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JP4104602B2 - Method for cleaning and removing contaminants or impurities of fine porous material with a high-pressure fluid in a sealed container - Google Patents
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JP4104602B2 - Method for cleaning and removing contaminants or impurities of fine porous material with a high-pressure fluid in a sealed container - Google Patents

Method for cleaning and removing contaminants or impurities of fine porous material with a high-pressure fluid in a sealed container Download PDF

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JP4104602B2
JP4104602B2 JP2005041917A JP2005041917A JP4104602B2 JP 4104602 B2 JP4104602 B2 JP 4104602B2 JP 2005041917 A JP2005041917 A JP 2005041917A JP 2005041917 A JP2005041917 A JP 2005041917A JP 4104602 B2 JP4104602 B2 JP 4104602B2
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永和 邱
偉碩 羅
瑞岳 林
萬貴 姚
子龍 何
貴▲ちー▼ 李
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南緯實業股▲ふん▼有限公司
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Description

本発明は微細化多孔性材料の汚染物或いは不純物を密閉容器中で高圧流体により洗浄除去する方法に係り、高圧流体技術(超臨界流体と液体二酸化炭素)、洗浄技術、微細化多孔性材料加工工程を包含し、特に大量の洗浄用水を必要とせず廃水の排出による環境保護問題を発生しない方法に関する。   The present invention relates to a method for cleaning and removing contaminants or impurities of a microporous material with a high-pressure fluid in a sealed container, and includes a high-pressure fluid technology (supercritical fluid and liquid carbon dioxide), a cleaning technology, and processing of a microporous material. In particular, the present invention relates to a method that does not require a large amount of cleaning water and does not cause environmental protection problems due to wastewater discharge.

一般に金属材料、高分子材料、セラミック材料及びその複合材料で形成された軸受、濾過器、消音器、冷却器等の部品には相当な数量の孔がある。例えば、軸受の孔は潤滑油を保存するのに用いられて機器が運転する時に潤滑油が熱により釈放されて回転軸を潤滑し、磨耗と騒音を減らし、冷却時に潤滑油は毛細孔の原理により孔中に戻り、これが粉末冶金製品の有する特性である。   In general, parts such as bearings, filters, silencers, and coolers formed of metal materials, polymer materials, ceramic materials, and composite materials thereof have a considerable number of holes. For example, bearing holes are used to store lubricating oil, and when the equipment is operated, the lubricating oil is released by heat to lubricate the rotating shaft, reducing wear and noise, and when cooling, the lubricating oil is the principle of pores This is a characteristic of powder metallurgy products.

これらの微細化多孔性材料は、加工過程或いは使用後に残留する汚染物或いは不純物が、部品に詰まりを発生する問題がある。   These miniaturized porous materials have a problem that contaminants or impurities remaining after processing or use cause clogging of parts.

現在の洗浄方式に存在する問題は以下のとおりである。
1.大量の酸液、アルカリ液或いは水を使用し、時間とエネルギーを消耗する。
2.水の表面張力は大きく、即時に材料外層から内層に浸透せず、空気圧等の外力を組合せなければ浸透しない。
3.洗浄時に、水が外層より内装に送られて微細化多孔性構造中に吸着しやすく、別に乾燥処理のための空気を送り込むか、加熱乾燥させる必要がある。
The problems existing in the current cleaning method are as follows.
1. Uses a large amount of acid solution, alkali solution or water, and consumes time and energy.
2. The surface tension of water is large and does not immediately penetrate from the material outer layer to the inner layer, and does not penetrate unless an external force such as air pressure is combined.
3. At the time of cleaning, water is sent from the outer layer to the interior and is easily adsorbed into the fine porous structure, and it is necessary to send air for drying treatment or to heat and dry it separately.

本発明は、環境保護と、微細化多孔性材料製造工程の簡易化と生産効率アップのために、微細化多孔性材料の汚染物或いは不純物を密閉容器中で高圧流体により洗浄除去する方法を提供する。   The present invention provides a method for cleaning and removing contaminants or impurities of a microporous material in a sealed container with a high-pressure fluid in order to protect the environment, simplify the manufacturing process of the microporous material, and increase production efficiency. To do.

