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...kin/Unit 5 Finite-Difference Approximation to Linear-Flow Equations/fd1d_linearflow.ipynb
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{ | ||
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"metadata": { | ||
"colab": { | ||
"name": "fd1d_linearflow.ipynb", | ||
"provenance": [], | ||
"collapsed_sections": [], | ||
"authorship_tag": "ABX9TyNXN1hI1PA52xiT8k/v0165", | ||
"include_colab_link": true | ||
}, | ||
"kernelspec": { | ||
"name": "python3", | ||
"display_name": "Python 3" | ||
} | ||
}, | ||
"cells": [ | ||
{ | ||
"cell_type": "markdown", | ||
"metadata": { | ||
"id": "view-in-github", | ||
"colab_type": "text" | ||
}, | ||
"source": [ | ||
"<a href=\"https://colab.research.google.com/github/yohanesnuwara/reservoir-engineering/blob/master/Reservoir%20Simulation%20Ertekin/Unit%205%20Finite-Difference%20Approximation%20to%20Linear-Flow%20Equations/fd1d_linearflow.ipynb\" target=\"_parent\"><img src=\"https://colab.research.google.com/assets/colab-badge.svg\" alt=\"Open In Colab\"/></a>" | ||
] | ||
}, | ||
{ | ||
"cell_type": "markdown", | ||
"metadata": { | ||
"id": "eOe4EUXrFd9G", | ||
"colab_type": "text" | ||
}, | ||
"source": [ | ||
"# **Unit 5 Finite-Difference Approximations to Linear-Flow Problems**\n", | ||
"\n", | ||
"## Explicit Formulation\n", | ||
"\n", | ||
"$$p_{i}^{n+1} = (\\frac{\\alpha_c B_l \\Delta t}{V_b \\phi c_l})_i \\cdot q_{lsc_i} + (\\frac{\\alpha_c B_l \\Delta t}{V_b \\phi c_l})_i \\cdot [T_{lx_{i+1/2}}^{n} p_{i+1}^{n}-(T_{lx_{i+1/2}}^{n} + T_{lx_{i-1/2}}^{n})p_{i}^{n}+T_{lx_{i-1/2}}p_{i-1}^{n}]$$\n", | ||
"\n", | ||
"In the following codes, $(\\frac{\\alpha_c B_l \\Delta t}{V_b \\phi c_l})_i$ will be written as `factor`" | ||
] | ||
}, | ||
{ | ||
"cell_type": "code", | ||
"metadata": { | ||
"id": "IJsmLh1xKz8S", | ||
"colab_type": "code", | ||
"colab": {} | ||
}, | ||
"source": [ | ||
"import numpy as np\n", | ||
"import matplotlib.pyplot as plt\n", | ||
"import pandas as pd" | ||
], | ||
"execution_count": 0, | ||
"outputs": [] | ||
}, | ||
{ | ||
"cell_type": "code", | ||
"metadata": { | ||
"id": "rJZBuBCVK6JV", | ||
"colab_type": "code", | ||
"colab": { | ||
"base_uri": "https://localhost:8080/", | ||
"height": 134 | ||
}, | ||
"outputId": "e871c872-7bd9-49e5-f833-63db4056e97e" | ||
}, | ||
"source": [ | ||
"!git clone https://github.com/yohanesnuwara/reservoir-engineering" | ||
], | ||
"execution_count": 2, | ||
"outputs": [ | ||
{ | ||
"output_type": "stream", | ||
"text": [ | ||
"Cloning into 'reservoir-engineering'...\n", | ||
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"Receiving objects: 100% (845/845), 4.95 MiB | 30.33 MiB/s, done.\n", | ||
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], | ||
"name": "stdout" | ||
} | ||
] | ||
}, | ||
{ | ||
"cell_type": "markdown", | ||
"metadata": { | ||
"id": "N-NT2lf1GKb3", | ||
"colab_type": "text" | ||
}, | ||
"source": [ | ||
"## Example 5.8 \n", | ||
"\n", | ||
"![Example 5 8](https://user-images.githubusercontent.com/51282928/75949840-09e36380-5eda-11ea-824c-dd5c9ac6f6d5.PNG)" | ||
] | ||
}, | ||
{ | ||
"cell_type": "code", | ||
"metadata": { | ||
"id": "dLVKK7xd7fGK", | ||
"colab_type": "code", | ||
"colab": {} | ||
}, | ||
"source": [ | ||
"\"Task. determine pressure distribution during first year of production with timestep 10 days\"\n", | ||
"\n", | ||
"# known\n", | ||
"pi = 6000 # initial pressure, in psia\n", | ||
"delta_x = 1000 # ft\n", | ||
"delta_y = 1000\n", | ||
"delta_z = 75\n", | ||
"B = 1 # phase FVF, assumed constant over pressure, rb/stb\n", | ||
"c = 3.5E-06 # phase compressibility, psi^-1\n", | ||
"k_x = 15 # perm in x direction, md\n", | ||
"poro = 0.18\n", | ||
"mu = 10 # phase viscosity, cp\n", | ||
"\n", | ||
"delta_t = 10 # days\n", | ||
"qsc = -150 # minus means production, stb/d\n", | ||
"\n", | ||
"# calculate " | ||
], | ||
"execution_count": 0, | ||
"outputs": [] | ||
} | ||
] | ||
} |