JPH1094766A - Washing device using high density liquefied gas - Google Patents

Washing device using high density liquefied gas

Info

Publication number
JPH1094766A
JPH1094766A JP8252962A JP25296296A JPH1094766A JP H1094766 A JPH1094766 A JP H1094766A JP 8252962 A JP8252962 A JP 8252962A JP 25296296 A JP25296296 A JP 25296296A JP H1094766 A JPH1094766 A JP H1094766A
Authority
JP
Japan
Prior art keywords
pressure
liquefied gas
resistant
cleaning
washer
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.)
Granted
Application number
JP8252962A
Other languages
Japanese (ja)
Other versions
JP3074290B2 (en
Inventor
Kunio Arai
邦夫 新井
Hiroshi Inomata
宏 猪股
Richard Lee Smith
スミス・リチャード・リー
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SHOES REFRESHER KAIHATSU KYODO
SHOES REFRESHER KAIHATSU KYODO KUMIAI
Original Assignee
SHOES REFRESHER KAIHATSU KYODO
SHOES REFRESHER KAIHATSU KYODO KUMIAI
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Priority to JP08252962A priority Critical patent/JP3074290B2/en
Application filed by SHOES REFRESHER KAIHATSU KYODO, SHOES REFRESHER KAIHATSU KYODO KUMIAI filed Critical SHOES REFRESHER KAIHATSU KYODO
Priority to US09/043,413 priority patent/US6092538A/en
Priority to PCT/JP1997/003409 priority patent/WO1998013149A1/en
Priority to EP97941235A priority patent/EP0893166A4/en
Priority to KR1019980702074A priority patent/KR100342720B1/en
Priority to CA002232768A priority patent/CA2232768C/en
Priority claimed from CA002232768A external-priority patent/CA2232768C/en
Priority to NO19981308A priority patent/NO316665B1/en
Priority to CN98108789A priority patent/CN1107554C/en
Publication of JPH1094766A publication Critical patent/JPH1094766A/en
Application granted granted Critical
Publication of JP3074290B2 publication Critical patent/JP3074290B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B08CLEANING
    • B08BCLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B3/00Cleaning by methods involving the use or presence of liquid or steam
    • B08B3/04Cleaning involving contact with liquid
    • B08B3/10Cleaning involving contact with liquid with additional treatment of the liquid or of the object being cleaned, e.g. by heat, by electricity or by vibration
    • B08B3/12Cleaning involving contact with liquid with additional treatment of the liquid or of the object being cleaned, e.g. by heat, by electricity or by vibration by sonic or ultrasonic vibrations

Landscapes

  • Cleaning Or Drying Semiconductors (AREA)
  • Cleaning By Liquid Or Steam (AREA)

Abstract

PROBLEM TO BE SOLVED: To enable almost complete reduction of expense items, attainment of effective washing by revelation of strong washing force and dissolving of resticking by this, and washing of fouling components of hardly soluble inorganic compounds, polar materials and the like even in the case of solvent having critical temperature near room temperature. SOLUTION: In a recirculation system in which high density liquefied gas is closed, plural preaching nozzles 3, low pressure chambers 10 for expanding compressed liquid 5, and a forcibly agitating device of soundwave generators 12 and an agitating blade 11 are arranged in a pressure washer 1 to attain strong washing accompanied by bubbling. A pressure recovery vessel 14 for receiving washing treated liquid is positioned below the washer 1, and a drain cylinder 16 which is freely attachably and detachably assembled therewith is provided, hung therefrom, and also a temperature controller 15 is incorporated in the vessel 14, and contaminated liquid of preaching is immediately received from the pressure washing chamber by a chamber branching function. Furthermore, the washer 1 is made in vapor phase communication with a high density liquefied gas feeding cylinder 18 above, and solvent separation and conveyance is performed by vaporization by the temperature controller 15, and also contaminant settled and concentrated liquid is discharged through a drain cylinder 16.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、高価なコンプレッ
サーやポンプ等の高圧発生装置を一切必要とせずに高い
洗浄効率を奏する高密度液化ガスを使用の洗浄装置に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cleaning apparatus using a high-density liquefied gas which achieves high cleaning efficiency without requiring any high-pressure generator such as an expensive compressor or pump.

【0002】[0002]

【従来の技術】耐圧洗浄器内に半導体等の被洗浄物を収
納し、超臨界供給手段により、超臨界流体を耐圧洗浄器
に注入して超臨界流体を被洗浄物に接触させると、被洗
浄物に付着する水分、有機物が超臨界流体に溶解し、超
臨界流体に移動する。この水分や有機物を溶解した超臨
界流体を、適宜の手段により、耐圧洗浄器から排除する
と、あとに精密洗浄された被洗浄物が得られる。このも
のは水分が除去されているので、従来の所謂ウエット洗
浄法における煩わしい乾燥仕上げが不要である。
2. Description of the Related Art When an object to be cleaned such as a semiconductor is accommodated in a pressure-resistant cleaning device, a supercritical fluid is injected into the pressure-resistant cleaning device by a supercritical supply means, and the supercritical fluid is brought into contact with the object to be cleaned. Water and organic substances adhering to the cleaning object dissolve in the supercritical fluid and move to the supercritical fluid. When the supercritical fluid in which the water or the organic substance is dissolved is removed from the pressure-resistant cleaning device by an appropriate means, an object to be cleaned which is precisely cleaned later can be obtained. Since the water has been removed, it is not necessary to perform a troublesome dry finish in a conventional so-called wet cleaning method.

