• Title/Summary/Keyword: 증발가스량

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Effects of Charging Conditions on Evaporating Temperature for Diffusion Absorption Refrigerator (확산형 흡수식 냉장고에서 작동매체 충진조건이 증발온도에 미치는 영향)

  • 김선창;김영률;백종현;박승상
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
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    • v.15 no.10
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    • pp.828-834
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    • 2003
  • A diffusion absorption refrigerator is a heat-generated refrigeration system. It uses a three-component working fluid consisting of the refrigerant (ammonia), the absorbent (water) and the auxiliary gas (hydrogen or helium). In this study, experimental investigations have been carried out to examine the effects of charging conditions of working fluids on the evaporating temperature for diffusion absorption refrigerator. Experimental parameters considered in the present experiments are charging concentration, solution charge and system pressure determined by auxiliary gas charged. As a result, in the charging condition of 35% of concentration and 20 kg$_{f}$cm$^2$ of system pressure, the system has the lowest evaporating temperature. It was found that there exists a minimum value of solution charge for the operation of diffusion absorption refrigerator.r.

Research on Improving Drying Technology For Sewage Waste Using Direct Flotation Using Heat Storage Media (축열메디아 활용 직접부상방식을 이용한 하수찌꺼기의 건조기술 향상에 관한 연구)

  • Sung-Il Noh;Ung-Yong Kim;Sung-Gyun Jo;Hyun-Gon Shin
    • Journal of the Korea Organic Resources Recycling Association
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    • v.31 no.4
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    • pp.5-11
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    • 2023
  • This study was conducted to improve energy efficiency and problems such as clumping and fouling in the glue zone that occur in the moisture content range of 40 to 60% when sewage dehydration residue is directly fed into the dryer. The temperature of the hot air is low at 270~300℃, and the paddle-type flotation method and dehydrated residue are applied to the circulated heat storage media to increase the contact area with the hot air, thereby reducing energy recovery and gas emissions. The water content of the dried residue is 2.7. ~7 .5%, the heat of evaporation of moisture was 608.0~690.6 kcal/kg·H2O, which confirmed an energy saving effect of about 8.8% compared to the heat of evaporation of moisture of 714.5 kcal/kg·H2O when no heat storage media was used.

Thermal Analysis Comparison of IMO with USCG Design Condition for the INGC During the Cool-down Period (급냉각기간에서 IMO설계조건과 USCG 설계조건에 대한 LMGC 화물탱크의 열해석 비교)

  • Lee, Jung-Hye
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.28 no.11
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    • pp.1390-1397
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    • 2004
  • This study is concerned with the thermal analysis during the cool-down period of 135,000㎥ class GT-96 membrane type LNG carrier under IMO and USCG design condition. During the cool-down period, the spraying rate for the NG cooling decreases as the temperature of NG falls down from -4$0^{\circ}C$ to -l3$0^{\circ}C$, and the spraying rate for the cooling of the insulation wall increases as the temperature gradient of the insulation wall is large. It was confirmed that there existed the largest temperature decrease at the first barrier and the first insulation, which are among the insulation wall, especially in the top side of the insulation wall under IMO and USCG design condition. Also, as the NG temperature distribution is fixed, the outer temperature condition under the design condition has influence on the temperature variation at the insulation. By the 3-D numerical calculation about the cargo tank and the cofferdam during the cool-down period, the temperature variation in hulls and insulations is precisely predicted under IMO and USCG design condition. From the comparison between two conditions; IMO design condition shows more severe temperature gradient than USCG design condition, therefore, it provides the conservative estimation of the BOG.

Measurement Emission of Greenhouse Gases from Composting Process for Pig Slurry (돈 슬러리 발효증발 퇴비화 시스템의 온실가스 배출량 측정)

  • 박치호;윤태한;감재환
    • Journal of Animal Environmental Science
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    • v.7 no.2
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    • pp.111-118
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    • 2001
  • This study was performed for measuring the emission of greenhouse gases, $CH_4,\;N_2O$, from the composting process for pig slurry. For the experiment the benchscale pilot plant was designed by 1$m^3$ volume reactor with a closed type and operated; sawdust 142kg filled before input slurry, slurry about 10~20l inputed per day (total 380l), air supplied 5l/min for 24 hours, mixing time 10 min./day and 1 time a day. From the total experiment period(30days), the amount of VS degradation and emission $CH_4$, $N_2O$ were 10.9kg-VS and 1,582.4g-$CH_4$, 68.1g-$N_2O$ respectively. Based on VS inputed the emission of $CH_4$, $N_2O$ were 15.3(g-$CH_4$/kg-V $S_{input}$), 0.7(g-$N_2O$ /kg-V $S_{input}$), and based on VS degradated were 145.2(g-$CH_4$/kg-V $S_{removed}$), 6.2(g-$N_2O$ /kg-V $S_{removed}$).