本発明が応用する技術手段及び従来の技術に対する効果は以下のようである。即ち、密閉容器中で、高圧流体を利用し、その高い拡散係数と高い浸透能力、特定温度と圧力下で有する溶剤能力を有して急速に汚染物或いは不純物を溶解させて付帯する特性により、上述の周知の洗浄方法における問題を克服し、即ち、大量に有機薬水、溶剤と洗浄用水を使用する問題を改善し、並びに微細化多孔性材料を使用した製品の品質と寿命を増し、洗浄、乾燥ステップと時間を短縮し、経営コストを減らす。   The technical means applied by the present invention and the effects of the conventional technology are as follows. That is, by using a high-pressure fluid in a closed container, and having a high diffusion coefficient and high penetration ability, a solvent ability to have under a specific temperature and pressure, and rapidly accumulating contaminants or impurities, Overcoming the problems in the above known cleaning methods, i.e. improving the problem of using large amounts of organic chemical water, solvent and cleaning water, as well as increasing the quality and life of products using micronized porous materials, cleaning Shorten drying steps and time, reduce operating costs.

本発明で二酸化炭素を使用する場合の長所は以下のとおりである。
1.不良な生理作用がない。即ち二酸化炭素は炭酸水と人体代謝中のいずれにもあり、一般に公認された安全物質であり、使用が認められている。
2.環境に対して無害で、不燃性で、爆発性がなく、腐食性がなく、化学性が安定し、純度が高く、無毒である。
3.安価で大量取得可能で、石化工業の影響を受けず、並びに液体形式で大量に保存できる。
4.相当な揮発性を具え、ゆえに非常に容易に且つ安全に溶質と分離し、即ち溶質と溶剤の回収が容易で残留問題がなく、低温下で反応が行なえ、サーモセンシティブの物質を破壊することがない。
5.液態二酸化炭素溶剤性質は炭化水素溶剤に近い。
Advantages when carbon dioxide is used in the present invention are as follows.
1. There is no bad physiological effect. In other words, carbon dioxide is present in both carbonated water and human metabolism, and is a generally recognized safety substance and is approved for use.
2. Harmless to the environment, non-flammable, non-explosive, non-corrosive, stable chemical, high purity, non-toxic.
3. It is inexpensive and can be obtained in large quantities, is not affected by the petrochemical industry, and can be stored in large quantities in liquid form.
4). It has considerable volatility and therefore can be separated from solutes very easily and safely, i.e. the recovery of solutes and solvents is easy, there are no residual problems, the reaction can take place at low temperatures and the thermosensitive substances can be destroyed. Absent.
5. Liquid carbon dioxide solvent properties are close to hydrocarbon solvents.

