JP4612163B2 - Cleaning method and cleaning apparatus - Google Patents

Cleaning method and cleaning apparatus Download PDF

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Publication number
JP4612163B2
JP4612163B2 JP2000245958A JP2000245958A JP4612163B2 JP 4612163 B2 JP4612163 B2 JP 4612163B2 JP 2000245958 A JP2000245958 A JP 2000245958A JP 2000245958 A JP2000245958 A JP 2000245958A JP 4612163 B2 JP4612163 B2 JP 4612163B2
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Japan
Prior art keywords
cleaning
cleaned
chamber
cleaning liquid
liquid
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JP2000245958A
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Japanese (ja)
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JP2002059093A (en
Inventor
賢一 田辺
英稔 安藤
暢之 森
昇 平本
竹志 戸谷
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Subaru Corp
IHI Machinery and Furnace Co Ltd
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Fuji Jukogyo KK
IHI Machinery and Furnace Co Ltd
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Description

【0001】
【発明の属する技術分野】
本発明は、比較的低温で洗浄する必要のある被洗浄体、例えばハニカムコア単体および片側面に板材を接着したハニカムコアを、ノルマルパラフィン洗浄液を使用して洗浄する洗浄方法および洗浄装置に関する。
【0002】
【従来技術】
ハニカムサンドイッチ構造体は重量に比して機械的強度が大きいという特性を有することから、ハニカムコアの両面に板材を接着したハニカムサンドイッチパネルは、軽量かつ高剛性が要求される航空機や人工衛星等の構造材等に広く応用されている。
【0003】
ハニカムコアの材質としては、アルミニウム合金、マグネシウム、チタン等の非鉄金属が多く採用されており、ハニカムコアは、これらの金属を箔状にし、この箔を部分的に接着し、これを6角セル型や4角セル型等に展張して製造するものであり、接着部分(ノードボンド)を有するのが構造の特徴である。また、ハニカムサンドイッチパネルは、ハニカムコア片側面の切削加工、切削加工面への板材の接着、ハニカムコア他側面の切削加工、切削加工面への板材の接着の各工程によって製造し、ハニカムコアと板材との間は硬化エポキシ系フィルム接着剤を用いて接着する。
【0004】
ハニカムコアと板材との接着性能および接着耐久性は、ハニカムサンドイッチパネルを航空機の構造材等として一次接着または二次接着して用いた後の構造材等全体の機械的強度および耐久性に著しい影響を及ぼすため、接着前に板材、ハニカムコア単体および片側面に板材を接着したハニカムコアそれぞれを十分に洗浄する必要がある。
【0005】
ハニカムコアの接着前洗浄にあたっては、従来トリクロルエタンおよびトリクロルエチレンのような塩素系溶剤による蒸気脱脂が行われてきた。しかし、トリクロルエタンは、日本においては成層圏のオゾン層保護に関するモントリオール議定書が1988年9月30日に採択されて1996年から生産輸入および使用が禁止されており、もはや洗浄に用いることはできない。また、トリクロルエチレンについては、大気汚染防止法の規制はないものの、作業者の健康障害および環境汚染を懸念して規制強化の方向で取り組まれている。上記塩素系溶剤の代替洗浄剤であるフッ素系溶剤(HCFC:水素、塩素、フッ素、炭素化合物)も2020年までには全廃されることが決まっており、従来の洗浄法に変わる環境に配慮した洗浄法の検討が急務となっている。
【0006】
これに対し、特開平9−71883号公報には、アルカリ塩類や界面活性剤を主成分とする水溶液を用いる水系脱脂法は、ノードボンドの強度が接着剤吸湿により低下し、アルカリ塩類および水分がコア内部に滞留することにより製造期間中または運用期間中に腐食損傷が発生するため不適当であり、また、炭化水素系の溶剤(N−メチル−2−ピロリドン、ノルマルパラフィン系、イソパラフィン系、ナフテン系)、準水系(アルコールを主体とし、水および界面活性剤を含有した溶液)、ハロゲン化物、アルコール類、ケトン類について広く検討したところ、添加剤を含有しないノルマルパラフィン洗浄剤がハニカムコアの洗浄に適していることが開示されている。
【0007】
【発明が解決しようとする課題】
一方、多様なセル形状、セルサイズ、および厚みを有するハニカムコア単体および片側面に板材を接着したハニカムコアに関し、十分に洗浄するためには、セルの開放端を下方に向けて洗浄液を下方から供給して洗浄するのが有効であると考えられる。また、セル奥部まで充分に洗浄液が行き渡るようにしなければハニカムコア切削時等に付着した汚染物質が残存する結果となり、ハニカムサンドイッチパネル組上げ時の十分な接着強度および接着耐久性の確保が困難になると懸念される。
【0008】
そこで、本発明の目的は、作業者の健康障害および環境汚染に関して問題のないノルマルパラフィン洗浄液を用いて、ハニカムコア単体および片側面に板材を接着したハニカムコアを清浄かつ十分に洗浄し、さらに、例えばマグネシウムやチタン等の非鉄金属のように熱による焼けを嫌う被洗浄体や液層への浸漬を好まない被洗浄体の洗浄にも適用可能な洗浄方法および洗浄装置を提供することである。
【0009】
【課題を解決するための手段】
上記の課題を達成するための請求項1に記載の発明は、被洗浄体を洗浄室内に配置する被洗浄体配置工程と、前記洗浄室内の気圧を0.27〜4.00kPaの範囲に、かつ、被洗浄体の温度を70〜85℃の範囲に保ちながらノルマルパラフィン洗浄液を下方から噴出させて被洗浄体を洗浄する洗浄工程と、前記洗浄室内の気圧を1.33kPa以下の範囲に、かつ、被洗浄体の温度を70〜85℃の範囲に保ちながら被洗浄体を乾燥する乾燥工程と、を含み、前記洗浄工程が、ノルマルパラフィン洗浄液を洗浄室内の下部に配置した洗浄液貯蔵部に導入した後、洗浄室内の気圧を0.27〜1.33kPaの範囲に保ちながら洗浄液を沸騰させる洗浄液沸騰工程と、前記洗浄室内の気圧を1.33〜4.00kPaの範囲に保ちながら不活性ガスを洗浄液が押し上げられるように洗浄液中に送り込む不活性ガス供給工程と、のうちの少なくとも一方の工程により、被洗浄体の下方から洗浄液を吹き付けて被洗浄体を洗浄する工程であることを特徴とする。
【0010】
請求項1に記載の洗浄方法によれば、洗浄および乾燥工程を通じて被洗浄体の温度が70〜85℃の温度範囲に保たれるので、熱による焼けを嫌う非鉄金属でも安心して洗浄することができる。また、洗浄工程では、洗浄室の気圧が0.27〜4.00kPaの範囲にある低圧条件下において、洗浄液沸騰工程によれば、ノルマルパラフィン洗浄液が被洗浄体の下部から多方向に吹き付けられるので、霧状のノルマルパラフィン粒子が複雑形状を持つ被洗浄体の奥部まで到達し、良好に洗浄することができる。不活性ガス供給工程によれば、洗浄室の気圧が1.33〜4.00kPaである低圧条件において不活性ガスによりノルマルパラフィン洗浄液が被洗浄体の下部から垂直方向に吹き付けられるので、霧状のノルマルパラフィン粒子が不活性ガスの圧力により勢いよく被洗浄体の奥部まで到達し、一般的な蒸気脱脂の効果があまり期待できない熱容量の小さい被洗浄体でも清浄な洗浄を達成することができ、液層への浸漬を好まない被洗浄体についても洗浄を行うことができる。
【0011】
請求項2に記載の発明は、請求項1における被洗浄体がハニカムコア単体または片側面に板材を接着したハニカムコアであり、前記被洗浄体配置工程においてハニカムコアのセルの開放端を下方に向けて水平に洗浄室内に配置することを特徴とする。この洗浄方法によれば、洗浄および乾燥工程を通じてハニカムコアの温度が70〜85℃の温度範囲に保たれるので、ハニカムコアと板材との接着部の接着強度劣化を防止することができ、またハニカムコアの開放端が下方に向いているので、下方から霧状のノルマルパラフィン粒子が供給され、また洗浄後の汚染洗浄液が下方に落下するため、複雑形状を持つ片側面に板材を接着したハニカムコアの奥部まで清浄に洗浄することができる。
【0012】
請求項3に記載の発明は、前記洗浄工程において、被洗浄体を水平方向に揺動させることを特徴とする。この洗浄方法によれば、被洗浄体の奥部、細部に至るまで死角なくノルマルパラフィン粒子が供給されるため、洗浄を徹底的に行うことができる。
【0015】
請求項に記載の発明は、前記被洗浄体配置工程と洗浄工程の間に、洗浄室内の気圧を1.33〜4.00kPaに保ちながら、70〜85℃の温度範囲にあるノルマルパラフィン洗浄液の蒸気を洗浄室内に供給して被洗浄体を蒸気洗浄する一次蒸気脱脂工程を有することを特徴とする。この洗浄方法によれば、70〜85℃の温度範囲にある蒸気が洗浄室内に供給されるので、被洗浄体の加熱が可能になると共に、油分、切粉、粘着剤、埃等を浮き上がらせて洗浄することができ、さらに洗浄工程を行う際の被洗浄体の湿潤性を向上させることもできる。
