• 제목/요약/키워드: Methane hydrate

검색결과 120건 처리시간 0.028초

sI 천연 메탄하이드레이드의 존재 : 결정구조 변화의 분광학적 분석 (Preponderant Occurrence of sl natural methane hydrates: Spectroscopic analysis of crystalline structure transition)

  • 연순화;설지웅;이흔
    • 한국신재생에너지학회:학술대회논문집
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    • 한국신재생에너지학회 2006년도 춘계학술대회
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    • pp.387-390
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    • 2006
  • We report here that under strong attacksof external $CH_4$ guest molecules the sII and sH methane hydrates are structurally transformed to the crystalline me framework of sI, leading to favorable change of the lattice dimension of the host-guest networks. The High Power Decoupling $^{13}C$ NMR and Raman spectroscopies were used to identify structure transitions of the mixed $CH_4+C_2H_6$ hydrates (sIIl) and hydrocarbons (methylcyclohexane, isopentane) + $CH_4$ hydrates (sH). The resulting spectra indicate that most of the synthesized sII and sH hydrates were transformed to methane hydrate of sl under 110 bar and particularly the coexistence of sl with sII or sH appear according to the surrounding methane-rich gas conditions. The present findings might be expected to Provide rational evidences regarding the preponderant occurrence of naturally-occurring sI methane hydrates in marine sediments.

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가스하이드레이트 생성조건 최적화에 관한 실험적 연구 (Experimental Study on Optimal Generation of Methane Hydrate)

  • 윤석호;이정호;이공훈;박상진
    • 대한설비공학회:학술대회논문집
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    • 대한설비공학회 2009년도 하계학술발표대회 논문집
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    • pp.1317-1321
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    • 2009
  • Natural gas liquefaction plant and LNG carrier needs large capital investment. Therefore a lot of small or middle scale natural gas fields aren't developed due to poor profitability. If natural gas is made to gas hydrate instead of liquefaction, developing small-scale natural gas field can be profitable because building cost of gas hydrate plant and carrier are economical. Because the process of making gas hydrate consumes much energy, the gas hydrate formation process has to be optimized for energy consumption. In this study, gas hydrate formation process was investigated experimentally. Experimental apparatus consists of reactor, pressure regulator, chiller, and magnetic stirrer. 99.95% methane was used to make gas hydrate. Tests were conducted at variable pressure and temperature condition.

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메탄/천연가스 하이드레이트의 제조 및 특성 비교 분석 (A Comparative Analysis on characteristics and Manufacture of Methane/Natural Gas Hydrates)

  • 이영철;조병학;백영순
    • 한국가스학회지
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    • 제7권3호
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    • pp.32-43
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    • 2003
  • 이 연구는 단성분계(메탄)과 다성분계(천연가스) 하이드레이트의 상평형 조건을 관찰하고, 반응시간에 따른 하이드레이트 생성 거동을 관찰하여 비교 분석하였다. 단성분과 다성분계 하이드레이트의 차이점은 크게 유도지체시간과 안정 영역이다. 반응시 다성분계 하이드레이트는 가스의 성분들이 서로 다른 농도변화를 나타내었으며, 제조된 하이드레이트를 해리시켰을 때도 서로 다른 해리 속도에 의해 각 가스 성분들의 농도가 변화되었다. 압력이 6 MPa이고, 온도가 276.65 K이며, 교반속도가 600 rpm일때 다성분계 하이드레이트 제조시 메탄이외의 여러 가스 성분들에 의해 하이드레이트 핵 생성이 빠르게 진행되어 유도지체시간은 짧다. 그리고 단성분계 하이드레이트는 단일 성분으로 이루어져 있으므로 안정 영역이0.055 mole of $CH_4$/mole of water에서 보다 뚜렷하게 관찰되고, 다성분계 하이드레이트는 안정 영역이 0.04 mole of $CH_4/$mole of water에서 관찰된다.

