• Title/Summary/Keyword: BOR (boil-off-ratio)

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A Study on the Computation of Hull Temperature Distribution and Boil off Ratio of MRV Type LNG Carrier (MRV형 LNG선의 선체온도분포 및 증발률 산정에 관한 연구)

  • 천병일;김용모;김경근
    • Transactions of the Korean Society of Mechanical Engineers
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    • v.18 no.4
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    • pp.986-996
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    • 1994
  • Insulation system of LNG carrier has made important roles such as maintaining a proper Boil off Ratio(BOR) for the cargo and avoiding the excessive low temperature of the adjacent inner hull beyond the permissible limit. At the same time, safety and economy of the LNG transportation by the ship are connected with the performance of the insulation system. Also, thermal insulation system of LNG carrier is one of the most advanced technique with the structure analysis of tank, welding and assembling. In this study a computer program is developed to calculate the hull temperature distribution and BOR, which are important factors in thermal design for the Moss Rosenberg Verft spherical tank type LNG carrier. Detailed results for hhull temperature distribution close to LNG tank, BOR and the thickness effect of insulation material are reported in this paper in the range of standare design sea condition.

Determination of Boil-Off gas Ratio for the Design of Underground LNG Storage System in Rock Cavern (암반동굴식 지하 LNG 저장 시스템 설계를 위한 기화율의 산정)

  • Chung, So-Keul;Lee, Hee-Suk;Jeong, Woo-Cheol;Park, Eui-Seob
    • Tunnel and Underground Space
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    • v.17 no.1 s.66
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    • pp.56-65
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    • 2007
  • A new underground LNG storage concept in the rock mass has been developed by combining underground cavern construction and new ice-ring harrier technologies with the conventional cryogenic insulation system. Technical feasibility of the storage system has been verified through construction and operation of the pilot storage cavern and a full-scale project is expected to start in the near future. One of the most important issues in the LNG storage system is the operational efficiency of the storage to minimize heat loss during a long period of operation due to the cryogenic heat transfer. This paper presents several important results of heat transfer and coupled hydro-thermal analyses by a finite element code Temp/W and Seep/W. A series of heat transfer analyses for full-scale caverns were performed to determine design parameters such as boil-off gas ratio (BOR), insulation thickness and pillar width. The result of the coupled hydro-mechanical analysis showed that BOR for underground storage system remains at about 0.04 %/day during the early stage of the operation. This value could be even much lower when the discontinuities in the rock masses are taken into consideration.

Scale Effect Analysis of LNG Cargo Containment System Using a Thermal Resistance Network Model (열저항 네트워크 모델을 이용한 LNG 화물창 Scale Effect 분석)

  • Hwalong You;Taehoon Kim;Changhyun Kim;Minchang Kim;Myungbae Kim;Yong-Shik Han;Le-Duy Nguyen;Kyungyul Chung;Byung-Il Choi;Kyu Hyung Do
    • Journal of the Society of Naval Architects of Korea
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    • v.60 no.4
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    • pp.222-230
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    • 2023
  • In the present work, the scale effect on the Boil-Off Rate (BOR) was investigated based on an analytical method to systematically evaluate the thermal performance of a Liquefied Natural Gas (LNG) Cargo Containment System (CCS). A two-dimensional thermal resistance network model was developed to accurately estimate the heat ingress into the CCS from the outside. The analysis was performed for the KC-1 LNG membrane tank under the IGC and USCG design conditions. The ballast compartment of both the LNG tank and cofferdam was divided into six sections and a thermal resistance network model was made for each section. To check the validity of the developed model, the analysis results were compared with those from existing literature. It was shown that the BOR values under the IGC and USCG design conditions were agreed well with previous numerical results with a maximum error of 1.03% and 0.60%, respectively. A SDR, the scale factor of the LNG CCS was introduced and the BOR, air temperature of the ballast compartment, and the surface temperature of the inner hull were obtained to examine the influence of the SDR on the thermal performance. Finally, a correlation for the BOR was proposed, which could be expressed as a simple formula inversely proportional to the SDR. The proposed correlation could be utilized for predicting the BOR of a full-scale LNG tank based on the BOR measurement data of lab-scale model tanks.

Design of BOG re-liquefaction system of 20,000 m3 liquid hydrogen carrier

  • Byeongchang Byeon;Hwalong You;Dongmin Kim;Keun Tae Lee;Mo Se Kim;Gi Dock Kim;Jung Hun Kim;Sang Yoon Lee;Deuk Yong Koh
    • Progress in Superconductivity and Cryogenics
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    • v.25 no.3
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    • pp.49-55
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    • 2023
  • This paper presents the design of a re-liquefaction system as a BOG (boil-off gas) handling process in liquid hydrogen transport vessels. The total capacity of the re-liquefaction system was assumed to be 3 ton/day, with a BOR (boil-off rate) of 0.2 %/day inside the cargo. The re-liquefaction cycle was devised using the He-Brayton Cycle, incorporating considerations of BOG capacity and operational stability. The primary components of the system, such as compressors, expanders, and heat exchangers, were selected to meet domestically available specifications. Case studies were conducted based on the specifications of the components to determine the optimal design parameters for the re-liquefaction system. This encompassed variables such as helium mass flow rate, the number of compressors, compressor inlet pressure and compression ratio, as well as the quantity and composition of expanders. Additionally, an analysis of exergy destruction and exergy efficiency was carried out for the components within the system. Remarkably, while previous design studies of BOG re-liquefaction systems for liquid hydrogen vessels were confined to theoretical and analytical realms, this research distinguishes itself by accounting for practical implementation through equipment and system design.

Numerical Model of Heat Diffusion and Evaporation by LNG Leakage at Membrane Insulation (LNG 화물창 방열재 균열에 따른 액화천연가스의 확산 및 온도 예측을 위한 수치 모델)

  • Lee, Jang Hyun;Kim, YoonJo;Hwang, Se Yun
    • Journal of Ocean Engineering and Technology
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    • v.28 no.6
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    • pp.517-526
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    • 2014
  • The leakage of cryogenic LNG through cracks in the insulation membrane of an LNG carrier causes the hull structure to experience a cold spot as a result of the heat transfer from the LNG. The hull structure will become brittle at this cold spot and the evaporated natural gas may potentially lead to a hazard because of its flammability. This paper presents a computational model for the LNG flow and heat diffusion in an LNG insulation panel subject to leakage. The temperature distribution in the insulation panel and the speed of gas diffusion through it are simulated to assess the safety level of an LNG carrier subject that experiences a leak. The behavior of the leaked LNG is modeled using a multiphase flow that considers the mixture of liquid and gas. The simulation model considers the phase change of the LNG, gas-liquid multiphase interactions in the porous media, and accompanying rates of heat transfer. It is assumed that the NO96-GW membrane storage is composed of glass wool and plywood for the numerical simulation. In the numerical simulation, the seepage, heat diffusion, and evaporation of the LNG are investigated. It is found that the diffusion speed of the leakage is very high to accelerate the evaporation of the LNG.