A novel LNG/O2 combustion gas and steam mixture cycle with energy storage and CO2 capture

被引:24
作者
Chen, Yaping [1 ]
Zhu, Zilong [1 ]
Wu, Jiafeng [1 ]
Yang, Shifan [1 ]
Zhang, Baohuai [1 ]
机构
[1] Southeast Univ, Sch Energy & Environm, Minist Educ, Key Lab Energy Thermal Convers & Control, Nanjing 210096, Jiangsu, Peoples R China
关键词
Gas and steam mixture cycle (GSMC); Mixture of H2O and CO2; CO2; capture; Power load shaving; Energy storage; LIQUEFIED NATURAL-GAS; HEAT-TRANSFER CHARACTERISTICS; CRYOGENIC EXERGY UTILIZATION; LNG COLD ENERGY; POWER-PLANTS; KALINA CYCLE; POSTCOMBUSTION CAPTURE; WASTE HEAT; FLUE-GAS; SYSTEM;
D O I
10.1016/j.energy.2016.12.127
中图分类号
O414.1 [热力学];
学科分类号
摘要
A gas and steam mixture cycle (GSMC) is presented with a mixture of LNG/O-2 (liquid natural gas/oxygen) combustion product and feedwater as working medium, integrating features of high efficiency power generation, peak shaving, energy storage and CO2 capture. The liquefied oxygen is produced during off-peak hours. During the operation hours, the cryogenic liquids of both LNG and oxygen are pumped to a high pressure and preheated before entering the combustors through the burners. The combustion product heats and mixes with the atomized feedwater to form supercritical H2O/CO2 mixture vapor for power generation in a turbine unit. The CO2 vapor is separated from condensate water in the condenser and liquefied by the cryogenic liquids of both LNG and oxygen after being compressed to a higher pressure. The circulation feedwater is injected to the annular channel between flame tube and shell cylinder of modular combustor via feedwater heating system. The results show that under the conditions of turbine inlet parameters of 40 MPa/800 degrees C and condensation temperature of 30 degrees C, the output power efficiency based on the thermal value of LNG fuel is 49.2% and the equivalent net efficiency is 46.4%, which accounts for 1/4 off-peak electricity consumption for liquid O-2 production. (C) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:128 / 137
页数:10
相关论文
共 41 条
[11]   Pilot-scale multistage membrane process for the separation of CO2 from LNG-fired flue gas [J].
Choi, Seung-Hak ;
Kim, Jeong-Hoon ;
Lee, Yongtaek .
SEPARATION AND PURIFICATION TECHNOLOGY, 2013, 110 :170-180
[12]   Practical operation strategies for pumped hydroelectric energy storage (PHES) utilising electricity price arbitrage [J].
Connolly, D. ;
Lund, H. ;
Finn, P. ;
Mathiesen, B. V. ;
Leahy, M. .
ENERGY POLICY, 2011, 39 (07) :4189-4196
[13]   Novel cogeneration power system with liquefied natural gas (LNG) cryogenic exergy utilization [J].
Deng, SM ;
Jin, HG ;
Cai, RX ;
Lin, RM .
ENERGY, 2004, 29 (04) :497-512
[14]   Influence of baffle configurations on flow and heat transfer characteristics of trisection helical baffle heat exchangers [J].
Dong, Cong ;
Chen, Ya-Ping ;
Wu, Jia-Feng .
ENERGY CONVERSION AND MANAGEMENT, 2014, 88 :251-258
[15]   Study on a new IGCC (Integrated Gasification Combined Cycle) system with CO2 capture by integrating MCFC (Molten Carbonate Fuel Cell) [J].
Duan, Liqiang ;
Sun, Siyu ;
Yue, Long ;
Qu, Wanjun ;
Yang, Yongping .
ENERGY, 2015, 87 :490-503
[16]  
Global CCS Institute (GCCSI), 2010, STAT CCS PROJ INT RE
[17]  
He LP, 2015, J ENERGY INST, V89, P215
[18]  
IEA, 2021, Ammonia Technology Roadmap
[19]  
KALINA AI, 1984, J ENG GAS TURB POWER, V106, P737, DOI 10.1115/1.3239632
[20]   Performance evaluation of porous sodium aluminate sorbent for halide removal process in oxy-fuel IGCC power generation plant [J].
Kobayashi, Makoto ;
Akiho, Hiroyuki ;
Nakao, Yoshinobu .
ENERGY, 2015, 92 :320-327