請求項1の発明は微細化多孔性材料を密閉容器の反応タンク中に置き、高圧ポンプと高圧管アクセサリを利用して流体保存タンク中の流体を反応タンク中に導入すると共に、温度と圧力の制御と調節により、高密度、高拡散性、低粘度、低誘電率と極めて低い表面張力を有する気態或いは液態の流体により、微細化多孔性材料の汚染物或いは不純物を除去し、
前記反応タンクが高圧管アクセサリと高圧バルブを利用して分離タンクに接続され、分離タンクが高圧管アクセサリと高圧バルブで流体回収ポンプに接続され、流体回収ポンプが高圧管アクセサリと高圧バルブで流体保存タンクに接続され、こうして主回路が形成され、分離タンクと流体保存タンクが高圧管アクセサリと高圧バルブを利用して接続されて副回路が形成されたことを特徴とする、微細化多孔性材料の汚染物或いは不純物を密閉容器中で高圧流体により洗浄除去する方法としている。
請求項2の発明は、前記流体保存タンク、反応タンク、分離タンクの上方及び下方にそれぞれ圧力メータと高圧バルブが設けられ、流体が高圧管アクセサリを通り排出回収され、汚染物或いは不純物が下部に堆積させられて高圧バルブの開放動作により収集されることを特徴とする、請求項1に記載の微細化多孔性材料の汚染物或いは不純物を密閉容器中で高圧流体により洗浄除去する方法としている。
請求項3の発明は、前記流体保存タンク、反応タンク、分離タンクの外部に温度制御装置が設けられたことを特徴とする、請求項1に記載の微細化多孔性材料の汚染物或いは不純物を密閉容器中で高圧流体により洗浄除去する方法としている。
請求項4の発明は、操作温度が微細化多孔性材料の特性により決定され、摂氏4〜120±1度とされることを特徴とする、請求項1に記載の微細化多孔性材料の汚染物或いは不純物を密閉容器中で高圧流体により洗浄除去する方法としている。
請求項5の発明は、操作圧力が微細化多孔性材料の特性により決定され、10〜300kg/cm 2 とされることを特徴とする、請求項1に記載の微細化多孔性材料の汚染物或いは不純物を密閉容器中で高圧流体により洗浄除去する方法としている。
請求項6の発明は、流体が、二酸化炭素、プロパン、キセノン、亜酸化窒素、水素、窒素とされることを特徴とする、請求項1記載の微細化多孔性材料の汚染物或いは不純物を密閉容器中で高圧流体により洗浄除去する方法としている。
The invention according to claim 1, placing the fine porous material in the reaction tank of the closed container, along with utilizing a high pressure pump and the high-pressure pipe accessory for introducing a fluid in the fluid storage tank during the reaction tank, the temperature and pressure By controlling and adjusting the density, high-density, high-diffusion, low-viscosity, low-dielectric constant and extremely low surface tension can be used to remove contaminants or impurities in the microporous material .
The reaction tank is connected to a separation tank using a high-pressure pipe accessory and a high-pressure valve, the separation tank is connected to a fluid recovery pump via a high-pressure pipe accessory and a high-pressure valve, and the fluid recovery pump is stored as a fluid using a high-pressure pipe accessory and a high-pressure valve. Of a microporous material characterized in that it is connected to a tank, thus forming a main circuit, and a separation tank and a fluid storage tank are connected using a high-pressure pipe accessory and a high-pressure valve to form a sub-circuit . It is a method of cleaning and removing contaminants or impurities with a high-pressure fluid in a sealed container.
According to the second aspect of the present invention , a pressure meter and a high-pressure valve are provided above and below the fluid storage tank, reaction tank, and separation tank, respectively, and the fluid is discharged and collected through the high-pressure pipe accessory. The method according to claim 1, wherein the contaminants or impurities of the microporous material are deposited and collected by an opening operation of the high-pressure valve.
According to a third aspect of the present invention , there is provided a temperature control device provided outside the fluid storage tank, the reaction tank, and the separation tank. It is a method of washing and removing with a high-pressure fluid in a sealed container.
The invention according to claim 4, the operating temperature is determined by the properties of the fine porous material, characterized in that it is a 4 to 120 ± 1 ° C, contamination of the fine porous material according to claim 1 In this method, substances or impurities are washed away with a high-pressure fluid in a sealed container.
The invention of claim 5 is characterized in that the operating pressure is determined by the characteristics of the refined porous material, and is 10 to 300 kg / cm 2 . Alternatively, the impurities are washed away with a high-pressure fluid in a sealed container.
The invention according to claim 6 is characterized in that the fluid is carbon dioxide, propane, xenon, nitrous oxide, hydrogen, nitrogen, and the contaminants or impurities of the microporous material according to claim 1 are sealed. In this method, the container is cleaned and removed with a high-pressure fluid.

本発明は、微細化多孔性材料を密閉容器中に入れ、温度と圧力を制御と調節し、高圧流体の高密度、高拡散性、低粘度、低誘電率及び極めて低い表面張力の溶剤特性を利用し、高圧流体を微細化多孔性材料の外層より微細化多孔構造を通して内層に進入させ、並びに加工過程或いは使用後に残留した汚染物或いは不純物を溶解させ、流体の流動により汚染物或いは不純物を内層より微細化多孔性材料を通して釈放させ、微細化多孔性材料の汚染物或いは不純物を洗浄除去する目的を達成し、加工、洗浄用水を節約し、廃水処理と汚染排出問題を減らし、操作時間を短縮し、汚染物或いは不純物の除去と分離収集を一度に完成でき、大量の電力を消耗して微細化多孔性材料を乾燥させる必要がないことを特徴とする。   The present invention puts a fine porous material in a closed container, controls and adjusts temperature and pressure, and provides high pressure fluid density, high diffusivity, low viscosity, low dielectric constant and extremely low surface tension solvent properties. The high-pressure fluid is made to enter the inner layer through the microporous structure from the outer layer of the microporous material, and the contaminants or impurities remaining after processing or use are dissolved. Release through finer porous material to achieve the purpose of cleaning and removing contaminants or impurities of the finer porous material, save processing and cleaning water, reduce wastewater treatment and pollution discharge problems, reduce operation time In addition, contaminants and impurities can be removed and separated and collected at the same time, and it is not necessary to consume a large amount of power and dry the microporous material.

