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 PDFInfo
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- 239000012530 fluid Substances 0.000 title claims description 72
- 239000000356 contaminant Substances 0.000 title claims description 29
- 239000012535 impurity Substances 0.000 title claims description 29
- 238000004140 cleaning Methods 0.000 title claims description 22
- 239000011148 porous material Substances 0.000 title claims description 20
- 238000000034 method Methods 0.000 title claims description 17
- 238000000926 separation method Methods 0.000 claims description 24
- 238000003860 storage Methods 0.000 claims description 24
- 238000011084 recovery Methods 0.000 claims description 17
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 14
- 239000012229 microporous material Substances 0.000 claims description 14
- 239000007789 gas Substances 0.000 claims description 11
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 7
- 239000001569 carbon dioxide Substances 0.000 claims description 7
- 239000007788 liquid Substances 0.000 claims description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 4
- GQPLMRYTRLFLPF-UHFFFAOYSA-N Nitrous Oxide Chemical compound [O-][N+]#N GQPLMRYTRLFLPF-UHFFFAOYSA-N 0.000 claims description 4
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 claims description 4
- 239000001257 hydrogen Substances 0.000 claims description 2
- 229910052739 hydrogen Inorganic materials 0.000 claims description 2
- 125000004435 hydrogen atom Chemical class [H]* 0.000 claims description 2
- 229910052757 nitrogen Inorganic materials 0.000 claims description 2
- 239000001272 nitrous oxide Substances 0.000 claims description 2
- 239000001294 propane Substances 0.000 claims description 2
- 229910052724 xenon Inorganic materials 0.000 claims description 2
- FHNFHKCVQCLJFQ-UHFFFAOYSA-N xenon atom Chemical compound [Xe] FHNFHKCVQCLJFQ-UHFFFAOYSA-N 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 239000002904 solvent Substances 0.000 description 6
- 239000000126 substance Substances 0.000 description 5
- 229910000831 Steel Inorganic materials 0.000 description 4
- 239000010959 steel Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000010687 lubricating oil Substances 0.000 description 3
- 238000009792 diffusion process Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 230000005856 abnormality Effects 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229910010293 ceramic material Inorganic materials 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000003631 expected effect Effects 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 230000009972 noncorrosive effect Effects 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 230000007903 penetration ability Effects 0.000 description 1
- 230000001766 physiological effect Effects 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 238000004663 powder metallurgy Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
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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
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
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-
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
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。
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
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
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
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 (
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
2. A refined porous material, for example, a bearing is inspected and confirmed to be normal, and the temperature is already set in a
3. The
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
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
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.
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
Claims (6)
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.
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