【0003】上記の汚染物を溶解した超臨界流体を分離
槽で減圧させると溶解している汚染物が析出し、汚染物
を放出した超臨界流体は再び利用することが可能であ
る。これは、図4の純物質の状態図と超臨界流体のグラ
フに見られるように臨界点近傍で、圧力および温度の条
件がP>Pc (臨界圧力),T>Tc (臨界温度)であ
る高密度流体のことを意味する超臨界流体がもつ他に見
られない特性の (1)わずかの圧力変化で大きな密度変化が得られる。
一般に物質の溶解度は密度と比例するので、圧力変化の
みにより大きな溶解度差が得られることになる。 (2)超臨界流体の密度は、液体と類似しているが、低
粘性,高拡散性である。したがって、物質移動の面でよ
り有利になる。をたくみに利用した半導体基板等の洗浄
に用いられるようになった最新の洗浄技術である。
When the supercritical fluid in which the contaminants are dissolved is depressurized in a separation tank, the dissolved contaminants are precipitated, and the supercritical fluid that has released the contaminants can be reused. This is because the pressure and temperature conditions are P> P c (critical pressure) and T> T c (critical temperature) near the critical point as seen in the phase diagram of the pure substance and the graph of the supercritical fluid in FIG. (1) A large change in density can be obtained by a slight change in pressure.
In general, since the solubility of a substance is proportional to the density, a large difference in solubility can be obtained only by a change in pressure. (2) The density of a supercritical fluid is similar to that of a liquid, but has low viscosity and high diffusivity. Therefore, it is more advantageous in terms of mass transfer. This is the latest cleaning technology that has come to be used for cleaning semiconductor substrates and the like that make good use of the technology.

【0004】その原理は、第一に、超臨界流体の粘度が
小さいことは、狭い部分への侵入がし易いことを示し、
該流体の密度が大きいことは、基板に付着・含浸する汚
染物質、特に有機質の流体への溶解性が高いこと、第二
に、上記した洗浄作用は、汚染物質を含有する超臨界流
体がもたらすが、その密度を小さくすることにより溶解
作用が小さくなり、その分、上記した含有成分を液状及
び固体状に析出する。従って、減圧された分離槽で、こ
れらの成分を回収できることを利用して成る。汚染物を
析出して浄化された超臨界流体は貯蔵手段を介して耐圧
洗浄器にリサイクルするとして閉じられた再循環システ
ムが構築される。採用されるガスとしては、炭酸ガス、
酸化窒素、エタン、ヘキサン、プロパン等が用いられる
が、特に、炭酸ガスは、不燃性、無害、低廉であり、し
かも、臨界温度が31.1℃、臨界圧力が72.8気圧
であって、取扱いが容易であるので好ましく用いられて
いる。
[0004] The principle is that firstly, the low viscosity of the supercritical fluid indicates that it is easy to penetrate into narrow parts,
The high density of the fluid means that the contaminants attached to and impregnated on the substrate have high solubility in organic fluids. Secondly, the above-mentioned cleaning action is provided by the supercritical fluid containing the contaminants. However, by reducing the density, the dissolving action is reduced, and accordingly, the above-mentioned components are deposited in a liquid or solid state. Therefore, it utilizes the fact that these components can be recovered in a decompressed separation tank. A closed recirculation system is constructed in which the supercritical fluid purified by depositing the contaminants is recycled to the pressure washer through the storage means. The gases used are carbon dioxide,
Nitrogen oxide, ethane, hexane, propane and the like are used. In particular, carbon dioxide is nonflammable, harmless, inexpensive, and has a critical temperature of 31.1 ° C. and a critical pressure of 72.8 atm. It is preferably used because it is easy to handle.

【0005】既述の再循環システムにおける流体搬送手
段には一般にコンプレッサーやポンプ等の高圧発生装置
が用いられる。これ等の装置は高い耐圧能力が要求され
るので,洗浄装置はきわめて高価になる。洗浄力を溶解
作用のみに依存したのでは、効果的でない場合には、強
制攪拌を加えるとしたり、超音波エネルギーをキャビテ
ーションすなわち気泡の形成およびそれに続く崩壊を生
起させるべく投射したりすることもなされる。また、難
溶の各種汚れ成分に有効なエントレーナも解明されてい
る。
[0005] Generally, a high-pressure generator such as a compressor or a pump is used as a fluid conveying means in the recirculation system described above. Since these devices require high pressure resistance, the cleaning device becomes extremely expensive. Relying solely on the dissolving power, if not effective, may require forced agitation or the application of ultrasonic energy to cavitation, i.e., the formation of bubbles and subsequent collapse. You. In addition, effective entrainers for various hardly soluble dirt components have been elucidated.

【0006】上述の如き超臨界流体の特性は亜臨界流体
をも持つ。亜臨界流体とは、圧力─温度状態図において
臨界点手前の領域にある流体をいい、圧縮液体と圧縮気
体の併存状態にある。この領域の流体は、超臨界流体と
は区別される。亜臨界あるいは広義には臨界点近傍の超
臨界領域に存在するものは高密度液化ガスと称する。
[0006] The characteristics of the supercritical fluid as described above also include a subcritical fluid. A subcritical fluid is a fluid in a region just before a critical point in a pressure-temperature state diagram, in which a compressed liquid and a compressed gas coexist. Fluids in this region are distinguished from supercritical fluids. Subcritical or, in a broad sense, those present in the supercritical region near the critical point are called high-density liquefied gases.

【0007】この臨界点近傍の高密度液化ガスを溶媒に
使用するとして超臨界流体の厳しい耐圧要求を緩らげ、
出費項目の低減化を期した比較的簡単な洗浄用手段の提
案が特開平7─171527号等にある。当該特開平7
─171527号の特徴は洗浄器に温度制御手段を配
し、かつ、超音波エネルギーによるキャビテーション利
用にある。
The use of a high-density liquefied gas near the critical point as a solvent relaxes the strict pressure requirement of the supercritical fluid,
Japanese Patent Application Laid-Open No. 171527/1995 proposes a relatively simple cleaning means for reducing the cost items. Japanese Patent Laid-Open No. 7
The feature of the '171527 is that a temperature control means is provided in the cleaning device, and that cavitation using ultrasonic energy is used.

【0008】すなわち、洗浄器において温度制御手段で
液化を促して超音波エネルギーによるキャビテーション
を作用させ、超臨界状態の洗浄利点を断念した不利を補
うとした点にある。
That is, in the cleaning device, liquefaction is promoted by temperature control means to cause cavitation by ultrasonic energy, thereby compensating for the disadvantage of abandoning the advantages of cleaning in a supercritical state.

