• Journal of Advanced Marine Engineering and Technology
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• v.27 no.7
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• pp.839-844
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• 2003

As sea water is being used as only heat source of LNG open rack vaporizer, serious problem has been risen in LNG terminal by the lack of heating energy source for LNG vaporization due to the temperature drop of sea water in winter. In this paper the new double-tube triple-flow(TRIDEX) vaporizer was suggested to solve the problem and the system was thermally analysed. LPG(liquefied petroleum gas) and sea water were introduced as the heat sources for LNG TRIDEX vaporizer. The flow patterns of TRIDEX vaporizer are as follows: LNG flow in the annular space, PG(petroleum gas) flow in the inner tube, and sea water flow in the outside of the double pipe. The overall LNG vaporization system was consisted of TRIDEX vaporizer, LPG vaporizer and PG heater. LPG in TRIDEX was directly dispersed in the sea water desalination unit, so that LPG turns to be gas phase for the reuse in TRIDEX vaporizer. New TRIDEX vaporizer system for LNG evaporation was analysed as much more effective than the present single tube one in the case of colder temperature of sea water in winter.

• Korean Journal of Air-Conditioning and Refrigeration Engineering
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• v.9 no.2
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• pp.189-197
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• 1997

The vaporizing characteristics of LNG(liquefied natural gas) via heat exchanger with sea water are analytically studied for an open rack vaporizer(ORV). This study is intended to supply the design data for the domestic fabrication of the corrosion-resistant vaporizer tube. A computational program is developed to predict the exit temperature of LNG for various conditions. In the program, thesimple and justifiable heat transfer models are selected for fully-developed internal flow of LNG, the star-shaped finned-tube, and the external falling films of sea water, as well as the possible ice formation and the fouling on the tube walls. It is found that the enongh corrugation inside of the tube wall is the most significant in the vaporizer performance for the current operating conditions. the effects of other design parameters on the heat exchanger between LNG and sea water are quantitatively presented.

• Journal of the Korean Institute of Gas
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• v.23 no.1
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• pp.41-46
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• 2019

LNG is supplying to consumers as gas phase vaporized by major seawater vaporizer, i.e.. open rack vaporizers. But as soon as the temperature of seawater drops below $5^{\circ}C$ in winter, the submerged evaporators should be operated and cause a lot of energy consumption because of their natural gas combustion. In order to reduce the consumption amount, in this study new two-way supplying method of seawater instead of the present one-way supplying system is introduced and analysed the technical possibilities and economical savings. The results showed that in case of the temperature of seawater becomes below $2.5^{\circ}C$, LNG can be evaporated using ORV without operating S MV. If this system is applied in Incheon LNG terminal, the energy saving reaches 11,770 Ton of LNG as 11,760 million won. By the analysis, the two-way supplying system of seawater in ORV can be the most effective method to be able to save huge amount of energy every year.

• Journal of the Korean Institute of Gas
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• v.5 no.3 s.15
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• pp.45-50
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• 2001

Open rack vaporizer (ORV) has been used in liquefied natural gas (LNG) receiving terminal in order to vaporize LNG into natural gas (NG) by heat exchange with seawater The U-type ORV which had been operated with seawater for 14 years is one of the important utilities of the gas production and the weld part of tube connected with header_ pipe had experienced many corrosion problems. To elucidate the cause of corrosion at weld part of vaporizer tube, corrosion potentials were compared by parts. This study concerns on the measurement of corrosion pit depth using non-destructive method and the evaluation of stress distribution in an aspect of safety with finite element analysis. In order to confirm the reliability of galvanic corrosion between weld parts and base metal, the measurement of corrosion potential by parts was conducted for 20 minutes in 3.5$\%$(wt.) NaCl solution. Many non-destructive methods were tried to measure the remaining thickness of vaporizer tube at fields. For general corrosion, tangential radiography test was confirmed as an effective method. In case of a fine corrosion pit, the shape of corrosion pit was reproduced using surface replication method. From collected data, stress distributions were quantitatively evaluated with 2-dimensional finite element method and the diagnostic evaluation on internal pressure of the U-type vaporizer could be made.

• 한국신재생에너지학회:학술대회논문집
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• 2010.06a
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• pp.157-157
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• 2010

우리나라는 기후변화협약에 대응하기 위한 교토의정서를 비준한 국가로서, 아직 온실가스의 의무감축 대상 국가는 아니다. 그러나 2012년부터 시작될 교토의정서 2차 공약기간 중에 브라질, 중국 및 인도와 같이 2차 의무감축대상이 가장 유력시 되는 국가로 지목되고 있으므로, 이러한 변화에 능동적으로 대처할 수 있는 기술적, 사회적, 정책적 방안이 신속히 마련될 필요가 있다. CCS(carbon capture & storage)란 화석연료로 부터 연소시 대기 중으로 배출되는 온실가스($CO_2$)를 포집하여 재생 또는 지중, 해양에 저장하는 기술로서 국가녹색성장 핵심기술중의 하나로 분류되며, 대료적인 $CO_2$ 발생대상인 석탄화력발전소로 부터 $CO_2$ 회수방안, 회수, 처리관련 연구를 포함하여 국내외 적으로 활발한 연구가 이루어 지고 있다. 순산소 연소기술을 통한 $CO_2$ 회수, 처리기술은 연료(천연가스, 석탄, 석유)의 산화제를 공기대신 순도 95% 이상의 고농도 산소를 이용하여 순산소연소를 하며, 이때 발생하는 배가스의 대부분은 $CO_2$와 수증기로 구성되어 있다. 발생된 배가스의 약 70~80%를 다시 연소실로 재순환시켜 연소기의 열적 특성에 적절한 연소가 가능하도록 최적화함과 동시에 배가스의 $CO_2$ 농도를 80% 이상으로 농축시켜 회수를 용이하게 하며, 특히 공해물질은 NOx 발생량을 10ppM 이하로 줄일 수 있다. 천연가스가 생산되는 LNG기지에서 LNG를 기화시키기 위하여 해수식 기화기(ORV : Open Rack Vaporizer와 수중연소식 기화기(SMV ; Submerged Combustion Vaporizer)를 사용하고 있으며, 특히 SMV는 버너를 이용하여 $-162^{\circ}C$ LNG를 $10^{\circ}C$의 LN로 기화시키는 설비로서 이때 연소시 $CO_2$를 상당량 발생시킨다. 본 논문에서는 SMV에서 순산소 연소방식을 적용하여 연료인 천연가스를 연소시키고, 이때 발생되는 $CO_2$와 수분이 주 성분인 배가스를 연소기에 재순환시켜, 연소실내 고온문제를 해결하며, 최종적으로 배가스중 $CO_2$는 $-162^{\circ}C$의 LNG 냉열을 이용하여 고순도의 액체 $CO_2$로 액화시키므로서 $CO_2$의 회수, 처리문제를 해결하는 방식을 소개하고자 한다. 이러한 방식은 천연가스에서 발생되는 $CO_2$ 회수를 LNG 냉열을 활용하므로서 폐열을 활용하는 에너지 효율적인 문제와 사용가능한 고순도 $CO_2$로 회수하므로서 환경적인 문제를 처리하는 기술이라 할 수 있다.