• Title/Summary/Keyword: 가스 분리

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Decrease efficiency of Offensive Odor from Pig Excreta by Yeast Strain, Pichia farinosa NASS-2 Isolated from Soy Bean Paste (된장에서 분리한 효모(Pichia farinosa NASS-2)의 돈분 악취감소효과)

  • Yoo, Jae Hong;Park, In Cheol;Kim, Wan Gyu
    • The Korean Journal of Mycology
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    • v.40 no.4
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    • pp.254-257
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    • 2012
  • The different microbial species were isolated from soy bean paste samples. A yeast strain NASS-2 was effective to decrease odor activity on pig excreata was identified as Pichia farinosa based on nucleotide sequences of 18S ribosomal DNA and Internal transcribed space (ITS). The extracellular fraction of P. farinosa NASS-2 was effective to decrease odor activity of pig excrements. Optimal medium component for decreasing order activity on odor material composed of soluble starch 2.0% (w/v) and yeast extract 0.8% (v/v). The decrease of odor material was maximum at $28^{\circ}C$ for 72 hours with pH 5.5. When the P. farinosa NASS-2 culture broth was treated to pig excrements, the removal efficiency was an average concentration with 1.38 ppm of ammonia gas.

Manufacturing and Application of Activated Carbon and Carbon Molecular Sieves in Gas Adsorption and Separation Processes (가스 흡착 및 분리공정용 활성탄소와 탄소분자체의 제조 및 응용)

  • Jeong, Seo Gyeong;Ha, Seongmin;Lee, Young-Seak
    • Applied Chemistry for Engineering
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    • v.33 no.5
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    • pp.488-495
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    • 2022
  • Activated carbon (AC) and carbon molecular sieve (CMS) have attracted attention as porous materials for recovery and separation of greenhouse gases. The carbon molecular sieve having uniform pores is used for collecting and separating gases because it may selectively adsorb a specific gas. The size and uniformity of pores determine the performance of the CMS, and chemical vapor deposition (CVD) is widely used to coat the surface with a predetermined thickness in order to control the CMS's micropores. This CVD method can be used to control the size of pores in CMS manufacturing, but it must be optimized because of its various experimental variables. Therefore, in order to produce AC and CMS for gas adsorption and separation, this review focuses on various activation processes and pore control technologies by CVD and surface treatment.

Separation and Recovery of F-gases (불화 온실 가스 저감 및 분리회수 기술의 연구개발 동향)

  • Nam, Seung-Eun;Park, Ahrumi;Park, You-In
    • Membrane Journal
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    • v.23 no.3
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    • pp.189-203
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    • 2013
  • F-gases, gases containing fluorine such as perfluorocarbons (PFCs), sulfurhexafluoride ($SF_6$), nitrogen trifluoride ($NF_3$) are known to have green house effects. Although the net emission rates of gases containing fluorine are much lower than those of $CO_2$, their contribution to global warming cannot be ignored because of their extremely high global warming potential (GWP). F-gases mainly have been used for a variaty of applications in the semiconductor/LCD processes and in the electric power distribution industry of the national key industry. One of practical solutions of controlling the emission rates of F-gases is to reuse by separation and recovery of F-gases of low concentration from the gases mixtures with nitrogen or air. This work investigates some methods for F-gases recovery and separation around the membrane-based process.

Hydrate Phase Equilibria for the Ternary $N_2$ + HFC-134a + Water and $N_2$ + $SF_6$ + Water Mixtures (질소 + HFC-134a와 질소 + $SF_6$의 가스 하이드레이트 상평형)