【0009】[0009]

【発明が解決しようとする課題】叙上の従来の高密度液
化ガス利用の洗浄手段にあっては、以下列挙の難点がみ
られる。 (1)閉じられた再循環システムにおける汚れ成分分
離、溶媒回収工程における高密度液化ガスの搬送動力に
貯蔵手段に圧縮器で搬送圧力を付与する手段を採用して
おり出費項目の低減化不充分のままである。 (2)洗浄力の不足を超音波によるキャビテーションで
補うとしているが、被洗浄物の汚染度合によってはこの
程度の強制攪拌では不充分な場合もあり、か様な事態に
対応し得ないし、また、洗浄作用は被洗浄物を液体中に
浸漬しておいてなすものであるが、液体中には固体状の
汚染物質も多く存在し浮遊しており、これが被洗浄物に
再付着することとなる。かかる再付着が許容されない物
にあっては、再度洗浄流体で洗浄するという工程が追加
されねばならないという不便がある。 (3)溶媒に室温付近に臨界温度を有する(CO2 等)
高密度液化ガスを使用する場合、難溶性の汚れ成分特に
無機化合物や極性物質の汚れ成分の洗浄には、全く効果
がないが、かかる難溶性の汚れ成分の洗浄についての解
決がなされていない。
The above-mentioned conventional cleaning means using high-density liquefied gas has the following difficulties. (1) A means for applying a conveying pressure by a compressor to a storage means is used for a conveying power of the high-density liquefied gas in a closed recirculation system for separating dirt components and a solvent for a high-density liquefied gas. Remains. (2) The lack of detergency is compensated for by cavitation using ultrasonic waves. However, depending on the degree of contamination of the object to be cleaned, such forced stirring may not be sufficient, and such situations cannot be dealt with. The cleaning action is performed by immersing the object to be cleaned in a liquid.However, there are many solid contaminants in the liquid, which are suspended, and this reattaches to the object to be cleaned. Become. In the case where such re-adhesion is not allowed, there is an inconvenience that a step of washing again with a washing fluid must be added. (3) The solvent has a critical temperature near room temperature (such as CO 2 )
When a high-density liquefied gas is used, there is no effect at all for cleaning hardly soluble dirt components, particularly dirt components of inorganic compounds and polar substances, but there is no solution for cleaning such hardly soluble dirt components.

【0010】本発明は、叙上の事情に鑑みなされたもの
で、その目的とするところは、ほぼ完璧な出費項目の低
減化、強力な洗浄力発現とこれによる再付着の解消によ
る効率的洗浄の達成、室温付近に臨界温度を有する溶媒
の場合でも難溶の無機化合物や極性物質等の汚れ成分の
洗浄を可能とさせる等を達成した高密度液化ガスを使用
の洗浄装置を提供しようとするものである。
SUMMARY OF THE INVENTION The present invention has been made in view of the above circumstances, and has as its object the almost perfect reduction of the cost items, the development of a strong cleaning power, and the efficient cleaning by eliminating reattachment. To provide a cleaning apparatus using a high-density liquefied gas that has achieved, for example, a solvent having a critical temperature near room temperature, enabling the cleaning of contaminant components such as hardly soluble inorganic compounds and polar substances. Things.

【0011】[0011]

【課題を解決するための手段】上記目的を達成するため
に、本発明の高密度液化ガスを使用の洗浄装置は、被洗
浄物を収納する洗浄カゴを器内空中に支持し当該被洗浄
物へ圧縮液体を直射噴霧する複数のノズルと器上部に接
続の低圧室とを備え、器底に回転翼と器側壁に当該回転
翼に指向した音波発生装置とからなる攪拌装置を設けた
耐圧洗浄器と、該耐圧洗浄器よりも低い位置に設置の温
度調節手段を備えると共に着脱自在に組付くドレンボン
ベを垂下設の洗浄処理後の洗浄液体を受け入れるための
耐圧洗浄器の分室としての耐圧回収容器と、該耐圧洗浄
器よりも高い位置に設置の温度調節手段を備えると共に
該耐圧容器上部ガスを受け入れるために耐圧回収容器と
の間の上部間を連絡の貯蔵手段としての高密度液化ガス
供給シリンダーと、該高密度液化ガス供給シリンダーと
耐圧洗浄器との間の液送管途中に接続のエントレーナ容
器とから閉じられた再循環システムが構成され、これ等
各圧縮液体送受容器間の上部間を互いの上部ガスが連通
し得るよう連絡して成るとしたものである。
In order to achieve the above object, a cleaning apparatus using a high-density liquefied gas according to the present invention comprises: Pressure washing with a plurality of nozzles for directly spraying the compressed liquid into the container and a low-pressure chamber connected to the upper part of the vessel, and a stirrer comprising a rotor at the bottom and a sound wave generator directed to the rotor at the side of the vessel. A pressure recovery container as a compartment of a pressure-resistant washer for receiving a cleaning liquid after a cleaning process, wherein a drain cylinder is provided with a temperature control means installed at a lower position than the pressure-resistant washer and detachably assembled. And a high-density liquefied gas supply cylinder as storage means for providing a temperature control means installed at a position higher than the pressure-resistant washer and communicating between the upper part of the pressure-resistant container and the pressure-resistant recovery vessel to receive the upper gas. When A closed recirculation system is configured from a connected entrainer vessel in the middle of the liquid feed pipe between the high-density liquefied gas supply cylinder and the pressure-resistant washer. The upper gas is connected so that it can communicate with the upper gas.

【0012】耐圧洗浄器に対し耐圧回収容器、高密度液
化ガス供給シリンダーから成るリサイクル系を切換え自
在に複数設けるを良しとする。上記装置のおいて、溶媒
原料ボンベを耐圧洗浄器よりも高い位置に設置すると共
に温度調節手段を備え、かつ、耐圧洗浄器との上部間を
互いの上部ガスが連通し得るように連絡すると良い。
It is preferable that a plurality of recycle systems including a pressure-resistant recovery vessel and a high-density liquefied gas supply cylinder are provided for the pressure-resistant washer in a switchable manner. In the above apparatus, it is preferable that the solvent material cylinder is installed at a position higher than the pressure-resistant washer and that the apparatus is provided with a temperature adjusting means, and that the upper gas and the pressure-resistant washer are communicated so that the upper gases can communicate with each other. .

