Available power generation cycles to be coupled with the liquid natural gas (LNG) vaporization process in a Spanish LNG terminal

The boil off gas in Spanish LNG terminals is managed using recondensers. The electricity consumed by these terminals is bought in the Spanish wholesale market. Several power generating options using current available equipment and assuring the availability of the current terminal process have been analyzed thermoeconomically. A new combined cycle using a gas turbine and a pure NH3 Rankine cycle coupled with the natural gas vaporization process has been chosen as the most advisable one to be installed, due to the lower thermoeconomic cost obtained as shown in a new graphical representation similar to the existing exergetic cost diagrams.

[1]  Yousef S.H. Najjar,et al.  Efficient use of energy by utilizing gas turbine combined systems , 2001 .

[2]  Hongtan Liu,et al.  Characteristics and applications of the cold heat exergy of liquefied natural gas , 1999 .

[3]  Hongguang Jin,et al.  Novel cogeneration power system with liquefied natural gas (LNG) cryogenic exergy utilization , 2004 .

[4]  L. Tagliafico,et al.  On the recovery of LNG physical exergy by means of a simple cycle or a complex system , 2002 .

[5]  J. Szargut,et al.  Utilization of the cryogenic exergy of liquid natural gas (LNG) for the production of electricity , 2009 .

[6]  E. D. Rogdakis,et al.  A Kalina power cycle driven by renewable energy sources , 2009 .

[7]  William D. Baasel,et al.  Preliminary chemical engineering plant design , 1976 .

[8]  Yong Tae Kang,et al.  A combined power cycle using refuse incineration and LNG cold energy , 2000 .

[9]  Ge Yan,et al.  Effect of parameters on performance of LNG-FPSO offloading system in offshore associated gas fields , 2010 .

[10]  Kirk Hanawa An Ericsson Cycle GT Design by LNG Cryogenic Heat Utilization , 2000 .

[11]  Yoshiharu Tsujikawa,et al.  Utilization of the cryogenic exergy of LNG by a mirror gas-turbine , 2004 .

[12]  Truls Gundersen,et al.  A liquefied energy chain for transport and utilization of natural gas for power production with CO2 capture and storage – Part 3: The combined carrier and onshore storage , 2009 .

[13]  O. M. Ibrahim Design considerations for ammonia-water rankine cycle , 1996 .

[14]  Truls Gundersen,et al.  A liquefied energy chain for transport and utilization of natural gas for power production with CO2 capture and storage – Part 1 , 2009 .

[15]  Vega Rodrigálvarez,et al.  Calculation models for prediction of Liquefied Natural Gas (LNG) ageing during ship transportation , 2010 .

[16]  Celidonio Dispenza,et al.  Exergy recovery during LNG regasification: Electric energy production - Part one , 2009 .

[17]  Tao Lu,et al.  Analysis and optimization of a cascading power cycle with liquefied natural gas (LNG) cold energy recovery , 2009 .

[18]  Yousef S.H. Najjar,et al.  Cryogenic power conversion with regasification of LNG in a gas turbine plant , 1993 .

[19]  Yousef S.H. Najjar,et al.  A cryogenic gas turbine engine using hydrogen for waste heat recovery and regasification of LNG , 1991 .

[20]  Xiaojun Shi,et al.  A combined power cycle utilizing low-temperature waste heat and LNG cold energy , 2009 .

[21]  Mohammad Ameri,et al.  The study of capacity enhancement of the Chabahar gas turbine installation using an absorption chiller , 2004 .

[22]  E. Querol,et al.  Boil off gas (BOG) management in Spanish liquid natural gas (LNG) terminals , 2010 .

[23]  Noam Lior,et al.  A novel near-zero CO2 emission thermal cycle with LNG cryogenic exergy utilization , 2006 .

[24]  Truls Gundersen,et al.  A liquefied energy chain for transport and utilization of natural gas for power production with CO2 capture and storage - Part 2: The offshore and the onshore processes , 2009 .

[25]  A. Valero,et al.  On-line monitoring of power-plant performance, using exergetic cost techniques , 1996 .

[26]  C. Invernizzi,et al.  Carbon dioxide power cycles using liquid natural gas as heat sink , 2009 .

[27]  Jinyue Yan,et al.  Ammonia-water bottoming cycles : a comparison between gas engines and gas diesel engines as prime movers , 2001 .

[28]  E. Stefanakos,et al.  A REVIEW OF THERMODYNAMIC CYCLES AND WORKING FLUIDS FOR THE CONVERSION OF LOW-GRADE HEAT , 2010 .

[29]  H. Leibowitz,et al.  First Kalina combined-cycle plant tested successfully , 1997 .

[30]  Julius Woolf,et al.  Environmental Impact Study , 1972 .

[31]  Jung-In Yoon,et al.  Cycle analysis of air-cooled absorption chiller using a new working solution , 1999 .

[32]  Tae-Seung Kim,et al.  Power augmentation of combined cycle power plants using cold energy of liquefied natural gas , 2000 .

[33]  F. J. Wang,et al.  Performance improvement for a simple cycle gas turbine GENSET--a retrofitting example , 2002 .

[34]  T. Gundersen,et al.  A liquefied energy chain for transport and utilization of natural gas for power production with CO2 capture and storage - Part 4: Sensitivity analysis of transport pressures and benchmarking with conventional technology for gas transport , 2009 .

[35]  Meherwan P. Boyce,et al.  Gas turbine engineering handbook , 1981 .

[36]  Antonio G. Ramos,et al.  Novel application for exergy and thermoeconomic analysis of processes simulated with Aspen Plus , 2011 .