multivariate production systems optimization - Stanford University
multivariate production systems optimization - Stanford University
multivariate production systems optimization - Stanford University
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more stable than unmodified Newton’s Method, and was to optimize long-term financial<br />
objectives.<br />
7.1.2 Developing the Reservoir Component<br />
To replicate the reservoir dynamics and inflow performance in the well model, this study<br />
adopted a reservoir model developed by Borthne (1986) at the Norwegian Institute of<br />
Technology, as discussed in Chapter 2. The reservoir model was originally designed with<br />
just this purpose in mind--to provide a simple but functional reservoir component to be<br />
included in a larger model. The model provides an accurate representation of constrained<br />
reservoir performance that requires minimal computer processing. Borthne’s model is a<br />
black-oil model that performs a generalized material balance calculation in concert with an<br />
inflow performance relationship based on pseudopressure. The reservoir model is<br />
constrained by both pressure and flowrate. In addition to specifying a minimum flowing<br />
well pressure, two flowrates must be specified: a minimum flowrate and a maximum target<br />
flowrate. The model attempts to satisfy the target flowrate without violating the minimum<br />
flowing well pressure. For more details on the reservoir component used in the well<br />
model, see Chapter 2.<br />
7.1.3 Developing the Tubing Component<br />
The next stage in the model development was to design and develop a component to model<br />
the multiphase flow through the vertical flowstring. For this we relied on the many<br />
empirical correlations that have been developed over the years. Three correlations were<br />
selected to be included in the model. These were the modified Hagedorn & Brown<br />
correlation (1965), the Orkiszewski correlation (1967), and the Aziz, Govier, and Fogarasi<br />
correlation (1972). All three correlations are extensively used in the petroleum industry.<br />
The Hagedorn and Brown (1965) correlation is one of the most empirical available, the<br />
Aziz et al. (1972) correlation has the strongest theoretical basis.<br />
Gradient maps of the three correlations were generated and are shown in Figures<br />
7.4 through 7.9. Figures 7.4 and 7.5 show the gradient surface generated by the modified<br />
Hagedorn and Brown (1965) correlation. The transition from the original Hagedorn and<br />
Brown correlation, representing slug flow, to the Griffith & Wallis (1961) correlation,<br />
representing bubble flow, is very distinct. Figures 7.6 and 7.7 show the Aziz et al. (1972)<br />
correlation with their suggested flow map superimposed. Note theat the map appears<br />
continuous everywhere except at the boundary between bubble flow and slug flow.<br />
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