Method employing pressure transients in hydrocarbon recovery operations
09803442 · 2017-10-31
Assignee
Inventors
Cpc classification
E21B28/00
FIXED CONSTRUCTIONS
E21B43/16
FIXED CONSTRUCTIONS
International classification
E21B43/16
FIXED CONSTRUCTIONS
E21B28/00
FIXED CONSTRUCTIONS
Abstract
A method to induce pressure transients in fluids for use in hydrocarbon recovery operations by inducing the pressure transients in a fluid by a collision process. The collision process employs a moving object (103,203,303,403) that collides outside the fluid with a body (102,202,302,402) that is in contact with the fluid inside a partly enclosed space (101,201,301,401). Furthermore, the pressure transients must be allowed to propagate in the fluid. The fluid may be one or more of the following group: primarily water, consolidation fluid, treatment fluid, cleaning fluid, drilling fluid, fracturing fluid and cement.
Claims
1. A method in hydrocarbon recovery operations on a subterranean formation and comprising the application of at least one fluid into the formation, the method comprising: providing at least one partly enclosed space containing a fluid in fluid connection with the fluid in the formation, arranging a body in the partly enclosed space such that a first surface portion of the body is in contact with said fluid and a second surface portion of the body is free of contact with said fluid, the body hereby being positioned so as to separate the fluid filled part of said space from a part of said at least one partly enclosed space without fluid, arranging at least one object outside the fluid filled part of said space and outside said fluid, and inducing pressure transients in said fluid such as to propagate in said fluid and into the formation thereby enhancing a penetration rate of the fluid into the formation, where said pressure transients are induced by a collision process generated by the object falling onto and colliding with said second surface portion of the body such that the collision occurs outside said fluid filled part of said space and outside said fluid without the object making contact with the fluid, wherein said collision process is such that said body is moved about 1 mm or less by said collision process.
2. The method in hydrocarbon recovery operations according to claim 1, where said at least one fluid is provided from at least one reservoir in fluid communication with said partly enclosed space.
3. The method in hydrocarbon recovery operations according to claim 2 further comprising the step of transporting said at least one fluid from said at least one reservoir, by means of at least one fluid transporting apparatus.
4. The method in hydrocarbon recovery operations according to claim 1 where said collision process comprises the object being caused to fall onto said body by means of the gravity force.
5. The method in hydrocarbon recovery operations according to claim 1 where said fluid in the at least one partly enclosed space is a liquid.
6. The method in hydrocarbon recovery operations according to claim 1 where said object collides with said body in air, wherein the air is a fluid different from the first fluid.
7. The method in hydrocarbon recovery operations according to claim 1 further comprising generating a number of said collision processes at time intervals.
8. The method in hydrocarbon recovery operations according to claim 7 where said collision processes are generated at time intervals in the range of 2-20 sec.
9. The method in hydrocarbon recovery operations according to claim 7 comprising the step of generating a first sequence of collision processes with a first setting of pressure amplitude and time between the collisions, followed by a second sequence of collision processes with a different setting of pressure amplitude and time between the collisions.
10. The method in hydrocarbon recovery operations according to claim 9 where said setting of pressure amplitude is changed by changing the mass of said moving object, or changing the velocity of said moving object relative to the velocity of said body.
11. The method in hydrocarbon recovery operations according to claim 1 where said partly enclosed space comprises a first and a second part separated by said body and where the method further comprises filling the first part with fluid prior to said collision process.
12. The method in hydrocarbon recovery operations according to claim 1, where said at least one moving object is connected to at least one wave motion capturing system.
13. The method in hydrocarbon recovery operations according to claim 12, characterized in that said at least one wave motion capturing system comprises at least one floating buoy arranged such as to be set in motion by waves, and where the motion of said at least one floating buoy induces movement of said object, thereby obtaining a nonzero momentum of said object prior to the collision with said body.
14. The method in hydrocarbon recovery operations according to claim 7 where said collision processes are generated at time intervals in the range of 4-10 sec.
15. The method in hydrocarbon recovery operations according to claim 1, wherein said collision process is such that said body moves about 1 mm over a time interval of about 5 ms.
16. The method in hydrocarbon recovery operations according to claim 1, wherein the pressure transients suppress a tendency for blocking and maintain a fluid condition of the subterranean formation.
17. The method in hydrocarbon recovery operations according to claim 1, wherein the pressure transients enhance the area at which the fluid is applied to the subterranean formation.
18. The method in hydrocarbon recovery operations according to claim 1, wherein exchange of fluids is enhanced by pressure transients in the subterranean formation.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) In the following different embodiments of the invention will be described with reference to the drawings, wherein:
(2)
(3)
(4)
(5)
(6)
(7)
(8)
(9)
(10)
DETAILED DESCRIPTION OF POSSIBLE EMBODIMENTS
(11) The invention of the present patent application is based on employing pressure transients induced by a collision process in hydrocarbon recovery operation.
