KR20090018183A - DESIGN AND MANUFACTURE OF HIGH PRESSURE TOWER FOR 400KG/cm^2, 170 m^2?H, D.P. -63°C DESICCANT AIR DRYER - Google Patents
DESIGN AND MANUFACTURE OF HIGH PRESSURE TOWER FOR 400KG/cm^2, 170 m^2?H, D.P. -63°C DESICCANT AIR DRYER Download PDFInfo
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- KR20090018183A KR20090018183A KR1020090000258A KR20090000258A KR20090018183A KR 20090018183 A KR20090018183 A KR 20090018183A KR 1020090000258 A KR1020090000258 A KR 1020090000258A KR 20090000258 A KR20090000258 A KR 20090000258A KR 20090018183 A KR20090018183 A KR 20090018183A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/26—Drying gases or vapours
- B01D53/261—Drying gases or vapours by adsorption
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/0407—Constructional details of adsorbing systems
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- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Drying Of Gases (AREA)
Abstract
Description
일반적인 공기드라이어는 냉동식과 흡착식이 있으며 이들은 이슬점 온도에 따라 3도 이상의 경우에는 냉동식 그리고 그 이하의 이슬점 온도가 필요할 경우에는 흡착식이 사용됨. Common air dryers are either refrigerated or adsorptive. They are refrigerated at temperatures above 3 degrees and adsorptive when dew point temperatures below are required.
사용처의 요구에 의하여 개발한 압력 400kg/cm2, 용량 100 cfm(170 ㎥/h), 이슬점 온도 -63℃, 그리고 연속 운전 조건에 맞는 흡착식 드라이어를 개발 공급함에 있어 새로운 기술이 적용됨New technology is applied in developing and supplying adsorption dryer suitable for pressure 400kg / cm2, capacity 100 cfm (170 ㎥ / h), dew point temperature -63 ℃, and continuous operating conditions developed according to the requirements of the user.
금번에 적용된 압력 용기는 산업안전보건법 혹은 고압가스안전관리법에 의해 적용을 받지 않는 소형으로서 받는 압력용기 및 관련 배관 및 제어용 밸브 및 제어 장치 그리고 입토출부의 필터류로 구분되며, 효율적인 면을 고려하여 흡착제의 재 생 방법을 달리하는 몇몇 가지의 방법이 사용되고 있음.The pressure vessel applied to this time is divided into the pressure vessel and the related piping and control valve and control device which are not applied by the Industrial Safety and Health Act or the High Pressure Gas Safety Management Act, and the filter type of the inlet / outlet. There are several different ways of playing.
금번 특고압 드라이어의 개발의 경우에는 사용처에서 제시한 해결하고자 하는 과제에 열거된 조건에 맞춘 설계이며 및 이미 생산되고 있는 제품임. In the case of the development of this special high-pressure dryer, it is a product that is designed and manufactured in accordance with the conditions listed in the problem to be solved presented by the user.
1. 분해 조립이 가능1. Can be disassembled and assembled
2. 압력 변화(0 ~ 400kg/cm2) 및 온도 변화 (상온 ~ 175℃)에 따른 수축 팽창 발생시에 연속적으로 기밀을 유지할 수 있는 압력 용기2. Pressure vessel that can keep airtight continuously when shrinkage expansion occurs due to pressure change (0 ~ 400kg / cm2) and temperature change (room temperature ~ 175 ℃)
3. 400 kg/cm2G 이상의 압력 및 100 cfm(170m3/hr)의 용량, 이슬점 온도 -63℃에 적합한 사이즈의 적용3. Application of a size suitable for pressures above 400 kg / cm2G and a capacity of 100 cfm (170 m3 / hr), dew point temperature of -63 ° C.
흡착제의 주기적인 교환이 가능하고 온도 및 압력의 변화에 따른 수축 팽창 및 강도 변화에 항구적인 강도를 유지하여 400kg/cm2, 100icfm, -63℃ 이슬점 온도등 관련된 조건을 만족시켜 항공 우주 연구 등에 관련되는 연구 설비 등에 적용 가능함 Periodic exchange of adsorbent is possible, and it maintains constant strength in shrinkage expansion and strength change according to temperature and pressure change, and satisfies related conditions such as 400kg / cm2, 100icfm, -63 ℃ dew point temperature, etc. Applicable to research facilities
요구되는 조립 가능하며 압력, 유량, 이슬점에 맞는 Vessel과 연결 Port의 Size, 그리고 압력 및 온도 변화에 따른 수축 팽창시 기밀을 유지하는 메커니즘의 설계 제작 및 시험.Design, fabrication and testing of the required assembly, size of vessel and connecting port according to pressure, flow rate and dew point, and mechanism to maintain airtightness when contracted and expanded according to pressure and temperature changes.
건조 사이클의 경우 헤드의 흡입구를 통해서 흡입된 습공기가 몸통에 충전된 흡착제를 통과하며 건조되며, 하부 리턴 및 중심 튜브 그리고 헤드의 토출을 통해 배출되어 후단부에 연결되는 사용처로 공급됨.In the drying cycle, the wet air sucked through the suction port of the head passes through the adsorbent filled in the body and is dried.
재생 사이클의 경우도 같은 경로를 통과하게 되나, 다른 점은 공급되는 공기가 건조된 공기이며 1~3%의 소량이 흡입되며, 밴드 히이터에 전력이 공급되어 몸통 및 흡착제가 가열되어 소량이 흘러가는 건조 공기에 의해 흡착제가 건조됨.In the case of the regeneration cycle, the same path is passed, but the difference is that the supplied air is dried air, in which a small amount of 1 to 3% is sucked in, and the band heater is supplied with electric power to heat the torso and the adsorbent. The adsorbent is dried by dry air.
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KR1020090000258A KR20090018183A (en) | 2009-01-05 | 2009-01-05 | DESIGN AND MANUFACTURE OF HIGH PRESSURE TOWER FOR 400KG/cm^2, 170 m^2?H, D.P. -63°C DESICCANT AIR DRYER |
KR1020090035442A KR100926766B1 (en) | 2009-01-05 | 2009-04-23 | Absorption type gas drying tower |
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KR1020090000258A KR20090018183A (en) | 2009-01-05 | 2009-01-05 | DESIGN AND MANUFACTURE OF HIGH PRESSURE TOWER FOR 400KG/cm^2, 170 m^2?H, D.P. -63°C DESICCANT AIR DRYER |
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KR1020090035442A KR100926766B1 (en) | 2009-01-05 | 2009-04-23 | Absorption type gas drying tower |
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KR101708815B1 (en) | 2015-01-30 | 2017-02-21 | 대우조선해양 주식회사 | Wing type apparatus for diffusing regeneration gas into dehydration bed |
KR101586841B1 (en) | 2015-02-02 | 2016-01-19 | 대우조선해양 주식회사 | Spiral tube type apparatus for diffusing regeneration gas into dehydration bed |
KR102174712B1 (en) | 2019-09-18 | 2020-11-05 | 현대피에프주식회사 | Dehydration cartridge with easy change of molecular sieve |
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JP4083320B2 (en) * | 1998-10-09 | 2008-04-30 | 株式会社キッツ | Hollow fiber membrane dryer |
KR100628945B1 (en) * | 2004-12-24 | 2006-09-27 | 주식회사 에어젠 | Moisture remover for air compressor |
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