• Title/Summary/Keyword: 액화

검색결과 975건 처리시간 0.184초

Economic Evaluations of Direct/indirect Coal Liquefaction Processes (직.간접석탄액화공정의 경제성 평가)

  • Park, Joo-Won;Bae, Jong-Soo;Kweon, Yeong-Jin;Kim, Hak-Joo;Jung, Heon;Han, Choon
    • 한국신재생에너지학회:학술대회논문집
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    • 한국신재생에너지학회 2009년도 춘계학술대회 논문집
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    • pp.857-860
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    • 2009
  • This report examines the economic feasibility of a commercial 50,000 barrel per day direct/indirect coal liquefaction (DCL/ICL) facility to produce commercial-grade diesel and naphtha liquids from medium-sulfur bituminous coal. The scope of the study includes capital and operating cost estimates, sensitivity analysis and a comparative financial analysis. Based on plant capacity of 50,000BPD, employing Illinois #6 bituminous coal as feed coal the total capital cost appeared $3,994,858,000(DCL) and $4,942,976,000(ICL). Also, the internal rate of return of DCL/ICL appeared 13.27% and 12.68% on the base condition. In this case, coal price and sale price of products were the most influence factors. And ICL's payback period(6.8 years) was longer than DCL's (6.6 years). According to sensitivity analyses, the important factors on DCL/ICL processes were product sale price, feed coal price and the capital cost in order.

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Process Design and Cost Estimation of Carbon Dioxide Compression and Liquefaction for Transportation (이산화탄소 수송을 위한 압축 및 액화 공정 설계 및 비용 평가)

  • Yang, Seeyub;Lee, Ung;Lim, Youngsub;Jeong, Yeong Su;Kim, Jeongnam;Lee, Chiseob;Han, Chonghun
    • Korean Chemical Engineering Research
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    • 제50권6호
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    • pp.988-993
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    • 2012
  • Energy and cost analysis of the preprocessing for carbon capture and storage transportation such as supercritical compression and liquefaction is done using chemical simulation model. Direct compression to supercritical phase (process 1-1), liquefaction and pumping (process 1-2), carbon dioxide compression and expansion as a refrigerant itself (process 2), usage of other refrigerant with compression and expansion (process 3-1), with absorption chiller (process 3-2), cascade refrigeration (process 3-2) have been simulated and evaluated. The specific cost is about 4 to 7 $/ton.

Performance Analysis of the Experimental Liquid Rocket Engine using Liquefied Natural Gas as a Fuel (액화천연가스를 연료로 하는 시험용 액체로켓엔진의 성능해석)

  • 한풍규;이성웅;김경호;윤영빈
    • Proceedings of the Korean Society of Propulsion Engineers Conference
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    • 한국추진공학회 2004년도 제22회 춘계학술대회논문집
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    • pp.198-204
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    • 2004
  • Using liquefied natural gas as a fuel, water, natural gas and liquefied natural gas-cooled firing tests were conducted. With the viewpoint of characteristic velocity, and specific impulse, the effect of OF mixture ratio and fuel inlet temperature into a combustion chamber were analyzed. OF mixture ratio and fuel inlet temperature into a combustion chamber have great influence on the performance. Characteristic velocity and theoretical specific impulse attain the maximum value at 0.72~0.75 and 0.75 of OF mixture ratio, respectively. Engine performance has a tendency to increase, proportional to fuel inlet temperature into a combustion chamber affected by the regenerative cooling.

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Advanced Dual Refrigerant Expansion Cycle for LNG Liquefaction (천연가스 액화용 이중 냉매 팽창 사이클)

  • Kim, Minki;Kim, Mungyu;Lee, Kihwan;Kim, Hyobin;Lee, Donghun;Min, Joonho;Kim, Jinmo
    • Plant Journal
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    • 제15권2호
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    • pp.46-55
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    • 2019
  • This paper presents a LNG Liquefaction cycle configuration using two stages of methane expansion (i.e. spliting into two stages as warm & cold to generate an additional inflection point within a cold composite curve) and a single stage of nitrogen expansion to improve the efficiency of the conventional Methane & Nitrogen Expansion Cycle. In comparison with Double Nitrogen Expansion Cycel and Methane & Nitrogen Expansion Cycle, the cycle efficiency has increased approximately from 13.92 and 13.13 to 12.08 kW/ton/day (8~15% efficiency increase). A Life Cycle Cost (LCC) analysis based on Net Present Value (NPV) also show an improvement in therms of project NPV, against a minor increment of a CAPEX.

Development of a Volatile organic Compounds(VoCs) Liquefier on Integrated Management System based on ICT (ICT 기반의 휘발성 유기 화합물(VoC) 액화기 통합관리시스템 개발)

  • Kim, Gwan-Hyung
    • Journal of the Korea Institute of Information and Communication Engineering
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    • 제19권6호
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    • pp.1301-1306
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    • 2015
  • This paper is to automate the intelligent and equipment to recycle the volatile organic compounds in various a gas stations and a laundry, in real life. In addition, based the ZigBee module and TCP/IP communications on ICT technologies, it's propose an integrated management system to monitor and manage an liquid at a remote location.Furthermore, it's propose a service model that can be freely managed from a remote location based on the app on android. In this paper, we present a communication protocol of the bridge modules and a liquefier of intelligent control system based ZigBee and MCU(Micro Controller Unit). Through the development of smart app based android mobile services in an integrated management system, it's represent for liquefier to a DB server for remote management(MS SQL 2012) and a web server (OS: Windows 2008).