図1は本発明の回収型のシステム表示図である。高圧管アクセサリ1により流体保存タンク10、高圧ポンプ20、反応タンク30、分離タンク40、流体回収ポンプ50が連接されて主回路を構成し、並びに別の高圧管アクセサリ2により流体保存タンク10と分離タンク40が連接されて、副回路を構成する。主回路の流体保存タンク10、高圧ポンプ20、反応タンク30、分離タンク40、流体回収ポンプ50の間には高圧バルブV2、V3、V5、V7、V9が設けられ、副回路の流体保存タンク10と分離タンク40の間には高圧バルブV8が設けられている。このほか、流体保存タンク10、反応タンク30、分離タンク40の上方及び下方にそれぞれ圧力メータP1〜P3と高圧バルブV1、V4、V6が設けられている。   FIG. 1 is a collection type system display diagram of the present invention. The high pressure pipe accessory 1 connects the fluid storage tank 10, the high pressure pump 20, the reaction tank 30, the separation tank 40, and the fluid recovery pump 50 to form a main circuit, and the separate high pressure pipe accessory 2 separates the fluid storage tank 10 from the fluid storage tank 10. The tanks 40 are connected to form a sub circuit. High-pressure valves V2, V3, V5, V7, and V9 are provided between the main circuit fluid storage tank 10, the high-pressure pump 20, the reaction tank 30, the separation tank 40, and the fluid recovery pump 50. And a separation tank 40 are provided with a high-pressure valve V8. In addition, pressure meters P1 to P3 and high pressure valves V1, V4, and V6 are provided above and below the fluid storage tank 10, the reaction tank 30, and the separation tank 40, respectively.

そのうち、流体保存タンク10は、流体(液体と気体を包含する)の保存に用いられ、温度制御装置11が設けられ、該流体保存タンク10は流体の加圧と回収保存に供され、圧力操作範囲は10〜150kg/cm2 である。 Among them, the fluid storage tank 10 is used for storage of fluid (including liquid and gas), and a temperature control device 11 is provided. The fluid storage tank 10 is used for pressurization and recovery storage of fluid, and pressure operation range is 10~150kg / cm 2.

高圧ポンプ20は、流体(液体と気体を包含する)の加圧に供され、圧力操作範囲は10〜300kg/cm2 である。 The high-pressure pump 20 is used for pressurization of fluid (including liquid and gas), and the pressure operation range is 10 to 300 kg / cm 2 .

反応タンク30は、バッチ作業に供され開閉可能な蓋31を具えた高圧タンク32を具え、該高圧タンク32に温度制御装置33が設けられて摂氏4〜80度の温度制御範囲、10〜300kg/cm2 の圧力操作範囲で、微細化多孔性材料(図示せず)を収容し、並びに流体加圧後に汚染物或いは不純物除去の動作を行なう。 The reaction tank 30 is provided with a high-pressure tank 32 provided with a lid 31 that can be opened and closed for batch operations, and a temperature control device 33 is provided in the high-pressure tank 32 to provide a temperature control range of 4 to 80 degrees Celsius, 10 to 300 kg. In a pressure operating range of / cm 2, a microporous material (not shown) is accommodated, and the operation of removing contaminants or impurities is performed after fluid pressurization.

分離タンク40は、常時開閉する必要がない蓋41を具えた高圧タンク42、及び温度制御装置43を具え、摂氏4〜80度の温度制御範囲、10〜300kg/cm2 の圧力操作範囲で、流体と汚染物或いは不純物を分離させ、流体を分離タンク40の上端の管路より排出回収し、汚染物或いは不純物を分離タンク40の下部に堆積させ、高圧バルブV6の開閉動作により収集する。 Separation tank 40 comprises a high-pressure tank 42 and the temperature control device 43, equipped with cap 41 that do not need to be opened and closed at all times, the temperature control range of 4 to 80 degrees Celsius, a pressure operating range of the 10~300kg / cm 2, The fluid and the contaminants or impurities are separated, and the fluid is discharged and collected from the pipe line at the upper end of the separation tank 40, and the contaminants or impurities are accumulated in the lower part of the separation tank 40, and collected by opening and closing the high-pressure valve V6.

流体回収ポンプ50は、流体(液体と気体を包含する)の回収に使用され、圧力操作範囲は10〜300kg/cm2 である。 The fluid recovery pump 50 is used for recovery of fluid (including liquid and gas), and the pressure operation range is 10 to 300 kg / cm 2 .