【0013】[0013]

【作用】臨界点近傍の亜臨界,超臨界の両域に存在する
ところの高密度液化ガスの利点を存分に活用する。すな
わち、臨界点近傍ほど加温気化、冷却液化の所要エネル
ギーは小さくて済むが、溶媒の搬送をこの気化、液化状
態での蒸気圧差による圧送、蒸気圧差を背にしたレベル
差設定の重力落下搬送で全て達成したので、高価な高圧
発生装置の必要がなく、出費項目の低減化が期し得る。
The present invention makes full use of the advantages of high-density liquefied gas that exists in both the subcritical and supercritical regions near the critical point. In other words, the energy required for heating and vaporization and cooling and liquefaction is smaller in the vicinity of the critical point, but the transport of the solvent is carried out by vaporization, vapor pressure difference in the liquefied state, and gravity drop transport with the level difference set against the vapor pressure difference. As a result, there is no need for an expensive high-pressure generator, and reduction in cost items can be expected.

【0014】分室の耐圧回収器を下位に有する耐圧洗浄
器は、耐圧回収器と連通状態で、複数のノズルの噴射に
よる前洗浄で落とされる塊状等の再付着のおそれある汚
れを直ちに器外に排出し、次いで行われる器内に溶媒充
満のもとでなされる本洗浄は前洗浄で生じた汚れを全く
含まずに済む有利のもとになし得る。この結果、再付着
のおそれある塊状等の汚れ成分の再付着の機会は完全に
失われ再付着が阻止される。また、繰り返し反復が可能
なため、完璧な洗浄が期し得る。
The pressure-resistant washer having a pressure-recovery device in the lower part of the compartment is in communication with the pressure-recovery device, and immediately removes dirt that may be re-adhered, such as lumps or the like, which are dropped by pre-washing by spraying a plurality of nozzles. The main washing, which is performed under solvent filling in the vessel which is drained and then performed, may be advantageous in that it does not contain any dirt generated in the prewash. As a result, the chance of reattachment of lump components such as lump which may possibly reattach is completely lost, and reattachment is prevented. In addition, since it can be repeated repeatedly, perfect washing can be expected.

【0015】さらに、低圧室を有して溶媒充満時に膨張
させることができるため、臨界点近傍特有の現象である
膨張によるバブリングが容易に発生し、これに起因する
キャビテーション所謂攪拌力を溶媒全体で享受できる。
高密度液化ガス単体のみでは難溶で洗浄できない汚れ成
分の場合には、対象物に応じた界面活性剤の添加によ
り、所謂ミセル化現象にて汚れ成分が溶解することが発
見されたので、これを利用して無機化合物、極性物質の
洗浄をも達成される。また、ミセル化された汚れ成分は
そのバリア効果でもって、再付着は防止され、洗浄力を
向上させる。
In addition, since a low-pressure chamber is provided and can be expanded when the solvent is filled, bubbling due to expansion, which is a phenomenon unique to the vicinity of the critical point, easily occurs, and cavitation caused by this, so-called stirring power, is generated in the entire solvent. You can enjoy.
In the case of dirt components that are hardly soluble and cannot be cleaned with only a high-density liquefied gas alone, it has been discovered that the addition of a surfactant according to the target dissolves the dirt components in a so-called micellization phenomenon. The cleaning of the inorganic compound and the polar substance can also be achieved by utilizing the above. Further, the micelle-formed dirt component is prevented from re-adhering due to its barrier effect, and the detergency is improved.

【0016】[0016]

【発明の実施の形態】本発明の実施の形態を図1に基づ
いて説明する。耐圧洗浄器1は被洗浄物を収納する洗浄
カゴ2を複数(効果的洗浄に必要)のノズル3の直下の
空中に支持する。ノズル3は首振り可能が好ましい。ノ
ズル3からジェット噴流で洗浄カゴ4内の被洗浄物に投
射されて前洗浄がなされる。ジェット噴流の当射の衝撃
エネルギーは汚染物質を強制剥離するのに有効である。
DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described with reference to FIG. The pressure-resistant cleaning device 1 supports a cleaning basket 2 for storing an object to be cleaned in the air immediately below a plurality of (necessary for effective cleaning) nozzles 3. The nozzle 3 is preferably capable of swinging. Pre-cleaning is performed by projecting from the nozzle 3 onto the object to be cleaned in the cleaning basket 4 by a jet stream. The impact energy of the jet jet is effective in forcibly separating contaminants.

【0017】当該耐圧洗浄器1に高圧配管4,該ノズル
3を介して圧縮液体5を送り込む高密度液化ガスを充填
の溶媒原料ボンベ6は、図示例にあっては、温度制御可
能に温度調節器7を装備のボックス8内に収容され、該
耐圧洗浄器1より高い位置に設置されていて、レベル差
落下作用のもと圧縮液体5を送り込むものとしている
(温度調節器7によるボンベ6が対耐圧洗浄器1よりも
高温設定での蒸気圧差で移送は確実にされるうえに、両
容器上部間連絡の高圧配管9の気相連通によりバックア
ップされる)。
In the illustrated example, a solvent raw material cylinder 6 filled with a high-density liquefied gas for feeding a compressed liquid 5 through the high-pressure pipe 4 and the nozzle 3 to the pressure-resistant washer 1 is temperature-controllable in the illustrated example. The compressed liquid 5 is accommodated in a box 8 equipped with a vessel 7 and is installed at a position higher than the pressure-resistant washer 1 so that the compressed liquid 5 is fed under a level difference dropping action. The transfer is ensured by the vapor pressure difference at a higher temperature setting than the pressure-resistant washer 1, and is backed up by the gas-phase communication of the high-pressure pipe 9 communicating between the upper portions of both containers.)