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메탄 하이드레이트 탐사를 위한 3 차원 탄성파 탐사와 해저면 지구화학탐사의 융합 기술 (Fusion of 3D seismic exploration and seafloor geochemical survey for methane hydrate exploration)

  • 장구보 정웅;소림 임명;등정 철재
    • 지구물리와물리탐사
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    • 제10권1호
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    • pp.37-43
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    • 2007
  • MH21 연구 컨소시엄에서는 일본 난카이 트러프 동부의 메탄 하이드레이트 탐사를 위해 고분해능 3 차원 탄성파 탐사와 해저면 지구화학탐사를 수행해 왔다. 메탄 하이트레이트가 존재하는 천부지층을 영상화 하기 위해 수행된 고분해능 3 차원 탄성파탐사 결과, 천부 지층에 대한 훌륭한 지질 정보를 획득할 수 있었다. 이러한 정보들은 지질학적, 지구화학적 모델을 구축하는데 유용하며, 특히 메탄가스 또는 메탄을 포함하는 유체의 이동통로, 지구화학적 메탄 하이드레이트 지시자등을 포함하는 복잡한 해저면 지질구조를 이해하는데 유용하다. 수중잠수정을 이용해 확인된 메탄 유출 지점과 탄성파 단면의 비교 결과, 해저면 하부의 메탄가스층 및 메탄 하이드레이트 저류층과 해저면 메탄 하이드레이트 지시자 사이의 특정적인 관계가 확인되었다. 해저지형도와 해저면 반사파로부터 영상화된 해저면 반사파진폭 영상 역시 넓은 지역에 대한 이들 관계를 이해하는 유용하며, 이러한 자료에 기반한 새로운 지구화학적 해저면 탐사도 요구된다. 메탄 하이드레이트 저류층과 해저면 메탄 하이드레이트 지시자 사이의 관계는 고분해능 3 차원 탄성파탐사 자료의 해석을 통해 점점 더 분명해지고 있다. MH21 연구 컨소시엄은 향후 고분해능 3 차원 탄성파탐사로부터 구축된 지질학적, 지구화학적 모델에 기반하여 해저면 지구화학탐사를 수행할 것이다. 이 논문에서는 3 차원 탄성파 탐사와 해저면 지구화학탐사기술의 융합에 의한 일본에서의 메탄 하이트레이트 탐사에 대해 소개한다.

가스하이드레이트 구조 변형을 통한 메탄 저장에 관한 연구 (Study of Methane Storage through Structure Transition of Gas Hydrate)

  • 이주동;이만식;김영석
    • 한국신재생에너지학회:학술대회논문집
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    • 한국신재생에너지학회 2006년도 추계학술대회
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    • pp.54-57
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    • 2006
  • Structure H formation experiments were conducted in a semi-batch stirred vessel using methane as the small guest substance and neohexane(NH), tert-butylmethylether(TBME) and methylcyclohexane(MCH) as the large molecule guest substance (LMGS). The results indicate that the rates of gas uptake and induction times are generally dependent on the magnitude of the driving force. When tert-butyl methyl ether is used as the LMGS rapid hydrate formation, much smaller induct ion time and rapid decomposition can be achieved. Liquid-liquid equilibrium (LLE) data for the above LMGS with water have been measured under atmospheric pressure at 275.5, 283.15K, and 298.15K. It was found that TBME is the most water soluble followed by NM and MCH. The solubility of water in the non-aqueous liquid was found to increase in the following order: MCH

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Gas Hydrate Systems at Hydrate Ridge;Results from ODP Leg 204

  • Lee, Young-Joo;Kim, Ji-Hoon;Ryu, Byong-Jae
    • 한국신재생에너지학회:학술대회논문집
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    • 한국신재생에너지학회 2007년도 춘계학술대회
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    • pp.531-533
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    • 2007
  • We report and discuss molecular and isotopic properties of hydrate-bound gases from 55 samples and void gases from 494 samples collected during Ocean Drilling Program (ODP) Leg 204 at Hydrate Ridge offshore Oregon. Gas hydrates appear to crystallize in sediments from two end-member gas sources (deep allochthonous and in situ) as mixtures of different proportions. In an area of high gas flux at the Southern Summit of the ridge (Sites 1248-1250), shallow (0-40 meters below the seafloor (mbsf)) gas hydrates are composed of mainly allochthonous mixed microbial and thermogenic methane and a small portion of thermogenic C2+ gases, which migrated vertically and laterally from as deep as 2-2.5 km depths. In contrast, deep (50-105 mbsf) gas hydrates at the Southern Summit (Sites 1248 and 1250) and on the flanks of the ridge (Sites 1244-1247) crystallize mainly from microbial methane and ethane generated dominantly in situ. A small contribution of allochthonous gas may also be present at sites where geologic and tectonic settings favor vertical gas migration from greater depth (e.g., Site 1244).