【0016】
請求項に記載の発明は、前記洗浄工程と乾燥工程の間に、被洗浄体の下方からノルマルパラフィン洗浄液からなるシャワー液を供給して被洗浄体を洗浄する仕上げ洗浄工程と、洗浄室内の気圧を1.33〜4.00kPaの範囲に保ちながら70〜85℃の温度範囲にあるノルマルパラフィン洗浄液の蒸気を洗浄室内に供給して被洗浄体を蒸気洗浄する二次蒸気脱脂工程と、を有することを特徴とする。この洗浄方法によれば、仕上げ洗浄工程で清浄な洗浄液が被洗浄体の下部から供給されるので、充分な仕上げ洗浄が可能となり、二次蒸気脱脂工程では蒸気洗浄により液層への浸漬を好まない被洗浄体の仕上げ洗浄が可能になるとともに乾燥が促進される。
【0017】
請求項に記載の発明は、被洗浄体を内部配置する密閉可能な洗浄室と、洗浄液蒸気を洗浄室内に供給する洗浄液蒸気供給手段と、前記洗浄室内を真空吸引する真空吸引手段と、前記洗浄室内の下部に配置して前記被洗浄体の下方からシャワー液を供給するシャワー液供給手段と、前記洗浄室の前記シャワー液供給手段よりもさらに下部に配置した洗浄液貯蔵部と、前記洗浄液貯蔵部にノルマルパラフィン洗浄液を供給する洗浄液供給手段と、前記洗浄液貯蔵部の底部に配置して洗浄液を排出する洗浄液排出手段と、前記洗浄液貯蔵部に配置して不活性ガスを洗浄室内に供給する不活性ガス供給手段と、洗浄室内の温度を70〜85℃に調整する洗浄室温度調整手段と、を備前記不活性ガス供給手段は、前記真空吸引手段により前記洗浄室内の気圧が1.33〜4.00kPaの範囲に保たれた状態で、被洗浄体の下方から洗浄液を吹き付けて被洗浄体を洗浄するために、洗浄液が押し上げられるように洗浄液中に不活性ガスを送り込むことを特徴とする洗浄装置である。この洗浄装置によれば、請求項1に記載の洗浄方法を効果的に実施することができる。
【0018】
請求項7に記載の発明は、請求項7に記載の洗浄装置において、更に、前記洗浄室に内部配置した被洗浄体を水平方向に揺動させる揺動手段を備えることを特徴とする。この洗浄装置によれば、被洗浄体の奥部、細部に至るまで死角なくノルマルパラフィン粒子が供給されるため、洗浄を徹底的に行うことができる。
【0019】
請求項に記載の発明は、請求項またはに記載の洗浄装置において、更に蒸気発生室および洗浄液貯蔵室を含み、前記洗浄液貯蔵部内の洗浄液を蒸気発生室に導き蒸気を発生させ、発生させた蒸気を前記洗浄室内に導く流路系統と、蒸気発生室で発生させた蒸気を凝縮させて洗浄液貯蔵室に導き、洗浄液貯蔵室から洗浄液を前記シャワー液供給手段および洗浄液供給手段に導く流路系統と、を備えることを特徴とする。この洗浄装置によれば、洗浄液を他のタンク等へ移動することなく洗浄することができるため、洗浄時間を任意に設定することができる上に、被洗浄体が比較的大きいハニカムコアの洗浄においても洗浄剤の使用量を低減でき、周辺施設や管理コストの軽減をも図ることができる。
【0020】
【発明の実施の形態】
以下、本発明の実施の形態について、図面に基づいて説明する。
【0021】
図1は本洗浄方法を実施するための洗浄装置本体1の構成を示した断面図である。この洗浄装置本体1には、まず開閉扉2が設けられており、これを通じて被洗浄体の搬入搬出および洗浄室4の密閉および開放が行われるようになっている。また、洗浄室4は、外壁が二重構造となっており、2枚の外壁間は洗浄液蒸気の通路3になっている。蒸気通路3は、蒸気の熱によって洗浄室4の内部を加熱すると共に洗浄室4の内部からの熱の逃げすなわち放熱も防止して保温効果の高い洗浄室4を構成する温度調整手段として設けられている。洗浄室4の内部の加熱および温度制御は、他に温度調整手段としてのスチームヒーター(図示せず)によって行うことができるようにもなっている。
【0022】
さらに、洗浄室4には洗浄液蒸気供給手段として蒸気供給口5が設けられており、70〜85℃に加熱された洗浄液の蒸気が洗浄室4内に供給されるようになっている。また、洗浄室4には真空吸引手段として真空排気口6が設けられており、洗浄室4の内部が排気されて一定の気圧に保たれるようになっている。
【0023】
また、洗浄室4内には、ガイドローラー8および揺動手段としての揺動シリンダー9が設けられる。ガイドローラー8は被洗浄体15を搭載している搬送容器7を開閉扉2を通じて搬入搬出するためのものであり、揺動シリンダー9は搬送容器7を揺動させて、すなわち被洗浄体15を揺動させて洗浄効果を高めるためのものである。
【0024】
さらに、洗浄室4内には、上記の搬送容器設置部の下部に仕上げ洗浄に用いるシャワー液を供給するシャワー液供給手段であるシャワーノズル10が設けられている。本実施の形態では、シャワーノズル10は洗浄室4の上下方向を中心方向としたフルコーンノズルとしており、例えば長さが3820mm、幅が1600mmの有効洗浄範囲内でほぼ均一の流量密度を持つようにノズル配置されている。なお、フルコーンノズル以外のノズルを使用することもできる。
【0025】
また、シャワーノズル10の下部には、洗浄液を貯蔵する洗浄液貯蔵部であるドレインパン11が設けられており、ドレインパン11の上部11aは開放されている。ドレインパン11内には不活性ガスを供給する不活性ガス供給手段である噴射ノズル12が設けられている。本実施の形態では、噴射ノズル12は、配管の上側方向に設けた穿孔12aより不活性ガスが噴出する構造としており、例えば長さが3820mm、幅が1600mmの有効洗浄範囲内で洗浄液が上方側に不活性ガスによって垂直方向に吹き付けられるようになっている。洗浄液は、洗浄液供給手段である洗浄液供給口13からドレインパン11に供給され、洗浄液排出手段である洗浄液排出口14から排出されるようになっている。もっとも洗浄液の供給はシャワーノズル10を用いて行っても良い。また、本実施の形態では、不活性ガスによる洗浄液の吹き付けのための噴射ノズルを設けているが、別途噴霧ノズルを洗浄室4内の下方に設けて洗浄液を上方に向けて噴霧しても良い。
【0026】
図2は、本洗浄方法を実施するための洗浄装置全体の概要を示した図である。洗浄装置本体1の蒸気供給口5は蒸気通路3および蒸気供給管21を介して蒸気発生室22と接続されている。蒸気発生室22は使用済み洗浄剤の貯蔵室を兼ねており、洗浄液排出管23を介して洗浄液排出口14にも接続されている。蒸気発生室22の下部には洗浄液を加熱して蒸気を発生させるためのスチームヒーター24が設けられているが、スチームヒーター24は洗浄室4および洗浄液貯蔵室25等の加熱および温度制御も行うようになっている。蒸気発生室22には第1次のドレインタンクにあたる濃縮タンク26および第1の凝縮器27が接続されており、汚れや水分等の蒸留再生できない液のみを濃縮できるようになっており、濃縮液は廃液タンク28に送られるようになっている。
【0027】
蒸気発生器22は第2の凝縮器29を通して洗浄液貯蔵室25に接続されており、蒸留再生された清浄な洗浄液のみが洗浄液貯蔵室25に貯蔵されるようになっている。洗浄液貯蔵室25はシャワー液供給管30を通してシャワーノズル10と接続されており、また、洗浄液供給管31を通して洗浄液供給口13と接続されている。
【0028】
洗浄装置本体1の真空排気口6は、第3の凝縮器32を通して真空ポンプ33に接続されており、真空ポンプ33の出口側はさらにミストトラップ34に接続されている。また、第3の凝縮器32により凝縮された洗浄液は凝縮液タンク35に蓄えられ、蒸気発生室22に戻されるようになっている。
【0029】
上述のようにシャワーノズル10、洗浄液貯蔵室25、蒸気発生室22、およびドレインパン11を接続することにより、洗浄液を他のタンク等へ移動することなく洗浄することができるため、洗浄時間を任意に設定することができる。また、被洗浄体が比較的大きいハニカムコアの洗浄においても洗浄剤の使用量は1500リットルで済み、第3石油類の指定数量(2000リットル)の範囲内で管理できるため、周辺施設や管理コストの軽減を図ることができる。さらに、廃液タンク28やミストトラップ33を設けることにより、環境適合性の要求を満足することもできる。
【0030】
以下、図1、図2および図6に示す工程説明図を参照して洗浄方法および作用について説明する。
【0031】
まず、被洗浄体15を搬送容器7に搭載し、洗浄装置本体1の開閉扉2を開き、ガイドローラー8に沿って搬入して洗浄室4の中央に配置した後、開閉扉2を閉じて洗浄室4を密閉する。このとき、被洗浄体15として図3に示すような片側面に板材42を接着した6角セル型ハニカムコア41を洗浄する場合には、図4に示すような搬送容器であるバスケット43内に、ハニカムコア41の開放端を下に向けて収容し、シャワーノズル10の中央方向がハニカムコア41のセル軸方向に向くように配置する。洗浄を洗浄室4内で行うのは、引火点70℃のノルマルパラフィン洗浄液を用いて洗浄しても火災の恐れがなく、安全に洗浄を行うことができるからである。
【0032】
次に、図6(1)に示す一次蒸気脱脂工程S1を行う。この一次蒸気脱脂S1を行うには、まず、真空ポンプ33により真空排気口6を通して洗浄室4を真空吸引し、洗浄室4内を0.66kPa以下とする。次に、スチームヒーター24で炭素数11〜12を主体とするノルマルパラフィン洗浄液の入っている蒸気発生室22を70〜85℃に加熱し、発生した蒸気を蒸気供給管21を通して洗浄室4内に供給し、真空吸引して洗浄室4内の気圧を1.33〜4.00kPaに保ちながら、被洗浄体15を蒸気脱脂する。
【0033】
ここで、蒸気温度を70〜85℃の範囲にするのは、被洗浄体15を洗浄温度まで加熱して蒸気脱脂を行うのに十分な温度にするためであり、また、洗浄室4内の気圧を1.33〜4.00kPaとするのは、図5に示した本実施の形態において使用したノルマルパラフィン洗浄液の蒸気圧曲線からわかるように、蒸気濃度を十分にして蒸気脱脂効果を高めるためである。この一次蒸気脱脂S1により、油分(機械作動油等)、切粉(切削加工残渣)、粘着剤、埃等を浮きあがらせて蒸気洗浄を行うことができ、また洗浄工程の際における被洗浄体15の湿潤性の向上に寄与させることができる。