  • Cha, In-Uk;Lee, Seung-Min;Lee, Ju-Dong;Lee, Gang-Woo;Seo, Yong-Won
    • 한국신재생에너지학회:학술대회논문집
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    • 2008.10a
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    • pp.213-215
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    • 2008
  • 최근 지구온난화가 국제적인 이슈화되면서 온실가스의 효과적인 처리에 많은 관심이 집중되고 있다. 냉매로 주로 사용되는 HFC-134a와 절연제로 주로 사용되고 있는 $SF_6$는 각각 이산화탄소의 11,700배와 23,900배의 지구온난화지수를 가지는 온실가스이다. 본 연구에서는 이 두 물질의 효과적인 분리/회수를 위하여 가스 하이드레이트 형성을 이용한 방법을 제안하였다. 하이드레이트 형성법을 이용 할 경우 공정이 단순하고 저압에서 분리가 가능하므로 타 분리공정과의 경쟁이 가능할 것으로 예상된다. 본 실험은 275-290 K의 온도범위와 3 - 30 bar의 압력범위에서 질소 + HFC-134a (20, 40, 60, 80%)와 질소 + $SF_6$ (10, 30, 50, 70%)의 혼합기체를 사용하여 각 조성에 따른 하이드레이트(H)-물($L_W$)-기상 (V)의 3상 평형점을 측정하였다. HFC-134a 또는 $SF_6$의 조성이 낮은 혼합기체의 3상 평형점은 순수 질소의 3상 평형점에 비하여 주어진 온도에서 평형압력이 현저히 낮은 것을 볼 수 있었으며 HFC-134a 또는 $SF_6$의 조성이 증가할 수록 순수한 HFC-134a 또는 $SF_6$의 3상 평형점에 근접하는 것을 볼 수 있었다. 특히 $SF_6$는 다른 기체와 달리 하이드레이트의 생성/해리에 긴 시간이 필요하다는 것을 알 수 있었다. 본 실험에서 얻어진 결과는 하이드레이트를 이용한 HFC-134a와 $SF_6$ 분리 공정의 중요한 기초 자료가 되며 다른 혼합 기체의 분리 공정에도 응용될 수 있을 것이다.

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Study on Materials and Process Systems for $CO_2$ separation from Combustion of Fossil Fuels (배기가스에서 이산화탄소 분리를 위한 재료 및 공정에 대한 이론적 고찰)

  • Han, Sang-Il;Hwang, Kyu-Suk
    • Journal of the Korean Applied Science and Technology
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    • v.31 no.3
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    • pp.375-386
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    • 2014
  • Carbon dioxide ($CO_2$) is a green-house gas which causes the global warming problems. Anthropogenic emissionspredominantly from the combustion of coal, oil, and natural gas in electricity generations are expected to increase continuously in the future, resulting in increased $CO_2$ concentration in the atmosphere. In this study, we investigated materials properties and process systems for $CO_2$ separation with an emphasis of the post-combustion process.

The Development of gasket for Proton Exchange Membrane Fuel Cell (고분자 전해질 연료전지용 Gasket 개발)

  • Chun, Hyun-A;Seoung, Dong-Muk;Kim, Tae-Min
    • 한국신재생에너지학회:학술대회논문집
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    • 2007.06a
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    • pp.166-168
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    • 2007
  • 고분자 전해질 연료전지는 다수의 단위 cell을 적층하여 stack을 형성하게 되며, 각 단위 cell 은 분리판과 MEA 사이에 gasket을 장착하게 된다. 이때 장착된 gasket은 분리판과 MEA사이의 일정한 gap을 유지하여 가스를 균일하게 분배되도록 할 뿐만 아니라, 가스 유출을 막는 sealing 재(材)로서의 역할을 한다. 따라서 고분자 전해질 연료전지의 성능확보를 위해서는 내구성 및 가스 기밀성이 우수한 gasket 개발이 무엇보다 중요하다. 본 연구에서는 이러한 gasket 물성을 만족시킬 수 있는 고분자 전해질 연료전지용 gasket을 개발하고자 하였으며, 이를 검증하기 위하여 가혹 조건에서 실험을 수행하였다. 그 결과 종래의 gasket 보다 열적, 화학적 및 가스기밀성 변에서 우수한 고분자 전해질 연료전지용 gasket을 얻을 수 있었다.