上述の本発明の提供する微細化多孔性材料の汚染物或いは不純物を密閉容器中で高圧流体により洗浄除去する方法に用いられるシステムは、流体回収ポンプ50を省略でき、流体保存タンク10には一般のスチールボンベ10’を使用可能である。   The system used in the method of cleaning and removing the contaminants or impurities of the fine porous material provided by the present invention with a high-pressure fluid in a sealed container can omit the fluid recovery pump 50, and the fluid storage tank 10 generally includes Steel cylinder 10 'can be used.

図2は本発明の分離型のシステム表示図であり、反応後に分離された汚染物と流体が直接排出されて回収されず、このため分離型と称される。   FIG. 2 is a diagram showing the separation type system of the present invention, and the contaminants and fluid separated after the reaction are directly discharged and not recovered, and are therefore called separation type.

上述の本発明の提供する微細化多孔性材料の汚染物或いは不純物を密閉容器中で高圧流体により洗浄除去する方法に使用される装置は、そのうちの分離タンク40と流体保存タンク10を省略可能であり、流体保存タンク10は一般のスチールボンベ10’を使用可能であり、図3に示されるのは本発明の基本型のシステム表示図である。反応後に汚染物と流体は直接排出されて分離回収されず、このため基本型と称される。   The apparatus used for the method of cleaning and removing the contaminants or impurities of the fine porous material provided by the present invention with a high-pressure fluid in a sealed container can omit the separation tank 40 and the fluid storage tank 10. The fluid storage tank 10 can use a general steel cylinder 10 ', and FIG. 3 shows a basic system display diagram of the present invention. After the reaction, the contaminants and fluid are directly discharged and not separated and recovered, and are therefore referred to as the basic type.

実際の洗浄時には、回収型が最も好ましい実施例であり、その操作ステップは以下のとおりである。   In actual cleaning, the recovery type is the most preferred embodiment, and the operation steps are as follows.

操作前に、全ての高圧バルブV1〜V9が閉じられているかを検査し、並びに全てのタンク(流体保存タンク10、反応タンク30、分離タンク40)、高圧管アクセサリ1、2、高圧ポンプ20、流体回収ポンプ50と圧力メータP1〜P3に異常がないかを検査し、流体保存タンク10の圧力メータP1の圧力値が50kg/cm2 以上であるかを検査し、圧力不足であれば、高圧バルブV1をシステム外部の気体供給スチールボンベに接続し、システムの正常操作に必要な気体を供給する。 Before operation, check that all high pressure valves V1 to V9 are closed, as well as all tanks (fluid storage tank 10, reaction tank 30, separation tank 40), high pressure pipe accessories 1, 2, high pressure pump 20, The fluid recovery pump 50 and the pressure meters P1 to P3 are inspected for abnormalities, and the pressure value of the pressure meter P1 of the fluid storage tank 10 is inspected to be 50 kg / cm 2 or more. The valve V1 is connected to a gas supply steel cylinder outside the system to supply gas necessary for normal operation of the system.