【0018】耐圧洗浄器1上部に接続して当該器空間拡
張用の低圧室10,…が設けられている。当該低圧室1
0によって耐圧洗浄器1中に充満の圧縮液体5に膨張に
よるバブリングを発生させることが可能である。また、
図3cに詳示の如く、洗浄カゴ2直下の器1底に回転翼
11を設けると共に器1側壁に該回転翼11を指向した
音波発生装置12を配して、超音波エネルギーとその投
射で回転する回転翼11とのキャビテーション,強制攪
拌動の相乗作用で一層の強力攪拌を可能とする。しかし
て、充満した圧縮液体5中に浸漬してなされる被洗浄物
の本洗浄は強烈なる攪拌のもとでなされ得る。叙上のバ
ブリング、キャビテーションは、その急激な減圧により
バクテリアや細菌を破壊・死滅させるのに有効となる。
A low-pressure chamber 10,... For expanding the space of the apparatus is provided connected to the upper part of the pressure-resistant cleaning apparatus 1. The low-pressure chamber 1
With 0, it is possible to cause bubbling of the filled compressed liquid 5 in the pressure-resistant washer 1 due to expansion. Also,
As shown in detail in FIG. 3c, a rotating blade 11 is provided on the bottom of the vessel 1 directly below the washing basket 2 and a sound wave generator 12 directed to the rotating blade 11 is arranged on the side wall of the vessel 1, and the ultrasonic energy and its projection are used. Cavitation with the rotating blades 11 and synergistic action of forced agitation enable more powerful agitation. Thus, the main cleaning of the object to be cleaned, which is performed by immersion in the filled compressed liquid 5, can be performed under intense stirring. The above-mentioned bubbling and cavitation are effective in destroying and killing bacteria and bacteria by the rapid decompression.

【0019】該配管4のノズル3手前にエントレーナ容
器13が接続されている。該エントレーナ容器13に
は、高密度液化ガス単体のみでは難溶で洗浄できない汚
れ成分を有する場合、汚れ成分に応じて親油,親水ある
いは両親媒性界面活性剤が予じめ収容され、オリフィス
作用でもって配管4内の圧縮液体5中に吸引添加され
る。当該界面活性剤は難溶な汚れ成分を所謂ミセル化現
象でもって溶かすので、そのバリア効果で再付着が生じ
難い。
An entrainer container 13 is connected to the pipe 4 just before the nozzle 3. When the entrainer container 13 has a dirt component that is hardly soluble and cannot be washed with only the high-density liquefied gas alone, an lipophilic, hydrophilic, or amphiphilic surfactant is stored in advance depending on the dirt component, and the orifice action Thus, it is sucked into the compressed liquid 5 in the pipe 4. Since the surfactant dissolves the hardly soluble dirt component by a so-called micellization phenomenon, reattachment hardly occurs due to its barrier effect.

【0020】耐圧洗浄器1よりも低い位置に洗浄液体
5′を受け入れる耐圧回収容器14が配される。受入れ
は、レベル差落下、蒸気圧差、気相連通作用によりすみ
やかになされる。当該容器14は温度調節器15を内蔵
し、かつ、器底より着脱自在に組付くドレンボンベ16
を垂下する。よって再循環系との連絡を断っておいてた
っぷりと汚れ成分を収容したドレンボンベ16を取りは
ずし所定場所で空にして再装着することが可能である。
耐圧回収容器14は耐圧洗浄器1の分室役割を果たす。
すなわち、上述の前洗浄時連通して落下する汚れ(塊状
のものを含む)をたっぷりと含んだ洗浄液体5’を直ち
に受け入れて耐圧洗浄器1内に止まらせない(図3
a)。よって、該連通を断ってなされる耐圧洗浄器1内
に圧縮液体5を充満させてなされる前述の本洗浄では前
洗浄での汚れを含むことなくなされるので洗浄効率の向
上が図れる(図3b)。これによって、所謂再付着は完
全に解消する。
At a position lower than the pressure-resistant washer 1, a pressure-resistant recovery container 14 for receiving the cleaning liquid 5 'is arranged. Acceptance is made promptly by falling levels, vapor pressure differences, and gas phase communication. The container 14 has a built-in temperature controller 15 and a drain cylinder 16 detachably assembled from the bottom of the container.
Droop. Therefore, it is possible to remove the drain cylinder 16 containing a large amount of the dirt component, remove the drain cylinder 16 from the communication with the recirculation system, and empty the drain cylinder 16 at a predetermined place, and then remount the drain cylinder 16.
The pressure-resistant recovery container 14 serves as a compartment of the pressure-resistant cleaning device 1.
In other words, the cleaning liquid 5 'containing plenty of dirt (including lumps) that is communicated and dropped during the pre-cleaning described above is immediately received and does not stop in the pressure-resistant cleaning device 1 (FIG. 3).
a). Therefore, in the above-described main cleaning, which is performed by filling the compressed liquid 5 in the pressure-resistant cleaning device 1 that is cut off the communication, the cleaning is performed without including dirt in the pre-cleaning, and the cleaning efficiency can be improved (FIG. 3B). ). Thereby, the so-called redeposition is completely eliminated.

【0021】この洗浄を反復することで高い洗浄効率が
保証される。しかして、耐圧洗浄器と耐圧回収器14と
により再付着阻止機能を有した優れた洗浄機構が提供さ
れる。しかして、高密度液化ガス単体のみでは難溶で洗
浄し切れない汚れ成分を含む場合、その汚れ成分に応じ
た界面活性剤を投入させ、その所謂ミセル化現象による
洗浄力向上と再付着防止機能を、ノズルの衝撃エネルギ
ーの強制剥離、バブリングによるキャビテーション、超
音波による攪拌と共に合目的に複合化させるとして、一
層の洗浄効率向上を図ることができる。
By repeating this cleaning, high cleaning efficiency is guaranteed. Thus, an excellent cleaning mechanism having a function of preventing redeposition is provided by the pressure-resistant cleaning device and the pressure-resistant recovery device 14. However, when a high-density liquefied gas alone contains a dirt component that is hardly soluble and cannot be completely cleaned, a surfactant is introduced according to the dirt component to improve the detergency and prevent re-adhesion by the so-called micelle phenomenon. Can be combined as desired with forced separation of the impact energy of the nozzle, cavitation by bubbling, and stirring by ultrasonic waves, thereby further improving the cleaning efficiency.

