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Use of Transient Simulators to Assess Gas Lift Viability for Offshore Angola. 2002 North American Gas Lift Workshop. SHAUNA NOONAN / FRED BROWNLEE. Actually a better title would be:. Produce 40,000 BWPD from 23,000 ft MD (8800 ft TVD) via Gas Lift Fact or Fiction?. Presentation Outline.
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Use of Transient Simulators to Assess Gas Lift Viability for Offshore Angola 2002 North American Gas Lift Workshop SHAUNA NOONAN / FRED BROWNLEE
Actually a better title would be: Produce 40,000 BWPD from 23,000 ft MD (8800 ft TVD) via Gas Lift Fact or Fiction?
Presentation Outline • Operating Parameters • Discussion on software (transient and static programs) • Work scope • Some of the results • What did we learn? • Questions
Parameters • 4500 psi injection pressure at wellhead • Target production of 40,000 bwpd / well • 0.68 gravity injection gas • Up to 30 MMscfd source gas available / well • 1.06 gravity water • Wellhead pressure of 250 psi • Reservoir Pressure of 3500 psi • Dry Tree (offshore in 1200 ft water)
From previous nodal analysis... • The target rate may be reached via conventional gas lift for a flow area equivalent to 8 5/8” tubing. • This would require gas lift rates of approximately 20 MMscfd. BUT…..
We have the following concerns: • Strategic importance of this well for project development • Static nodal program cannot predict whether the well could be unloaded. • Transient program can predict unloading conditions, but uses flow correlations that are not valid for large tubing sizes (greater than 5.5”) • Existing transient flow program is not capable of reverse flow completions analysis. • At the high injection pressures required, is the gas actually in a gaseous state at the orifice?
OLGA 2000 “OLGA 2000 is the market-leading simulator for transient multiphase flow of oil, water and gas in well and pipelines with process equipment. “ • Over 10,000 experiments were run in eight years on the SINTEF Two-Phase Flow Laboratory near Trondheim, Norway • The tests were run in both steady state and transient modes • The resultant data / correlations reside within OLGA 2000 • ChevronTexaco has been using this program for many years to assess flow assurance issues in pipelines and risers. It has not been used for downhole analysis applications • Limited to single point gas lift configurations
The Plan • Evaluate various completion options for high rate water wells using three different flow analysis software packages: • Well Evaluation Manager (WEM) using OLGAs • Dynalift • OLGA2000 • Evaluate Dynalift when used for large tubing completions • Develop & validate the well unloading sequence • Confirm importance of surface controlled downhole choke
Scope of Study The following scenarios were evaluated: • Case WA1: Lift gas injection down 11¾” casing with 8⅝” tubing. • Case WA2: Lift gas injection down 11¾” casing with IPC 7” tubing • Case WA3: Lift gas injection down 11¾” casing with IPC 8⅝” tubing • Case WB1: Lift gas injection down 3½” tubing with 9⅝” casing • Case WB2: Lift gas injection down 2⅞” tubing, with 9⅝” casing
Case WA1 • Notes: • Separation between WEM & OLGA2000 not fully explained; (possibility - OLGA2000 starting with transient flow first) • Dynalift example uses 0.5” orifice - significant at higher flow rates (problems with 1”) • OLGA2000 & WEM assume a fixed pressure differential not a fixed choke
Note the 180,000 bwpd slug OLGA predicted during the unloading cycle.
Effect of IPC Roughness Difference Case WA1: 0.0018 Case WA3: 0.00006
Case WB1 OLGA2000 & WEM include pressure loss from casing connections in annulus; Dynalift uses equivalent area
WHAT DID WE LEARN? • Have a higher degree of confidence that this well could be unloaded. • Question of conventional versus reverse gas lift must include drilling feasibility and operational safety concerns • WEM OLGAs works well for assessing well performance but does not answer unloading questions • For higher rate / pressure single point gas lift systems, surface controlled downhole gas lift valves are mandatory to reduce upsets while unloading the well