JP2019528395A - refrigerator - Google Patents
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- JP2019528395A JP2019528395A JP2019506375A JP2019506375A JP2019528395A JP 2019528395 A JP2019528395 A JP 2019528395A JP 2019506375 A JP2019506375 A JP 2019506375A JP 2019506375 A JP2019506375 A JP 2019506375A JP 2019528395 A JP2019528395 A JP 2019528395A
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- cooling device
- adsorption
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- 239000003507 refrigerant Substances 0.000 claims abstract description 24
- 238000001816 cooling Methods 0.000 claims abstract description 23
- 238000001179 sorption measurement Methods 0.000 claims abstract description 22
- 239000001307 helium Substances 0.000 claims abstract description 9
- 229910052734 helium Inorganic materials 0.000 claims abstract description 9
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 claims abstract description 9
- 238000011144 upstream manufacturing Methods 0.000 claims abstract description 7
- 239000002341 toxic gas Substances 0.000 claims abstract description 5
- 239000007789 gas Substances 0.000 claims description 33
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 3
- 229910052757 nitrogen Inorganic materials 0.000 claims description 3
- 239000001301 oxygen Substances 0.000 claims description 3
- 229910052760 oxygen Inorganic materials 0.000 claims description 3
- 238000005057 refrigeration Methods 0.000 claims description 3
- 230000004888 barrier function Effects 0.000 claims description 2
- 239000000835 fiber Substances 0.000 claims description 2
- 238000000034 method Methods 0.000 claims description 2
- 239000000843 powder Substances 0.000 claims description 2
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 230000006835 compression Effects 0.000 description 4
- 238000007906 compression Methods 0.000 description 4
- 238000012423 maintenance Methods 0.000 description 3
- 229910052786 argon Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 238000007710 freezing Methods 0.000 description 2
- 230000008014 freezing Effects 0.000 description 2
- 229910052754 neon Inorganic materials 0.000 description 2
- GKAOGPIIYCISHV-UHFFFAOYSA-N neon atom Chemical compound [Ne] GKAOGPIIYCISHV-UHFFFAOYSA-N 0.000 description 2
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B43/00—Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat
- F25B43/003—Filters
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B43/00—Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat
- F25B43/02—Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat for separating lubricants from the refrigerant
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B9/00—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B9/00—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
- F25B9/002—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B9/00—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
- F25B9/002—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant
- F25B9/008—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant the refrigerant being carbon dioxide
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/23—Separators
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2500/00—Problems to be solved
- F25B2500/16—Lubrication
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B31/00—Compressor arrangements
- F25B31/002—Lubrication
- F25B31/004—Lubrication oil recirculating arrangements
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Power Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Compressor (AREA)
- Compressors, Vaccum Pumps And Other Relevant Systems (AREA)
- Separation Of Gases By Adsorption (AREA)
Abstract
【解決手段】本発明は、実質的にヘリウム及びオイルを含む冷媒を圧縮するための圧縮機(10)を備えた、真空を生成するための冷凍機、特にクライオポンプに関する。圧縮機と共に、オイル分離器(20, 22, 24, 26)が冷媒の送出方向の下流側に配置されている。本発明は、冷媒が膨張する冷却装置(30)に更に関する。有毒ガスを吸着するために、吸着装置(28)が送出方向の冷却装置(30)の上流側に配置されている。The present invention relates to a refrigerator, particularly a cryopump, for generating a vacuum, comprising a compressor (10) for compressing a refrigerant substantially containing helium and oil. Along with the compressor, oil separators (20, 22, 24, 26) are arranged downstream in the refrigerant delivery direction. The present invention further relates to a cooling device (30) in which the refrigerant expands. In order to adsorb toxic gas, the adsorption device (28) is arranged upstream of the cooling device (30) in the delivery direction.
Description
本発明は、冷凍機、特には真空を生成するためのクライオポンプに関する。 The present invention relates to a refrigerator, particularly a cryopump for generating a vacuum.
