This document relates to microfluidics. More specifically, this document relates to microfluidic devices such as microfluidic chips, systems including microfluidic devices, and methods for assessing thermophysical properties of a fluid BACKGROUND
U.S. Pat. No. 8,485,026 (Mostowfi) discloses a method of measuring thermo-physical properties of a reservoir fluid. The method includes introducing the fluid under pressure into a microchannel, establishing a stabilized flow of the fluid through the microchannel, inducing bubble formation in the fluid disposed in the microchannel, and determining the thermo-physical properties of the fluid based upon the bubbles formed as the fluid flows through the microchannel.
U.S. Pat. No. 9,752,430 (Mostowfi et al.) discloses an apparatus for measuring phase behavior of a reservoir fluid. The apparatus includes a first sample container and a second sample container in fluid communication with a microfluidic device defining a microchannel. A first pump and a second pump are operably associated with the sample containers and the microfluidic device to fill the microchannel with a reservoir fluid and to maintain a predetermined pressure of reservoir fluid within the microchannel.
The following summary is intended to introduce the reader to various aspects of the detailed description, but not to define or delimit any invention.
Methods for assessing thermophysical properties of a study fluid are disclosed. According to some aspects, a method for assessing thermophysical properties of a study fluid includes: a. in a microfluidic channel, isolating at least a first slug of a study fluid within an isolation fluid; b. during and/or after step a., conducting a first optical investigation of the first slug to assess a thermophysical property of the study fluid; c. after step b., while maintaining the first slug in the microfluidic channel and isolated within the isolation fluid, modifying at least one of a pressure within the microfluidic channel and a temperature within the microfluidic channel; and d. during and/or after step c., conducting a second optical investigation of the first slug to re-assess the thermophysical property of the study fluid.
In some examples, step a. includes: filling the microfluidic channel with the isolation fluid, and while maintaining the microfluidic channel filled with the isolation fluid, loading the first slug into the microfluidic channel.
In some examples, step a. includes sandwiching the first slug of the study fluid between a first slug of the isolation fluid and a second slug of the isolation fluid. For example, step a. can include loading a set of secondary slugs of the study fluid into the microfluidic channel. The first slug of the isolation fluid can be sandwiched between the first slug of the study fluid and one of the secondary slugs of the study fluid, and the second slug of the isolation fluid can be sandwiched between the first slug of the study fluid and another one of the secondary slugs of the study fluid. For further example, step a. can include filling the microfluidic channel with the study fluid, and loading a first slug of the isolation fluid and a second slug of the isolation fluid into the microfluidic channel, to isolate the first slug of study fluid between the first slug of the isolation fluid and the second slug of the isolation fluid.
In some examples, step c. includes: while maintaining the microfluidic channel at a test temperature, and maintaining the first slug in the microfluidic channel and isolated within the isolation fluid, modifying the pressure in the microfluidic channel from a first pressure to a second pressure. Step b. can include assessing the thermophysical property of the study fluid at the test temperature and the first pressure. Step d. can include re-assessing the thermophysical property of the study fluid at the test temperature and the second pressure, and comparing the thermophysical property of the study fluid at the test temperature and second pressure to the thermophysical property of the study fluid at the test temperature and the first pressure.
The method can further include: e. repeating steps c. and d, to determine a bubble point pressure, a dew point pressure, a bubble point temperature, and/or a dew point temperature of the study fluid.
Modifying the pressure can include increasing or decreasing the pressure, and modifying the temperature can include increasing or decreasing the temperature.
In some examples, step c. includes: while maintaining the microfluidic channel at a test pressure and maintaining the first slug in the microfluidic channel and isolated within the isolation fluid, modifying the temperature in the microfluidic channel from a first temperature to a second temperature. Step d. can include assessing the thermophysical property of the study fluid at the test pressure and the second temperature.
In some examples, step d. includes inspecting an image of the slug to determine whether a bubble has appeared or dew has appeared. In some examples, step b. includes assessing a volume of a liquid phase and a volume of a gas phase in the first slug. Step d. can then include re-assessing the volume of the liquid phase and the volume of the gas phase of the first slug, and determining a change in the volume of the liquid phase and the volume of the gas phase over step c.
In some examples, step d. includes inspecting an image of the slug to determine whether asphaltenes have come out of solution, to assess the asphaltene onset pressure of the study fluid.
In some examples step d. includes inspecting an image of the slug to determine whether a gas hydrate has formed.
In some examples, step c. includes modifying the pressure to a predetermined pressure and modifying the temperature to a predetermined temperature. Step d. can include assessing a liquid volume of the first slug and a gas volume of the first slug to assess a gas to oil ratio of the study fluid. The predetermined pressure can be atmospheric pressure and the predetermined temperature can be about 60 degrees F. Step c. can include first lowering the temperature to the predetermined temperature, and then lowering the pressure to the predetermined pressure.