システムの一切が正常であることを確認した後、以下の操作動作を実行する。
1.ウォームアップ。即ち流体保存タンク10の温度を摂氏2〜4度に、反応タンク30の温度を摂氏40〜80±1度に、分離タンク40の温度を摂氏4〜80±1度に制御する。
2.微細化多孔性材料、例えば軸受を検査して異常がないことが確認されて既に温度が設定値摂氏40〜80±1度に達した反応タンク30内に置く。
3.反応タンク30の蓋31を閉じ、高圧バルブV2とV3を開き、二酸化炭素ガスで加圧の動作を行ない、圧力メータP2の圧力値が200kg/cm2 に達した時、高圧バルブV2とV3を閉じ、並びに5〜20分間の計時を開始する。
4.操作時間が終了した時、高圧バルブV5、V7、V8及びV9を開き、汚染物或いは不純物と気体を分離すると共に、気体の第1段階の回収循環使用の動作を行なう。
5.圧力メータP2とP3の圧力値が下がらなくなるのを待って、高圧バルブV8を閉じ、流体回収ポンプ50を開いて第2段階の気体回収の動作を行なう。
6.圧力メータP1とP2の圧力値が10kg/cm2 より小さくなった時、高圧バルブV5、V7、V9を閉じ、並びに高圧バルブV4を開いて反応タンク30中に残留する気体を排出し、圧力メータP2の圧力値が0kg/cm2 となった時に反応タンク30の蓋31を開き、軸受サンプルを取り出し、以上で一次の高圧流体による汚染物或いは不純物の洗浄動作を完成する。
After confirming that the system is operating properly, execute the following operations.
1. warm up. That is, the temperature of the fluid storage tank 10 is controlled to 2-4 degrees Celsius, the temperature of the reaction tank 30 is controlled to 40-80 ± 1 degrees Celsius, and the temperature of the separation tank 40 is controlled to 4-80 ± 1 degrees Celsius.
2. A refined porous material, for example, a bearing is inspected and confirmed to be normal, and the temperature is already set in a reaction tank 30 having reached a set value of 40 to 80 ± 1 degrees Celsius.
3. The lid 31 of the reaction tank 30 is closed, the high pressure valves V2 and V3 are opened, and the pressure is increased with carbon dioxide gas. When the pressure value of the pressure meter P2 reaches 200 kg / cm 2 , the high pressure valves V2 and V3 are turned on. Close and start timing for 5-20 minutes.
4). When the operation time is over, the high-pressure valves V5, V7, V8 and V9 are opened to separate the contaminants or impurities from the gas, and to perform the first-stage recovery / circulation operation of the gas.
5. After the pressure values of the pressure meters P2 and P3 are not lowered, the high pressure valve V8 is closed and the fluid recovery pump 50 is opened to perform the second stage gas recovery operation.
6). When the pressure values of the pressure meters P1 and P2 are smaller than 10 kg / cm 2 , the high pressure valves V5, V7, V9 are closed, and the high pressure valve V4 is opened to discharge the gas remaining in the reaction tank 30, and the pressure meter When the pressure value of P2 reaches 0 kg / cm 2 , the lid 31 of the reaction tank 30 is opened, the bearing sample is taken out, and the cleaning operation for contaminants or impurities by the primary high-pressure fluid is completed.

現在、一般に軸受の洗浄は超音波振動で水洗した後に、乾燥処理を行なうが、軸受中の微細化多孔性構造に被包された水分子を完全に除去できないと軸受に錆が発生しやすくなり、軸受品質と正常な使用寿命が損なわれる。   At present, bearings are generally washed with ultrasonic vibration and then dried, but if the water molecules encapsulated in the microporous structure in the bearing cannot be completely removed, the bearing is likely to rust. , Bearing quality and normal service life are impaired.

本発明の提供する微細化多孔性材料の汚染物或いは不純物を密閉容器中で高圧流体により洗浄除去する方法は、実際に反復操作試験を行なったところ、予期された作用効果を達成することが確認され、また現在市場にはない新規な発明であり、産業上の利用価値を有している。   The method of cleaning and removing the contaminants or impurities of the microporous material provided by the present invention with a high-pressure fluid in a sealed container has been confirmed to achieve the expected effects by actually performing repeated operation tests. It is a novel invention that is not present in the market and has industrial utility value.

本発明の回収型のシステム表示図である。It is a collection type | system | group system display figure of this invention. 本発明の分離型のシステム表示図である。It is a separation type system display figure of the present invention. 本発明の基本型のシステム表示図である。It is a system display figure of the basic type of the present invention.

符号の説明Explanation of symbols

1 高圧管アクセサリ
2 高圧管アクセサリ
10 流体保存タンク
10’ スチールボンベ
11 温度制御装置
20 高圧ポンプ
30 反応タンク
31 蓋
32 高圧タンク
33 温度制御装置
40 分離タンク
41 蓋
42 高圧タンク
43 温度制御装置
50 流体回収ポンプ
V1〜V9 高圧バルブ
P1〜P3 圧力メータ
DESCRIPTION OF SYMBOLS 1 High pressure pipe accessory 2 High pressure pipe accessory 10 Fluid storage tank 10 'Steel cylinder 11 Temperature control apparatus 20 High pressure pump 30 Reaction tank 31 Lid 32 High pressure tank 33 Temperature control apparatus 40 Separation tank 41 Lid 42 High pressure tank 43 Temperature control apparatus 50 Fluid recovery Pump V1-V9 High pressure valve P1-P3 Pressure meter

Claims (6)

