CO2 Storage Terminal for Ship Transportation

被引:20
作者
Lee, Ung [1 ]
Lim, Youngsub [1 ]
Lee, Sangho [1 ]
Jung, Jaeheum [1 ]
Han, Chonghun [1 ]
机构
[1] Seoul Natl Univ, Sch Chem & Biol Engn, Seoul 151742, South Korea
关键词
CARBON-DIOXIDE; SEQUESTRATION; CAPTURE; SYSTEM; LIQUID;
D O I
10.1021/ie200762f
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this article, an intermediate CO2 storage system for long-distance ship transportation was modeled. The storage terminal links the continuous CO2 liquefaction process to discrete marine ship transportation and performs as a buffer between them. It is composed of four distinct processes: a CO2 input process, a storage tank and loading process, a recirculation process, and a BOG (boiled-off gas) reliquefaction process. The entire system should be operated as a liquid phase. Consequently, operation conditions, tank capacity, insulation specification, and streamflow rates play a major role in operating the storage terminal securely. The goal of this study is to design a base case of the storage terminal and propose its appropriate operation condition which makes the terminal operate with minimum operation energy. Results of the base case simulations are compared with improperly insulated systems on the pipeline and tanks that generate more BOG than the base case. The total operation energies of the base case and case studies are presented, and it turns out that approximately three times the operation energy is required if the system is not properly designed.
引用
收藏
页码:389 / 397
页数:9
相关论文
共 17 条
[1]  
AOKI E, 1995, Patent No. 5464116
[2]  
ASPELUND A, 2004, INT C GREENH GAS CON, P2545
[3]   Gas conditioning -: The interface between CO2 capture and transport [J].
Aspelund, Audun ;
Jordal, Kristin .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2007, 1 (03) :343-354
[4]   Corrosion electrochemistry of fuel element materials in pond storage conditions [J].
Burrows, R ;
Harris, S ;
Stevens, NPC .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2005, 83 (A7) :887-892
[5]  
Barrio M., 2004, INT C GREENH GAS CON, P5
[6]  
BERGER B, INT C GREENH GAS CON
[7]   Performance modelling of a carbon dioxide removal system for power plants [J].
Desideri, U ;
Paolucci, A .
ENERGY CONVERSION AND MANAGEMENT, 1999, 40 (18) :1899-1915
[8]   MEASUREMENT AND CORRELATION OF THE (PRESSURE, DENSITY, TEMPERATURE) RELATION OF CARBON-DIOXIDE .2. SATURATED-LIQUID AND SATURATED-VAPOR DENSITIES AND THE VAPOR-PRESSURE ALONG THE ENTIRE COEXISTENCE CURVE [J].
DUSCHEK, W ;
KLEINRAHM, R ;
WAGNER, W .
JOURNAL OF CHEMICAL THERMODYNAMICS, 1990, 22 (09) :841-864
[9]  
GREEN DW, 2008, PENYS CHEM ENG HDB
[10]  
허철, 2008, 한국해양환경•에너지학회지, V11, P191