(12)
(13)
(14)
(15)
(16)
(17) During the experiments salt water is pumped from the reservoir 531 through a core material placed in the container 532. In these experiments Berea sandstone cores have been used with different permeabilities of about 100-500 mDarcy, which prior to the experiments were saturated with oil according to standard procedures. The oil recovered from the flooding by the salt water will accumulate at the top of the tube 533 during the experiments, and the volume of the salt water collected in the reservoir 534 is then equal to the volume transported from the reservoir 531 by the pumping device 540. The more specific procedures applied in these experiments follow a standard method on flooding experiments on Berea sandstone cores.
(18) The pipeline 511 is flexible in order to accommodate any small volume of fluid which may be accumulated in the pipeline during the collision process between the piston 502 and the object 503 due to the continuous transporting of fluid by the pumping device 540.
(19) The piston 502 is placed in the cylinder 501 in a bearing and the cylinder space beneath the piston is filled with fluid. In the experiments a hydraulic cylinder for water of about 20 ml is used. The total volume of salt water flowing through the container 532 was seen to correspond closely to the fixed flow rate of the pumping device. Thus, the apparatus comprising the hydraulic cylinder 501, the piston 502 and the object 503 contribute only insignificantly to the transport of salt water in these experiments. The collision of the object with the piston occurs during a very short time interval. Therefore, the fluid is not able to respond to the high impact force by a displacement resulting in a increase of the flow and thus altering of said fixed flow rate. Rather, the fluid is compressed by the impact and the momentum of the piston is converted into a pressure transient. Hence, any motion of the piston 502 during the collision process is believed to relate to a compression of the fluid beneath the piston and not due to any net displacement of fluid out of the hydraulic cylinder 501.
(20) The pressure transients during the performed experiments were generated by an object 503 with a weight of 5 kg raised to a height of 17 cm and caused to fall onto the cylinder thereby colliding with the piston 502 at rest. The hydraulic cylinder 501 used had a volume of about 20 ml and an internal diameter of 25 mm corresponding to the diameter of the piston 502. The apparatus for performing the collision process is illustrated in
(21) Experiments were made with pressure transients generated with an interval of about 6 sec (10 impacts/min) over a time span of many hours.
(22) The movement of the piston 502 caused by the collisions was insignificant compared to the diameter of the piston 502 and the volume of the hydraulic cylinder 501 resulting only in a compression of the total fluid volume which may be deducted from the following. The volume of the hydraulic cylinder 501 is about 20 ml and the fluid volume in the Berea sandstone core in the container is about 20-40 ml (cores with different sizes were applied). The total volume which can be compressed by the object 503 colliding with the piston 502 is therefore about 50-100 ml (including some pipeline volume). A compression of such volume with about 0.5% (demanding a pressure of about 110 Bar since the bulk modulus of water is about 22 000 Bar) represents a reduction in volume of about 0.25-0.50 ml corresponding to a downward displacement of the piston 502 with approximately 1 mm or less. Thus the piston 502 moves about 1 mm over a time interval of about 5 ms during which the pressure transients could have propagated about 5-10 m. This motion is insignificant compared with the diameter of the piston 502 and the volume of the hydraulic cylinder 501.
(23)
(24) A single pressure transient is shown in greater detail in
(25)
(26) The experiments performed without pressure transients (noted ‘A’) were performed with a static pressure driven fluid flow where the pumping device 540 was coupled directly to the core cylinder 532. In other words the hydraulic cylinder 501 including the piston 502 and object 503 was disconnected or bypassed. The same oil type of Decane was used in both series of experiments.
(27) The average (over the cross section of the core plug) flooding speed (in μm/s) is given by the flow rate of the pumping device. In all experiments, except 36, the apparatus for generating pressure transients contribute insignificantly to the total flow rate and thus the flooding speed, which is desirable since a high flooding speed could result in a more uneven penetration of the injected water, and thus led to an early water breakthrough. In the experiment 36 the experimental set-up further comprised an accumulator placed between the hydraulic cylinder 501 and the fluid pumping device 540, which is believed to have given an additional pumping effect causing the high flooding speed of 30-40 μm/s as reported in the table. As seen from the experimental data, application of pressure transients to the water flooding resulted in a significant increase in the oil recovery rate in the range of approximately 5.3-13.6% (experiments 2 and 4, respectively), thus clearly demonstrating the potential of the proposed hydrocarbon recovery method according to the present invention.
(28)
(29) The pressure transients are here generated by an impact load on the piston 502 in the fluid filled hydraulic cylinder 501. A mass 801 is provided on a vertically placed rod 802 which by means of a motor 803 is raised to a certain height from where it is allowed to fall down onto and impacting the piston 502. The impact force is thus determined by the weight of the falling mass and by the falling height. More mass may be placed on the rod and the impacting load adjusted. The hydraulic cylinder 501 is connected via a tube 511 (not shown in