KR20090009994A - Desgign and manufacture of deccicant type air dryer for 40kg/cm^2 - Google Patents
Desgign and manufacture of deccicant type air dryer for 40kg/cm^2 Download PDFInfo
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- KR20090009994A KR20090009994A KR1020090000223A KR20090000223A KR20090009994A KR 20090009994 A KR20090009994 A KR 20090009994A KR 1020090000223 A KR1020090000223 A KR 1020090000223A KR 20090000223 A KR20090000223 A KR 20090000223A KR 20090009994 A KR20090009994 A KR 20090009994A
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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
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/0027—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
- B01D46/0036—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions by adsorption or absorption
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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
- B01D53/266—Drying gases or vapours by filtration
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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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/96—Regeneration, reactivation or recycling of reactants
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- Environmental & Geological Engineering (AREA)
- Drying Of Gases (AREA)
Abstract
Description
일반적인 공기드라이어는 냉동식과 흡착식이 있으며 이들은 이슬점 온도에 따라 3℃ 이상의 경우에는 냉동식 그리고 그 이하의 이슬점 온도가 필요할 경우에는 흡착식이 사용됨. Common air dryers are refrigerated and adsorptive, and they are refrigerated when the temperature is above 3 ℃ and adsorption when the dew point temperature is lower than that.
최근에 사용처의 요구에 의하여 개발한 압력 400kg/cm2, 용량 100 cfm, 이슬점 온도 -63℃, 그리고 연속 운전 조건에 맞는 흡착식 드라이어를 개발 공급함에 있어 새로운 기술이 적용됨 New technology has been applied in the development and supply of adsorption dryers for pressures of 400 kg / cm2, capacity of 100 cfm, dew point temperature of -63 ° C, and continuous operating conditions, which have been developed recently according to the requirements of the users.
흡착식 공기 드라이어는 제어부, 배관부, 부속 장치부 및 압력 용기 및 내부 흡착제로 구성되며 그중 압력 용기는 산업안전보건법 혹은 고압가스안전관리법에 의해 용적 및 압력에 따라 규정을 준수해야 한다. 부속 장치부로 입토출부의 필터류와 효율적인 면을 고려한 흡착제의 재생 방법을 달리하는 몇몇 가지의 방법이 사용되고 있음.Adsorption air dryers consist of a control unit, piping, accessories, pressure vessels and internal adsorbents, of which pressure vessels must comply with regulations according to volume and pressure by the Industrial Safety and Health Act or the High Pressure Gas Safety Control Act. Several methods have been used to change the regeneration method of the adsorbent in consideration of the filters and the efficiency of the inlet and outlet parts as an accessory device part.
금번 특고압 드라이어의 개발의 경우에는 사용처에서 제시한 4가지의 조건에 맞춘 설계임. In the case of the development of this special high-pressure dryer, the design meets the four conditions suggested by the user.
1. 연속 운전 가능1. Continuous operation possible
2. 400 kg/cm2G 이상의 압력 및 100 cfm의 용량 적용2. Apply pressure over 400 kg / cm2G and capacity of 100 cfm
3. 히터에 의해 압력용기 및 내부의 흡착제에 175℃의 가열3. Heating at 175 ℃ to pressure vessel and adsorbent inside by heater
4. 이슬점 온도 -63℃4. Dew point temperature -63 ℃
항공 우주 산업에 관련되는 연구 설비 등에 적용할 수 있음Applicable to research facilities related to the aerospace industry
1. 연속 운전이 가능토록 두 개의 압력용기를 적용하여 서로 스위칭하며 압축공기를 제습하는 과정과 수분으로 오염된 흡착제를 재생하는 과정을 동시에 발생시키게 하였음.1. Two pressure vessels were applied to enable continuous operation, switching between each other, dehumidifying compressed air, and regenerating the adsorbent contaminated with moisture.
