KR20010012814A - 가스 공급원 및 분배 장치의 제조 방법 - Google Patents
가스 공급원 및 분배 장치의 제조 방법 Download PDFInfo
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- KR20010012814A KR20010012814A KR1019997010777A KR19997010777A KR20010012814A KR 20010012814 A KR20010012814 A KR 20010012814A KR 1019997010777 A KR1019997010777 A KR 1019997010777A KR 19997010777 A KR19997010777 A KR 19997010777A KR 20010012814 A KR20010012814 A KR 20010012814A
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- F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
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Abstract
Description
온도(°K) | 압력 상승 속도(토르/일) | 속도 상수 K(s-1) | LN K(s-1) |
275.45 | 1 | 2.26E-10 | -22.2 |
296.15 | 5.6 | 1.26E-9 | -20.5 |
303.15 | 10 | 2.26E-9 | -19.9 |
Claims (18)
- 수착성 유체의 유지 및 사용시 유체의 주문식 분배를 위한 흡수제 물질을 수용하고 있는 유체 저장 및 분배 용기의 제조 방법으로,용기에 흡수제 물질을 충전시키는 단계와, 수착성 유체를 용기로 유동시켜 용기내의 흡삭제 물질에 흡착되어 그 유체가 유지되도록 흡수제 물질을 수용하고 있는 용기를 수착성 유체의 공급원에 결합시키는 단계와, 상기 용기에는 초기량의 유체로 벌크(bulk) 충전된 다음, 유체 충전 온도 조건에 대해 감소된 온도 조건에서 초기량의 유체로 충전된 흡수제를 수용하고 있는 용기가 열적으로 상기 감소된 온조 조건으로 평형시키기에 충분한 시간동안 상기 유체를 저장하며, 상기 열적 평형에 후속하여 상기 유체로 용기의 충전을 완료하는 단계를 포함하는 것을 특징으로 하는 유체 저장 및 분배 용기의 제조 방법.
- 제1항에 있어서, 수착성 유체의 공급원은 수착성 유체의 공급부에 연결되고, 상기 용기에 연결되도록 배치된 충전 매니폴드인 것을 특징으로 하는 유체 저장 및 분배 용기의 제조 방법.
- 제2항에 있어서, 상기 충전 매니폴드는 자동 충전 매니폴드인 것을 특징으로 하는 유체 저장 및 분배 용기의 제조 방법.
- 제1항에 있어서, 상기 감소된 온도 조건은 용기를 감소된 온도 조건에서 유지시키는 특성 및 크기를 갖는 환경 제어 챔버에 의해 제공되는 것을 특징으로 하는 유체 저장 및 분배 용기의 제조 방법.
- 수착성 유체의 유지 및 사용시 유체의 주문식 분배를 위한 흡수제 물질을 수용하고 있는 유체 저장 및 분배 용기의 제조 방법으로,용기에 흡수제 물질을 충전시키는 단계와, 수착성 유체를 용기로 유동시켜 용기내의 흡수제 물질에 흡착되어 그 유체가 유지되도록 흡수제 물질을 수용하고 있는 용기를 수착성 유체의 공급원에 결합시키는 단계를 포함하며, 상기 수착성 유체는, 이 수착성 유체를 용기로 유동시키는 동안 흡착열 효과와, 용기로의 흡수제 물질의 수착성 유체의 흡착을 개선시키기 위해 수착성 유체를 용기로 유동시키기 전에 냉각되는 것을 특징으로 하는 유체 저장 및 분배 용기의 제조 방법.
- 제5항에 있어서, 상기 용기는 수착성 유체가 용기로 유동되는 동안 더 냉각되는 것을 특징으로 하는 유체 저장 및 분배 용기의 제조 방법.
- 제1항에 있어서, 상기 용기는 수착성 유체의 공급원으로부터의 용기 제거를 수용하고 상이한 열적 환경으로 이송시키기 위해 수착성 유체를 용기로 유동시키기 위한 가동 캐리어 구조체상에 유지되는 것을 특징으로 하는 유체 저장 및 분배 용기의 제조 방법.
- 제7항에 있어서, 상기 가동 캐리어 구조체는 용기를 수착성 유체 공급원에 상호 연결시키기 위해 매니폴드 연결 조립체가 설치되어 있는 가동 카트를 포함하는 것을 특징으로 하는 유체 저장 및 분배 용기의 제조 방법.
- 제1항에 있어서, 상기 용기에는 흡수제 물질과 접촉하는 유체의 흡착열을 분산시키기 위해 유체를 용기로 유동시키는 중에 엑티브(active) 냉각이 실행되는 것을 특징으로 하는 유체 저장 및 분배 용기의 제조 방법.
- 제1항에 있어서, 용기와 그 용기내의 흡수제 물질로부터의 탈가스를 위해 유체 유동 전에 용기를 주기적으로 정제시키는 것을 특징으로 하는 유체 저장 및 분배 용기의 제조 방법.
- 제1항에 있어서, 상기 용기에는 흡수제 물질과 접촉하는 유체의 흡착열을 분산시키기 위해 유체를 용기로 유동시키는 중에 과충전 및 블로우 다운 조건에서 실행되는 것을 특징으로 하는 유체 저장 및 분배 용기의 제조 방법.