The implementation of liquefaction equipment monitoring system based on Android (안드로이드 기반의 유증기 액화장치 모니터링 시스템 구현)

  • Park, Man-Kyu;Tack, Han-Ho;Kim, Gwan-Hyung
    • Journal of the Korea Institute of Information and Communication Engineering
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    • 제20권3호
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    • pp.583-589
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    • 2016
  • Volatile organic compounds(VOCs) are regarded as a harmful cause substance not only causing air pollutions but also causing global warming phenomenon. For this reason, VOCs are managed politically to reduce emissions by each country. In particular, the vapor from the gas station contains VOCs which is harmful to the human body such as carcinogens benzene and pollute the atmosphere, the Ministry of Environment defined every gas station must install vapor recovery equipment to recover volatile organic compounds. Recently, there are many accidents caused by existing vapor treatment methods, the liquefaction recovery technology is getting the spotlight to cool the vapor at the field. However, because the liquefaction recovery technology have risks of fire or explosion in accordance with temperature, the real time monitoring is critical factor. In this paper, we implement an Android-based monitoring application for liquified vapor recovery device which attached sensor module for temperature and power to monitoring real time information.

Estimation of explosion risk potential in fuel gas supply systems for LNG fuelled ships (액화 천연 가스 연료 선박의 연료 공급 장치 폭발 잠재 위험 분석)

  • Lee, Sangick
    • Journal of Advanced Marine Engineering and Technology
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    • 제39권9호
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    • pp.918-922
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    • 2015
  • As international environmental regulations for pollutant and greenhouse gas emissions discharged from ships are being reinforced, it is drawing attention to use LNG as ship fuel. This paper compares the explosion risk potential in the LNG fuel gas supply systems of two types used in marine LNG fuelled vessels. By selecting 8500 TEU class container ships as target, LNG storage tank was designed and pressure conditions were assumed for the use of each fuel supply type. The leak hole sizes were divided into three categories, and the leak frequencies for each category were estimated. The sizes of the representative leak holes and release rates were estimated. The release rate and the leak frequency showed an inverse relationship. The pump type fuel gas supply system showed high leak frequency, and the pressure type fuel gas supply system showed high release rate. Computational fluid dynamics simulation was applied to perform a comparative analysis of the explosion risk potential of each fuel supply system.

Heat Transfer Characteristics of Plate-fin Heat Exchanger Using LNG FPSO Liquefaction Process (LNG FPSO 액화공정에 적용되는 플레이트 핀 열교환기의 열전달 특성)

  • Yoo, Sun-Il;Kim, Hyun-Woo;Jung, Young-Kwon;Yoon, Jung-In;Park, Seung-Ha;Kim, Chang-Su
    • Journal of Advanced Marine Engineering and Technology
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    • 제34권6호
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    • pp.798-805
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    • 2010
  • There are no domestic researches of plate fin heat exchanger in the field of cryogenic such as LNG FPSO liquefaction plant. In this study, condensing heat transfer characteristics of nitrogen according to three kinds of fin type in the plate fin heat exchanger were analyzed through simulation and experiment to secure independent technologies. In the simulation, nitrogen was condensed at 69bar and $-140^{\circ}C$ in serrated and wavy fin of plate-fin heat exchanger. The serrated fin shows the highest value of local heat transfer coefficient, followed by wavy and plain fin. The experimental results were shown errors less than 12% comparing with the simulation results.

A Probabilistic Analysis of Liquefaction Potential and Pore Water Pressure Build up due to Earthquake (지진하중에 의한 액화의 가능성과 간극수압의 발생에 관한 확률론적 연구)

  • Kim, Young-Su;Lee, Song;Cho, Woo-Chul
    • Geotechnical Engineering
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    • 제8권2호
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    • pp.31-44
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    • 1992
  • The probabilistic and statistical model is used to estimate the probability of liquefaction potential and pore water pressure build up due to earthquake in fully saturated sand deposit for each case of being structure(anisotropic) or not(isotropic). To execute this paper, dynamic shear strength parameters to show the relationship between shear strength and cyclic loading under isotropic or anisotropic condition in saturated sand deposit are presented. Using these parameters, the program which Predicts Pore water Pressure build up due to earthquake is developed. Using the 3-dimensional Random Field Model considering uncertainty of resistance and strength parameter, the program which computes the probability of liquefaction potential is developed. The developed program is applied to a case study, and then the result shows that the probability of liquefaction in isotropic condition is higher than in anisotropic condition. The ratio of pore water pressure tends to decrease as Kc increases.

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Starch Liquefaction and Residence Time Distribution in Twin-Screw Extrusion of ${\alpha}$-Starch (호화전분의 쌍축형 압출성형에서 전분액화 및 체류시간 분포)

  • Kim, Sung-Uk;Lee, Seung-Ju
    • Korean Journal of Food Science and Technology
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    • 제41권4호
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    • pp.369-373
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    • 2009
  • ${\alpha}$-Waxy corn starch was used as a feed for twin-screw extrusion in order to enhance starch liquefaction with added thermostable ${\alpha}$-amylase (derived from Bacillus licheniformis). The residence time distribution and starch liquefaction were investigated. The starch liquefaction was analyzed in terms of reducing sugar contents, molecular size from gel permeation chromatography (GPC), and microstructure from scanning electron microscopy (SEM). The use of ${\alpha}$-starch contributed to the production of more reducing sugar than the use of raw starch use alone. From GPC, the effect of ${\alpha}$- starch on the molecular size reduction was shown to be small. From SEM, irregular and damaged surface were observed on the extrudate from ${\alpha}$-starch, as compared to those from raw starch. The spread of residence time distribution curves was greater with feed of ${\alpha}$-starch than raw starch, indicating that ${\alpha}$-starch was hard to flow forward during extrusion. This could be improved by increasing the feed moisture content and barrel temperature of extruder.