【0022】耐圧洗浄容器1との間には気相連通用の配
管17が連絡されている。耐圧回収容器14の気相は更
に耐圧洗浄容器1より高い位置に設置の閉じられた再循
環システムの貯蔵手段としての高密度液化ガス供給シリ
ンダー18上部と配管19を介して連絡していて、耐圧
回収容器14の温度調節器15で加温気化された溶媒は
蒸気圧差をもって上位のシリンダー18に搬送されるも
のとなっている。一方、気相の密度は低く溶解力も小さ
いため、比重の重い汚染物質やエントレーナは下の液相
に濃縮されて沈澱する。この濃縮部をドレンボンベ16
に落下させて系外に排出して汚れ成分の分離をなす。つ
まり、この耐圧回収容器14と高密度液化ガス供給シリ
ンダー18とからなる分離回収機構は、汚れ成分の除去
と溶媒の回収搬送を何ら高圧発生装置を要せずに達成す
る。究極的な出費項目の低減化実現である。
A pipe 17 for communicating with the gas phase is connected to the pressure-resistant washing vessel 1. The gas phase of the pressure recovery container 14 is further connected to the upper part of the high-density liquefied gas supply cylinder 18 as storage means of a closed recirculation system installed at a position higher than the pressure-resistant cleaning container 1 via a pipe 19, The solvent heated and vaporized by the temperature controller 15 of the recovery container 14 is transported to the upper cylinder 18 with a vapor pressure difference. On the other hand, since the gas phase has a low density and a low dissolving power, contaminants and entrainers having a high specific gravity are concentrated and precipitated in a lower liquid phase. This enrichment section is replaced with a drain cylinder 16
To separate the contaminated components by discharging to the outside of the system. That is, the separation and recovery mechanism including the pressure-resistant recovery container 14 and the high-density liquefied gas supply cylinder 18 achieves the removal of the dirt component and the recovery and transportation of the solvent without any high-pressure generator. This is the ultimate reduction in cost items.

【0023】シリンダー18は温度調節器20を内蔵し
ていて、これをもって上記気化溶媒を冷却液化する。シ
リンダー18下部の配管21は耐圧洗浄器1のノズル3
に連絡すべく該配管4に接続している。このレベル差落
下搬送を補完すべく気相間連絡管22が架配されてい
る。尚、この際、該温度調節器20の加温による温度差
設定でもって落下を補完する。ここに温度調節手段のみ
で洗浄溶媒の循環が可能な全く新規な再循環システムが
提供される。
The cylinder 18 has a built-in temperature controller 20, which cools and vaporizes the vaporized solvent. The pipe 21 below the cylinder 18 is the nozzle 3 of the pressure-resistant washer 1
Is connected to the pipe 4. A gas-phase communication pipe 22 is provided to complement the level difference drop conveyance. At this time, the fall is complemented by setting the temperature difference by heating the temperature controller 20. Here, there is provided a completely new recirculation system in which the washing solvent can be circulated only by the temperature control means.

【0024】[0024]

【実施例】図2紹介のものは、上述の再循環系(耐圧回
収容器14−高密度液化ガス供給シリンダー18)を複
数設(図示例は2系統)したものを示し、洗浄器1の稼
動を高め得る。両系統の液送は三方弁バルブ23,24
で切換えされ、気送は三方弁バルブ25夫々持ち出しの
バルブ26,26によって連絡・遮断がなされる。これ
を用いて、溶媒をCO2 とした操作態様例を以下説明す
る。
FIG. 2 shows an example in which a plurality of the above-mentioned recirculation systems (pressure-recovery container 14-high-density liquefied gas supply cylinder 18) are provided (two systems in the illustrated example). Can be increased. The three-way valve 23, 24
The pneumatic feeding is communicated and shut off by valves 26, 26 taken out of the three-way valve 25, respectively. Using this, an operation example in which the solvent is CO 2 will be described below.

【0025】本発明装置全体を空調コントロール装置2
7で人が作業しやすい温度20℃に保たれた室28内に
配置した。温度調節器7によりボンベ6を30℃にコン
トロールした。洗浄器1内の圧縮液体5は界面活性剤や
被洗浄物のために20℃位に低下した。耐圧回収容器1
4では温度調節器15で30℃に再加温した。これで上
澄液はほとんどが気化した。一系統の気化時間は4ガロ
ンで40分程であったので2系統で20分に短縮する。
高密度液化ガス供給シリンダー18では温度調節器20
で0℃に冷却し圧縮液体5を充満させた。
The entire apparatus of the present invention is an air-conditioning control device 2
7 and placed in a room 28 maintained at a temperature of 20 ° C., where humans can easily work. The cylinder 6 was controlled at 30 ° C. by the temperature controller 7. The pressure of the compressed liquid 5 in the cleaning device 1 dropped to about 20 ° C. due to the surfactant and the object to be cleaned. Pressure recovery container 1
In No. 4, the temperature was reheated to 30 ° C. by the temperature controller 15. Most of the supernatant was now vaporized. Since the vaporization time of one system was about 40 minutes in 4 gallons, it is reduced to 20 minutes in two systems.
The high temperature liquefied gas supply cylinder 18 has a temperature controller 20.
And cooled to 0 ° C. to fill the compressed liquid 5.

【0026】一方、洗浄器1における被洗浄物の挿入か
ら洗浄まで10分位要するが、2系統にする事で、次の
洗浄の待機時間がほとんど無い、高稼動率が実現でき
た。
On the other hand, it takes about 10 minutes from the insertion of the object to be cleaned to the cleaning in the cleaning device 1, but by using two systems, a high operation rate with little waiting time for the next cleaning can be realized.

【0027】[0027]