微細化多孔性材料を密閉容器の反応タンク中に置き、高圧ポンプと高圧管アクセサリを利用して流体保存タンク中の流体を反応タンク中に導入すると共に、温度と圧力の制御と調節により、高密度、高拡散性、低粘度、低誘電率と極めて低い表面張力を有する気態或いは液態の流体により、微細化多孔性材料の汚染物或いは不純物を除去し、
前記反応タンクが高圧管アクセサリと高圧バルブを利用して分離タンクに接続され、分離タンクが高圧管アクセサリと高圧バルブで流体回収ポンプに接続され、流体回収ポンプが高圧管アクセサリと高圧バルブで流体保存タンクに接続され、こうして主回路が形成され、分離タンクと流体保存タンクが高圧管アクセサリと高圧バルブを利用して接続されて副回路が形成されたことを特徴とする、微細化多孔性材料の汚染物或いは不純物を密閉容器中で高圧流体により洗浄除去する方法。
Place the micronized porous material in the reaction tank of the sealed container, introduce the fluid in the fluid storage tank into the reaction tank using a high pressure pump and high pressure pipe accessories, and control and adjust the temperature and pressure to increase the Removes contaminants or impurities in micronized porous materials with gas or liquid fluids with density, high diffusivity, low viscosity, low dielectric constant and very low surface tension ,
The reaction tank is connected to a separation tank using a high-pressure pipe accessory and a high-pressure valve, the separation tank is connected to a fluid recovery pump via a high-pressure pipe accessory and a high-pressure valve, and the fluid recovery pump is stored as a fluid using a high-pressure pipe accessory and a high-pressure valve. Of a microporous material characterized in that it is connected to a tank, thus forming a main circuit, and a separation tank and a fluid storage tank are connected using a high-pressure pipe accessory and a high-pressure valve to form a sub-circuit . A method of cleaning and removing contaminants or impurities with a high-pressure fluid in a sealed container.
前記流体保存タンク、反応タンク、分離タンクの上方及び下方にそれぞれ圧力メータと高圧バルブが設けられ、流体が高圧管アクセサリを通り排出回収され、汚染物或いは不純物が下部に堆積させられて高圧バルブの開放動作により収集されることを特徴とする、請求項1に記載の微細化多孔性材料の汚染物或いは不純物を密閉容器中で高圧流体により洗浄除去する方法。A pressure meter and a high-pressure valve are provided above and below the fluid storage tank, reaction tank, and separation tank, respectively, and fluid is discharged and collected through the high-pressure pipe accessory, and contaminants or impurities are deposited on the bottom, and The method for cleaning and removing contaminants or impurities of a finely porous material according to claim 1, wherein the contaminant or impurities are collected by an opening operation. 前記流体保存タンク、反応タンク、分離タンクの外部に温度制御装置が設けられたことを特徴とする、請求項1に記載の微細化多孔性材料の汚染物或いは不純物を密閉容器中で高圧流体により洗浄除去する方法。The temperature control device is provided outside the fluid storage tank, the reaction tank, and the separation tank. How to wash away. 操作温度が微細化多孔性材料の特性により決定され、摂氏4〜120±1度とされることを特徴とする、請求項1に記載の微細化多孔性材料の汚染物或いは不純物を密閉容器中で高圧流体により洗浄除去する方法。The operating temperature is determined by the characteristics of the microporous material and is set to 4 to 120 ± 1 degrees Celsius. Cleaning and removing with high pressure fluid. 操作圧力が微細化多孔性材料の特性により決定され、10〜300kg/cmThe operating pressure is determined by the characteristics of the micronized porous material, 10 to 300 kg / cm 22 とされることを特徴とする、請求項1に記載の微細化多孔性材料の汚染物或いは不純物を密閉容器中で高圧流体により洗浄除去する方法。 The method for cleaning and removing contaminants or impurities of the fine porous material according to claim 1 with a high-pressure fluid in a sealed container. 流体が、二酸化炭素、プロパン、キセノン、亜酸化窒素、水素、窒素とされることを特徴とする、請求項1記載の微細化多孔性材料の汚染物或いは不純物を密閉容器中で高圧流体により洗浄除去する方法。2. The fine porous material contaminants or impurities according to claim 1, wherein the fluid is carbon dioxide, propane, xenon, nitrous oxide, hydrogen, nitrogen, and is cleaned with a high-pressure fluid in a sealed container. How to remove.
JP2005041917A 2005-02-18 2005-02-18 Method for cleaning and removing contaminants or impurities of fine porous material with a high-pressure fluid in a sealed container Expired - Fee Related JP4104602B2 (en)

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