• Title/Summary/Keyword: 이산화탄소 액화

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A Study on the Power Generation Using Supercritical Carbon Dioxide (초임계 이산화탄소를 활용한 발전에 대한 연구)

  • NOH, SANGGYUN
    • Journal of Hydrogen and New Energy
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    • v.30 no.4
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    • pp.297-302
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    • 2019
  • In this paper, the power generation efficiency increase has been studied for a Rankine cycle using both supercritical carbon dioxide as a working fluid and LNG as a coolant with PRO/II with PROVISION release 10.0 from Aveva company. Peng-Robinson equation of the state model with Twu's alpha function was selected for the modeling of the power generation cycle using LNG cold heat. Power generation efficiency was increased from 24.82% to 57.76% when using LNG as a coolant for supercritical carbon dioxide power generation cycle.

Comparative Research on the Carbon Dioxide Liquefaction Using Several Refrigerants (몇 가지 냉매를 사용한 이산화탄소 액화에 대한 비교 연구)

  • ILSU PARK;PHILSUNG HWANG;KICHEOL JUNG;JUNESHU ANH;JUNGHO CHO
    • Journal of Hydrogen and New Energy
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    • v.34 no.2
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    • pp.226-233
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    • 2023
  • In this study, we compared the performance of several refrigeration cycles using different refrigerants and utilizing the cold heat of liquefied natural gas (LNG) for the liquefaction of carbon dioxide. The final conditions for the liquefied CO2 were set to -20℃ and 20 bar. The refrigerants used included R404a, ammonia, propane, and propylene using a vapor recompression refrigeration cycle. For the refrigeration cycle, the CO2 at room temperature and pressure was compressed in a two-stage compression process with an intermediate cooling stage using a refrigeration unit. To compare with the liquefaction process using refrigeration, we compressed the CO2 to 8 bar in a single compression stage and cooled it to around -50℃ using the cold heat of the LNG before liquefying it. Results showed that using ammonia as the refrigerant required the least amount of compressor power for the liquefaction process, and the heat transfer area of the evaporator was the smallest when using propylene as the refrigerant. Using the cold heat of LNG instead of refrigeration using R404a resulted in approximately 69% less energy consumption.

Effect of Fuels on $CO_2$ Emission in CVS-75 Mode (CVS-75모드에서 사용연료에 따른 자동차의 이산화탄소 배출특성)

  • Kim, Yong-Tae;Lee, Ho-Kil;Kang, Jung-Ho;Chung, Jae-Woo;Chung, Yon-Jong
    • Transactions of the Korean Society of Automotive Engineers
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    • v.17 no.4
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    • pp.72-78
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    • 2009
  • The regulation for $CO_2$ emissions from vehicles have become much more stringent in recent years. These more stringent regulations request vehicle manufacturers to develop alternative fuels to reduce exhaust emissions. In this paper, $CO_2$ emission of gasoline, diesel and LPG vehicles in the CVS-75mode is analyzed. The experimental results indicated that the cold starting acceleration period of $CO_2$ emission was much longer compared to the hot start acceleration period. For example, gasoline vehicle and LPG fuel vehicle had 21% higher $CO_2$ emission and diesel vehicle had 34% higher $CO_2$ emission.

Spray Characteristics of a Coal Slurry with Liquid Carbon Dioxide (고압 저등급탄-이산화탄소 슬러리 분무특성에 관한 연구)

  • KIM, CHANGYEON;KIM, HAKDUCK;SONG, JUHUN
    • Journal of Hydrogen and New Energy
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    • v.26 no.4
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    • pp.357-362
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    • 2015
  • There is potential method to utilize the liquid carbon dioxide ($LCO_2$) in coal gasification plants. The $LCO_2$ could be used to effectively transport coal particles instead of conventional carrier such as liquid water ($H_2O$) particularly in wet-fed gasifier. However, there is a lack of fundamental study on the atomization behavior of $LCO_2$ coal slurry under high pressure condition. In this study, the flashing spray characteristics of a coal mixture with $LCO_2$ was examined during a throttling process by using a flow visualization system. The spray of coal water slurry which is in the Rayleigh-type break up mode was significantly different. This difference indicates that the coal water slurry did not effectively transport the coal, as compared to $LCO_2$ coal slurry.

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

  • SANGGYUN NOH
    • Journal of Hydrogen and New Energy
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    • v.34 no.5
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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.

Development of a Methanol Absorption System for the Removal of $H_2S$, COS, $CO_2$ in Syngas from Biomass Gasifier (바이오매스 가스화 내의 $H_2S$, COS, $CO_2$ 복합 제거를 위한 메탄올 흡수탑 개발)

  • Eom, Won Hyun;Kim, Jae Ho;Lee, See Hoon
    • Applied Chemistry for Engineering
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    • v.23 no.1
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    • pp.23-27
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    • 2012
  • To make synthetic liquid fuel from biomass such as wood pellet, energy crop and so on, a biomass to liquid (BTL) process by using a biomass gasifier with Fisher-Tropsch (FT) reaction was developed. However $H_2S$, COS and $CO_2$ in syngas from biomass gasifiers resulted in a decrease of the conversion efficiency and the deactivation of the catalyst. To remove acid gases in syngas, a lab-scale methanol absorption tower was developed and the removal characteristics of acid gases were investigated. The methanol absorption tower efficiently removed $H_2S$ and COS with a removal of $CO_2$, so it could be useful process for the BTL process.

