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The shut-in temperature log is included in Appendix A, and a compressed plot of the log <br /> is shown in Figure 3.2. The log was run after the wellbore fluid had been static for about 73 <br /> hours following a change over from mud to a six percent potassium chloride completion fluid. <br /> The temperature profile is normal, although there are some small anomalies which are apparent <br /> residuals of drilling fluid invasion. There are no indications of interzonal flow, which would be <br /> characterized by a smooth, isothermal (or nearly isothermal) interval in the profile. <br /> 4.0 CLEANOUT AND PRODUCTION BY NITROGEN LIFT <br /> It was originally planned that after perforating, the well would be produced for water <br /> samples using an electric submersible pump. However, because of the running sand problem, <br /> it was clear that a pump would not work. Instead, the sand was cleaned out and the well was <br /> produced for samples in a combined operation using nitrogen injection through coil tubing. This <br /> was done on May 15. <br /> Nitrogen was injected at rates of 300 to 400 scfm through 1'/z-in. coil tubing to produce <br /> the well by gas lift and to clean out the sand. Production (returns) from the well were piped <br /> from the tubing head side outlet valves to the rig's shale shaker and mud tank. During the <br /> nitrogen lift operation, water was transferred from the mud tank to a 500-barrel temporary <br /> holding tank from which it was pumped, filtered and transferred to three clean 500-barrel tanks. <br /> The filtered formation water was stored in the clean tanks for an injection test to be done later. <br /> During the cleanout and production operation, the four 500-barrel tanks were gauged periodically <br /> to determine the volume of water produced and the flow rate between gaugings. Water <br /> Mesquite Group, Inc. -5 <br />