The optimization of LNG dehydration process / Muhammad Hazim Mohd Shafie

Natural gas is the one of the most important energy in this era. It being delivered to the consumers via pipelines by compressing the gas or liquefying the gas which is known as liquefied natural gas (LNG). Due to technical and economic reasons, LNG is more favourable process to transport the gas. Hydrocarbon contains water vapour since it is found deep in underground reservoirs at high temperature and pressure. This water vapour can form the hydrate and cause corrosion in pipelines. Therefore, this research is done to simulate a gas dehydration process and to optimize the parameters in absorption dehydration process. The parameters are the type of glycol used, the glycol flow rate, number of stages in absorber column, reboiler temperature and gas inlet temperature on glycol dehydration unit. The software used for this research is Aspen HYSYS. Based on the simulated data, the optimized parameters of dehydration process has been proposed. It is showed that triethylene glycol (TEG) is the most effective type of glycol followed by diethylene glycol (DEG) and ethylene glycol (EG). The higher the number of trays, the lower the amount of water content in the dry gas. Furthermore, the lower water content in the dry gas stream can be achieved by decreasing the temperature of the inlet gas of the absorption column. Results also shown that the higher the temperature of the reboiler the lower the water content of the natural gas stream. The optimum parameters of gas dehydration were at 12 number of stages with 200°C reboiler temperature and 20°C inlet gas temperature.