The Effect of Pressure-Decline Rate and Pressure Gradient on the Behavior of Solution-Gas Drive in Heavy Oil

2009 ◽  
Vol 12 (03) ◽  
pp. 390-398 ◽  
Author(s):  
Hussain Sheikha ◽  
Mehran Pooladi-Darvish

Summary Heavy-oil recovery under solution-gas drive is affected by several interacting factors including pressure-decline rate and pressure gradients. It has been suggested that a high pressure decline rate (dp/dt) generates larger supersaturation and faster nucleation that leads to more-dispersed gas bubbles, while a high pressure gradient (?p) increases the viscous forces acting on the gas phase, enhancing bubble break up and gas dispersion. Both effects lead to lower gas mobility, affecting oil recovery; however, the relative importance of each is not known. Finding this is important to develop mathematical models and to allow extrapolation of experimental results to field conditions, where the relative importance of these factors changes with time and space. Previous experimental studies were affected by a combination of the two effects. In this paper, we distinguish between the effect of the pressure-decline rate and pressure gradient on gas mobility and oil recovery by varying these independently. In the experimental work reported in this paper, change in confining pressure is used to create a change in pressure-decline rate, and a change in production rate is used to change the pressure gradient. Several depletion experiments at varying pressure-decline rates and production rates are reported here. At a constant pressure-decline rate, the recovery factor tripled when the flow rate was increased by one order of magnitude. Similar experiments were conducted when the pressure-decline rate was increased by one order of magnitude but the flow rate was kept constant. In this case, the recovery factor did not change significantly. The results of this study clearly indicate that the pressure gradient has a much greater effect on gas mobility and oil recovery than pressure-decline rate has. This paper presents the experimental results and their analysis, along with the implications of these findings on modeling of solution-gas drive in heavy oils.

SPE Journal ◽  
2016 ◽  
Vol 21 (04) ◽  
pp. 1236-1253 ◽  
Author(s):  
Tae Wook Kim ◽  
E.. Vittoratos ◽  
A. R. Kovscek

Summary Recovery processes with a voidage-replacement ratio (VRR) (VRR = injected volume/produced volume) of unity rely solely on viscous forces to displace oil, whereas a VRR of zero relies on solution-gas drive. Activating a solution-gas-drive mechanism in combination with waterflooding with periods of VRR less than unity (VRR < 1) may be optimal for recovery. Laboratory evidence suggests that recovery for VRR < 1 is enhanced by emulsion flow and foamy (i.e., bubbly) crude oil at pressures under bubblepoint for some crude oils. This paper investigates the effect of VRR for two crude oils referred to as A1 (88 cp and 6.2 wt% asphaltene) and A2 (600 cp and 2.5 wt% asphaltene) in a sandpack system (18-in. length and 2-in. diameter). The crude oils are characterized with viscosity, asphaltene fraction, and acid/base numbers. A high-pressure experimental sandpack system (1 darcy and Swi = 0) was used to conduct experiments with VRRs of 1.0, 0.7, and 0 for both oils. During waterflood experiments, we controlled and monitored the rate of fluid injection and production to obtain well-characterized VRR. On the basis of the production ratio of fluids, the gas/oil and /water relative permeabilities were estimated under two-phase-flow conditions. For a VRR of zero, the gas relative permeability of both oils exhibited extremely low values (10−6−10−4) caused by internal gas drive. Waterfloods with VRR < 1 displayed encouraging recovery results. In particular, the final oil recovery with VRR = 0.7 [66.2% original oil in place (OOIP)] is more than 15% greater than that with VRR = 1 (55.6% OOIP) with A1 crude oil. Recovery for A2 with VRR = 0.7 (60.5% OOIP) was identical to the sum of oil recovery for solution-gas drive (19.1% OOIP) plus waterflooding (40.1% OOIP). An in-line viewing cell permitted inspection of produced fluid morphology. For A1 and VRR = 0.7, produced oil was emulsified, and gas was dispersed as bubbles, as expected for a foamy oil. For A2 and VRR < 1, foamy oil was not clearly observed in the viewing cell. In all cases, the water cut of VRR = 1 is clearly greater than that of VRR = 0.7. Finally, three-phase relative permeability was explored on the basis of the experimentally determined two-phase oil/water and liquid/gas relative permeability curves. Well-known algorithms for three-phase relative permeability, however, did not result in good history matches to the experimental data. Numerical simulations matched the experimental recovery vs. production time acceptably after modification of the measured krg and krow relationships. A concave shape for oil relative permeability that is suggestive of emulsified oil in situ was noted for both systems. The degree of agreement with experimental data is sensitive to the details of gas (gas/oil system) and oil (oil/water system) mobility.


