Progressing Cavity Pumps by Shauna Noonan (Ed.)

By Shauna Noonan (Ed.)

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Vibration The vibration sensors supplied with the tool are accelerometers mounted to measure acceleration in both the radial (Vx) and vertical (Vz) directions. For both wells, the Vz sensor did not appear to give valid results as the values reported were essentially all zeros, so only Vx is plotted with surface speed during completion of the test matrix (Fig. 7 and Fig. 8). Both wells, there appears to be no correlation between vibration and speed, with exception to Well B at speeds higher than 200 rpm and then there is an interesting event that occurred during the ramp-up from 300 rpm to 400 rpm, where at approximately 350 rpm, the vibration is reduced.

Obtaining further understanding of the circumstances which led to the failure during design, manufacture or operation of the PCP systems is required to ensure that the proper actions are taking place to reduce the likelihood of that failure reoccurring. Figure 4 plots several failure causes associated with failed rotor and stator components in a certain field. In the case of the failed stator components, most of the failed components failed not due to deficiencies in the equipment but due to the operation of the equipment (in this case, properly running dry due to the absence of a pump-off control system).

This is an important advantage over competing high temperature ESP technology. Acknowledgements The authors wish to acknowledge the management of TOTAL, PCM and KUDU Industries Inc. for their permission to publish this work and their permanent support of our research effort. 89 kPa Temperatures: (5/9)*(°F-32) = °C Stator Q N delivery pressure Rotor (steel) Figure 1: PCP principle SPE 110479 5 Figure 2: Conventional (elastomer) PCP section External envelop Figure 5: One Joslyn Well Pad with Metal PCP wellheads Hydroformed stator Figure 3: Metal PCP principle Drive Head Electrical Motor Well Head Sucker Rods Rod centralizers Figure 6: Detail of Metal PCP Drive Head used on Joslyn Pads Pump (Stator/rotor) Stop Bushing Torque Anchor Figure 7: Crude viscosity versus temperature Figure 4: Typical Rod Driven-PCP equipment 6 SPE 110479 Overall efficiency vs delta p 70% 65% 60% Overall efficiency (%) m3/d Liquid flowrate vs head @ 200°C - 17 cpo 260 240 220 200 180 160 140 120 100 80 60 40 20 400 RPM 350 RPM 300 RPM - 20 40 60 80 100 55% 50% 45% 40% 200 RPM 30% 100 RPM 25% 120 140 92°C-320 cpo @ 300rpm 92°C-320 cpo @ 200rpm 92°C-320 cpo @ 100 rpm 200°C- 17 cpo @ 400rpm 200°C- 17 cpo @ 300rpm 200°C- 17 cpo @ 200rpm 35% 20% - 20 40 60 Delta-P (bar) Figure 8: 400 MET1000 Bench Test–Liquid Flowrate@ 200°C(390F) 60% Volumetric efficiency (%) 90 50% 80 40% 70 30% 100rpm 60 200rpm 50 350rpm 40 80 100 120 50 100 500 cP 10% 30 60 140 wa ter 20% 300rpm 40 120 Figure 11: 400 MET1000 Bench Test -Overall Efficiency Pump efficiency 100 20 100 70% Volumetric efficiency @ 150°C - 37 cpo 0 80 DeltaP (bar) 140 DeltaP (bar) Figure 9: 400 MET1000 Bench Test -Vol.

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