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Effects of Mg content ratio on the structure and corrosion properties of Al-Mg films

  • Jeong, Jae-Hun;Yang, Ji-Hun;Song, Min-A;Kim, Seong-Hwan;Jeong, Jae-In
    • Proceedings of the Korean Vacuum Society Conference
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    • 2016.02a
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    • pp.165.1-165.1
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    • 2016
  • Zn의 수요는 매년 증가하지만 매장량의 한계로 대체용 물질계가 개발이 필요한 시점이다. Zn보다 상대적으로 풍부하고 동일 두께의 Zn 코팅층과 비교하여 우수한 내식성을 보이는 Al과 Mg의 코팅층을 제작하여 Al-Mg 코팅 강판의 특성 분석 및 평가를 실시하였다. Al-Mg 코팅층은 99.99%의 Al, 99.9%의 Mg target을 사용하여 스퍼터링을 이용하여 냉연강판 위에 코팅하였다. 증발물질과 기판과의 거리는 7cm 이며, 기판은 세척을 실시한 후 클리닝 챔버에 장착하고 ~10-5 Torr 까지 진공배기를 실시하였다. 클리닝 챔버가 기본 압력까지 배기되면 아르곤 가스를 주입하고 기판 홀더에 -800 V의 직류 전압을 인가하여 약 30분간 글로우 방전 청정을 실시하였다. 기판의 청정이 끝나면 아르곤 가스를 차단하고 코팅 챔버로 시편을 이송 후 코팅층 성분의 구성형태에 따라 Al과 Mg을 코팅하였다. Al-Mg 코팅층은 $3{\mu}m$의 두께를 기준으로 Mg wt.%의 비율을 5% ~ 90%까지 변화시키며 코팅하였다. 그리고 후속 공정으로 질소 분위기 $400^{\circ}C$에서 10분간 열처리를 하였다. Al-Mg 코팅층을 주사전자현미경으로 관찰한 결과, 표면에서는 Al-Mg 코팅층에 존재하는 Mg 함량이 높아질수록 grain의 크기가 증가하였고 단면에서는 열처리 전의 치밀한 구조에서 열처리 후에는 주상구조 혹은 grain 구조가 선명해지는 것을 볼 수 있었으며 글로우방전분광기로 Al과 Mg의 성분 비율변화를 확인할 수 있었다. 또한 Al-Mg가 코팅된 강판을 염수분무시험을 통해서 내부식 특성을 확인하였다. Al-Mg 코팅 강판의 염수분무시험 결과, Mg 함량이 낮은 Al-Mg 코팅층은 열처리 후 뚜렷한 내식성 향상을 보였으며 Mg 조성 변화에 따라 일정한 경향성을 보였다. 하지만 Mg 함량이 높은 Al-Mg 코팅층은 열처리 후 급격한 내식성 저하와 함께 시편간의 편자가 커지는 것을 확인 할 수 있었다. 최적의 내식성을 보이는 Mg의 조성을 확인하기 위해서는 향후 보다 변별력이 높은 평가가 결과가 필요하다고 판단되어진다.

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The Condensation Heat Transfer of R-22 and R-410A in an Inner Diameter Tube of 1.77 mm (내경 1.77 mm관내 R-22와 R-410A의 응축열전달)

  • Son, Chang-Hyo;Roh, Geon-Sang
    • Journal of the Korean Institute of Gas
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    • v.12 no.1
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    • pp.48-53
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    • 2008
  • The condensation heat transfer coefficients of R-22 and R-410A in a small diameter tube were investigated. The main components of the refrigerant loop consist of a receiver, a variable-speed pump, a mass flowmeter, an evaporator (preheater), and a condenser (test section). The test section consists of smooth, horizontal copper tube of 3.38 mm outer diameter and 1.77 mm inner diameter. The refrigerant mass fluxes varied from 450 to $1050\;kg/(m^2s)$ and the average inlet and outlet qualities were 0.05 and 0.95. The main results were summarized as follows : the condensation heat transfer coefficient also increases with increasing mass flux and quality. The condensation heat transfer coefficient of R-410A was slightly higher than that of R-22. Most of correlations proposed in the large diameter tube showed significant deviations with experimental data except for the ranges of low quality and low mass flux.