【0034】
次に、洗浄工程S2を行う。洗浄工程S2は、一般には、洗浄室4内を真空吸引して0.27〜4.00kPaの範囲に、被洗浄体15の温度を70〜85℃の範囲にそれぞれ保ちながらノルマルパラフィン洗浄液を被洗浄体15の下方から噴出させて行う。
【0035】
洗浄液の噴出は、ノルマルパラフィン洗浄液を洗浄室4内の下部に配置したドレインパン11に導入した後、洗浄室4内の気圧を0.27〜1.33kPaの範囲に保ちながら洗浄液を沸騰させる洗浄液沸騰工程S2aと、洗浄室4内の気圧を1.33〜4.00kPaの範囲に保ちながら不活性ガスを洗浄液が押し上げられるように洗浄液中に送り込む不活性ガス供給工程S2bと、のうちの少なくとも一方の工程により、被洗浄体15の下方から洗浄液を吹き付けて行うのが好適である。
【0036】
図6(2)に示す洗浄液沸騰工程S2aは、洗浄液供給口13から洗浄液貯蔵室25の洗浄液をドレインパン11に供給した後、蒸気通路3またはヒーターによる温度制御により被洗浄体15の温度を70〜85℃に保ちながら、真空吸引して洗浄室4内の気圧を0.27〜1.33kPaの範囲に保つことにより、ノルマルパラフィン洗浄液の沸騰現象を引き起こして洗浄液を吹き付けて行う。このとき、洗浄効果を高めるために搬送容器7を揺動シリンダー9で揺動させる。
【0037】
被洗浄体15の温度を70〜85℃に保つのは、70℃未満では洗浄が不十分だからであり、85℃以下に保つのは片側面に板材を接着したハニカムコアを洗浄する際のハニカムコア41と板材42との接着部の接着強度劣化とハニカムコア材の焼けを防止するためである。洗浄室4内の気圧を0.27〜1.33kPaの範囲に保つのは、0.27kPa未満では沸騰が激しすぎて霧状のノルマルパラフィン粒子による安定な洗浄を行うことができないからであり、1.33kPaを越えると沸騰現象を起こすことができないからである(図5参照)。
【0038】
上記洗浄液沸騰工程S2aにより、霧状のノルマルパラフィン粒子が被洗浄体15の下部から多方向に飛散して吹き上げられるので、通常のシャワー洗浄に比べて複雑形状を持つ被洗浄体15の洗浄を良好に行うことができる上に、霧状のノルマルパラフィン粒子が被洗浄体15の内部にまで効率よく供給されるため、一般的な蒸気脱脂の効果があまり期待できない熱容量の小さい被洗浄体15および液層への浸漬をあまり好まない被洗浄体15を清浄に洗浄することができる。
【0039】
なお、清浄な洗浄液および洗浄装置を用いて突沸現象を引き起こせば、運動エネルギーの大きい洗浄液の飛沫が多方向に飛散するので、凹凸の激しい複雑形状の被洗浄体15の洗浄を上下側面を問わず行うことができる。
【0040】
不活性ガス供給工程S2bは、洗浄液供給口13から洗浄液貯蔵室25の洗浄液をドレインパン11に噴射ノズル12が充分に隠れるまで供給した後、窒素等の不活性ガスを噴射ノズル12から噴射し、洗浄液を吹き付けて行う。このとき、真空吸引して洗浄室4内の気圧を1.33〜4.00kPaの範囲に保ち、蒸気通路3またはヒーターによる温度制御により、被洗浄体15の温度を70〜85℃に保つ。また、洗浄効果を高めるために搬送容器7を揺動シリンダー9で揺動させる。
【0041】
洗浄室4内の気圧を1.33〜4.00kPaの範囲に保つのは、1.33kPa以下では洗浄室4内の温度が不均一であった場合にノルマルパラフィン系洗浄液の沸点に近づくのを回避するためであり、4.00kPa以上ではノルマルパラフィン洗浄液が霧化せず洗浄が促進されないからである。不活性ガスを用いるのは残存酸素濃度を低下させて火災の危険性を低減するためである。
【0042】
上記不活性ガス供給工程S2bにより、洗浄室4の気圧が1.33〜4.00kPaである低圧条件下において、不活性ガスによりノルマルパラフィン洗浄液が被洗浄体15の下部から垂直方向に吹き上げられるので、通常のシャワー洗浄に比べて指向性の良い洗浄が達成される上に、噴射圧を大きくすることにより、例えば厚みのあるハニカムコアの場合でも洗浄することができる。また、霧状のノルマルパラフィン粒子が被洗浄体15の奥部にまで効率よく供給されるため、一般的な蒸気脱脂の効果があまり期待できない熱容量の小さい被洗浄体15および液層への浸漬をあまり好まない被洗浄体15を清浄に洗浄することができる。
【0043】
次に、仕上げ洗浄工程S3と二次蒸気脱脂工程S4とを行う。図6(3)に示す仕上げ洗浄工程S3は、洗浄液貯蔵室25から清浄な洗浄液をシャワー液供給管30を通してシャワーノズル10に供給して行う。このとき、被洗浄体15に付着している汚染液を洗い流すために搬送容器7を揺動シリンダー9で揺動させる。この工程により、清浄な洗浄液が被洗浄体15の下部から供給されるので充分な仕上げ洗浄が可能となる。
【0044】
二次蒸気脱脂工程S4は、蒸気発生室22で発生した蒸気を蒸気供給管21を通して洗浄室4内に供給し、真空吸引して洗浄室4内の気圧を1.33〜4.00kPaに保ちながら被洗浄体15を蒸気洗浄することにより行う。ここで、蒸気温度を70〜85℃の範囲にし、洗浄室4内の気圧を1.33〜4.00kPaにするのは、蒸気濃度を充分にして仕上げ脱脂効果を高めるとともに乾燥促進効果をも図るためである。この工程は、液層への浸漬をあまり好まない被洗浄体を清浄に洗浄する場合に特に有効である。
【0045】
また、仕上げ洗浄工程S3に続き二次蒸気脱脂工程S4を行うことにより、仕上げ洗浄を徹底して行うことができ、乾燥促進も図ることができる。
【0046】
最後に、図6(4)に示す乾燥工程S5を行う。この工程S5は、真空ポンプ33により洗浄室4の気圧を1.33kPa以下の範囲にし、被洗浄体15の温度を蒸気通路3またはヒーターにより70〜85℃の範囲に制御して、被洗浄体15を乾燥することにより行う。被洗浄体15の温度を70〜85℃の範囲としたのは、許容できる程度の時間内で乾燥するためであり、85℃以下にしたのは、ハニカムコア41の焼けを防止すると共にハニカムコア41と板材42との接着部の接着強度劣化を防止するためである。乾燥後、洗浄室4を大気開放して被洗浄体15を搬出する。
【0047】
以下に、片側面に板材を接着したハニカムコアを洗浄する場合について、詳細に説明する
図3に示す片側面に板材42を接着した6角セル型ハニカムコア41(長さ2300mm、幅1400mm、厚み100mm)を、図4に示すステンレス製のバスケット43(長さ3700mm、幅1700mm、深さ150mm)内に、ハニカムコア41の開放端を下に向けて収容し、シャワーノズル10の中央方向がハニカムコア41のセル軸方向に向くように配置する。
【0048】
次に、真空ポンプ33により洗浄室4内を真空吸引し、洗浄室4内の気圧を0.66kPa以下とした後、スチームヒーター24でノルマルパラフィン洗浄液の入っている蒸気発生室22を70〜85℃に加熱する。発生した蒸気を蒸気供給管21を通して洗浄室4内に供給し、真空吸引して洗浄室4内の気圧を1.33〜4.00kPaに保ちながら、ハニカムコア41を10〜15分間蒸気脱脂する。
【0049】
次に、洗浄液供給口13から洗浄液貯蔵室25の洗浄液をドレインパン11に噴射ノズル12が充分に隠れるまで供給した後、ヒーターによる温度制御によりハニカムコア41の温度を70〜85℃に保ちながら、真空吸引して洗浄室4内の気圧を0.27〜1.33kPaの範囲に保ち、ノルマルパラフィン洗浄液の沸騰現象を引き起こして5〜10分間洗浄液を吹き付ける。バスケット43は揺動シリンダー9で揺動させる。
【0050】
さらに、窒素ガスを噴射ノズル12から噴射し、5〜10分間洗浄液を吹き上げる。このとき、真空吸引して洗浄室4内の気圧を1.33〜4.00kPaの範囲に保ち、ヒーターによる温度制御により、ハニカムコア41の温度を70〜85℃に保つ。また、バスケット43を揺動シリンダー9で揺動させる。
【0051】
次に、洗浄液貯蔵室25から清浄な洗浄液をシャワー液供給管30を通してシャワーノズル10に供給して1〜2分間仕上げ洗浄を行う。このとき、真空吸引して洗浄室4内の気圧を1.33〜4.00kPaの範囲に保ち、ヒーターによる温度制御によりハニカムコア41の温度を70〜85℃の範囲に保つ。また、バスケット43を揺動シリンダー9で揺動させる。さらに、蒸気発生室22で発生した蒸気を蒸気供給管21を通して洗浄室4内に供給し、真空吸引して洗浄室4内の気圧を1.33〜4.00kPaに保ちながらハニカムコア41を10〜20分蒸気脱脂する。
【0052】
最後に、真空ポンプ33により洗浄室4の気圧を1.33kPa以下の範囲にし、ハニカムコア41の温度をヒーターにより70〜85℃の範囲に制御して、15分間乾燥する。乾燥後、洗浄室4を大気開放してハニカムコア41を搬出する。
【0053】
以上の工程により洗浄した片側面に板材42を接着した6角セル型ハニカムコア41について、洗浄効果を確認した。まずハニカムコア切削時に使用した鉱物油が残っているか否かを調査するために紫外線照射検査を行ったが、残渣は検出されなかった。また、強度試験の1つであるノードボンド強度試験(MIL−C−7438、要求値40(lb/.625in)以上)を行ったところ、60.2(lb/.625in)の値が得られ、トリクロルエチレン洗浄法による49.9(lb/.625in)に比較しても良好な結果が得られた。
【0054】
また、図7に示すように、上記の片側面に板材42を接着した6角セル型ハニカムコア41のコア開放面に120℃硬化エポキシ系フィルム接着剤を用いてアルミニウム面板44を接着し、ハニカムサンドイッチパネルを組上げたところ、十分な接着強度および接着耐久性が確保され、構造強度の大きい構造体が得られた。したがって、本発明による洗浄効果が十分であることが確認された.