【発明の効果】本発明は、以上説明したように構成され
ているので、以下に記載されるような効果を奏する。 (1)閉じられた再循環システム内のみでなく、これに
接続の溶媒原料ボンベからの溶媒の搬送の全てがレベル
差、蒸気圧差、気相連通の耐圧要求を受ける必要のない
機器を介して達成され、出費項目の低減化が著しい。 (2)耐圧洗浄器、耐圧回収器、高密度液化ガス供給シ
リンダー等の洗浄機構、分離回収機構は、強力な洗浄力
と効率的な汚染物系外排除と高圧発生装置を用いずに済
ませた溶媒回収を実現し、安価で効率的な洗浄装置を提
供する。 (3)高密度液化ガス単体のみでは難溶で洗浄できない
汚れ成分の場合には、対象物に応じた界面活性剤の添加
により、所謂ミセル化現象にて汚れ成分が溶解させるの
で、より一層洗浄効率を高めることができる。
Since the present invention is configured as described above, it has the following effects. (1) Not only in the closed recirculation system but also through the equipment that does not need to receive the level difference, the vapor pressure difference, and the pressure resistance of the gas phase communication, all of the transport of the solvent from the solvent material cylinder connected to it. This has been achieved, and the cost items have been significantly reduced. (2) The cleaning mechanism and separation / collection mechanism of the pressure-resistant washer, pressure-recovery device, high-density liquefied gas supply cylinder, etc. eliminated strong cleaning power, efficient removal of contaminants, and no high-pressure generator. Solvent recovery is provided, and an inexpensive and efficient cleaning device is provided. (3) In the case of a dirt component that cannot be washed because it is hardly soluble only with a high-density liquefied gas alone, the dirt component is dissolved by a so-called micellization phenomenon by adding a surfactant according to an object, so that further cleaning is performed. Efficiency can be increased.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明装置の基本的構成説明図である。FIG. 1 is an explanatory diagram of a basic configuration of a device of the present invention.

【図2】本発明装置のリサイクル系統を複数化例の説明
図である。
FIG. 2 is an explanatory diagram of an example in which a plurality of recycling systems of the apparatus of the present invention are provided.

【図3】aは耐圧洗浄器における荒洗浄,bは同じく本
洗浄,cは攪拌装置の説明図である。
3A is a diagram illustrating a rough cleaning in a pressure-resistant cleaning device, FIG. 3B is a diagram illustrating a main cleaning, and FIG.

【図4】純物質の状態図と超臨界流体、亜臨界流体領域
のグラフである。
FIG. 4 is a phase diagram of a pure substance and a graph of a supercritical fluid and a subcritical fluid region.

【符号の説明】[Explanation of symbols]

1 耐圧洗浄器 2 洗浄カゴ 3 ノズル 4 高圧配管 5 圧縮液体 5′ 洗浄液体 6 溶媒原料ボンベ 7 温度調節器 8 ボックス 9 高圧配管 10 低圧室 11 回転翼 12 音波発生装置 13 エントレーナ容器 14 耐圧回収容器 15 温度調節器 16 ドレンボンベ 17 配管 18 高密度液化ガス供給シリンダー 19 配管 20 温度調節器 21 配管 22 気相間連絡管 23 三方弁バルブ 24 三方弁バルブ 25 三方弁バルブ 26 バルブ 27 空調コントロール装置 28 室 DESCRIPTION OF SYMBOLS 1 Pressure-resistant washing machine 2 Cleaning basket 3 Nozzle 4 High-pressure pipe 5 Compressed liquid 5 'Cleaning liquid 6 Solvent material cylinder 7 Temperature controller 8 Box 9 High-pressure pipe 10 Low-pressure chamber 11 Rotary blade 12 Sound generator 13 Entrainer container 14 Pressure-resistant recovery container 15 Temperature controller 16 Drain cylinder 17 Pipe 18 High-density liquefied gas supply cylinder 19 Pipe 20 Temperature controller 21 Pipe 22 Gas-phase communication pipe 23 Three-way valve valve 24 Three-way valve valve 25 Three-way valve valve 26 Valve 27 Air-conditioning controller 28 Room