- 유체에 친화성이 있는 흡수제 물질을 수용하고 있는 유체 저장 및 분배 용기를 제조하는 장치로서,상기 용기에는 흡수제 물질이 로딩되며, 상기 유체는 용기내의 흡수제 물질에 흡착되어 유지되도록 용기로 유동하며, 유체의 공급원과 유체 연통하게 배치된 매니폴드와, 용기로 유동하는 유체의 압력 및 온도 조건을 제어하기 위한 수단을 포함하는 것을 특징으로 하는 유체 저장 및 분배 용기 제조 장치.
- 제12항에 있어서, 상기 용기로의 유체 유동 속도를 용기로의 유체 유동의 제어된 압력 및 온도 조건에 일치하도록 제어하기 위한 질량 유동 제어기를 더 포함하는 것을 특징으로 하는 유체 저장 및 분배 용기 제조 장치.
- 제1항에 있어서, 상기 유체는 수소화물 가스, 할로겐 가스, 가스상의 유기 금속 Ⅴ족 화합물로 이루어진 그룹에서 선택된 가스를 포함하는 것을 특징으로 하는 유체 저장 및 분배 용기의 제조 방법.
- 제1항에 있어서, 상기 유체는 실레인, 디보란, 게르만, 플루오르, 암모니아, 포스핀, 아르신, 스티빈, 황화 수소, 셀레늄화 수소, 델루르화 수소, 3염화 붕소, 6염화 텅스텐, 염소, 브롬화 수소, 불화 수소, 요오드화 수소, 불화 수소로 이루어진 그룹에서 선택된 가스를 포함하는 것을 특징으로 하는 유체 저장 및 분배 용기의 제조 방법.
- 제1항에 있어서, 상기 흡수제 물질은 탄소 물질, 결정화 알루미노실리케이트 물질, 실리카, 알루미나, 매크로 그물 모양의 중합체 및 규조토로 이루어진 그룹에서 선택되는 것을 특징으로 하는 유체 저장 및 분배 용기의 제조 방법.
- 제1항에 있어서, 상기 흡수제 물질은 활성화된 탄소 물질을 포함하는 것을 특징으로 하는 유체 저장 및 분배 용기의 제조 방법.
- 제1항에 있어서, 상기 저장 및 분배 용기는 가늘고 긴 형상인 것을 특징으로 하는 유체 저장 및 분배 용기의 제조 방법.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US859,171 | 1997-05-20 | ||
US08/859,171 US5837027A (en) | 1996-05-20 | 1997-05-20 | Manufacturing process for gas source and dispensing systems |
PCT/US1998/010337 WO1998052678A1 (en) | 1997-05-20 | 1998-05-20 | Manufacturing process for gas source and dispensing systems |
Publications (2)
Publication Number | Publication Date |
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KR20010012814A true KR20010012814A (ko) | 2001-02-26 |
KR100545497B1 KR100545497B1 (ko) | 2006-01-25 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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KR1019997010777A KR100545497B1 (ko) | 1997-05-20 | 1998-05-20 | 가스 공급원 및 분배 장치의 제조 방법 |
Country Status (8)
Country | Link |
---|---|
US (1) | US5837027A (ko) |
EP (1) | EP1017474B1 (ko) |
JP (2) | JP4612920B2 (ko) |
KR (1) | KR100545497B1 (ko) |
AT (1) | ATE336291T1 (ko) |
AU (1) | AU7584198A (ko) |
DE (1) | DE69835600T2 (ko) |
WO (1) | WO1998052678A1 (ko) |
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CN108006433A (zh) * | 2017-12-25 | 2018-05-08 | 杭州福斯达深冷装备股份有限公司 | 一种液化罐 |
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-
1997
- 1997-05-20 US US08/859,171 patent/US5837027A/en not_active Expired - Lifetime
-
1998
- 1998-05-20 KR KR1019997010777A patent/KR100545497B1/ko not_active IP Right Cessation
- 1998-05-20 AT AT98923580T patent/ATE336291T1/de not_active IP Right Cessation
- 1998-05-20 AU AU75841/98A patent/AU7584198A/en not_active Abandoned
- 1998-05-20 DE DE69835600T patent/DE69835600T2/de not_active Expired - Lifetime
- 1998-05-20 EP EP98923580A patent/EP1017474B1/en not_active Expired - Lifetime
- 1998-05-20 JP JP55059298A patent/JP4612920B2/ja not_active Expired - Lifetime
- 1998-05-20 WO PCT/US1998/010337 patent/WO1998052678A1/en active IP Right Grant
-
2010
- 2010-07-29 JP JP2010170705A patent/JP2010249324A/ja active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108006433A (zh) * | 2017-12-25 | 2018-05-08 | 杭州福斯达深冷装备股份有限公司 | 一种液化罐 |
CN108006433B (zh) * | 2017-12-25 | 2023-09-22 | 杭州福斯达深冷装备股份有限公司 | 一种液化罐 |
Also Published As
Publication number | Publication date |
---|---|
DE69835600T2 (de) | 2007-08-23 |
KR100545497B1 (ko) | 2006-01-25 |
EP1017474A1 (en) | 2000-07-12 |
US5837027A (en) | 1998-11-17 |
EP1017474B1 (en) | 2006-08-16 |
WO1998052678A1 (en) | 1998-11-26 |
JP2002511915A (ja) | 2002-04-16 |
DE69835600D1 (de) | 2006-09-28 |
AU7584198A (en) | 1998-12-11 |
JP2010249324A (ja) | 2010-11-04 |
JP4612920B2 (ja) | 2011-01-12 |
ATE336291T1 (de) | 2006-09-15 |
EP1017474A4 (en) | 2002-11-13 |
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