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Performance and Availability of Seawater Distiller with Heat Pipe Utilizing Low-Grade Waste Heat (저급 폐열 이용 히트파이프 해수담수기의 성능과 유용성)

  • Park, Chang-Dae;Chung, Kyung-Yul;Tanaka, Hiroshi
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.37 no.1
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    • pp.81-86
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    • 2013
  • Exhaust gas from a small portable electric generator is simply exhausted to the surroundings because the capacity and quality of the waste heat of this gas is generally not sufficient to recover and utilize. We have proposed a seawater distiller utilizing the thermal energy of waste gas from an electric generator. The distiller recovers heat from the waste gas by means of a heat pipe and uses it effectively through a multiple-effect diffusion-type structure. We constructed an experimental apparatus with a vertical single-effect still having a 4-stroke 50 cc generator engine and found that the experimental results for distillate productivity show good agreement with the theoretical predictions. The results show that the distiller can recover 52 W of waste heat from the gas at $171^{\circ}C$, and ~85% of the recovered heat can be utilized for distillation to produce 70 g/h of fresh water. This is equivalent to a productivity of 500 g/h in the case of a 10-effect still. Therefore, the proposed distiller should be useful in remote areas where electricity and water grids are inadequate.

Numerical and Experimental Study on the Coal Reaction in an Entrained Flow Gasifier (습식분류층 석탄가스화기 수치해석 및 실험적 연구)

  • Kim, Hey-Suk;Choi, Seung-Hee;Hwang, Min-Jung;Song, Woo-Young;Shin, Mi-Soo;Jang, Dong-Soon;Yun, Sang-June;Choi, Young-Chan;Lee, Gae-Goo
    • Journal of Korean Society of Environmental Engineers
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    • v.32 no.2
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    • pp.165-174
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    • 2010
  • The numerical modeling of a coal gasification reaction occurring in an entrained flow coal gasifier is presented in this study. The purposes of this study are to develop a reliable evaluation method of coal gasifier not only for the basic design but also further system operation optimization using a CFD(Computational Fluid Dynamics) method. The coal gasification reaction consists of a series of reaction processes such as water evaporation, coal devolatilization, heterogeneous char reactions, and coal-off gaseous reaction in two-phase, turbulent and radiation participating media. Both numerical and experimental studies are made for the 1.0 ton/day entrained flow coal gasifier installed in the Korea Institute of Energy Research (KIER). The comprehensive computer program in this study is made basically using commercial CFD program by implementing several subroutines necessary for gasification process, which include Eddy-Breakup model together with the harmonic mean approach for turbulent reaction. Further Lagrangian approach in particle trajectory is adopted with the consideration of turbulent effect caused by the non-linearity of drag force, etc. The program developed is successfully evaluated against experimental data such as profiles of temperature and gaseous species concentration together with the cold gas efficiency. Further intensive investigation has been made in terms of the size distribution of pulverized coal particle, the slurry concentration, and the design parameters of gasifier. These parameters considered in this study are compared and evaluated each other through the calculated syngas production rate and cold gas efficiency, appearing to directly affect gasification performance. Considering the complexity of entrained coal gasification, even if the results of this study looks physically reasonable and consistent in parametric study, more efforts of elaborating modeling together with the systematic evaluation against experimental data are necessary for the development of an reliable design tool using CFD method.

