• 한국초전도ㆍ저온공학회논문지
• /
• 제22권4호
• /
• pp.45-50
• /
• 2020

In this research, the variation of round-trip efficiency in a liquid air energy storage system (LAES) is calculated and an optimal configuration is found. The multiple stages of cold energy storage are simulated with several materials that process latent heat at different temperature ranges. The effectiveness in the charging and discharging processes of LAES is newly defined, and its relationship with the round-trip efficiency is examined. According to defined correlation, the effectiveness of the discharging process significantly affects the overall system performance. The round-trip efficiency is calculated for the combined cold energy storage materials of aqueous dimethyl sulfoxide (DMSO) solution, ethanol, and pentane theoretically. The performance of LAES varies depending on the freezing point of the cold storage materials. In particular, when the LAES uses several cold storage materials, those materials whose freezing points are close to room temperature and liquid air temperature should be included in the cold storage materials. In this paper, it is assumed that only latent heat is used for cold energy storage, but for more realistic analyzes, the additional consideration of the transient thermal situation to utilize sensible heat is required. In the case of such a dynamic system, since there is certainly more increased heat capacity of the entire storage system, the volume of the cold energy storage system will be greatly reduced.

• 한국가스학회지
• /
• 제24권4호
• /
• pp.56-61
• /
• 2020

수소의 액화에는 예냉 에너지, 상변화 에너지, 수소 변환열 제거 등 다량의 에너지가 요구되어진다. 본 논문의 목적은 예냉공정에 필요한 에너지로 LNG냉열로 액체질소를 제조하여 사용하는 LNG냉열 간접 이용 방식과, Cold box의 단열에 냉공기를 이용하는 새로운 에너지절약 공정을 제안하여 수소액화 수율을 향상시키고자 하였다. 분석 결과를 보면, LNG냉열 간접이용 방식은 에너지 절약과 함께 액체수소 플랜트의 안전성을 제공하는 장점을 갖는다. 새로운 Cold box 단열 방식은 외벽 철판 3mm/우레탄폼 20cm/공기 5cm/우레탄폼 20cm/설비의 구조일 때 현재 펄라이트 단열에 비교하여 열유입량이 약 35%~50%가 감소하게 된다. 또한 냉공기 보다 온도가 높은 설비는 냉각의 효과를 얻게 된다. 수소액화 플랜트의 공정에 본 결과를 적용한다면 액체 수율이 50% 내외로 크게 향상되는 효과를 제공하게 된다.

• 한국수소및신에너지학회논문집
• /
• 제30권3호
• /
• pp.276-281
• /
• 2019

The process of separating oxygen and nitrogen from the air is mainly performed by electric liquefaction, which consumes a lot of electricity, resulting in higher operating costs. On the other hand, when used for cold energy of LNG, electric power can be reduced compared to the electric Linde cycle. Currently, LNG cold energy is used in the cold refrigeration warehouse, separation of air-liquefaction, and LNG cold energy generation in Japan. In this study, the system using LNG cold energy and the Linde cycle process system were simulated by PRO/II simulators, respectively, to cool the elevated air temperature from the compressor to about $-183^{\circ}C$ in the air liquefaction separation process. The required amount of electricity was compared with the latent heat utilization fraction of LNG, the LNG supply pressure, and the LNG cold energy usage. At the air flow rate of $17,600m^3/h$, the power source unit of the Linde cycle system was $0.77kWh/m^3$, compared with $0.3kWh/m^3$.

• 한국가스학회지
• /
• 제14권6호
• /
• pp.27-30
• /
• 2010

본 논문은 LNG 냉열에너지를 이용한 지역집단 냉방에너지 시스템을 공급하기 위한 시스템 공정설계에 관한 연구이다. 새로이 개발한 LNG 냉방시스템은 여러 개의 열교환기, LNG 저장탱크, 열매체 저장탱크, 여러 개의 냉열에너지 저장탱크, 가스냉방기, 압축기, 정압기, 저온 및 고온에너지 공급배관 등으로 구성되도록 설계하였다. 또한, 가스냉방기는 여름철에 도시가스 소모량에 의해 충분하지 못한 LNG 냉열에너지를 안정적으로 공급하기 위해 설치되었다. 냉방에너지 공급시스템은 공기라는 열매체와 200kcal/kg의 냉열에너지를 가진 LNG 사이의 열교환 작용에 의해 냉방에너지를 공급하는 효율성과 안전성을 함께 갖추고 있다. 또한, LNG 냉열에너지를 이용한 지역집단 냉방에너지 공급시스템은 공기중으로 CO2나 프레온 가스를 방출하기 않는다는 장점을 간고 있다.