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축류식 가이드 베인 구조 -반건식 세정기

  • 한국환경기술인연합회
    • Environmental engineer
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    • s.121
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    • pp.46-49
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    • 1996
  • 반건식 세정기는 기존습식처리 설비의 단점인 폐수 및 백연의 발생, 설비의 내구성 저하 등을 보완한 유해가스 처리설비로 탁월한 가스 및 중금속 제거효율, 백연 및 폐수의 발생이 전무하며, 반응생성물의 분리제거로 후단집진설비의 부하를 최대한 줄 일 수 있는 21세기 첨단 유해가스 제거기술의 결정체이다.

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Characteristics of Water Gas Shift and Membrane Process for Pre-combustion CO2 Capture (연소전 CO2 포집을 위한 수성가스반응과 분리막 공정 특성)

  • Kim, Jeong-Nam;You, Jong-Kyun;Choi, Soo-Hyun;Baek, Il-Hyun
    • Journal of the Korea Academia-Industrial cooperation Society
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    • v.17 no.1
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    • pp.21-27
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    • 2016
  • Global warming due to greenhouse gas emissions is considered as a major problem worldwide, and many countries are making great efforts to reduce carbon dioxide emissions. Many technologies in post-combustion, pre-combustion and oxy-fuel combustion $CO_2$ capture have been developed. Among them, a hybrid pre-combustion $CO_2$ capture system of a water gas shift (WGS) reactor and a membrane gas separation unit was investigated. The 2 stage WGS reactor integrated high temperature shift (HTS) with a low temperature shift (LTS) was used to obtain a higher CO conversion rate. A Pd/Cu dense metal membrane was used to separate $H_2$ from $CO_2$ selectively. The performance of the hybrid system in terms of CO conversion and $H_2$ separation was evaluated using a 65% CO, 30 % $H_2$ and 5% $CO_2$ gas mixture for applications to pre-combustion $CO_2$ capture. The experiments were carried out over the range of WGS temperatures ($200-400^{\circ}C$), WGS pressures (0-20bar), Steam/Carbon (S/C) ratios (2.5-5) in a feed gas flow rate of 1 L/min. A very high CO conversion rate of 99.5% was achieved with the HTS-LTS 2 stage water gas shift reactor, and 83% $CO_2$ was concentrated in the retentate using the Pd/Cu membrane.

Effects of CO and $CO_2$ on Hydrogen Permeation through Pd-coated V-Ti-Ni Alloy Membranes (Pd 코팅된 V-Ti-Ni 합금 분리막을 통한 수소투과에서 CO와 $CO_2$의 영향)

  • Jeon, Sung-Il;Park, Jung-Hoon;Lee, Yong-Taek
    • Membrane Journal
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    • v.21 no.3
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    • pp.290-298
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    • 2011
  • The influence of co-existing gases on the hydrogen permeation was studied through a Pd-coated $V_{53}Ti_{26}Ni_{21}$ alloy membrane. The hydrogen permeation characteristics of Pd-coated $V_{53}Ti_{26}Ni_{21}$ alloy membrane have been investigated in the pressure range 1-3 bar under pure hydrogen and hydrogen mixture gas with carbon dioxide and carbon monoxide at $450^{\circ}C$. Preliminary hydrogen permeation experiments have been confirmed that hydrogen flux was $5.36mL/min/cm^2$ for a Pd-coated $V_{53}Ti_{26}Ni_{21}$ alloy membrane (thick: 0.5 mm) using pure hydrogen as the feed gas. In addition, hydrogen fluxes were 4.46, 5.20, $3.91mL /min/cm^2$ for$V_{53}Ti_{26}Ni_{21}$ alloy membrane using $H_2/CO_2$, $H_2/CO$ and $H_2/CO_2/CO$ as the feed gas respectively. Therefore, the hydrogen permeation flux decreased with decrease of hydrogen partial pressure irrespective of temperature and pressure when $H_2/CO_2$, $H_2/CO$ and $H_2/CO_2/CO$ mixture applied as feed gas respectively and permeation fluxes were satisfied with Sievert's law in different feed conditions. It was found from XRD results after permeation test that the Pd-coated $V_{53}Ti_{26}Ni_{21}$ alloy membrane had good stability and durability for various mixtures feeding condition.