• 제목/요약/키워드: Cryogenic distillation column

검색결과 9건 처리시간 0.029초

심랭식공기분리공정에서 질소증류탑의 엑서지 해석 (Exergy Analysis of Nitrogen Distillation Column in the Cryogenic Air Separation Process)

  • 용평순;이성철
    • 한국초전도ㆍ저온공학회논문지
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    • 제4권1호
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    • pp.145-150
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    • 2002
  • The distillation column is one of large energy consumable units in the cryogenic air separation process and the accurate energy analysis of this unit is necessary for choice of energy saving process. In this work, the energy method was adopted for energy analysis of a cryogenic nitrogen distillation column. In order to designing the energy saving distillation column, the exergy distribution of feed air, exergy efficiency and exergy loss for process condition was investigated and the optimal process condition to minimize the exergy loss was found. The result from this work can be used as a guideline for the choice of the process design conditions and efficiency improvement of cryogenic distillation column.

심냉 증류를 통한 전자급 고순도 이산화탄소의 분리 공정에 대한 전산 모사 연구 (A Computer Simulation Study on the Separation Process for Electronic Grade, Highly Pure Carbon Dioxide through a Cryogenic Distillation)

  • 박일수;문흥만;조정호
    • 한국수소및신에너지학회논문집
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    • 제34권1호
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    • pp.83-89
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    • 2023
  • In this study, a computer simulation work has been performed for the separation of electronic grade highly pure carbon dioxide more than 7 N purity through a cryogenic distillation process. For the cold utility as a cooling medium for a condenser of the cryogenic distillation column, propylene was utilized as a refrigerant in the vapor-recompression refrigeration cycle. Through this work, it was concluded that the cryogenic distillation column with two stage compression and refrigeration cycle were essential to obtain a highly-pure liquefied CO2.

수소동위원소 분리를 위한 초저온증류장치 (Cryogenic Distillation Apparatus for Hydrogen Isotopes Separation)

  • 송규민;손순환;김광신;김위수
    • 한국초전도저온공학회:학술대회논문집
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    • 한국초전도저온공학회 2001년도 학술대회 논문집
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    • pp.163-166
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    • 2001
  • KEPCO has a plan to construct TRF (tritium removal facility) in wolsong nuclear power plant site by 2005. In advance of WTRF construction, the pilot plant was installed at KEPRI in order to show process reliability of WTRF. The main processes of this pilot plant are LPCE(liquid phase catalytic exchange) and CD (cryogenic distillation). Deuterium is separated from heavy water in LPCE process and concentrated in CD process. CD process consists of cold box, where are a distillation column and heat exchangers, vacuum system, cryogenic refrigerant supply system and instrument & control system. The experience of the pilot plant will be used in WTRF design review, operating procedure revision and fundamental education for the operators.

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이산화탄소 액화를 위한 증기 재압축 냉동 공정과 액체질소 냉열을 이용한 냉동 공정의 비교 연구 (Comparative Study on the Refrigeration Processes between Refrigeration Using Vapor Recompression and Refrigeration Using LN2 Cold Heat for the Carbon Dioxide Liquefaction)

  • 노상균
    • 한국수소및신에너지학회논문집
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    • 제34권5호
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    • pp.549-554
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    • 2023
  • In this paper, three kinds of studies have been completed to obtain highly purified carbon dioxide having more than 7N purity as an electronic grade quality. PRO/II with PROVISION release January 2023 from AVEVA company was used, and Peng-Robinson equation of the state model with Twu's alpha function was selected for the modeling of the cryogenic distillation process. When using LN2 cold heat, we can obtain highest recovery of carbon dioxide as a bottom product for a cryogenic distillation column.