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 被洗浄物を収納する洗浄カゴを器内空中
に支持し当該被洗浄物へ圧縮液体を直射噴霧する複数の
ノズルと器上部に接続の低圧室とを備え、器底に回転翼
と器側壁に当該回転翼に指向した音波発生装置とからな
る攪拌装置を設けた耐圧洗浄器と、該耐圧洗浄器よりも
低い位置に設置の温度調節手段を備えると共に着脱自在
に組付くドレンボンベを垂下設の洗浄処理後の洗浄液体
を受け入れるための耐圧洗浄器の分室としての耐圧回収
容器と、該耐圧洗浄器よりも高い位置に設置の温度調節
手段を備えると共に該耐圧容器上部ガスを受け入れるた
めに耐圧回収容器との間の上部間を連絡の貯蔵手段とし
ての高密度液化ガス供給シリンダーと、該高密度液化ガ
ス供給シリンダーと耐圧洗浄器との間の液送管途中に接
続のエントレーナ容器とから閉じられた再循環システム
が構成され、これ等各圧縮液体送受容器間の上部間を互
いの上部ガスが連通し得るよう連絡して成るとしたこと
を特徴とする高密度液化ガスを使用の洗浄装置。
1. A washing basket for accommodating an object to be washed is supported in the interior of a container, and a plurality of nozzles for directly spraying a compressed liquid onto the object to be washed and a low-pressure chamber connected to an upper portion of the container are provided. A pressure washer provided with a stirrer comprising a wing and a sound wave generator directed to the rotary wing on the side wall of the vessel, and a drain cylinder provided with a temperature control means installed at a position lower than the pressure washer and detachably assembled. A pressure-resistant recovery container as a compartment of a pressure-resistant washer for receiving the cleaning liquid after the washing treatment, and a temperature control means installed at a higher position than the pressure-resistant washer, and receiving the upper gas of the pressure-resistant container. A high-density liquefied gas supply cylinder as a storage means for communicating between the upper part between the high-pressure liquefied gas supply cylinder and the pressure-recovery container, and an entrainer capacity connected in the middle of the liquid feed pipe between the high-density liquefied gas supply cylinder and the pressure-resistant washer A high-density liquefied gas, characterized in that a closed recirculation system is constituted from the vessel and the upper portion between each of the compressed liquid receivers is communicated so that the upper gases can communicate with each other. Use of washing equipment.
【請求項2】 耐圧洗浄器に対し耐圧回収容器、高密度
液化ガス供給シリンダーから成るリサイクル系を切換え
自在に複数設けたことを特徴とする請求項1記載の高密
度液化ガスを使用の洗浄装置。
2. A cleaning apparatus using a high-density liquefied gas according to claim 1, wherein a plurality of recyclable systems comprising a pressure-resistant recovery vessel and a high-density liquefied gas supply cylinder are provided for the pressure-resistant cleaning device in a freely switchable manner. .
【請求項3】 溶媒原料ボンベを耐圧洗浄器よりも高い
位置に設置すると共に温度調節手段を備え、かつ、耐圧
洗浄器との上部間を互いの上部ガスが連通し得るように
連絡した請求項1又は2記載の高密度液化ガスを使用の
洗浄装置。
3. The method according to claim 1, wherein the solvent raw material cylinder is installed at a higher position than the pressure-resistant washer, the temperature-controlling means is provided, and the upper gas and the pressure-resistant washer are communicated so that upper gas can communicate with each other. A cleaning apparatus using the high-density liquefied gas according to 1 or 2.
【請求項4】 被洗浄物を収納する洗浄カゴを器内空中
に支持し当該被洗浄物へ圧縮液体を直射噴霧する複数の
ノズルと器上部に接続の低圧室とを備え、器底に回転翼
と器側壁に当該回転翼に指向した音波発生装置とからな
る攪拌装置を設けた耐圧洗浄器の下位に、温度調節手段
を備えると共に着脱自在に組付くドレンボンベを垂下設
しの洗浄処理後の洗浄液体を受け入れるための分室とし
ての耐圧回収容器を付属させた再付着阻止機能を有する
洗浄機構。
4. A plurality of nozzles for supporting a washing basket for accommodating an object to be washed in the inside of a vessel and directly spraying a compressed liquid onto the article to be washed and a low-pressure chamber connected to an upper portion of the vessel, and rotating at a bottom of the vessel. After the cleaning process, a drain cylinder equipped with a temperature control means and detachably assembled is provided below the pressure-resistant washer provided with an agitator comprising a wing and a sound wave generator directed to the rotary wing on the side wall of the vessel. A cleaning mechanism with a re-adhesion prevention function with a pressure-resistant recovery container attached as a compartment for receiving the cleaning liquid.
【請求項5】 温度調節手段を備えると共に着脱自在に
組付くドレンボンベを垂下設の耐圧回収容器と、耐圧洗
浄器よりも高い位置に設置の温度調節手段を備えると共
に耐圧容器上部ガスを受け入れるために耐圧回収容器と
の間の上部間を連絡の高密度液化ガス供給シリンダーと
から成る汚れ成分分離、溶媒回収のために高圧発生装置
を不要とした分離回収機構。
5. A pressure recovery container provided with a temperature control means and a drain cylinder which is removably assembled, and a temperature control means installed at a position higher than the pressure-resistant washer to receive a gas above the pressure container. A separation and recovery mechanism that does not require a high-pressure generator for separating dirt components and recovering the solvent, which consists of a high-density liquefied gas supply cylinder that communicates between the upper part and the pressure recovery container.
【請求項6】 高密度液化ガス単体のみでは難溶で洗浄
できない汚れ成分を有する場合,汚れ成分に応じて親
油,親水あるいは両親媒性界面活性剤をエントレーナ容
器を介して溶媒中に添加して,その所謂ミセル化現象に
よる洗浄力向上と再付着防止機能を,ノズルの衝撃エネ
ルギーの強制剥離,バブリングによるキャビテーショ
ン,超音波による攪拌と共に合目的に複合化させるとし
た請求項1,2又は3記載の高密度液化ガスを使用の洗
浄装置の取り扱い方法。
6. When there is a dirt component that is hardly soluble and cannot be washed with only a high-density liquefied gas alone, an lipophilic, hydrophilic or amphiphilic surfactant is added to the solvent via an entrainer container according to the dirt component. The function of improving the detergency and preventing re-adhesion due to the so-called micellarization phenomenon is combined with the purpose together with forced separation of impact energy of the nozzle, cavitation by bubbling, and stirring by ultrasonic waves. A method for handling a cleaning apparatus using the high-density liquefied gas described above.
JP08252962A 1996-09-25 1996-09-25 Cleaning equipment using high-density liquefied gas Expired - Fee Related JP3074290B2 (en)

Priority Applications (8)

Application Number Priority Date Filing Date Title
JP08252962A JP3074290B2 (en) 1996-09-25 1996-09-25 Cleaning equipment using high-density liquefied gas
PCT/JP1997/003409 WO1998013149A1 (en) 1996-09-25 1997-09-25 Washing means using liquefied gas of high density
EP97941235A EP0893166A4 (en) 1996-09-25 1997-09-25 Washing means using liquefied gas of high density
KR1019980702074A KR100342720B1 (en) 1996-09-25 1997-09-25 Cleaning means using high density liquefied gas
US09/043,413 US6092538A (en) 1996-09-25 1997-09-25 Method for using high density compressed liquefied gases in cleaning applications
CA002232768A CA2232768C (en) 1996-09-25 1998-03-20 Method for using high density compressed liquefied gases in cleaning applications
NO19981308A NO316665B1 (en) 1996-09-25 1998-03-23 Method of cleaning and recycling of solvent in a closed recirculation system and cleaning equipment using a high density compressed liquid gas
CN98108789A CN1107554C (en) 1996-09-25 1998-03-27 Method for using high density compressed liquefied gases in cleaning applications

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
JP08252962A JP3074290B2 (en) 1996-09-25 1996-09-25 Cleaning equipment using high-density liquefied gas
CA002232768A CA2232768C (en) 1996-09-25 1998-03-20 Method for using high density compressed liquefied gases in cleaning applications
NO19981308A NO316665B1 (en) 1996-09-25 1998-03-23 Method of cleaning and recycling of solvent in a closed recirculation system and cleaning equipment using a high density compressed liquid gas
CN98108789A CN1107554C (en) 1996-09-25 1998-03-27 Method for using high density compressed liquefied gases in cleaning applications

Publications (2)

Publication Number Publication Date
JPH1094766A true JPH1094766A (en) 1998-04-14
JP3074290B2 JP3074290B2 (en) 2000-08-07

Family

ID=31982400

Family Applications (1)

Application Number Title Priority Date Filing Date
JP08252962A Expired - Fee Related JP3074290B2 (en) 1996-09-25 1996-09-25 Cleaning equipment using high-density liquefied gas

Country Status (1)

Country Link
JP (1) JP3074290B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113644333A (en) * 2021-08-11 2021-11-12 华南师范大学 Device and method for recycling electrolyte in battery

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113644333A (en) * 2021-08-11 2021-11-12 华南师范大学 Device and method for recycling electrolyte in battery

Also Published As

Publication number Publication date
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