-01-20 | 杭州诺华电子有限公司 | Electric fine cleaning device for medical instruments |
CN115889369B (en) * | 2023-02-24 | 2023-07-18 | 山西钢科碳材料有限公司 | Method for cleaning gel of acrylonitrile polymerization reaction kettle |
-
1999
- 1999-11-15 JP JP32374099A patent/JP4283396B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JP2001139604A (en) | 2001-05-22 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP4283396B2 (en) | Cleaning method, cleaning device and cleaning material for chemical reaction vessel | |
JP2003181400A (en) | Method for removing material from inner surface by using core/shell particle | |
CN115197794A (en) | Cleaning agent, cleaning method and cleaning machine for cleaning 3D printing component | |
NZ207073A (en) | Removing paint particles from gas stream by scrubbing | |
CN108746016A (en) | A kind of automobile die cycle high-efficiency washing device | |
JP2001294951A (en) | Method for recovering platinum from platimum containing film of gas turbine engine parts | |
JPH0663950A (en) | Treatment of painted plastic chip | |
CN109201606B (en) | Stripping and combining process for UV ink on surface of metal substrate | |
JP2012071217A (en) | Washing method for inside of coating material pipe | |
JP3200934B2 (en) | Paint film peeling method | |
CN109225097B (en) | Reaction kettle cleaning system and method | |
CN110252428A (en) | Multifunctional exchange resin regeneration washing column | |
JPH1157683A (en) | Method for treatment of optical disk waste and treating apparatus | |
CN109201607B (en) | Stripping and combining device for UV ink on surface of metal substrate | |
JPH10202138A (en) | Washing method for reaction vessel | |
CN212216368U (en) | Circuit board surface cleaning device for copper plating of circuit board | |
JPH07331138A (en) | Method and apparatus for removing coating film from resin article | |
JP2005170982A (en) | Method for removing polymer scale of vinyl polymer | |
JPH11241194A (en) | Method for washing apparatus deposited with heavy hydrocarbon based sludge and piping structure for washing | |
CN219132885U (en) | A salt washing device for regenerating plastic granules | |
CN214078152U (en) | Novel paint removing device | |
WO2019078279A1 (en) | Coating film removal method and coating film removal device for coated plastics | |
JP2015077541A (en) | Coating film removal method and coating film removal device | |
WO2024125746A1 (en) | Method of treating ancillary articles used in manufacture of epoxy polymer containing item | |
JPH1161470A (en) | Cleaning of equipment fouled with heavy hydrocarbon-based sludge stuck thereto |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20060609 |
|
A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20080804 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20080818 |
|
A521 | Written amendment |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20081014 |
|
TRDD | Decision of grant or rejection written | ||
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20090302 |
|
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 |
|
A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20090319 |
|
R150 | Certificate of patent or registration of utility model |
Ref document number: 4283396 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20120327 Year of fee payment: 3 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130327 Year of fee payment: 4 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20140327 Year of fee payment: 5 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
EXPY | Cancellation because of completion of term |