- Page 1 and 2:
MULTIVARIATE PRODUCTION SYSTEMS OPT
- Page 3 and 4:
iii Approved for the Department: Ro
- Page 5 and 6:
Acknowledgements I would like to th
- Page 7 and 8:
5.2.4 Determine Partial Fugacities
- Page 9 and 10:
List of Figures Figure 1.1 Graphica
- Page 11 and 12:
Chapter 1 INTRODUCTION The performa
- Page 13 and 14:
eservoir model. Kuller and Cummings
- Page 15 and 16:
optimization, it is merely the proc
- Page 17 and 18:
Chapter 2 RESERVOIR AND INFLOW PERF
- Page 19 and 20:
where RS = V GO S 9 V OO S rS = V O
- Page 21 and 22:
The source-sink term of Equation 2.
- Page 23 and 24:
Δ φ SG BG + SO RS BO ρGO S S ρG
- Page 25 and 26:
3. Estimate the average reservoir p
- Page 27 and 28:
which is valid for steady-state, ra
- Page 29 and 30:
Chapter 3 VERTICAL MULTIPHASE FLOW
- Page 31 and 32:
μNS = μL λL + μG λG 21 (3.8) T
- Page 33 and 34:
-dP = 1 Qα + Q β Mα + Mβ g gC d
- Page 35 and 36:
• The term NGV NL 0.38 ND 2.14 is
- Page 37 and 38:
HL = 1 - 1 2 1 + VM VS - 1 + VM VS
- Page 39 and 40:
A paper by Hazim and Nimat (1989) p
- Page 41 and 42:
NV ≤ 18 25 18 < NV < 250 69 NV -0
- Page 43 and 44:
NWE Nμ > 0.005 ε = 0.3713 σL D 3
- Page 45 and 46:
NLV 100. 10. 1.0 0.1 Bubble Griffit
- Page 47 and 48:
V M < 10 δ ≥ -0.065 VM V M > 10
- Page 49 and 50:
RETURN ΔZ=.95 Δ Z ΔP=.95 Δ Pnew
- Page 51 and 52:
• maintain stable pressure downst
- Page 53 and 54:
R P = producing gas-liquid ratio, M
- Page 55 and 56:
flowrate is straightforward. Fortun
- Page 57 and 58:
Mass Flux Residual G1 - G2 0 Spurio
- Page 59 and 60: segregation. The gas phase must exi
- Page 61 and 62: API, GOR, Bo API Gravity First Stag
- Page 63 and 64: Zi = Xi L + Yi V (5.3) where V and
- Page 65 and 66: aα m = ∑ ∑ YiYj aα ij i j bm
- Page 67 and 68: ψ1 = 2 cos θ 3 - Ω 3 (5.28) ψ2
- Page 69 and 70: Chapter 6 NONLINEAR OPTIMIZATION Th
- Page 71 and 72: IMSL (1987). For a broad overview o
- Page 73 and 74: The minimum of a function can occur
- Page 75 and 76: F(x + hj ej - hi ei) F(x - hi ei) F
- Page 77 and 78: 6.2.1 The Method of Steepest Descen
- Page 79 and 80: The second step of the Greenstadt (
- Page 81 and 82: direct search method is simple to u
- Page 83 and 84: Original Triangular Polytope Worst
- Page 85 and 86: Chapter 7 RESULTS Each of the prece
- Page 87 and 88: Figure 7.2: Flow Rate Surface of Si
- Page 89 and 90: more stable than unmodified Newton
- Page 91 and 92: Figure 7.5: Hagedorn and Brown Grad
- Page 93 and 94: Figure 7.7: Aziz, Govier, and Fogar
- Page 95 and 96: Figure 7.9: Orkeszewski Gradient Ma
- Page 97 and 98: The Sachdeva et al. (1986) model wa
- Page 99 and 100: Figure 7.11: Constrained Present Va
- Page 101 and 102: At the end of each time step, the w
- Page 103 and 104: Figure 7.13: Present Value Surface
- Page 105 and 106: Figure 7.15: Profile of Tubing Diam
- Page 107 and 108: Figure 7.17: Close-up of Tubing Dia
- Page 109: Figure 7.19: First Derivative of Se
- Page 113 and 114: Figure 7.23: Second Mixed-Partial D
- Page 115 and 116: Figure 7.24: Minimum Eigenvalue of
- Page 117 and 118: Figure 7.26: Curvature of Hessian M
- Page 119 and 120: Figure 7.27: Convergence Path of Un
- Page 121 and 122: Figure 7.29: Convergence Path of Po
- Page 123 and 124: Figure 7.31: Convergence Path of Tr
- Page 125 and 126: • Nonlinear optimization may be u
- Page 127 and 128: Nomenclature Α Area. B Flow regime
- Page 129 and 130: xe Expansion point. xr Reflection p
- Page 131 and 132: Bibliography [1] Achong, I.: “Rev
- Page 133 and 134: [23] Charnes, A., and Cooper, W. W.
- Page 135 and 136: Techniques,” SPE Paper 12159, pre
- Page 137: [67] Strang, G.: Introduction to Ap