なお、本発明の洗浄方法は、70〜85℃の範囲で洗浄を行うので、マグネシウムやチタン等の熱による焼けを嫌う非鉄金属でも安心して洗浄することができる。また、霧状の洗浄液粒子で洗浄するので、ハニカムコアに限らず、複雑形状の被洗浄体や、洗浄液の浸漬による腐食等が懸念される部位を持つ被洗浄体でも洗浄できる。さらに、ハニカムコアを洗浄する場合でもセル形状およびセルサイズの如何にかかわらず洗浄することができる。
【0055】
【発明の効果】
以上説明したように、本発明の洗浄方法によれば、洗浄および乾燥工程を通じて被洗浄体の温度が70℃〜85℃の温度範囲に保たれるので、熱による焼けを嫌う非鉄金属でも安心して洗浄することができ、片側面に板材を接着したハニカムコアでも、ハニカムコアと板材との接着部の接着強度劣化を防止して洗浄を行うことができる。また、霧状のノルマルパラフィン粒子が被洗浄体の奥部にまで効率よく供給されるため、一般的な蒸気脱脂の効果があまり期待できない熱容量の小さい被洗浄体でも、液層への浸漬を嫌う被洗浄体でも、清浄な洗浄を達成することができる。
【0056】
また、本発明の洗浄装置によれば、上述の洗浄方法を効果的に実施することができ、さらに、洗浄液を他のタンク等へ移動することなく洗浄することができるため、洗浄時間を任意に設定することができる上に、被洗浄体が比較的大きいハニカムコアの洗浄においても洗浄剤の使用量を低減でき、周辺施設や管理コストの軽減をも図ることができる。
【図面の簡単な説明】
【図1】本発明の実施の形態に使用される洗浄装置本体の構成を示す断面図である。
【図2】同じく、洗浄装置全体の構成を示す図である。
【図3】片側面に板材を接着した6角セル型ハニカムコアの図である。
【図4】ハニカムコアを搭載する搬送容器(バスケット)の図である。
【図5】本発明の実施の形態に使用されるノルマルパラフィン系洗浄剤の蒸気圧曲線を示すグラフである。
【図6】本発明の実施の形態における洗浄の概要を示す工程説明図である。
【図7】片側面に板材を接着した6角セル型ハニカムコアの他の面に板材を接着して組上げたハニカムサンドイッチパネルの図である。
【符号の説明】
1 洗浄装置本体
3 蒸気通路
4 洗浄室
5 蒸気供給口(洗浄液蒸気供給手段)
6 真空排気口(真空吸引手段)
10 シャワーノズル(シャワー液供給手段)
11 ドレインパン(洗浄液貯蔵部)
12 不活性ガス噴射ノズル(不活性ガス供給手段)
13 洗浄液供給口(洗浄液供給手段)
14 洗浄液排出口(洗浄液排出手段)
15 被洗浄体
22 蒸気発生室
25 洗浄液貯蔵室
41 ハニカムコア
43 バスケット
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a cleaning method and a cleaning apparatus for cleaning an object to be cleaned that needs to be cleaned at a relatively low temperature, for example, a honeycomb core alone and a honeycomb core having a plate member bonded to one side using a normal paraffin cleaning solution.
[0002]
[Prior art]
Since the honeycomb sandwich structure has a characteristic that the mechanical strength is larger than the weight, the honeycomb sandwich panel in which the plate material is bonded to both sides of the honeycomb core is used for an aircraft, an artificial satellite, or the like that is required to be lightweight and highly rigid. Widely applied to structural materials.
[0003]
Many non-ferrous metals such as aluminum alloy, magnesium, and titanium are used as the material for the honeycomb core. The honeycomb core is made of these metals in the form of foil, and this foil is partially bonded to form a hexagonal cell. It is manufactured by being expanded into a mold, a quadrangular cell mold or the like, and has a bonded portion (node bond) as a feature of the structure. Further, the honeycomb sandwich panel is manufactured by each process of cutting the honeycomb core on one side, bonding the plate material to the cut surface, cutting the other side of the honeycomb core, and bonding the plate material to the cut surface. The board material is bonded using a cured epoxy film adhesive.
[0004]
The bonding performance and bonding durability between the honeycomb core and the plate material have a significant effect on the mechanical strength and durability of the entire structural material after the honeycomb sandwich panel is used as an aircraft structural material, either primary or secondary bonded. Therefore, it is necessary to sufficiently clean the plate material, the honeycomb core alone, and the honeycomb core having the plate material bonded to one side before bonding.
[0005]
In the pre-bonding cleaning of the honeycomb core, steam degreasing using a chlorine-based solvent such as trichloroethane and trichloroethylene has been conventionally performed. However, in Japan, the Montreal Protocol on the protection of the stratospheric ozone layer was adopted on September 30, 1988 in Japan, and its production, import and use have been prohibited since 1996, and it can no longer be used for cleaning. Trichlorethylene is being addressed in the direction of stricter regulations, although there are no regulations under the Air Pollution Control Law but concerns about health problems and environmental pollution of workers. Fluorine solvents (HCFC: hydrogen, chlorine, fluorine, carbon compounds), which are alternative cleaning agents for the above chlorinated solvents, have also been decided to be completely abolished by 2020. There is an urgent need to consider cleaning methods.
[0006]
On the other hand, in JP-A-9-71883, an aqueous degreasing method using an aqueous solution mainly composed of alkali salts or surfactants reduces the strength of node bonds due to moisture absorption by the adhesive, and alkali salts and moisture are reduced. It is unsuitable because it stays inside the core and causes corrosion damage during the production period or operation period. It is also unsuitable for hydrocarbon solvents (N-methyl-2-pyrrolidone, normal paraffin, isoparaffin, naphthene). System), quasi-aqueous system (solutions mainly composed of alcohol, water and surfactant), halides, alcohols, and ketones. Normal paraffin detergents that do not contain additives are used to clean honeycomb cores. It is disclosed that it is suitable.
[0007]
[Problems to be solved by the invention]
On the other hand, for honeycomb cores having various cell shapes, cell sizes and thicknesses, and honeycomb cores having a plate bonded to one side, in order to perform sufficient cleaning, the cleaning liquid is applied from below with the open end of the cells facing downward. It is considered effective to supply and wash. In addition, if the cleaning solution does not reach the back of the cell sufficiently, contaminants attached when the honeycomb core is cut, etc. will remain, and it will be difficult to ensure sufficient adhesion strength and adhesion durability when assembling the honeycomb sandwich panel. It is a concern.
[0008]
Accordingly, an object of the present invention is to clean and sufficiently clean the honeycomb core alone and the honeycomb core in which the plate material is bonded to one side surface, using a normal paraffin cleaning liquid that does not have a problem regarding health problems and environmental pollution of the worker, For example, it is to provide a cleaning method and a cleaning apparatus applicable to cleaning of an object to be cleaned that does not like to be burned by heat, such as magnesium and titanium, and an object to be cleaned that does not like immersion in a liquid layer.