特にクライオポンプに適用される冷凍機を使用すると、10 K未満の非常に低い温度を得ることが可能である。そのため、例えば、閉じた真空室で最大10-10 mbarの非常に高い真空を生成することが可能である。冷凍システムは、例えばスクロールポンプのような圧縮ポンプを備えており、圧縮ポンプを用いて冷媒を圧縮する。冷媒としてヘリウムが使用される。冷媒は一般に、圧縮中のヘリウムの過度の加熱を防ぐために一定の割合のオイルを含んでいる。熱交換器が、冷媒の送出方向に見て圧縮機の下流側に最初に配置されているため、媒体の冷却を可能にする。その後、ヘリウム中のオイルを分離する。例えば、複数のオイル分離器、特に少なくとも1つのプレ分離器及び少なくとも1つの細分離器を設けて、オイルの分離を行う。更に、オイル分離器は典型的に、オイル蒸気などを濾過するために吸着器を有している。吸着器の後では、冷媒が非常に高い程度までヘリウムのみから構成されているように、冷媒は実質的にクリーンである。オイルの割合はppb 範囲内である。 In particular, when using a refrigerator applied to a cryopump, it is possible to obtain a very low temperature of less than 10 K. Thus, for example, it is possible to generate a very high vacuum of up to 10 −10 mbar in a closed vacuum chamber. The refrigeration system includes a compression pump such as a scroll pump, and compresses the refrigerant using the compression pump. Helium is used as the refrigerant. The refrigerant typically contains a proportion of oil to prevent excessive heating of the helium during compression. Since the heat exchanger is initially arranged downstream of the compressor as viewed in the refrigerant delivery direction, it allows cooling of the medium. Thereafter, the oil in the helium is separated. For example, a plurality of oil separators, in particular at least one pre-separator and at least one fine separator, are provided for oil separation. In addition, oil separators typically have an adsorber for filtering oil vapor and the like. After the adsorber, the refrigerant is substantially clean so that the refrigerant is made up of only helium to a very high degree. The proportion of oil is in the ppb range.
時々、比較的短い作動期間の後すぐに冷凍機に問題が生じる。コールドヘッドのような冷却装置の最低温度への冷却が、短い作動期間後すぐに不可能になる場合がある。従って、所望の低温を生成することができるようにコールドヘッドを定期的に保守して清浄化することが必要である。このため、高いコストを伴う。 Sometimes problems occur with the refrigerator immediately after a relatively short operating period. Cooling to a minimum temperature of a cooling device such as a cold head may not be possible immediately after a short operating period. Therefore, it is necessary to periodically maintain and clean the cold head so that the desired low temperature can be generated. This entails high costs.
本発明は、保守間隔を延ばすことができる冷凍機を提供することを目的とする。 An object of this invention is to provide the refrigerator which can extend a maintenance space | interval.
この目的は、本発明によれば請求項1の特徴により達成される。 This object is achieved according to the invention by the features of claim 1.
本発明の冷凍機は、特に10 K未満の低温を冷却装置に生成する役目を果たす。この目的に適した冷凍機は、例えば、本出願人のCoolpower シリーズの機械である。冷凍機は、冷媒を圧縮する圧縮機を備えている。場合によっては複数の特に連続するオイル分離器を有してもよいオイル分離器が、冷媒の送出方向の圧縮機の下流側に配置されている。特に、オイル分離器は、粗分離器及び/又はプレ分離器及び特に複数の細分離器を有してもよい。オイル分離器が、冷媒を清浄化するためのオイル吸着器を有していることが更に好ましい。更に、熱交換器が圧縮機とオイル分離器との間に設けられてもよい。更に、冷凍機は、コールドヘッドのような冷却装置を備えている。冷媒は冷却装置で膨張する。 The refrigerator of the present invention serves to generate a low temperature of less than 10 K in the cooling device. A refrigerator suitable for this purpose is, for example, the applicant's Coolpower series of machines. The refrigerator includes a compressor that compresses the refrigerant. In some cases, an oil separator, which may have a plurality of particularly continuous oil separators, is arranged downstream of the compressor in the refrigerant delivery direction. In particular, the oil separator may comprise a coarse separator and / or a pre-separator and in particular a plurality of fine separators. More preferably, the oil separator has an oil adsorber for cleaning the refrigerant. Furthermore, a heat exchanger may be provided between the compressor and the oil separator. Furthermore, the refrigerator includes a cooling device such as a cold head. The refrigerant expands in the cooling device.
研究により、クライオポンプがなぜ所望の低温に冷却することができないかについての現在の仮説が完全には正確ではないことが示されている。現在まで、清浄化の後であっても冷媒に依然として存在する微量のオイル及び/又は水が夫々、冷却装置及びコールドヘッドの頻繁な保守作業の必要性の原因であると仮定されていた。研究により、冷却装置の損傷が特に窒素及び酸素の存在によるものであることが現在示されている。ネオン、アルゴン、二酸化炭素などの他のガスが生じる場合、これらのガスも悪影響を及ぼす場合がある。 Studies have shown that the current hypothesis about why the cryopump cannot cool to the desired low temperature is not completely accurate. To date, it has been assumed that trace amounts of oil and / or water still present in the refrigerant even after cleaning are responsible for the need for frequent maintenance work of the cooling system and cold head, respectively. Research currently indicates that damage to the cooling device is due in particular to the presence of nitrogen and oxygen. If other gases such as neon, argon, carbon dioxide are produced, these gases may also have an adverse effect.
