DescriptionPresentation at ESAT 2018 Conference
ABSTRACTOver the past 25 years, offshore gas processing operations have seen a proliferation in the development of subsea installations with complete subsea processing facilities soon to be a reality. Novel technologies – including subsea dehydration and compression units – are aimed at gas-dominated wells with the purpose of production and export directly from the seabed. Subsea production presents opportunities for improved efficiencies and increased profitability. To achieve the required dew point specification, water is absorbed from the gas stream through contact with a glycol such as ethylene glycol (MEG). The design and operation of these dehydration units require a thorough understanding of the phase equilibrium between the gas, water and glycol, at the process conditions observed in subsea installations. This understanding is achieved through a combination of accurate phase equilibrium data and thermodynamic models.
For this purpose we have performed phase equilibrium measurements for two systems: MEG + H2O + CH4 and MEG + H2O + Natural Gas. Experimental temperatures range from
15 – 50 °C, with measurements at pressures of 60 and 125 bar. The experiments were performed in a purpose-built rig at Statoil’s Research and Development Center in Trondheim, Norway. Glycol-rich mixtures have been prepared (>90 wt% in the liquid phase) in order to replicate dehydration applications. Glycol content has been determined using adsorption tubes which are analysed in a GC-MS, while water content was measured using Karl Fischer titration. For the natural gas systems, component analysis for C1-C6, N2 and CO2 has been performed with the use of gas chromatography. The experimental uncertainty is shown to be ~10% depending on the type of measurement.
Thermodynamic modelling is done using the Cubic-Plus-Association (CPA) equation of state. The model provides a good qualitative description for the vapour phase content for MEG and H2O, which are critical product specifications for dehydrated natural gas. For the description of MEG, we evaluate the performance of our new 4F association scheme against the literature 4C scheme. The use of uncertainty analysis in the parameterization of the models allows for the determination of operating ranges for process designs. This transference of uncertainty, from the data to the model and to the design, provides greater insight for the decision-maker regarding the process feasibility of a given design.
|Period||10 Jun 2018 → 13 Jun 2018|
|Held at||Institute of Chemical Process Fundamentals of the CAS, Czech Republic|
|Degree of Recognition||International|
Multicomponent Vapor–Liquid Equilibrium Measurement and Modeling of Ethylene Glycol, Water, and Natural Gas Mixtures at 6 and 12.5 MPa
Research output: Contribution to journal › Journal article › Research › peer-review
Ternary Vapor–Liquid Equilibrium Measurements and Modeling of Ethylene Glycol (1) + Water (2) + Methane (3) Systems at 6 and 12.5 MPa
Research output: Contribution to journal › Journal article › peer-review