[0009]
[Means for Solving the Problems]
The invention according to claim 1 for achieving the above-described object is a to-be-cleaned object arranging step for disposing a to-be-cleaned object in a cleaning chamber, and a pressure in the cleaning chamber in a range of 0.27 to 4.00 kPa. And while maintaining the temperature of the object to be cleaned in the range of 70 to 85 ° C., the normal paraffin cleaning liquid is jetted from below to clean the object to be cleaned, and the atmospheric pressure in the cleaning chamber is 1.33 kPa or less, And a drying step of drying the object to be cleaned while maintaining the temperature of the object to be cleaned in the range of 70 to 85 ° C. In the cleaning process, after the normal paraffin cleaning liquid is introduced into the cleaning liquid storage section disposed in the lower part of the cleaning chamber, the cleaning liquid is boiled in which the cleaning liquid is boiled while maintaining the atmospheric pressure in the range of 0.27 to 1.33 kPa. And at least one step of supplying an inert gas into the cleaning liquid so that the cleaning liquid is pushed up while maintaining the pressure in the cleaning chamber in a range of 1.33 to 4.00 kPa, This is a step of cleaning the object to be cleaned by spraying a cleaning liquid from below the object to be cleaned. It is characterized by that.
[0010]
According to the cleaning method of the first aspect, since the temperature of the object to be cleaned is maintained in the temperature range of 70 to 85 ° C. throughout the cleaning and drying process, it is possible to clean even non-ferrous metals that dislike burning due to heat. it can. In the cleaning process, the pressure in the cleaning chamber is in the low pressure range of 0.27 to 4.00 kPa. According to the cleaning liquid boiling process, normal paraffin cleaning liquid is sprayed in multiple directions from the bottom of the object to be cleaned, so that the mist-like normal paraffin particles reach the back of the object to be cleaned having a complex shape and be cleaned well. Can do. According to the inert gas supply step, the normal paraffin cleaning liquid is sprayed vertically from the lower part of the object to be cleaned under a low pressure condition where the pressure in the cleaning chamber is 1.33 to 4.00 kPa. Normal paraffin particles reach the back of the object to be cleaned with the pressure of the inert gas. A clean object can be achieved even with a to-be-cleaned object having a small heat capacity, for which the effect of general steam degreasing cannot be expected so much, and an object to be cleaned that does not like immersion in a liquid layer can also be cleaned.
[0011]
According to a second aspect of the present invention, the object to be cleaned in claim 1 is a honeycomb core having a honeycomb core alone or a plate member bonded to one side surface, and the open end of the cells of the honeycomb core is directed downward in the object to be cleaned arrangement step. It is characterized by being placed horizontally in the cleaning chamber. According to this cleaning method, since the temperature of the honeycomb core is maintained in the temperature range of 70 to 85 ° C. throughout the cleaning and drying process, it is possible to prevent deterioration in the adhesive strength of the bonded portion between the honeycomb core and the plate material. Because the open end of the honeycomb core faces downward, mist-like normal paraffin particles are supplied from below, and the contaminated cleaning liquid drops downward, so a honeycomb with a plate attached to one side with a complex shape Clean up to the back of the core.
[0012]
According to a third aspect of the present invention, the object to be cleaned is swung horizontally in the cleaning step. According to this cleaning method, normal paraffin particles are supplied without blind spots to the back and details of the object to be cleaned, so that cleaning can be performed thoroughly.
[0015]
Claim 4 According to the invention described in item 1, the vapor of the normal paraffin cleaning liquid in the temperature range of 70 to 85 ° C. is maintained between the cleaning object arranging step and the cleaning step while maintaining the atmospheric pressure in the cleaning chamber at 1.33 to 4.00 kPa. It has a primary steam degreasing step for supplying steam into the cleaning chamber and cleaning the object to be cleaned with steam. According to this cleaning method, steam in the temperature range of 70 to 85 ° C. is supplied into the cleaning chamber, so that the object to be cleaned can be heated and oil, chips, adhesives, dust, etc. are lifted up. In addition, the wettability of the object to be cleaned during the cleaning process can be improved.
[0016]
Claim 5 According to the invention, the cleaning process is performed by supplying a shower liquid made of a normal paraffin cleaning liquid from below the object to be cleaned to clean the object to be cleaned between the cleaning process and the drying process. A secondary steam degreasing step of supplying a vapor of a normal paraffin cleaning liquid in a temperature range of 70 to 85 ° C. while keeping the temperature in a range of 33 to 4.00 kPa into the cleaning chamber to steam clean the object to be cleaned. Features. According to this cleaning method, a clean cleaning liquid is supplied from the lower part of the object to be cleaned in the final cleaning process, so that sufficient final cleaning is possible. In the secondary steam degreasing process, immersion in the liquid layer is preferred by steam cleaning. It is possible to finish and clean the object to be cleaned, and to accelerate drying.
[0017]
Claim 6 The invention described in (1) includes a sealable cleaning chamber in which an object to be cleaned is disposed, cleaning liquid vapor supply means for supplying cleaning liquid vapor into the cleaning chamber, vacuum suction means for vacuum suction of the cleaning chamber, Shower liquid supply means that is disposed in the lower portion and supplies shower liquid from below the object to be cleaned, a cleaning liquid storage section that is disposed further below the shower liquid supply means in the cleaning chamber, and a cleaning liquid storage section Normal paraffin A cleaning liquid supply means for supplying a cleaning liquid, a cleaning liquid discharge means for discharging the cleaning liquid disposed at the bottom of the cleaning liquid storage section, and an inert gas supply means for supplying an inert gas into the cleaning chamber disposed in the cleaning liquid storage section And a cleaning chamber temperature adjusting means for adjusting the temperature in the cleaning chamber to 70 to 85 ° C. e , The inert gas supply means cleans the object to be cleaned by spraying a cleaning liquid from below the object to be cleaned in a state where the pressure in the cleaning chamber is maintained in the range of 1.33 to 4.00 kPa by the vacuum suction means. In order to push up the cleaning solution so that the cleaning solution is pushed up. A cleaning device characterized by the above. According to this cleaning apparatus, the cleaning method according to claim 1 can be effectively carried out.
[0018]
A seventh aspect of the present invention is the cleaning apparatus according to the seventh aspect, further comprising swinging means for swinging an object to be cleaned disposed in the cleaning chamber in a horizontal direction. According to this cleaning apparatus, normal paraffin particles are supplied without blind spots to the back and details of the object to be cleaned, so that cleaning can be performed thoroughly.
[0019]
Claim 8 The invention described in claim 6 Or 7 The cleaning apparatus according to claim 1, further comprising a steam generation chamber and a cleaning liquid storage chamber, a flow path system for guiding the cleaning liquid in the cleaning liquid storage section to the steam generation chamber, generating steam, and guiding the generated steam into the cleaning chamber; And a flow path system for condensing the steam generated in the steam generation chamber and guiding it to the cleaning liquid storage chamber, and leading the cleaning liquid from the cleaning liquid storage chamber to the shower liquid supply means and the cleaning liquid supply means. According to this cleaning apparatus, since the cleaning liquid can be cleaned without moving to another tank or the like, the cleaning time can be arbitrarily set, and the honeycomb core having a relatively large object to be cleaned can be cleaned. In addition, the amount of cleaning agent used can be reduced, and the peripheral facilities and management costs can be reduced.
[0020]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
[0021]
FIG. 1 is a cross-sectional view showing a configuration of a cleaning apparatus main body 1 for carrying out this cleaning method. The cleaning device main body 1 is first provided with an opening / closing door 2 through which the object to be cleaned is carried in and out and the cleaning chamber 4 is sealed and opened. The cleaning chamber 4 has a double outer wall, and a cleaning liquid vapor passage 3 is provided between the two outer walls. The steam passage 3 is provided as a temperature adjusting means that heats the inside of the cleaning chamber 4 with the heat of the steam and prevents the heat escape from the inside of the cleaning chamber 4, that is, the heat dissipation, and constitutes the cleaning chamber 4 having a high heat retaining effect. ing. Heating and temperature control inside the cleaning chamber 4 can be performed by a steam heater (not shown) as temperature adjusting means.
[0022]
Further, the cleaning chamber 4 is provided with a steam supply port 5 as a cleaning solution vapor supply means so that the cleaning solution steam heated to 70 to 85 ° C. is supplied into the cleaning chamber 4. Further, the cleaning chamber 4 is provided with a vacuum exhaust port 6 as a vacuum suction means so that the inside of the cleaning chamber 4 is evacuated and kept at a constant pressure.
[0023]
In the cleaning chamber 4, a guide roller 8 and a swing cylinder 9 as a swing means are provided. The guide roller 8 is for carrying the carrying container 7 carrying the object 15 to be carried in and out through the open / close door 2, and the swing cylinder 9 swings the carrying container 7, that is, the object 15 to be washed is moved. It is intended to enhance the cleaning effect by swinging.
[0024]
Further, in the cleaning chamber 4, a shower nozzle 10 which is a shower liquid supply means for supplying a shower liquid used for finishing cleaning is provided at the lower part of the transfer container installation portion. In the present embodiment, the shower nozzle 10 is a full cone nozzle with the vertical direction of the cleaning chamber 4 as the central direction. For example, the shower nozzle 10 has a substantially uniform flow density within an effective cleaning range of 3820 mm in length and 1600 mm in width. Nozzle is arranged. A nozzle other than the full cone nozzle can also be used.
[0025]
Further, a drain pan 11 which is a cleaning liquid storage unit for storing the cleaning liquid is provided at the lower portion of the shower nozzle 10, and the upper portion 11 a of the drain pan 11 is opened. In the drain pan 11, an injection nozzle 12 which is an inert gas supply means for supplying an inert gas is provided. In the present embodiment, the injection nozzle 12 has a structure in which an inert gas is ejected from a perforation 12a provided in the upper direction of the pipe. For example, the cleaning liquid is on the upper side within an effective cleaning range of 3820 mm in length and 1600 mm in width. Are sprayed in the vertical direction by an inert gas. The cleaning liquid is supplied to the drain pan 11 from a cleaning liquid supply port 13 that is a cleaning liquid supply means, and is discharged from a cleaning liquid discharge port 14 that is a cleaning liquid discharge means. However, the cleaning liquid may be supplied using the shower nozzle 10. In the present embodiment, the spray nozzle for spraying the cleaning liquid with the inert gas is provided. However, a separate spray nozzle may be provided below the cleaning chamber 4 to spray the cleaning liquid upward. .
