As shown in figure below, the reservoir has two different flow boundaries on both sides of geometry, Ax = 1000 ft, Ay = 750 ft, Az = 50 ft, B = B = 1RB/STB, c = 1.6 x 10-6 psi ky = 50 md, Ø = 0.27, Bc = 0.001127, µ 30 cp, ac = 5.615. The initial reservoir pressure is 4500 psi. Generate a system of finite- difference equations for the first timestep of (Implicit) formulation for At =15 days of one month of production. Other values and the necessary boundary conditions are illustrated in the Figure 1. Let partial differential equation a is ax (B.A). Ax + qse Voc aP %3D µB ax. acB° at 50 STB/D 80 STB/D No-flow boundary y 4 = 0 ax Figure 1
As shown in figure below, the reservoir has two different flow boundaries on both sides of geometry, Ax = 1000 ft, Ay = 750 ft, Az = 50 ft, B = B = 1RB/STB, c = 1.6 x 10-6 psi ky = 50 md, Ø = 0.27, Bc = 0.001127, µ 30 cp, ac = 5.615. The initial reservoir pressure is 4500 psi. Generate a system of finite- difference equations for the first timestep of (Implicit) formulation for At =15 days of one month of production. Other values and the necessary boundary conditions are illustrated in the Figure 1. Let partial differential equation a is ax (B.A). Ax + qse Voc aP %3D µB ax. acB° at 50 STB/D 80 STB/D No-flow boundary y 4 = 0 ax Figure 1
Computer Networking: A Top-Down Approach (7th Edition)
7th Edition
ISBN:9780133594140
Author:James Kurose, Keith Ross
Publisher:James Kurose, Keith Ross
Chapter1: Computer Networks And The Internet
Section: Chapter Questions
Problem R1RQ: What is the difference between a host and an end system? List several different types of end...
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