• 한국가스학회지
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• 제15권3호
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• pp.1-5
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• 2011

수소액화 공정은 수소 예냉 에너지, 액화에너지 그리고 Ortho/Para 변환열 제거 등 다량의 에너지가 요구되어 진다. 본 논문은 기존의 수소액화 공정에 LNG냉열을 이용하여 에너지절약 효과를 얻고자 기본설계 및 열해석을 수행하였다. 액화 소요에너지에 LNG냉열을 적용하면 수소액화공정의 에너지절약효과와 함께, LNG기지의 해수에 버려지는 LNG냉열을 회수, 이용하는 일석이조의 에너지절약기술이 된다. 열해석에 의한 설계를 수행한 결과 현재의 액체질소 예냉식 수소액화 플랜트의 소요에너지에 비하여 LNG냉열을 이용할 경우 소요동력량은 75%가 절감되었다. 이는 예냉을 액체질소 대신에 냉열을 사용하기 때문이다. 또한 LNG냉열량은 수소액화량 1T/D기준할 때 15T/D 유량이 요구되었다.

• Bulletin of the Korean Chemical Society
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• 제23권2호
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• pp.337-345
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• 2002

The equilibrium structures for the ground and transition states of $C_7H_7^+$ isomers have been investigated using sophisticated ab initio quantum mechanical techniques with various basis sets. The structures of tropyrium and benzyl cations have been fully optimized at the DZP CCSD(T) levels of theory. And the structures of o-, m-and p-tolyl cations are optimized fully up to the DZ CCSD(T) levels of theory. The geometries for the transition states between three isomers of tolyl cations have been optimized up to DZP CISD level of theory. The SCF harmonic vibrational frequencies for tropylium, benzyl, and three isomers of tolyl cations are all real numbers, which confirm the potential minima and each unique imaginary vibrational frequencies for TS1 and TS2 confirm the true transition states. The relative energy of the benzyl cation with respect to the tropyrium cation is predicted to be 28.5 kJ/mol and is in good agreement with the previous theoretical predictions. The 0 K heats of formation, ${\Delta}H^{\circ}_{f0}$, have been predicted to be 890, 1095, 1101, and 1110 kJ/mol for tropylium, ortho-, meta-, and para-tolyl cations by taking the experimental value of 919 kJ/mol for the benzyl cation as the base level. The relative stability between tolyl cations is in the order of ortho

• 한국수소및신에너지학회논문집
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• 제9권2호
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• pp.53-64
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• 1998

Thermal analysis on a Linde-Hampson hydrogen liquefaction system using cryogenic refrigerators as precooling has been carried out. Three commercially available models of cryogenic refrigerators, such as CTI l020CP, CVI CGR009 and CVI CGR011, are considered in the performance analysis. The effect of ortho-para conversion process during hydrogen liquefaction is also studied in detail. The results obtained indicate that the optimal hydrogen mass flow rate and the optimal compressed pressure exist for the maximum hydrogen liquefaction rate. The optimal compressed pressure is increased in the range of 80 - 120 bar with an increase in the hydrogen mass flow rate. It is also found that better performance could be obtained with a cryogenic refrigerator, which produces high cooling capacity at precooling temperature in the range of 80 - 100 K.