[0026]
FIG. 2 is a diagram showing an outline of the entire cleaning apparatus for carrying out this cleaning method. The steam supply port 5 of the cleaning apparatus main body 1 is connected to the steam generation chamber 22 via the steam passage 3 and the steam supply pipe 21. The steam generation chamber 22 also serves as a storage chamber for the used cleaning agent, and is also connected to the cleaning liquid discharge port 14 via the cleaning liquid discharge pipe 23. A steam heater 24 for heating the cleaning liquid and generating steam is provided at the lower part of the steam generation chamber 22. The steam heater 24 also performs heating and temperature control of the cleaning chamber 4 and the cleaning liquid storage chamber 25. It has become. A condensing tank 26 and a first condenser 27 corresponding to the first drain tank are connected to the steam generation chamber 22 so that only liquid that cannot be distilled and regenerated, such as dirt and moisture, can be concentrated. Is sent to the waste liquid tank 28.
[0027]
The steam generator 22 is connected to the cleaning liquid storage chamber 25 through the second condenser 29, and only the clean cleaning liquid that has been regenerated by distillation is stored in the cleaning liquid storage chamber 25. The cleaning liquid storage chamber 25 is connected to the shower nozzle 10 through the shower liquid supply pipe 30, and is connected to the cleaning liquid supply port 13 through the cleaning liquid supply pipe 31.
[0028]
The vacuum exhaust port 6 of the cleaning apparatus body 1 is connected to a vacuum pump 33 through a third condenser 32, and the outlet side of the vacuum pump 33 is further connected to a mist trap 34. The cleaning liquid condensed by the third condenser 32 is stored in the condensate tank 35 and returned to the steam generation chamber 22.
[0029]
By connecting the shower nozzle 10, the cleaning liquid storage chamber 25, the steam generation chamber 22, and the drain pan 11 as described above, the cleaning liquid can be cleaned without moving to another tank or the like. Can be set to In addition, even when cleaning a honeycomb core with a relatively large body to be cleaned, the amount of cleaning agent used is only 1500 liters and can be managed within the specified amount of third petroleum (2000 liters). Can be reduced. Furthermore, by providing the waste liquid tank 28 and the mist trap 33, it is possible to satisfy the requirements for environmental compatibility.
[0030]
Hereinafter, the cleaning method and operation will be described with reference to the process explanatory diagrams shown in FIGS. 1, 2, and 6.
[0031]
First, the object to be cleaned 15 is mounted on the transport container 7, the opening / closing door 2 of the cleaning apparatus main body 1 is opened, loaded along the guide roller 8 and placed in the center of the cleaning chamber 4, and then the opening / closing door 2 is closed. The cleaning chamber 4 is sealed. At this time, when cleaning the hexagonal cell type honeycomb core 41 with the plate material 42 bonded to one side as shown in FIG. 3 as the object 15 to be cleaned, it is placed in the basket 43 which is a transport container as shown in FIG. The honeycomb core 41 is accommodated with the open end facing downward, and the shower nozzle 10 is arranged so that the center direction of the shower nozzle 10 faces the cell axis direction of the honeycomb core 41. The reason why the cleaning is performed in the cleaning chamber 4 is that even if cleaning is performed using a normal paraffin cleaning liquid having a flash point of 70 ° C., there is no risk of fire and cleaning can be performed safely.
[0032]
Next, primary steam degreasing process S1 shown in FIG. 6 (1) is performed. In order to perform this primary vapor degreasing S1, first, the cleaning chamber 4 is vacuum-sucked through the vacuum exhaust port 6 by the vacuum pump 33, and the inside of the cleaning chamber 4 is set to 0.66 kPa or less. Next, the steam generation chamber 22 containing the normal paraffin cleaning liquid mainly composed of 11 to 12 carbon atoms is heated to 70 to 85 ° C. by the steam heater 24, and the generated steam is passed through the steam supply pipe 21 into the cleaning chamber 4. The object to be cleaned 15 is vapor degreased while being supplied and vacuumed to keep the pressure in the cleaning chamber 4 at 1.33 to 4.00 kPa.
[0033]
Here, the reason why the steam temperature is set in the range of 70 to 85 ° C. is to heat the cleaning target 15 to the cleaning temperature to a temperature sufficient to perform the steam degreasing, and in the cleaning chamber 4. The atmospheric pressure is set to 1.33 to 4.00 kPa in order to increase the vapor concentration and enhance the vapor degreasing effect as can be seen from the vapor pressure curve of the normal paraffin cleaning liquid used in the present embodiment shown in FIG. It is. By this primary steam degreasing S1, oil cleaning (machine oil, etc.), chips (cutting residue), adhesive, dust, etc. can be lifted to perform steam cleaning, and the object to be cleaned in the cleaning process 15 can contribute to the improvement of wettability.
[0034]
Next, cleaning process S2 is performed. In the cleaning step S2, the normal paraffin cleaning liquid is generally applied while vacuuming the inside of the cleaning chamber 4 to keep the temperature of the body 15 to be cleaned in the range of 0.27 to 4.00 kPa and in the range of 70 to 85 ° C. This is carried out by ejecting from below the cleaning body 15.
[0035]
The cleaning liquid is jetted out after the normal paraffin cleaning liquid is introduced into the drain pan 11 disposed in the lower part of the cleaning chamber 4 and then the cleaning liquid is boiled while maintaining the pressure in the cleaning chamber 4 within a range of 0.27 to 1.33 kPa. At least one of a boiling step S2a and an inert gas supply step S2b for feeding the inert gas into the cleaning liquid so that the cleaning liquid is pushed up while maintaining the atmospheric pressure in the cleaning chamber 4 in the range of 1.33 to 4.00 kPa. It is preferable that the cleaning liquid is sprayed from below the object to be cleaned 15 in one step.
[0036]
In the cleaning liquid boiling step S2a shown in FIG. 6 (2), the cleaning liquid in the cleaning liquid storage chamber 25 is supplied from the cleaning liquid supply port 13 to the drain pan 11, and then the temperature of the object to be cleaned 15 is controlled by the temperature control by the steam passage 3 or the heater. While maintaining at ˜85 ° C., vacuum suction is performed to maintain the atmospheric pressure in the cleaning chamber 4 in a range of 0.27 to 1.33 kPa, thereby causing a boiling phenomenon of the normal paraffin cleaning solution and spraying the cleaning solution. At this time, the transfer container 7 is swung by the swing cylinder 9 in order to enhance the cleaning effect.
[0037]
The temperature of the object to be cleaned 15 is maintained at 70 to 85 ° C. because the cleaning is insufficient when the temperature is less than 70 ° C., and the temperature is maintained at 85 ° C. or less when the honeycomb core having a plate material bonded to one side surface is cleaned. This is to prevent deterioration of the adhesive strength of the bonded portion between the core 41 and the plate material 42 and burning of the honeycomb core material. The reason why the air pressure in the cleaning chamber 4 is kept in the range of 0.27 to 1.33 kPa is that boiling is excessively less than 0.27 kPa, and stable cleaning with mist-like normal paraffin particles cannot be performed. This is because the boiling phenomenon cannot be caused when it exceeds 1.33 kPa (see FIG. 5).
[0038]
By the cleaning liquid boiling step S2a, the mist-like normal paraffin particles are scattered and blown up in multiple directions from the lower part of the object 15 to be cleaned, so that the object 15 having a complicated shape can be cleaned better than normal shower cleaning. In addition, since the mist-like normal paraffin particles are efficiently supplied to the inside of the body 15 to be cleaned, the body 15 to be cleaned and the liquid having a small heat capacity, in which the effect of general vapor degreasing cannot be expected so much. The to-be-cleaned object 15 which does not like immersion in the layer can be cleaned cleanly.
[0039]
In addition, if a bumping phenomenon is caused by using a clean cleaning liquid and a cleaning apparatus, the spray of cleaning liquid with a large kinetic energy is scattered in multiple directions. Can be done without.
[0040]
The inert gas supply step S2b supplies the cleaning liquid in the cleaning liquid storage chamber 25 from the cleaning liquid supply port 13 to the drain pan 11 until the injection nozzle 12 is sufficiently hidden, and then injects an inert gas such as nitrogen from the injection nozzle 12. Spray with cleaning solution. At this time, vacuum suction is performed to maintain the atmospheric pressure in the cleaning chamber 4 in the range of 1.33 to 4.00 kPa, and the temperature of the object to be cleaned 15 is maintained at 70 to 85 ° C. by temperature control using the vapor passage 3 or the heater. Further, the transfer container 7 is swung by the swing cylinder 9 in order to enhance the cleaning effect.
[0041]
The pressure in the cleaning chamber 4 is kept in the range of 1.33 to 4.00 kPa because the temperature in the cleaning chamber 4 is not uniform at 1.33 kPa or less and approaches the boiling point of the normal paraffin cleaning solution. This is to avoid this, and when it is 4.00 kPa or more, the normal paraffin cleaning liquid does not atomize and cleaning is not promoted. The inert gas is used to reduce the risk of fire by reducing the residual oxygen concentration.
