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Notional Field Development Final Report - EBN

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<strong>EBN</strong> <strong>Notional</strong> <strong>Field</strong> <strong>Development</strong> Plan<br />

capabilities, uses less base polymer resulting in much higher regained conductivity with low gel residue<br />

in the proppant pack.<br />

Table 3-2, Fracture Model Inputs is a summary of the inputs used for the fracture design modeling.<br />

Table 3-2, Fracture Model Inputs<br />

Casing:<br />

177.8 x 114.3 mm (7” 32.0 lb/ft x 4 ½”, 13.5 lb/ft)<br />

Perforations (Posidonia): 3100 m TVD (10,170 ft), 48 perfs w/10 mm (0.39”)<br />

Perforations (Aalburg): 3350 m TVD (10,990 ft), 48 perfs w/10 mm (0.39”)<br />

Permeability:<br />

100 nD<br />

Total Leakoff, Ct:<br />

0.00610 cm/min1/2 (0.0002 ft/min1/2)<br />

Min. Conc. for Fracture:<br />

2.44 kg/m2 (0.5 lbm/ft2)<br />

Fluid:<br />

Sirocco 30 lb/Mgal<br />

Proppant:<br />

20/40 RC (Atlas PRC), 30/50 RC (Atlas PRC)<br />

Stress Gradient*:<br />

0.105 bar/m (0.517 psi/ft)<br />

Closure Pressure (Posidonia):<br />

328.2 bar (4760 psi)<br />

Closure Pressure (Aalburg):<br />

357.1 bar (5180 psi)<br />

Fracture interaction<br />

Active<br />

DFN: Natural fracture spacing<br />

dy= dx= dz = 7.62 m (25 ft)<br />

DFN: Proppant distribution<br />

Uniform<br />

*The stress gradient was obtained honoring log derived mechanical properties. However, the stress<br />

values are lower than expected and lower that what is typically seen in other shale formations. These<br />

values need to be confirmed and updated after the DFIT and log analysis is completed on the vertical<br />

well.<br />

The recommended pumping schedule for both Planar and Discrete Fracture Modeling Scenarios is<br />

Table 3-3, Treatment Schedule for Fracture Design. The pad fluid is pumped during the first stage of the<br />

treatment to create initial fracture geometry. The pad is followed by eight sets of 20/40 or 30/50-mesh<br />

proppant slurry, helping to develop geometry, conductivity and fracture length. During these eight<br />

stages of the treatment, the proppant is staged up from 1 ppg (119.83 kg/m 3 ) to 8 ppg (958.61 kg/m 3 ).<br />

At the end of placing the slurry 17.413 m 3 of flush is pumped to clear tubulars of proppant. Each stage of<br />

the treatment is designed for an average slurry rate of 7.15 m 3 /min (45 bpm). Total liquid volume per<br />

stage is 477.34 m 3 (3000 bbls). Total proppant mass is 224,530 kg (495,000 lbs) per stage. This treatment<br />

creates a maximum surface treating pressure of 291 bar (4221 psi), assuming the current stress gradient<br />

of 0.105 bar/m (0.517 psi/ft).<br />

© 2011 Halliburton All Rights Reserved<br />

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