In some examples, step d. includes plotting a phase envelope for the oil composition.
In some examples, steps c. and d. are at least partially automated.
In some examples, during step b., the slug is generally stationary within the microfluidic channel.
Microfluidic systems are also disclosed. According to some aspects, a microfluidic system includes a microfluidic device having a microfluidic substrate. The microfluidic substrate has a microfluidic channel for isolating a slug of a study fluid within an isolation fluid. The system further includes a study fluid injection sub-system that houses the study fluid and that is configured to force the study fluid into the microfluidic channel. The system further includes an isolation fluid injection sub-system that houses the isolation fluid and that is configured to force the isolation fluid into the microfluidic channel. A pressure regulation sub-system regulates pressure in the microfluidic channel. A manifold provides fluid communication between the microfluidic device and the study fluid injection sub-system, the isolation fluid injection sub-system, and the pressure regulation sub-system. A temperature regulation sub-system regulates temperature within the microfluidic channel and the study fluid injection sub-system. An optical investigation sub-system provides optical access to at least a portion of the microfluidic channel.
In some examples, the microfluidic substrate further includes a study fluid inlet port in fluid communication with the microfluidic channel, an isolation fluid inlet port in fluid communication with the microfluidic channel, and an outlet port in fluid communication with the microfluidic channel. The microfluidic substrate can further include a bypass outlet port that is in fluid communication with the study fluid inlet port via a study fluid inlet channel. The study fluid injection sub-system can be in fluid communication with the study fluid inlet port, the isolation fluid injection sub-system can be in fluid communication with the isolation fluid injection port, and the pressure regulation sub-system can include a backpressure regulator in fluid communication with the outlet port.
In some examples, the isolation fluid is at least one of water, an ionic fluid, fluorocarbon oil, and a liquid metal.
In some examples, the system further includes a control sub-system connected to the study fluid injection sub-system, the isolation fluid injection sub-system, the pressure regulation sub-system, the temperature regulation sub-system, and the optical investigation sub-system, for providing automatic control of the microfluidic system.
The drawings included herewith are for illustrating various examples of articles, methods, and apparatuses of the present specification and are not intended to limit the scope of what is taught in any way. In the drawings:
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Various apparatuses or processes or compositions will be described below to provide an example of an embodiment of the claimed subject matter. No embodiment described below limits any claim and any claim may cover processes or apparatuses or compositions that differ from those described below. The claims are not limited to apparatuses or processes or compositions having all of the features of any one apparatus or process or composition described below or to features common to multiple or all of the apparatuses or processes or compositions described below. It is possible that an apparatus or process or composition described below is not an embodiment of any exclusive right granted by issuance of this patent application. Any subject matter described below and for which an exclusive right is not granted by issuance of this patent application may be the subject matter of another protective instrument, for example, a divisional patent application, and the applicants, inventors or owners do not intend to abandon, disclaim or dedicate to the public any such subject matter by its disclosure in this document.
As used herein, the term “assess” includes (but is not limited to) determination, estimation, prediction, analysis, testing, and study. For example, the statement that “microfluidic devices can be used to assess the bubble point pressure of an oil composition” indicates that microfluidic devices can be used to determine, to estimate, to predict, to analyze, to test, and/or to study the bubble point pressure of an oil composition.
As used herein, the term “study fluid” refers to any fluid assessed by the devices, systems, and methods disclosed herein. Example study fluids include oil compositions, refrigerants, water methane blends, and/or consumer chemicals.
As used herein, the term “oil composition” refers to a composition that includes or is made up of an oil. An oil composition may be synthetic or naturally derived. An oil composition can be a crude oil, or a crude oil fraction (e.g. a portion of a crude oil that has been distilled or otherwise separated from the crude oil). An oil composition can be a sample that resembles (e.g. has a composition substantially similar to) a crude oil or a crude oil fraction. An oil composition can be a dead oil (i.e. an oil composition taken from a subterranean formation and that does not flash at ambient temperature and pressure) or a live oil (i.e. an oil composition taken from a subterranean formation and having dissolved gases that spontaneously evolve at ambient pressure and temperature). An oil composition can be a gas, a liquid, and/or a supercritical composition. An oil composition can be a single-component composition or a multi-component composition.
As used herein, the term “isolation fluid” refers to a fluid that is substantially immiscible with a given study fluid, such as an oil composition. The term “isolation fluid” can refer to a liquid, a gas, a supercritical fluid, or a combination thereof. The term “isolation fluid” can refer to a single-component fluid, or a mixture of different components. Example isolation fluids include water, liquid metals or alloys, and/or ionic fluids. Specific examples of isolation fluids include mercury, galinstan, fluorocarbon oil and/or polyethylene glycol.