[0042]
By the inert gas supply step S2b, the normal paraffin cleaning liquid is blown up vertically from the lower portion of the body 15 to be cleaned under a low pressure condition where the pressure in the cleaning chamber 4 is 1.33 to 4.00 kPa. In addition, cleaning with better directivity compared to ordinary shower cleaning is achieved, and by increasing the injection pressure, for example, even a thick honeycomb core can be cleaned. Further, since the mist-like normal paraffin particles are efficiently supplied to the inner part of the object 15 to be cleaned, immersion in the object 15 to be cleaned and the liquid layer having a small heat capacity, in which the effect of general vapor degreasing cannot be expected so much. The to-be-cleaned object 15 which is not so much can be cleaned cleanly.
[0043]
Next, a finishing cleaning step S3 and a secondary steam degreasing step S4 are performed. 6 (3) is performed by supplying clean cleaning liquid from the cleaning liquid storage chamber 25 to the shower nozzle 10 through the shower liquid supply pipe 30. At this time, the transfer container 7 is swung by the swing cylinder 9 in order to wash away the contaminated liquid adhering to the object 15 to be cleaned. By this step, a clean cleaning liquid is supplied from the lower part of the body 15 to be cleaned, so that sufficient finish cleaning can be performed.
[0044]
In the secondary steam degreasing step S4, the steam generated in the steam generation chamber 22 is supplied into the cleaning chamber 4 through the steam supply pipe 21, and vacuumed to keep the atmospheric pressure in the cleaning chamber 4 at 1.33 to 4.00 kPa. However, the object 15 to be cleaned is steam cleaned. Here, when the steam temperature is set in the range of 70 to 85 ° C. and the pressure in the cleaning chamber 4 is set to 1.33 to 4.00 kPa, the steam concentration is sufficiently increased to enhance the finishing degreasing effect and also to promote the drying. This is for the purpose of illustration. This step is particularly effective when cleaning an object to be cleaned that does not so much be immersed in the liquid layer.
[0045]
Further, by performing the secondary steam degreasing step S4 after the finishing cleaning step S3, the finishing cleaning can be performed thoroughly, and drying can be promoted.
[0046]
Finally, a drying step S5 shown in FIG. 6 (4) is performed. In this step S5, the pressure in the cleaning chamber 4 is set to a range of 1.33 kPa or less by the vacuum pump 33, and the temperature of the cleaning target 15 is controlled to a range of 70 to 85 ° C. by the steam passage 3 or the heater. 15 is performed by drying. The reason why the temperature of the object to be cleaned 15 is in the range of 70 to 85 ° C. is to dry within an acceptable time. The reason why the temperature is 85 ° C. or less is to prevent the honeycomb core 41 from being burned and This is to prevent deterioration of the bonding strength of the bonding portion between 41 and the plate material 42. After drying, the cleaning chamber 4 is opened to the atmosphere and the body 15 to be cleaned is carried out.
[0047]
Hereinafter, the case of cleaning the honeycomb core having the plate material bonded to one side surface will be described in detail.
A hexagonal cell type honeycomb core 41 (length 2300 mm, width 1400 mm, thickness 100 mm) with a plate 42 bonded to one side surface shown in FIG. 3 is connected to a stainless steel basket 43 (length 3700 mm, width 1700 mm, depth) shown in FIG. 150 mm), the open end of the honeycomb core 41 is accommodated downward, and the shower nozzle 10 is arranged so that the center direction of the shower nozzle 10 faces the cell axis direction of the honeycomb core 41.
[0048]
Next, the inside of the cleaning chamber 4 is vacuumed by the vacuum pump 33 and the pressure in the cleaning chamber 4 is set to 0.66 kPa or less, and then the steam generation chamber 22 containing the normal paraffin cleaning liquid is set to 70 to 85 by the steam heater 24. Heat to ° C. The generated steam is supplied into the cleaning chamber 4 through the steam supply pipe 21, and vacuum suction is performed to keep the atmospheric pressure in the cleaning chamber 4 at 1.33 to 4.00 kPa while steam degreasing the honeycomb core 41 for 10 to 15 minutes. .
[0049]
Next, after supplying the cleaning liquid in the cleaning liquid storage chamber 25 from the cleaning liquid supply port 13 to the drain pan 11 until the spray nozzle 12 is sufficiently hidden, the temperature of the honeycomb core 41 is maintained at 70 to 85 ° C. by temperature control with a heater. Vacuum cleaning is performed to keep the pressure in the cleaning chamber 4 within a range of 0.27 to 1.33 kPa, causing a boiling phenomenon of the normal paraffin cleaning solution and spraying the cleaning solution for 5 to 10 minutes. The basket 43 is rocked by the rocking cylinder 9.
[0050]
Further, nitrogen gas is injected from the injection nozzle 12 and the cleaning liquid is blown up for 5 to 10 minutes. At this time, vacuum suction is performed to keep the pressure in the cleaning chamber 4 within a range of 1.33 to 4.00 kPa, and the temperature of the honeycomb core 41 is kept at 70 to 85 ° C. by temperature control using a heater. Further, the basket 43 is rocked by the rocking cylinder 9.
[0051]
Next, a clean cleaning liquid is supplied from the cleaning liquid storage chamber 25 to the shower nozzle 10 through the shower liquid supply pipe 30 to perform final cleaning for 1 to 2 minutes. At this time, vacuum suction is performed to keep the pressure in the cleaning chamber 4 within a range of 1.33 to 4.00 kPa, and the temperature of the honeycomb core 41 is kept within a range of 70 to 85 ° C. by temperature control using a heater. Further, the basket 43 is rocked by the rocking cylinder 9. Further, the steam generated in the steam generation chamber 22 is supplied into the cleaning chamber 4 through the steam supply pipe 21 and is sucked in vacuum to maintain the atmospheric pressure in the cleaning chamber 4 at 1.33 to 4.00 kPa while maintaining the honeycomb core 41 at 10. Steam degrease for ~ 20 minutes.
[0052]
Finally, the air pressure in the cleaning chamber 4 is set to a range of 1.33 kPa or less by the vacuum pump 33, and the temperature of the honeycomb core 41 is controlled to a range of 70 to 85 ° C. by a heater, and dried for 15 minutes. After drying, the cleaning chamber 4 is opened to the atmosphere and the honeycomb core 41 is unloaded.
[0053]
The cleaning effect was confirmed for the hexagonal cell type honeycomb core 41 in which the plate material 42 was bonded to one side surface cleaned by the above steps. First, an ultraviolet irradiation inspection was conducted to investigate whether or not the mineral oil used at the time of cutting the honeycomb core remained, but no residue was detected. Further, when a node bond strength test (MIL-C-7438, required value 40 (lb / .625 in) or more), which is one of strength tests, was performed, a value of 60.2 (lb / .625 in) was obtained. Even when compared with 49.9 (lb / .625 in) by the trichlorethylene washing method, good results were obtained.
[0054]
Further, as shown in FIG. 7, an aluminum face plate 44 is bonded to the core open surface of the hexagonal cell type honeycomb core 41 with the plate material 42 bonded to one side surface using a 120 ° C. cured epoxy film adhesive, When the sandwich panel was assembled, sufficient adhesion strength and adhesion durability were secured, and a structure having high structural strength was obtained. Therefore, it was confirmed that the cleaning effect of the present invention is sufficient.
In addition, since the washing | cleaning method of this invention performs washing | cleaning in the range of 70-85 degreeC, it can wash | clean with confidence also the nonferrous metal which dislikes the burning by heat | fever, such as magnesium and titanium. Further, since the cleaning is performed with the mist-like cleaning liquid particles, the cleaning is not limited to the honeycomb core, and the cleaning target having a complicated shape or the target to be cleaned may be corroded due to immersion of the cleaning liquid. Furthermore, even when the honeycomb core is washed, the honeycomb core can be washed regardless of the cell shape and the cell size.
[0055]
【The invention's effect】
As described above, according to the cleaning method of the present invention, the temperature of the object to be cleaned is maintained in the temperature range of 70 ° C. to 85 ° C. throughout the cleaning and drying process. Even a honeycomb core in which a plate material is bonded to one side surface can be cleaned while preventing deterioration of the adhesive strength of the bonded portion between the honeycomb core and the plate material. In addition, since mist-like normal paraffin particles are efficiently supplied to the inner part of the object to be cleaned, even objects to be cleaned with a small heat capacity that cannot be expected to have the effect of general vapor degreasing hate to be immersed in the liquid layer. Even the object to be cleaned can achieve clean cleaning.
[0056]
Moreover, according to the cleaning apparatus of the present invention, the above-described cleaning method can be effectively carried out, and further, the cleaning liquid can be cleaned without moving to another tank or the like, so that the cleaning time can be arbitrarily set. In addition, it is possible to reduce the amount of cleaning agent used in cleaning a honeycomb core having a relatively large object to be cleaned, and to reduce peripheral facilities and management costs.
[Brief description of the drawings]
FIG. 1 is a cross-sectional view showing a configuration of a cleaning apparatus main body used in an embodiment of the present invention.
FIG. 2 is a view similarly showing the configuration of the entire cleaning apparatus.
FIG. 3 is a diagram of a hexagonal cell type honeycomb core having a plate material bonded to one side surface.
FIG. 4 is a view of a transport container (basket) on which a honeycomb core is mounted.
FIG. 5 is a graph showing a vapor pressure curve of a normal paraffin cleaning agent used in the embodiment of the present invention.
FIG. 6 is a process explanatory diagram showing an outline of cleaning in the embodiment of the present invention.
Fig. 7 is a view of a honeycomb sandwich panel assembled by bonding a plate material to the other surface of a hexagonal cell type honeycomb core having a plate material bonded to one side surface.
