Petroleum Engineering 603 MIDTERM EXAM October 24, 2002 Name:_________________________________________ You may use one sheet of handwritten equations, attach to exam when turned in. You may use a calculator. Do not fold or unstaple the examination booklet. Time allotted for the examination is 120 minutes. When you have completed the examination, read and sign the statement below, then turn in the examination booklet. STATEMENT OF ACADEMIC INTEGRITY I pledge that I have neither given nor received aid in completing this examination. I have followed the strictures of the Texas A&M University Aggie Code of Honor during this examination. Signature: ____________________________________ 1 Beginning with the Continuity Equation, derive the Diffusivity Equation for single phase reservoir flow of an ideal gas, considering pressure squared (p2) to be the dependent variable. After completing the derivation, answer the following two questions: Were any nonlinear terms neglected? If so, describe them. What parts of the diffusivity term (ct/k) are expected to be nonlinear for reservoir flow of an ideal gas Continuity Equation: u = t Diffusivity Equation – Ideal Gas: 2 ct p 2 p 2 = k t 2 3 Consider reservoir flow of a slightly compressible, single phase fluid, in a horizontal, 1-D, linear reservoir. a) Show the partial differential equation that describes fluid flow for this reservoir geometry, using Wattenbarger’s usual oilfield units [Unit Conversion Constant = 0.00633]. List the units of each term of the partial differential equation. b) For each of the following flow solutions to the partial differential equation, show examples of the initial conditions and boundary conditions, expressed in equation form. For all cases, consider constant rate production for the left edge boundary condition. Transient (Infinite Acting) Steady State Pseudosteady State c) For each of the following flow solutions, discuss the reservoir flow conditions under which each solution would be applicable to analysis of field data. Transient (Infinite Acting) Steady State Pseudosteady State 4 5 The following sketch shows the dimensions of two adjacent reservoir simulation gridblocks (block centered grid). Calculate the water flow rate and direction between gridblocks, using single point upstream relative permeability (in units of scf/day), for: Gridblock 1 Gridblock 2 p Sw Z krw Pcow Bw w w/144 k 100 ft 1910.0 0.60 -5610.0 0.08 23.0 1.024 0.3350 0.48 100.0 1950.0 psia 0.80 -5615.0 ft, subsea 0.20 20.0 psia 1.020 rcf/scf 0.3360 cp 0.48 psia/ft 100.0 md 100 ft 100 ft 1 2 20 ft 6 7 Consider single phase flow of water containing a polymer. We will assume that the polymer flows with the water and also adsorbs onto the rock. Assume the concentration of polymer in the water phase to be C units [mass of polymer/volume of water] and adsorption of polymer onto the rock surface is Ĉ units [mass of polymer/rock volume]. Starting from first principles, derive a gridblock material balance equation for polymer mass. You may neglect diffusion of polymer in the water. [Hint: The polymer can be treated like a tracer except: it adsorbs onto the rock surface, and does not diffuse in the water] 8 9 10