Fluid production from unconsolidated reservoirs often leads in sand production,which poses a number of issues.Sand deposition in flowlines can result in significant pressure dips,pipe and facility damage,and obstructi...Fluid production from unconsolidated reservoirs often leads in sand production,which poses a number of issues.Sand deposition in flowlines can result in significant pressure dips,pipe and facility damage,and obstructions that decrease productivity.More research is needed to understand the movement and deposition of sand in oil-water-sand(O-W-S) fluxes.This article focuses on O-W-S flows in a 6-meter-long horizontal pipe with an inner diameter of 0.0381 m.The study looks at the flow behavior of high viscosity oil-water(O-W),water-sand(W-S),and oil-water-sand(O-W-S) flows.Experiments were carried out at 250 psig pressure in a laboratory flow test facility using various heavy synthetic oils(viscosities ranging from 3500 cP to 7500 cP at 25℃) and tap water.The sand concentration varied from 1% to 10%,with an average sand particle diameter of 145 μm and material density of 2630 kg/m~3.Water cuts ranged from 0.0 to 1.0.The experimental results revealed a minor change in pressure gradient between(O-W) and(O-W-S) flows.However,increasing the sand concentration in(O-W-S) flow resulted in higher pressure losses.The reduction factor of pressure gradient indicated that the highest decrease in pressure drop occurred at higher superficial oil velocities.Furthermore,a direct relationship was observed between the reduction factor and the decrease in water cut.The results also showed that the minimum required transportation velocity for sand slurry decreased with increasing superficial oil velocity,while the minimum transportation condition increased with higher sand concentration.The comparison between the expected pressure gradient from Bannwart and McKibben et al.and the actual experimental data demonstrated significant accuracy for the oil viscosities and superficial oil velocities used in the study.展开更多
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文摘Fluid production from unconsolidated reservoirs often leads in sand production,which poses a number of issues.Sand deposition in flowlines can result in significant pressure dips,pipe and facility damage,and obstructions that decrease productivity.More research is needed to understand the movement and deposition of sand in oil-water-sand(O-W-S) fluxes.This article focuses on O-W-S flows in a 6-meter-long horizontal pipe with an inner diameter of 0.0381 m.The study looks at the flow behavior of high viscosity oil-water(O-W),water-sand(W-S),and oil-water-sand(O-W-S) flows.Experiments were carried out at 250 psig pressure in a laboratory flow test facility using various heavy synthetic oils(viscosities ranging from 3500 cP to 7500 cP at 25℃) and tap water.The sand concentration varied from 1% to 10%,with an average sand particle diameter of 145 μm and material density of 2630 kg/m~3.Water cuts ranged from 0.0 to 1.0.The experimental results revealed a minor change in pressure gradient between(O-W) and(O-W-S) flows.However,increasing the sand concentration in(O-W-S) flow resulted in higher pressure losses.The reduction factor of pressure gradient indicated that the highest decrease in pressure drop occurred at higher superficial oil velocities.Furthermore,a direct relationship was observed between the reduction factor and the decrease in water cut.The results also showed that the minimum required transportation velocity for sand slurry decreased with increasing superficial oil velocity,while the minimum transportation condition increased with higher sand concentration.The comparison between the expected pressure gradient from Bannwart and McKibben et al.and the actual experimental data demonstrated significant accuracy for the oil viscosities and superficial oil velocities used in the study.
