Numerical Simulation of Methane Hydrate in Sandstone Cores - PowerPoint PPT Presentation

About This Presentation
Title:

Numerical Simulation of Methane Hydrate in Sandstone Cores

Description:

K. Nazridoust, G. Ahmadi and D.H. Smith. Department of Mechanical and Aeronautical Engineering ... Ice-like Crystalline Substances Made Up of Two or More Components ... – PowerPoint PPT presentation

Number of Views:104
Avg rating:3.0/5.0
Slides: 19
Provided by: kam71
Category:

less

Transcript and Presenter's Notes

Title: Numerical Simulation of Methane Hydrate in Sandstone Cores


1
Numerical Simulation of Methane Hydrate in
Sandstone Cores
K. Nazridoust, G. Ahmadi and D.H.
SmithDepartment of Mechanical and Aeronautical
Engineering Clarkson University, Potsdam, NY
13699-5725National Energy Technology
LaboratoryU.S. Department of Energy, Morgantown,
WV 26507-0
2
Gas Hydrates
  • Ice-like Crystalline Substances Made Up of Two or
    More Components
  • Host Component (Water) - Forms an Expanded
    Framework with Void Spaces
  • Guest Component (Methane, Ethane, Propane,
    Butane, Carbon Dioxide, Hydrogen Sulfide) - Fill
    the Void Spaces
  • Van der Waals Forces Hold the Lattice Together

3
Energy Content
4
Importance of Gas Hydrates
  • Potential Energy Resources
  • Potential Role in Climate Change
  • Issues During Oil and Gas Production
  • CO2 Sequestration

Objectives
  • To Provide A Fundamental Understanding of Species
    Flow During Hydrate Dissociation
  • To Assess the Reservoir Conditions During Hydrate
    Dissociation
  • To Develop a Module for Simulation of Gas
    Hydrates Dissociation to be Incorporated in
    FLUENT Code

5
Three-Phase Flow in Methane Hydrate Core,
Depressurization
6
Hydrate Core
7
Governing Equations
Continuity
Darcys Law
Saturation
Hydrate Dissociation - (Kim-Bishnoi, 1986)
Kinetic Model
Intrinsic Diss. Constant 124
kmol/Pa/s/m2, and Activation Energy ?E 78151
J/kmol
8
Governing Equations
Energy Equation
Effective Thermal Conductivity
Hydrate Dissociation Heat Sink
Masuda, et al. (1999), c 56,599 J/mol, d
-16.744 J/mol.K.
9
Governing Equations
Equilibrium Pressure
Makagon (1997), A 0.0342 K-1, B 0.0005 K-2, C
6.4804
Ambient Temperature
Outlet Press.
10
Initial Conditions
Core Temperature (K) 275.45
Initial Pressure (MPa) 3.75
Initial Hydrate Saturation 0.443
Initial Water Saturation 0.351
Initial Gas Saturation 0.206
Initial Porosity 0.182
Initial Absolute Permeability (mD) 97.98
Boundary and Ambient Conditions
Ambient Temp. (K) Outlet Valve Pressure (MPa)
Case1 274.15 2.84
Case2 275.15 2.84
Case3 276.15 2.84
Case4 275.15 2.99
Case5 275.15 3.28
11
Hydrate Core
12
Tamb.275.15K
Simulation
13
Tamb.275.15K
Simulation
14
Temperature Comparison with Data
Ambient Temp. (K) Outlet Valve Pressure (MPa)
Case2 275.15 2.84
15
Cumulative Gen./Diss. Comparison with Data
- Case (2)
Ambient Temp. (K) Outlet Valve Pressure (MPa)
Case2 275.15 2.84
16
Five-spot Technique
  • Four wells to form a square where steam or water
    is pumped in
  • Gas is pushed out through the 5th well in the
    middle of the square

17
Simulation
18
Conclusions
  • Depressurization method under favorable
    conditions is a feasible method for producing
    natural gas from hydrate.
  • Gas generation rate is sensitive to physical and
    thermal conditions of the core sample, the heat
    supply from the environment, and the outlet valve
    pressure.
  • Porosity and relative permeability are important
    factors affecting the hydrate dissociation and
    gas generation processes.
  • For the core studied the temperature near the
    dissociation front decreases due to hydrate
    dissociation and then increases by thermal
    convection.
  • Increasing the surrounding temperature increases
    the rate of gas and water production due to
    faster rate of hydrate dissociation.
  • Decreasing the outlet valve pressure increases
    the rate of hydrate dissociation and therefore
    the rate of gas and water production increases.
Write a Comment
User Comments (0)
About PowerShow.com