Dynamic LEED를 이용한 Ni/Pt(001)의 구조분석

  • 김상현;박종윤;민항기;변대현;서지근;김재성
    • Proceedings of the Korean Vacuum Society Conference
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    • 1999.07a
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    • pp.174-174
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    • 1999
  • Pt(001)의 깨끗한 표면은 재배열된 (5x20) 또는 (nxn) 구조를 갖는다. 이러한 재배열된 구조는 소?의 가스를 흡착에 대해서도 (1x1)구조로 다시 재배열되는 재배열인 쉽게 풀리는 준안정적 재배열 구조를 갖는 표면이다. Pt(100) 표면 위에 Ni과 같은 금속을 흡착시키는 경우도 동일하게 표면의 장력을 해소시켜 (1x1) 표면을 만든다. Pt와 Ni과 같은 덩어리 상태에서 Pt와 Ni가 질서있게 교차되어 배열되는 합금이 쉽게 이루어지는 물질들로 잘 알려져 있고, 이 합금은 Pt나 Ni와 동일한 규칙적인 fcc 구조를 갖는다. 따라서 Pt(100) 표면 위에 Ni를 흡착시키는 것은 Nm/Cu(100)과 같은 표면합금이나 Mn/Ag(1000에서 보이는 2층으로 된 표면 합금과 같은 표면 근방에 국한된 질서있는 표면 합금의 가능성이 있다. 또한 Ni/Pt(100)은 Ni과 Pt가 3대 1의 비로 조합될 때 나타나는 Ni3Pt의 층별구조인 표면에 Ni가 채워져 있고, 다음 층에 Ni와 Pt가 50%씩 질서 있게 섞여 있는 형태의 구조 즉 표면 밑 합금이 나타날 수 있는 가능성이 있는 물질계라는 점에서 관심을 갖게 한다. 본 연구는 LEED를 이용하여 Ni/Pt(100) 박막의 층별구조를 확인하고자 한다. PtNi 합금은 ATA(average t-matirx approximation)을 이용한 LEED 분석이 잘 적용되는 물질계로 알려져 있고, 본 연구는 ATA를 적용한 LEED I/V 분석을 통하여 Ni가 성장된 Pt(100) 표면의층별 농도비와 층별 구조를 구하고자 한다. 실험은 기본 압력이 3x10-11torr인 챔버에서 이루어졌으며, 증착시 압력은 5x10 torr이고, 증착은 열증발 방법을 이용하였다. Ni가 증착됨에 따라 (nxn) 재배열 표면에 기인한 extra spot들의 세기는 점차 감소하고 특정 증착량 이상에서부터 이 (nxn)의 spot들이 사라지고 깨끗한 (1x1) 패턴이 나타난다. 계속되는 증착량의 증가에 대해서도 이 (1x1) 형태는 유지되며, 표면의 질서에 따르는 c(2x20 패턴은 보이지 않았다. (1x1) LEED spot를 보임에도 불구하고 덩어리 절단 형태의 구조를 기반으로 한 LEED I/V 분석으로는 잘 맞출수 없었다. 이것은 Ni가 일정 이상 흡착된 경우 그 구조가 덩어리 절단 형태의 fcc(100) 구조와 벗어난 구조를 가지는 것으로 보인다.

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A Study on the Examination of Explosion Hazardous Area Applying Ventilation and Dilution (환기 및 희석을 적용한 폭발위험장소 검토에 관한 연구)

  • kim, Nam Suk;Lim, Jae Geun;Woo, In Sung
    • Journal of the Korean Institute of Gas
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    • v.22 no.4
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    • pp.27-31
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    • 2018
  • Classification of explosion hazard areas is very important in terms of cost and safety in the workplace handling flammable materials. This is because the radius of the hazardous area determines whether or not the explosion-proof equipment is installed in the electrical machinery and apparatus. From November 6, 2017, KS C IEC-60079-10-1: 2015 will be issued and applied as a new standard. It is important to understand and apply the difference between the existing standard and the new standard. Leakage coefficients and compression factors were added to the leakage calculation formula, and the formula of evaporation pool leakage, application of leakage ball size, and shape of explosion hazard area were applied. The range of the safety factor K has also been changed. Also, in the radius of the hazardous area, the existing standard applies the number of ventilation to the virtual volume, but the revised standard is calculated by using the leakage characteristic value. In this study, we investigated the differences from existing standards in terms of ventilation and dilution and examined the effect on the radius of the hazard area. Comparisons and analyzes were carried out by applying revised standards to workplaces where existing explosion hazard locations were selected. The results showed that even if the ventilation and dilution were successful, the risk radius was not substantially affected.