従って、本発明によれば、ガス吸着装置が、送出方向の冷却装置の上流側に配置されている。ガス吸着装置によって有毒ガスの少なくとも一部を冷媒から濾過する。その結果、冷却装置で凍結するこのようなガスが存在しなくなり、ひいては所要の保守間隔を延ばすことが可能になる。 Therefore, according to the present invention, the gas adsorption device is arranged on the upstream side of the cooling device in the delivery direction. At least a part of the toxic gas is filtered from the refrigerant by the gas adsorption device. As a result, there is no such gas freezing in the cooling device, and as a result, the required maintenance interval can be extended.
ガス吸着装置は、特に150 K 未満の温度、特に好ましくは120 K 未満の温度、特には70 K未満の温度で凍結する有毒ガスを吸着するように構成されていることが好ましい。言うまでもなく、ヘリウムは吸着されない。 The gas adsorbing device is preferably configured to adsorb toxic gases that freeze, in particular at temperatures below 150 K, particularly preferably at temperatures below 120 K, in particular at temperatures below 70 K. Needless to say, helium is not adsorbed.
ガス吸着装置は、好ましくは窒素及び/又は酸素を濾過及び/又は吸着する。ネオン、アルゴン又は二酸化炭素のようなコールドヘッドで凍結し得る他のガスも夫々濾過又は吸着することが好ましい。 The gas adsorber preferably filters and / or adsorbs nitrogen and / or oxygen. Other gases that can be frozen in a cold head such as neon, argon or carbon dioxide are also preferably filtered or adsorbed, respectively.
特に好ましい実施形態では、ガス吸着装置は、対応する有毒ガスの凍結が生じ得ない範囲に配置されている。従って、ガス吸着装置は、150 K を超える範囲、好ましくは150 K と300 K との間の範囲に配置されていることが好ましい。本明細書では、ガス吸着装置は、冷却装置の外側であって冷却装置の上流側に配置されてもよい。同様にガス吸着装置を、例えば冷却装置の入口に配置することが可能である。 In a particularly preferred embodiment, the gas adsorption device is arranged in a range where freezing of the corresponding toxic gas cannot occur. Accordingly, the gas adsorption device is preferably arranged in a range exceeding 150 K, preferably in a range between 150 K and 300 K. In the present specification, the gas adsorption device may be disposed outside the cooling device and upstream of the cooling device. Similarly, a gas adsorbing device can be placed at the inlet of the cooling device, for example.
ガス吸着装置が冷媒の流れ方向のオイル分離器の下流側に配置されていることが特に好ましい。特に、オイルによるガス吸着装置の汚染が生じ得ないように、ガス吸着装置は、オイル分離器のオイル吸着器の下流側に配置されている。 It is particularly preferable that the gas adsorbing device is arranged downstream of the oil separator in the refrigerant flow direction. In particular, the gas adsorbing device is arranged on the downstream side of the oil adsorber of the oil separator so that the oil does not contaminate the gas adsorbing device.
このガス吸着装置は、吸着層及び/又は吸着粉末及び/又は吸着繊維及び/又は吸着障壁として構成されてもよい。適切な吸着材料は、例えばゼオライトである。これは、例えば独国特許発明第69606117号明細書に記載されている。 The gas adsorption device may be configured as an adsorption layer and / or adsorption powder and / or adsorption fiber and / or adsorption barrier. A suitable adsorbing material is, for example, zeolite. This is described, for example, in German Patent 69606117.
更に本発明は、冷凍機の冷却材回路にガス吸着装置を使用する方法に関する。本明細書では、ガス吸着装置、特にガス吸着装置の上述された好ましい実施形態が使用される。具体的には、使用されるガス吸着装置は、クライオポンプを参照して上述された特徴を有している。 The invention further relates to a method of using a gas adsorber in a refrigerator coolant circuit. In the present description, the above-described preferred embodiments of the gas adsorption device, in particular the gas adsorption device, are used. Specifically, the gas adsorption device used has the characteristics described above with reference to a cryopump.
本発明を、好ましい実施形態及び添付図面を参照して以下により詳細に説明する。 The invention will be described in more detail below with reference to preferred embodiments and the accompanying drawings.