[Explanation of symbols]
1 Cleaning device body
3 Steam passage
4 Washing room
5 Vapor supply port (cleaning liquid vapor supply means)
6 Vacuum exhaust port (vacuum suction means)
10 Shower nozzle (shower liquid supply means)
11 Drain pan (cleaning liquid storage part)
12 Inert gas injection nozzle (inert gas supply means)
13 Cleaning liquid supply port (cleaning liquid supply means)
14 Cleaning liquid outlet (cleaning liquid discharging means)
15 Object to be cleaned
22 Steam generation chamber
25 Cleaning liquid storage room
41 Honeycomb core
43 baskets

Claims (8)

被洗浄体を洗浄室内に配置する被洗浄体配置工程と、
前記洗浄室内の気圧を0.27〜4.00kPaの範囲に、かつ、被洗浄体の温度を70〜85℃の範囲に保ちながらノルマルパラフィン洗浄液を下方から噴出させて被洗浄体を洗浄する洗浄工程と、
前記洗浄室内の気圧を1.33kPa以下の範囲に、かつ、被洗浄体の温度を70〜85℃の範囲に保ちながら被洗浄体を乾燥する乾燥工程と、を含み、
前記洗浄工程が、ノルマルパラフィン洗浄液を洗浄室内の下部に配置した洗浄液貯蔵部に導入した後、洗浄室内の気圧を0.27〜1.33kPaの範囲に保ちながら洗浄液を沸騰させる洗浄液沸騰工程と、前記洗浄室内の気圧を1.33〜4.00kPaの範囲に保ちながら不活性ガスを洗浄液が押し上げられるように洗浄液中に送り込む不活性ガス供給工程と、のうちの少なくとも一方の工程により、被洗浄体の下方から洗浄液を吹き付けて被洗浄体を洗浄する工程であることを特徴とする洗浄方法。
A to-be-cleaned object arranging step for arranging the to-be-washed object in the cleaning chamber;
Cleaning in which the object to be cleaned is cleaned by ejecting a normal paraffin cleaning liquid from below while maintaining the pressure in the cleaning chamber in the range of 0.27 to 4.00 kPa and the temperature of the object to be cleaned in the range of 70 to 85 ° C. Process,
Wherein the cleaning chamber pressure in the range 1.33 kPa, and viewed including the step of drying the cleaning object while keeping the temperature in the range of 70 to 85 ° C. of the cleaning object, and
After the cleaning step introduces the normal paraffin cleaning liquid into the cleaning liquid storage unit disposed at the lower part of the cleaning chamber, the cleaning liquid boiling step of boiling the cleaning liquid while maintaining the atmospheric pressure in the cleaning chamber in the range of 0.27 to 1.33 kPa, At least one of the inert gas supply step of sending the inert gas into the cleaning liquid so that the cleaning liquid is pushed up while maintaining the atmospheric pressure in the cleaning chamber in the range of 1.33 to 4.00 kPa, to be cleaned A cleaning method characterized by being a step of cleaning a body to be cleaned by spraying a cleaning liquid from below the body .
前記被洗浄体が、ハニカムコア単体または片側面に板材を接着したハニカムコアであり、前記被洗浄体配置工程においてハニカムコアのセルの開放端を下方に向けて水平に洗浄室内に配置することを特徴とする、請求項1に記載の洗浄方法。  The object to be cleaned is a honeycomb core alone or a honeycomb core in which a plate material is bonded to one side surface, and in the object to be cleaned arrangement step, the honeycomb core cells are arranged horizontally in the cleaning chamber with the open end facing downward. The cleaning method according to claim 1, wherein the cleaning method is characterized. 前記洗浄工程において、被洗浄体を水平方向に揺動させることを特徴とする、請求項1または2に記載の洗浄方法。  3. The cleaning method according to claim 1, wherein in the cleaning step, the object to be cleaned is swung horizontally. 前記被洗浄体配置工程と洗浄工程の間に、
洗浄室内の気圧を1.33〜4.00kPaに保ちながら、70〜85℃の温度範囲にあるノルマルパラフィン洗浄液の蒸気を洗浄室内に供給して被洗浄体を蒸気洗浄する一次蒸気脱脂工程を有することを特徴とする、請求項1〜のいずれか1項に記載の洗浄方法。
Between the cleaning object arranging step and the cleaning step,
A primary steam degreasing step is performed in which the vapor of the normal paraffin cleaning liquid in the temperature range of 70 to 85 ° C. is supplied into the cleaning chamber and the object to be cleaned is steam cleaned while maintaining the pressure in the cleaning chamber at 1.33 to 4.00 kPa. The washing | cleaning method of any one of Claims 1-3 characterized by the above-mentioned.
前記洗浄工程と乾燥工程の間に、
被洗浄体の下方からノルマルパラフィン洗浄液からなるシャワー液を供給して被洗浄体を洗浄する仕上げ洗浄工程と、洗浄室内の気圧を1.33〜4.00kPaの範囲に保ちながら70〜85℃の温度範囲にあるノルマルパラフィン洗浄液の蒸気を洗浄室内に供給して被洗浄体を蒸気洗浄する二次蒸気脱脂工程と、を有することを特徴とする、請求項1〜のいずれか1項に記載の洗浄方法。
Between the washing process and the drying process,
A finish cleaning process for supplying a shower liquid composed of a normal paraffin cleaning liquid from below the object to be cleaned to clean the object to be cleaned, and a pressure of 70 to 85 ° C. while maintaining the pressure in the cleaning chamber within a range of 1.33 to 4.00 kPa. and having a secondary vapor degreasing step of the cleaning object to vapor cleaning by supplying the vapor of normal paraffins cleaning liquid in the temperature range in the cleaning chamber, and according to any one of claims 1-4 Cleaning method.
被洗浄体を内部配置する密閉可能な洗浄室と、
洗浄液蒸気を洗浄室内に供給する洗浄液蒸気供給手段と、
前記洗浄室内を真空吸引する真空吸引手段と、
前記洗浄室内の下部に配置して前記被洗浄体の下方からシャワー液を供給するシャワー液供給手段と、
前記洗浄室の前記シャワー液供給手段よりもさらに下部に配置した洗浄液貯蔵部と、
前記洗浄液貯蔵部にノルマルパラフィン洗浄液を供給する洗浄液供給手段と、
前記洗浄液貯蔵部の底部に配置して洗浄液を排出する洗浄液排出手段と、
前記洗浄液貯蔵部に配置して不活性ガスを洗浄室内に供給する不活性ガス供給手段と、
洗浄室内の温度を70〜85℃に調整する洗浄室温度調整手段と、を備
前記不活性ガス供給手段は、前記真空吸引手段により前記洗浄室内の気圧が1.33〜4.00kPaの範囲に保たれた状態で、被洗浄体の下方から洗浄液を吹き付けて被洗浄体を洗浄するために、洗浄液が押し上げられるように洗浄液中に不活性ガスを送り込むことを特徴とする洗浄装置。
A sealable cleaning chamber in which the object to be cleaned is placed;
Cleaning liquid vapor supply means for supplying cleaning liquid vapor into the cleaning chamber;
Vacuum suction means for vacuum suction of the cleaning chamber;
Shower liquid supply means that is disposed in the lower part of the cleaning chamber and supplies shower liquid from below the object to be cleaned;
A cleaning liquid storage section disposed further below the shower liquid supply means of the cleaning chamber;
Cleaning liquid supply means for supplying a normal paraffin cleaning liquid to the cleaning liquid storage unit;
A cleaning liquid discharging means disposed at the bottom of the cleaning liquid storage section for discharging the cleaning liquid;
An inert gas supply means arranged in the cleaning liquid storage section to supply an inert gas into the cleaning chamber;
E Bei a cleaning compartment temperature adjusting means for adjusting the temperature of the wash chamber 70 to 85 ° C., the
The inert gas supply means cleans the object to be cleaned by spraying a cleaning liquid from below the object to be cleaned in a state where the pressure in the cleaning chamber is maintained within a range of 1.33 to 4.00 kPa by the vacuum suction means. In order to do so, an inert gas is sent into the cleaning liquid so that the cleaning liquid is pushed up .
更に、前記洗浄室に内部配置した被洗浄体を水平方向に揺動させる揺動手段を備えることを特徴とする、請求項に記載の洗浄装置。The cleaning apparatus according to claim 6 , further comprising a swinging unit configured to swing a body to be cleaned disposed in the cleaning chamber in a horizontal direction. 更に、蒸気発生室および洗浄液貯蔵室を含み、前記洗浄液貯蔵部内の洗浄液を蒸気発生室に導き蒸気を発生させ、発生させた蒸気を前記洗浄室内に導く流路系統と、前記蒸気発生室で発生させた蒸気を凝縮させて洗浄液貯蔵室に導き、洗浄液貯蔵室から洗浄液を前記シャワー液供給手段および洗浄液供給手段に導く流路系統と、を備えることを特徴とする、請求項またはに記載の洗浄装置。Furthermore, a steam generation chamber and a cleaning liquid storage chamber are included, the cleaning liquid in the cleaning liquid storage unit is guided to the steam generation chamber to generate steam, and the generated steam is generated in the cleaning chamber. condensing the vapor obtained by guided in the cleaning liquid storage chamber, characterized in that it comprises a flow path system for guiding the cleaning liquid from the cleaning liquid storage chamber to the shower liquid supplying means and the cleaning liquid supply means, and according to claim 6 or 7 Cleaning equipment.
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JPH04286187A (en) * 1991-03-15 1992-10-12 Fujitsu Ltd Removing method for flux of printed board unit
JPH05179473A (en) * 1991-12-27 1993-07-20 Nippon Heizu:Kk Degreasing cleaning method
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