Characteristics of $SF_6$ Gas Recycling Processes ($SF_6$가스 회수 공정들의 특성 연구)

  • Cho, Hoon;Woo, Dae-Sik;Choi, Yu-Mi;Han, Myung-Wan
    • Clean Technology
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    • v.17 no.4
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    • pp.329-335
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    • 2011
  • $SF_6$ gas is well known as a global warming gas. Global warming potential of $SF_6$ gas is 22,000 times higher than that of $CO_2$. Recycling of $SF_6$ gas is an essential technology for the sake of the environment and the economy. The recovery processes of $SF_6$ gas studied in this work were liquefaction, distillation, and crystallization processes because these processes were thought to be easily carried to the fields for recycling waste $SF_6$ gas. The processes were simulated and optimized using Aspen plus. The optimization problems were formulated to minimize energy consumption with satisfying product specification and desired recovery. The performance of the processes was compared based on the optimization results. Effects of major process variables on the recovery performance were investigated and optimal operation guide for changing product specification and product recovery was provided.

Analysis of Nano-particle and Emissions Characteristics for FTP75 Mode in LPLi Vehicle (FTP75 모드에 의한 LPG액상분사자동차의 배출가스 및 나노입자배출특성)

  • Lee, Ho-Kil;Kim, Yong-Tae
    • Journal of Hydrogen and New Energy
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    • v.20 no.2
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    • pp.161-167
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    • 2009
  • The regulation of the $CO_2$ emit from vehicles have become much more stringent in recent years. This stringent regulation is more request vehicle manufacturers to develop the alternative fuel vehicles for reducing exhaust emissions. LPG fuel is more clean energy compares with gasoline and diesel fuel. Especially, $CO_2$ emission of LPG Vehicle is less than gasoline vehicle and almost equal to diesel vehicle. For this reason, recently korean government is extending LPG fuel for hybrid car and light duty vehicle. In domestic, Propane is mixing $15{\sim}30%$ to butane for improvement of cold start at winter season. Therefore, In this paper was investigated that the characteristics of emissions according to propane mixing rate with 0, 10, 20, 30% were compared and analyzed by the vehicle test using LPG vehicle according to the FTP75 mode. It was also investigated the characteristics of nano-particle emit with propane mixing rate.

Fuel Efficiency and $CO_2$ Emission Characteristics on Driving Cycle Mode and Ignition Advance Condition Change of CNG/LPLI Bi-Fuel Vehicle (CNG/LPLI Bi-Fuel 자동차에서 주행시험 모드와 점화진각에 따른 연비 및 $CO_2$ 배출가스 특성)

  • Cho, Seungwan;Kim, Seonghoon;Kwon, Seokjoo;Park, Sungwook;Jeon, Chunghwan;Seo, Youngho
    • Journal of ILASS-Korea
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    • v.19 no.1
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    • pp.33-39
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    • 2014
  • Due to persist of high oil prices, LPG price stabilization and CNG modification project will be conducted. Present study describes the fuel efficiency and $CO_2$ emission characteristics on driving cycle mode and ignition advance condition change of CNG/LPG Bi-Fuel vehicle. In case of LPG Base and CNG Base condition, considerable $CO_2$ emissions are generated within range of high acceleration on FTP-75 and HWFET driving mode. However previous phenomena does not appear in CNG fuel $10^{\circ}CA$ and $15^{\circ}CA$ spark advance condition. As a result of analyzing the experimental data CNG $S/A10^{\circ}CA$, CNG $S/A15^{\circ}CA$, CNG Base, and LPG Base sequentially measured high fuel economy and low $CO_2$ emission characteristics.

Separation of Electronic Grade Highly Pure Carbon Dioxide Using Combined Process of Membrane, LNG Cold Heat Assisted Cryogenic Distillation (분리막 공정과 LNG 냉열 및 심냉 증류를 이용한 전자급 고순도 이산화탄소의 분리)

  • YOUNGSOO KO;KYUNGRYONG JANG;JUNGHOON KIM;YOUNGJOO JO;JUNGHO CHO
    • Journal of Hydrogen and New Energy
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    • v.35 no.1
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    • pp.90-96
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    • 2024
  • In this paper, a new technology to obtain electronic grade, highly pure carbon dioxide by using membrane and liquefied natural gas (LNG) cold heat assisted cryogenic distillation has been proposed. PRO/II with PROVISION release 2023.1 from AVEVA company was used, and Peng-Robinson equation of the state model with Twu's alpha function to predict pure component vapor pressure versus temperature more accurately was selected for the modeling of the membrane and cryogenic distillation process. Advantage of using membrane separation instead of selecting absorber-stripper configuration for the concentration of carbon dioxide was the reduction of carbon dioxide capture cost.