SPE Journal ◽  
2002 ◽  
Vol 7 (02) ◽  
pp. 213-220 ◽  
Author(s):  
R. Kumar ◽  
M. Pooladi-Darvish ◽  
T. Okazawa

1999 ◽  
Vol 2 (01) ◽  
pp. 37-45 ◽  
Author(s):  
Bernard Tremblay ◽  
George Sedgwick ◽  
Don Vu

Summary The cold production process has increased primary heavy oil production and has been applied with commercial success in the Lloydminster area (Alberta, Canada). In this process, the production of sand is encouraged in order to form high permeability channels (wormholes) within the formation. The process depends on the formation and flow of foamy oil into the wormholes as these grow away from the wellbore and into the reservoir. The formation and growth of a wormhole was visualized using a computed tomography scanner, in an experiment in which oil flowed through a horizontal sandpack and out an orifice. The only drive mechanism was the formation and expansion of methane bubbles within the live oil. The pressure gradient at the tip of the wormhole was approximately 1 MPa/m when it started to develop at the orifice. Two conditions appear necessary for wormholes to keep growing:the pressure gradient at the tip of the wormhole must be sufficiently large to dislodge the sand grains,the pressure gradient along the wormhole must be large enough to transport the sand from the tip to the orifice. The pressure gradient at the tip of the wormhole was 2.9 MPa/m when it reached its maximum length. This suggests that, although the pressure gradient at the tip was sufficient for erosion to occur, the sand could not be carried along the wormhole causing the wormhole to stop growing. The pressure depletion experiment suggests that wormholes can easily develop in uncemented sand in the field since the maximum oil production rate during wormhole growth (18 cm3/day) was significantly lower than in the field. The minimum pressure gradient (11 kPa/m) necessary for sand transport along the wormhole is important in calculating the extent of wormhole growth in the field. Introduction Cold production is a nonthermal recovery process used in uncemented heavy oil reservoirs in which sand and oil are produced together. Production rates from wells on cold production can be up to 30 times larger than the rate predicted by Darcy flow without sand production. In order to better understand the role of sand production in the cold production process, tracer injection tests were performed by well operators.1,2 Tracer dye velocities of 7 m/min were measured between certain wells. The dye showed up 18 h later at 2 km away from the injection well.1,2 The rapid flow of the tracer suggested that it flowed through a small channel excluding the possibility of a fracture or cavity around the well. We confirmed directly the development of high conductivity channels "wormholes" in the laboratory in two previous experiments.3,4 An orifice was located at the end of a sandpack and heavy oil was injected into the sandpack at constant flow rates. The heavy oil did not contain any dissolved gas. A high permeability channel (wormhole) was observed to develop at a critical flow rate. The drive mechanism in these experiments was external since a constant flow rate was maintained using a positive displacement pump. The drive mechanism for the cold production process is solution-gas drive.5 We wanted to determine whether or not a wormhole would develop under solution-gas drive. The pressure vessel used in the two previous external drive experiments was modified to handle the live oil. This required maintaining a back pressure at the orifice end of the sandpack. This back pressure was reduced at a constant rate of 205 kPa/day during the experiment. We observed that a wormhole developed in the sandpack even though the only drive mechanism was the expansion of gas bubbles in the heavy oil. The critical pressure gradient required for the wormhole to start growing (1 MPa/m) was significantly lower than in the two previous dead oil experiments: 800 MPa/m in a first experiment3 and 32 MPa/m in a second experiment.4 This significant difference in the critical pressure gradient is attributed to a destabilization of the sand grains at the wormhole tip due to the growth of the gas bubbles in the pressure depletion experiment. The wormhole stopped growing when the pressure gradient along the wormhole was equal to 11 kPa/m. These measurements are required in order to estimate how far these wormholes can extend in the field. This experiment shows that a wormhole can develop in a sandpack by solution gas drive. Materials The Clearwater sand used in preparing the pack was obtained from collection tanks at Suncor's former cold production pilot field in Burnt Lake, Alberta, Canada. The sand was packed in 2 cm layers with a hydraulic press under 27.6 MPa. The high packing stress was necessary to obtain a porosity of 34% representing field conditions (32-34%) and to give the sand a cohesive strength comparable to field values by creating more interlocking between sand grains. The porosity of naturally deposited sand ranges from 37% for a well-sorted, well-rounded, medium to coarse sand, to more than 50% for poorly sorted, fine-grained sands with irregular shaped grains.6 Either compaction or cementation is required to reduce the porosity of naturally deposited sands to field values. Porosity reduction by compaction of sand sediments can occur by plastic flow, crushing, fracturing, or pressure solution at grain contacts.7 An average particle size distribution of the sand after packing at 27.6 MPa is shown in Fig. 1. The average size of the sand grains was 198 microns. The fines content (less than 37 microns) was 8.4% by weight. The permeability of the sand pack was 1.7 Darcy. The pore volume of the sandpack was 2336 cm3.


