Jawaharlal Nehru Technological University Hyderabad
Jawaharlal Nehru Technological University Hyderabad B.Tech IV NATURAL GAS HYDRATES AND COAL BED METHANE Previous Question Paper (July - 2021 - R16)
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Describe in detail the K-factor method with neat sketches.
Answer
The K-factor method is a thermodynamic approach used to predict the conditions under which gas hydrates form by calculating the equilibrium ratio (K-value) of each component in the gas mixture. The K-value is defined as the ratio of the mole fraction of a component in the vapor phase (y) to its mole fraction in the hydrate phase (x), expressed as K = y/x.
The method relies on the principle that at hydrate equilibrium, the summation of the mole fractions of all components in the hydrate phase must equal unity (Σx = 1). Since x = y/K, the equilibrium condition is satisfied when Σ(y/K) = 1. The K-values are functions of temperature and pressure, typically derived from empirical charts or correlations specific to the hydrate structure (Structure I or II).
The calculation steps involve: 1) Assuming a temperature for a given pressure; 2) Determining the K-value for each component at that temperature and pressure from standard K-factor charts; 3) Calculating the sum Σ(y/K); 4) Iterating the temperature until the sum equals 1.0. A sketch of the K-factor chart would show log(K) on the y-axis against pressure on the x-axis, with individual curves for each gas component (methane, ethane, propane, etc.) showing a downward trend as pressure increases.
At what temperature will a hydrate form for pure methane at a pressure of 1,000psia? What are the compositions of the coexisting phases at this pressure? Express the water content of the gas in lb/MMCF.
Answer
For pure methane at 1,000 psia, the hydrate formation temperature is approximately 65°F (18.3°C). This value is obtained from standard hydrate equilibrium curves for pure methane.
At this pressure and temperature, the coexisting phases are the gas phase and the solid hydrate phase. The composition of the gas phase is 100% methane (y = 1.0). The composition of the hydrate phase is defined by the hydrate structure; for methane (Structure I), the hydrate cage occupancy results in a theoretical composition of approximately 1 mole of methane to 5.75 moles of water, or roughly 14.8 mole percent methane in the hydrate lattice.
The water content of the gas at 1,000 psia and 65°F is determined using standard water content charts for natural gas. For pure methane at these conditions, the water content is approximately 85 lb/MMCF.
Explain how to select effective kinetic inhibitors for natural gas hydrates.
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Discuss briefly the crystal structure of Type I natural gas hydrates.
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Give a brief note on the following:
Kinetics of hydrate formation
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Hydrate formation during drilling.
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Discuss in detail the depressurization with help of required sketches.
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Prediction of natural gas hydrate inhibitor vaporization rate using particle swarm optimization approach.
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Explain in detail the PVT analysis for oil reservoir.
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What are the environmental effects of CBM production? and how to enhance the green aspect of its development.
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What is the adsorption isotherm? Derive the isotherm for recovery prediction model of the micro pores coal sorption.
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Difference between coal bed methane vs conventional reservoirs.
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How to damage coal permeability during hydraulic fracturing?
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A sweet natural gas is flowing in a pipeline at 1,000psia (6.895 MPa). At this pressure the gas forms a hydrate at 65°F (18.3°C) provided sufficient water is present. First, estimate the minimum amount of water required in order to form a hydrate at 65°F and 1,000psia. If the gas has been dehydrated to 7lb/MMCF (112 mg/Sm3), at what temperature will this mixture form a hydrate? Finally, if the gas is dehydrated to 4 lb/MMCF (64 mg/Sm3), at what temperature will a hydrate form?
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