クライオポンプは、図示された実施形態ではスクロールポンプである圧縮機10を備えている。圧縮機10に、ライン12を介してヘリウムが供給され、ライン14を介してオイルが供給される。冷媒としての機能を果たすヘリウム及びオイルのこの圧縮された混合物は、ライン16を介して熱交換器18に運ばれる。熱交換器18で、圧縮によって加熱された冷媒を冷却する。その後、冷媒からオイルが濾過される。このためにオイル分離器が設けられている。図示された実施形態では、オイル分離器は、プレ分離器20、第1の細分離器22、第2の細分離器24及び吸着器26を有している。
The cryopump includes a
圧力逃し弁27が、高圧及び低圧間に第2の細分離器24と吸着器26との間に配置されている。
A
図示された実施形態では、ガス吸着装置28が、送出方向の吸着器26の下流側に配置されている。従って、ガス吸着装置28は、流れ方向の冷却装置30又はコールドヘッドの上流側に配置されている。
In the illustrated embodiment, a
ガス吸着装置28は冷却装置30の上流側の領域に配置されており、この領域の温度は、吸着されるガスが凍結する温度より高い。
The gas adsorbing
冷却装置で膨張した冷媒は、ライン32及びライン12を介して圧縮機10に戻る。同様に、分離したオイルはライン34、ライン36及びライン38を介して戻る。
The refrigerant expanded in the cooling device returns to the
Claims (8)
実質的にヘリウム及びオイルを含む冷媒を圧縮するための圧縮機(10)と、
前記冷媒の送出方向の前記圧縮機(10)の下流側に配置されたオイル分離器(20, 22, 24, 26)と、
前記冷媒が膨張する冷却装置(30)と
を備えており、
ガス吸着装置(28)が、前記送出方向の前記冷却装置(30)の上流側に配置されていることを特徴とする冷凍機。 A refrigerator for generating a vacuum, in particular a cryopump,
A compressor (10) for compressing a refrigerant substantially comprising helium and oil;
An oil separator (20, 22, 24, 26) disposed downstream of the compressor (10) in the refrigerant delivery direction;
A cooling device (30) for expanding the refrigerant,
A refrigerator having a gas adsorbing device (28) disposed upstream of the cooling device (30) in the delivery direction.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
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DE102016215985.2 | 2016-08-25 | ||
DE102016215985.2A DE102016215985A1 (en) | 2016-08-25 | 2016-08-25 | refrigeration machine |
PCT/EP2017/070032 WO2018036807A1 (en) | 2016-08-25 | 2017-08-08 | Refrigeration machine |
Publications (1)
Publication Number | Publication Date |
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JP2019528395A true JP2019528395A (en) | 2019-10-10 |
Family
ID=59631756
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2019506375A Pending JP2019528395A (en) | 2016-08-25 | 2017-08-08 | refrigerator |
Country Status (7)
Country | Link |
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US (1) | US20200386455A1 (en) |
EP (1) | EP3504487A1 (en) |
JP (1) | JP2019528395A (en) |
KR (1) | KR20190040214A (en) |
CN (1) | CN109661545A (en) |
DE (1) | DE102016215985A1 (en) |
WO (1) | WO2018036807A1 (en) |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS58187776A (en) * | 1982-04-27 | 1983-11-02 | 日本酸素株式会社 | Manufacture of argon |
JPS61240061A (en) * | 1985-04-15 | 1986-10-25 | ダイキン工業株式会社 | Helium refrigerator |
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2016
- 2016-08-25 DE DE102016215985.2A patent/DE102016215985A1/en not_active Withdrawn
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2017
- 2017-08-08 US US16/325,099 patent/US20200386455A1/en not_active Abandoned
- 2017-08-08 JP JP2019506375A patent/JP2019528395A/en active Pending
- 2017-08-08 CN CN201780051403.0A patent/CN109661545A/en active Pending
- 2017-08-08 EP EP17752355.2A patent/EP3504487A1/en not_active Withdrawn
- 2017-08-08 WO PCT/EP2017/070032 patent/WO2018036807A1/en unknown
- 2017-08-08 KR KR1020197005308A patent/KR20190040214A/en not_active Application Discontinuation
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JPS58187776A (en) * | 1982-04-27 | 1983-11-02 | 日本酸素株式会社 | Manufacture of argon |
JPS61240061A (en) * | 1985-04-15 | 1986-10-25 | ダイキン工業株式会社 | Helium refrigerator |
JPH0436552A (en) * | 1990-06-01 | 1992-02-06 | Hitachi Ltd | Refrigerator with cryogenic adsorption cylinder |
JPH09169506A (en) * | 1995-08-11 | 1997-06-30 | Boc Group Inc:The | Method for adsorbing and separating nitrogen from gas mixture |
JPH09225246A (en) * | 1996-02-26 | 1997-09-02 | Mitsubishi Heavy Ind Ltd | Gas separator |
JP2001517751A (en) * | 1997-09-22 | 2001-10-09 | フェルミン ヴィテリ, | Clean air engine for transportation and other power uses |
JP2000249414A (en) * | 1999-03-02 | 2000-09-14 | Iwatani Internatl Corp | Purity holding method of working refrigerant gas in pulse tube refrigerating machine |
Also Published As
Publication number | Publication date |
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WO2018036807A1 (en) | 2018-03-01 |
EP3504487A1 (en) | 2019-07-03 |
KR20190040214A (en) | 2019-04-17 |
DE102016215985A1 (en) | 2018-03-01 |
CN109661545A (en) | 2019-04-19 |
US20200386455A1 (en) | 2020-12-10 |
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