• 한국수소및신에너지학회논문집
• /
• 제28권4호
• /
• pp.401-406
• /
• 2017

When Liquified Natural Gas (LNG) is vaporized into NG for industrial and household usage, tremendous cold energy was transferred from LNG to seawater during phase-changing process. This heat exchanger loop is not only a waste of huge cold energy, but will cause thermal pollution to the coastal fishery area also when cold water was re-injected into the sea. In this study, an innovation design has been performed to reclaim the cold energy for -35 to $62^{\circ}C$ refrigerated warehouse. Conventionally, this was done by installing mechanical refrigeration systems, necessitating tremendous electrical power to drive temperature. A closed loop LNG heat exchangers in series was designed to replace the mechanical or vapor-compression refrigeration cycle by process simulator. The process simulation software of PRO II with provision has been used to simulate this process for various conditions, what to effect on cold energy and used energy for re-liquefaction and evaporation process. In addition, through analysis the effect of the change of LNG supply pressure on sensible and latent heat, optimum operational conditions was suggested for LNG cold energy warehouse.

• 한국원자력학회:학술대회논문집
• /
• 한국원자력학회 2005년도 춘계학술발표회
• /
• pp.9-10
• /
• 2005

• 한국원자력학회:학술대회논문집
• /
• 한국원자력학회 2005년도 춘계학술발표회
• /
• pp.27-28
• /
• 2005

• 한국가스학회지
• /
• 제15권3호
• /
• pp.1-5
• /
• 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.

• 한국수소및신에너지학회논문집
• /
• 제30권3호
• /
• pp.282-288
• /
• 2019

When liquefied natural gas (LNG) is vaporized to form natural gas for industrial and household consumption, a tremendous amount of cold energy is transferred from LNG to seawater as a part of the phase-change process. This heat exchange loop is not only a waste of cold energy, but causes thermal pollution to coastal fishery areas by dumping the cold energy into the sea. This project describes an innovative new design for reclaiming cold energy for use by cold storage warehouses (operating in the 35 to $62^{\circ}C$ range). Conventionally, warehouse cooling is done by mechanical refrigeration systems that consume large amounts of electricity for the maintenance of low temperatures. Here, a closed loop LNG heat exchange system was designed (by simulator) to replace mechanical or vapor-compression refrigeration systems. The software PRO II with PROVISION V9.4 was used to simulate LNG cold energy, gas re-liquefaction, and the vaporized process under various conditions. The effects on sensible and latent heats from changes to the array type of heat exchangers have been investigated, as well as an examination of the optimum.

• 한국수소및신에너지학회논문집
• /
• 제31권1호
• /
• pp.33-40
• /
• 2020

As hydrogen utilization becomes more active recently, a large amount of hydrogen should be supplied safely. Among the three supply methods, liquefied hydrogen, which is an optimal method of storage and transportation convenience and high safety, has a low temperature of -253℃, which is complicated by the liquefaction process and consumes a lot of electricity, resulting in high operating costs. In order to reduce the electrical energy required for liquefaction and to raise the efficiency, hydrogen is cooled by using a mixed refrigerant in a precooling step. The electricity required for the precooling process of the mixed refrigerant can be reduced by using the cold energy of LNG. Actually, LNG cold energy is used in refrigeration warehouse and air liquefaction separation process, and a lot of power reduction is achieved. The purpose of this study is to replace the electric power by using LNG cold energy instead of the electric air-cooler to lower the temperature of the hydrogen and refrigerant that are increased due to the compression in the hydrogen liquefaction process. The required energy was obtained by simulating mixed refrigerant (MR) hydrogen liquefaction system with LNG cold heat and electric system. In addition, the power replacement rate of the electric process were obtained with the pressure, the temperature of LNG, the rate of latent heat utilization, and the hydrogen liquefaction capacity, Therefore, optimization of the hydrogen liquefaction system using LNG cold energy was carried out.