| dc.description.abstract | The main objective of this thesis is to model a single mixed refrigerant process for offshore natural gas liquefaction using DWSIM as a simulation tools. Liquefied Natural Gas (LNG) in the energy sector is seen as a realistic source for providing
cleaner, small to large scale fuel, due to the ever-increasing global environmental
protection and high demand of electricity at a competitive rate. In this work, several
LNG processes existing and prospective ones are analysed thermodynamically. Due to
the growing demand for natural gas in the world today, transporting natural gas from
different parts of the world has become a necessity. Liquefying natural gas provides a
safer alternative and less expensive to transport, and to increase its storage capacity. The
liquefaction process requires natural gas to be cooled using a variety of methods and
cryogenic process also depressurized to atmospheric conditions for easier storage and
safer. This thesis analyzes the AP-X process for liquefaction of natural gas. The ability
AP-X process is analyzed in this study is assumed to be in Qatar. To analyzes the related
of thermodynamic factors, the DWSIM software was used to obtain the result. The
DWSIM process model was neither accurate nor robust enough to be well suited for
optimization and detailed analysis of the AP-X process. With regards to further work, it
is recommended to rebuild the model using alternative simulation software, preferably
providing a higher level of transparency with respect to process equations and
optimization procedures. A self-optimizing control structure for the process was not
determined in this thesis, but the procedures and simplifying assumptions were
discussed and achieved the final value Coefficient of Performance (COP) at 0.07. | en_US |