고순도 질소생산용 초저온 공기분리장치 개발 연구 (A Study on the Development of a Cryogenic Air Separation Unit to Produce High Purity Nitrogen)

  • 용평순;문흥만;이성철
    • 한국초전도ㆍ저온공학회논문지
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    • 제3권1호
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    • pp.69-73
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    • 2001
  • For developing the cryogenic air separation unit, it requires some technology such as basic process design. equipment design and manufacturing based on the cryogenic physical properties and separation theory. In this study, we developed a process and equipment for producing high purity nitrogen which has the production capacity of 1600N㎥/h under 1 ppm $O_2$ and $H_2O$. Also we found that the number of theoretical plate(NTP) of distillation column was 44 and maximum nitrogen recovery ration of this process was 42% from the process simulation. The performance test was also carried out for the nitrogen recovery ratio and equipment efficiency. The results showed that the optimum nitrogen recovery was 41% and the maximum equipment efficiency was attained.

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심냉 공기분리공정의 공기압축공정에서 전력비 절감을 위한 액화천연가스 냉열 활용에 대한 연구 (A Study on the Utilization of the LNG Cold Heat for the Reduction of the Power Consumption in Main Air Compressors in Cryogenic Air Separation)

  • 조두희;조정호
    • 한국수소및신에너지학회논문집
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    • 제31권3호
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    • pp.322-327
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    • 2020
  • In this work, a study for the reduction of the electric power consumption has been estimated in main air compressors in the air separation unit through cryogenic distillation columns with PRO/II with PROVISION V10.2 at AVEVA company. Both required LNG mass flow rate and cold heat contained in 1 ton of LNG were also predicted using Peng-Robinson equation of state with Twu's new alpha function. Through this work, we concluded that 32.33-48.69% of electric power could be saved by using LNG cold heat.

수소 동위원소 분리를 위한 77 K 극저온 파과 곡선 측정 시스템 제작 (Investigation of Cryogenic Breakthrough Curve Measurement System at 77 K for Hydrogen Isotopologue Separation)

  • 김수환;오현철
    • 한국재료학회지
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    • 제32권1호
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    • pp.36-43
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    • 2022
  • Breakthrough analysis has widely been explored for the dynamic separation of gaseous mixtures in porous materials. In general, breakthrough experiments measure the components of a flowing gas when a gaseous mixture is injected into a column filled with an adsorbent material. In this paper, we report on the design and fabrication of a breakthrough curve measurement device to study the dynamic adsorptive separation of hydrogen isotopologues in porous materials. Using the designed system, an experiment was conducted involving a 1:1 mixture of hydrogen and deuterium passed through a column filled with zeolite 13X (1 g). At room temperature, both hydrogen and deuterium were adsorbed in negligible amounts; however, at a temperature of 77 K, deuterium was preferentially adsorbed over hydrogen. The selectivity was different from that in the existing literature due to the different sample shapes, measurement methods, and column structures, but was at a similar level to that of cryogenic distillation (1.5).

질소, 산소, 아르곤에 대한 상태방정식의 신뢰도 (A Reliability of Equation of State for Nitrogen, Oxygen and Argon)

  • 용평순;문흥만;손무룡;이성철
    • 한국가스학회지
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    • 제1권1호
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    • pp.41-48
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    • 1997
  • 가스물성의 계산방법으로 상태방정식이 널리 사용되고 있으나 상태방정식의 종류에 따라서 물성예측에 서로 다른 차이를 보이고 있다. 본 연구는 가스의 액화온도에서 상온에 이르는 온도범위와 1bar에서 30bar에 이르는 압력범위에서 질소, 산소, 아르곤에 대한 상태방정식의 물성계산 신뢰도를 검토하고자 하였다. 이를 위하여 Aspen plus에서 제공하는 Soave-Redlich-Kwong, Peng-Robinson, BWR-Lee Staring 상태방정식을 비교대상으로 하였고 계산결과는 문헌치 및 virial식과 비교하였다. 또한 물성계산식이 공정에 미치는 영향을 고찰하기 위하여 초저온 공기분리장치의 증류탑 및 팽창터어빈 계산을 수행하여 상태방정식 차이에 의한 공정계산 차이를 비교, 분석하였다.

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