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감압법을 이용한 메탄 하이드레이트 생산에 대한 연구 (Study on methane hydrate production using depressurization method)

  • 박성식;김남진
    • 한국태양에너지학회 논문집
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    • 제30권1호
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    • pp.34-41
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    • 2010
  • Gas hydrates are solid solutions when water molecules are linked through hydrogen bonding and create host lattice cavities that can enclose many kinds of guest(gas) molecules. There are plenty of methane(gas) hydrate in the earth and distributed widely at offshore and permafrost. Several schemes, to produce methane hydrates, have been studied. In this study, depressurization method has been utilized for the numerical model due to it's simplicity and effectiveness. IMPES method has been used for numerical analysis to get the saturation and velocity profile of each phase and pressure profile, velocity of dissociation front progress and the quantity of produced gas. The values calculated for the sample length of 10m, show that methane hydrates has been dissolved completely in approximately 223 minutes and the velocity of dissociation front progress is 3.95㎝ per minute. The volume ratio of the produced gas in the porous media is found to be about 50%. Analysing the saturation profile and the velocity profile from the numerical results, the permeability of each phase in porous media is considered to be the most important factor in the two phase flow propagation. Consequently, permeability strongly influences the productivity of gas in porous media for methane hydrates.

실리카겔 공극에서의 이산화탄소 및 메탄 하이드레이트 상평형 측정 및 열역학적 예측 (Phase Equilibrium of the Carbon Dioxide and Methane Hydrate in Silica Gel Pores and Thermodynamic Prediction)

  • 강성필
    • 한국신재생에너지학회:학술대회논문집
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    • 한국신재생에너지학회 2007년도 춘계학술대회
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    • pp.477-480
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    • 2007
  • Hydrate phase equilibrium for the binary CO2+water and CH4+water mixtures in silica gel pore of nominal 6, 30, and 100 nm were measured and compared with the cacluated results based on van der Waals and Platteeuw model. At a specific temperature three-phase hydrate-water-vapor (HLV) equilibrium curves for pore hydrates were shifted to the higher-pressure condition depending on pore sizes when compared with those of bulk hydrates. Notably, hydrate phase equilibria for the case of 100 nominal urn pore size were nealy identical with those of bulk hydrates. The activities of water in porous silica gels were modified to account for capillary effect, and the calculation results were generally in good agreement with the experimental data.

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Formation and Dissociation Processes of Gas Hydrate Composed of Methane and Carbon Dioxide below Freezing

  • Hachikubo, Akihiro;Yamada, Koutarou;Miura, Taku;Hyakutake, Kinji;Abe, Kiyoshi;Shoji, Hitoshi
    • Ocean and Polar Research
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    • 제26권3호
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    • pp.515-521
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    • 2004
  • The processes of formation and dissociation of gas hydrates were investigated by monitoring pressure and temperature variations in a pressure cell in order to understand the kinetic behavior of gas hydrate and the controlling factors fur the phase transition of gas hydrate below freezing. Gas hydrates were made kom guest gases ($CH_4,\;CO_2$, and their mixed-gas) and fine ice powder. We found that formation and dissociation speeds of gas hydrates were not controlled by temperature and pressure conditions alone. The results of this study suggested that pressure levels at the formation of mixed-gas hydrate determine the transient equilibrium pressure itself.

실리카겔 공극에서의 이산화탄소 및 메탄 하이드레이트 상평형 측정 및 열역학적 예측 (Phase Equilibrium of the Carbon Dioxide and Methane Hydrate in Silica Gel Pores and Thermodynamic Prediction)

  • 강성필
    • 신재생에너지
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    • 제3권2호
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    • pp.47-52
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    • 2007
  • Hydrate phase equilibrium for the binary $CO_{2}$+water and $CH_{4}$+water mixtures in silica gel pore of nominal 6, 30, and 100 nm were measured and compared with the cacluated results based on van der Waals and Platteeuw model. At a specific temperature three-phase hydrate-water-vapor (HLV) equilibrium curves for pore hydrates were shifted to the higher-pressure condition depending on pore sizes when compared with those of bulk hydrates. Notably, hydrate phase equilibria for the case of 100 nominal nm pore size were nearly identical with those of bulk hydrates. The activities of water in porous silica gels were modified to account for capillary effect, and the calculation results were generally in good agreement with the experimental data.

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