2. 소용량 고압 조건을 적용하기 위하여 산업안전보건법 및 고압가스안전관리법에 적용 여부를 검토하여 압력 용기의 사이즈 및 두께를 적용하였음.2. In order to apply small-capacity high-pressure conditions, the application of the size and thickness of the pressure vessel was applied after examining the application to the Industrial Safety and Health Act and the High Pressure Gas Safety Management Act.
3. 수분에 오염된 흡착제를 재건조하기 위해서 압력용기 및 내부에 충전된 제습제 자체에 약간의 공기 흐름을 유지한 상태에서 175℃로 1시간 이상 유지시키는 장치로 밴드 형식의 히터를 적용하고 센서를 압력 용기에 부착하여 일정한 온도 를 유지할 수 있게 하였음.3. In order to rebuild the adsorbent contaminated with water, the band type heater is applied to the pressure vessel and the dehumidifying agent filled in the inside at 175 ℃ for at least 1 hour while maintaining some air flow. Attached to the pressure vessel to maintain a constant temperature.
4. 이슬점 온도를 주어진 4시간 정도의 시간동안 연속적 및 안정적으로 유지하기 위해서 Tower을 직렬로 두 개를 적용하였음.4. Two towers were applied in series to maintain the dew point temperature continuously and stably for a given 4 hours.
압축 장치에서 발생된 고압 습공기는 입구측의 1차 필터 및 드레인 장치를 통과하면서 일부 응축수가 제거된 상태에서 제어볼밸브(V1)을 통해 좌측 타워로 흡입되고, 타워 내부에 충전된 흡습제를 통과하면서 압축 공기 중에 포함된 수분이 흡습제에 의해 걸러지게 되며, 그 수분이 제거된 건공기는 제어볼밸브(V3) 및 2차 필터를 통해 시스템으로 공급된다. The high pressure humid air generated from the compression device is sucked into the left tower through the control ball valve (V1) while some condensate is removed while passing through the primary filter and the drain device on the inlet side, and passes through the absorbent charged inside the tower. The moisture contained in the compressed air is filtered by the moisture absorbent, and the dried air is removed to the system through the control ball valve V3 and the secondary filter.
이 때, 건공기의 일부(약 1~3%)는 유량조절밸브 및 체크밸브를 통해 우측 타워로 흘러가며 타워 외부에 설치된 밴드 히터에 의해 175℃로 가열되어 수분에 젖은 흡착제를 건조시키게 되며 흘러나온 수분이 함유된 공기는 방음장치를 통해 대기중으로 배출된다. At this time, part of the dry air (about 1 ~ 3%) flows to the right tower through the flow control valve and check valve, and is heated to 175 ℃ by the band heater installed outside the tower to dry the moisture absorbent. Moisture-containing air is released into the atmosphere through sound insulation.
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Application Number | Priority Date | Filing Date | Title |
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KR1020090000223A KR20090009994A (en) | 2009-01-05 | 2009-01-05 | Desgign and manufacture of deccicant type air dryer for 40kg/cm^2 |
KR1020090035439A KR100926764B1 (en) | 2009-01-05 | 2009-04-23 | Absorption type gas dryer |
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KR1020090000223A KR20090009994A (en) | 2009-01-05 | 2009-01-05 | Desgign and manufacture of deccicant type air dryer for 40kg/cm^2 |
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KR1020090000223A KR20090009994A (en) | 2009-01-05 | 2009-01-05 | Desgign and manufacture of deccicant type air dryer for 40kg/cm^2 |
KR1020090035439A KR100926764B1 (en) | 2009-01-05 | 2009-04-23 | Absorption type gas dryer |
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JPS577803A (en) * | 1980-06-17 | 1982-01-16 | Toshiba Corp | Air dehumidifier for ozonizer |
JP3363986B2 (en) * | 1994-03-02 | 2003-01-08 | 三菱重工業株式会社 | Solvent recovery method |
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