2021 ◽  
Author(s):  
Suwardi ◽  
Indah Widiyaningsih ◽  
Ratna Widyaningsih ◽  
Atma Budi Arta

SPE Journal ◽  
2016 ◽  
Vol 21 (01) ◽  
pp. 170-179 ◽  
Author(s):  
Songyan Li ◽  
Zhaomin Li

Summary Foamy-oil flow has been successfully demonstrated in laboratory experiments and site applications. On the basis of solution-gas-drive experiments with Orinoco belt heavy oil, the effects of temperature on foamy-oil recovery and gas/oil relative permeability were investigated. Oil-recovery efficiency increases and then decreases with temperature and attains a maximum value of 20.23% at 100°C. The Johnson-Bossler-Naumann (JBN) method has been proposed to interpret relative permeability characteristics from solution-gas-drive experiments with Orinoco belt heavy oil, neglecting the effect of capillary pressure. The gas relative permeability is lower than the oil relative permeability by two to four orders of magnitude. No intersection was identified on the oil and gas relative permeability curves. Because of an increase in temperature, the oil relative permeability changes slightly, and the gas relative permeability increases. Thermal recovery at an intermediate temperature is suitable for foamy oil, whereas a significantly higher temperature can reduce foamy behavior, which appears to counteract the positive effect of viscosity reduction. The main reason for the flow characteristics of foamy oil in porous media is the low gas mobility caused by the oil components and the high viscosity. High resin and asphaltene concentrations and the high viscosity of Orinoco belt heavy oil increase the stability of bubble films and prevent gas breakthrough in the oil phase, which forms a continuous gas, compared with the solution-gas drive of light oil. The increase in the gas relative permeability with temperature is caused by higher interfacial tensions and the bubble-coalescence rate at high temperatures. The experimental results can provide theoretical support for foamy-oil production.


2016 ◽  
Vol 137 ◽  
pp. 113-124 ◽  
Author(s):  
Teng Lu ◽  
Zhaomin Li ◽  
Songyan Li ◽  
Peng Wang ◽  
Zhuangzhuang Wang ◽  
...  

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