As used herein, the term “thermophysical property” can refer to (but is not limited to) one or more of the following parameters of a study fluid: volume (e.g. volume of a slug of a study fluid), phase state (e.g. whether a slug of a study fluid is in gaseous state, a liquid state, and/or a solid state), presence, absence, or change of a component (e.g. presence or absence of asphaltene solids, gas hydrates, a bubble, and/or dew), conditions under which a component appears, disappears, or changes (e.g. asphaltene onset pressure, dew point pressure, bubble point pressure, dew point temperature, dew point pressure, gas hydrate formation conditions of a study fluid), phase envelope, and ratio of one phase state to another (e.g. gas-to-oil ratio).
As used herein, the term “about” indicates a degree of variability in a value or range, for example, within 10%, within 5%, or within 1% of a stated value or of a stated limit of a range.
All numerical ranges listed herein are inclusive of the bounds of those ranges. For example, the statement that a certain measurement may be “between 25 cm and about 75 cm” means that the measurement may be 25 cm, or 75 cm, or any number therebetween.
Generally disclosed herein are microfluidic devices in the form of microfluidic chips, systems incorporating microfluidic devices, and related methods. The microfluidic devices, systems, and methods can be used to assess the thermophysical properties of study fluids. For example, the microfluidic devices, systems, and methods can be used in the oil and gas industry, in order to predict behavior of oil compositions in oil-bearing subterranean formations (e.g. in shale and/or tight oil formations, as well as fracture zones (also known as “frac zones”) created in such formations during hydraulic fracturing). More specifically, the microfluidic devices, systems, and methods can be used, for example, in order to assess the thermophysical properties of an oil composition. For example, the microfluidic devices, systems, and methods can be used to assess the bubble point pressure and/or temperature of an oil composition, the dew point pressure and/or temperature of an oil composition, to plot a phase envelope for an oil composition, and/or to assess a gas to oil ratio (GOR) of an oil composition.
In general, the microfluidic devices, systems, and methods disclosed herein can in some examples allow for fast, inexpensive, and/or reliable assessment of the thermophysical properties of oil compositions or other study fluids. More specifically, the microfluidic devices, systems, and methods disclosed herein can in some examples allow for fast, inexpensive, and/or reliable assessment of thermophysical properties such as bubble point pressure, phase envelope, and GOR. For example, the phase envelope of an oil composition can be assessed in a matter of hours (as opposed to days), using only a small volume of oil composition (e.g. less than 10 mL), with minimal labor and cost. Furthermore, the systems and methods disclosed herein can be automated and precisely controlled, which can allow for accuracy as well as reduced costs and reduced manpower.
In general, the microfluidic devices disclosed herein can include a microfluidic channel. The microfluidic channel can be loaded with one or more slugs of a study fluid, such as an oil composition, so that the slug(s) is/are isolated within an isolation fluid. As used herein, the term “isolated within an isolation fluid” indicates that a slug is bounded on opposite ends by isolation fluid, whether the isolation fluid is a generally continuous phase or is itself in slug form. For example, the microfluidic channel can be substantially filled with the isolation fluid, and a slug of the study fluid can then be loaded into the microfluidic channel so that the slug is isolated within the isolation fluid. Alternatively, the microfluidic channel can be substantially filled with the study fluid, and slugs of isolation fluid can be loaded into the microfluidic channel to isolate one or more slugs of the study fluid between the slugs of isolation fluid. While retaining the slug(s) in the microfluidic channel and isolated within the isolation fluid, various parameters can be modified, such as the pressure within the microfluidic channel and/or the temperature within the microfluidic channel, to assess the thermophysical properties of the study fluid. For example, the pressure in the microfluidic channel can be modified, and before, during, and after lowering the pressure, an optical investigation can be conducted (for example with the use of a microscope, and either in real time or by analyzing a video recording or still images) to assess the behavior of the slug(s) of the study fluid with lowering pressures. More specifically, in some examples, the microfluidic channel can be heated or cooled to a test temperature, and loaded with an isolation fluid. The microfluidic channel can then be pressurized to maintain the microfluidic channel well above the saturation pressure of the study fluid, and a slug of the study fluid can then be loaded into the microfluidic channel, so that the slug is in the microfluidic channel and isolated within the isolation fluid. The pressure in the microfluidic channel can then be lowered (e.g. in steps), and the slug can be observed at various pressures to determine the bubble point pressure. For example, images of the slug can be obtained as the pressure is lowered, and the volume of the slug can be measured at various pressures (i.e. can be measured once equilibrium has been reached at a given pressure step) using image analysis software. The volume can be plotted against pressure, and when the bubble point pressure is reached, the first bubble of the gas phase will appear, and the slope of the pressure-volume curve will change sharply. Alternatively, images of the slug can be obtained, and the bubble point pressure can be determined by observation of the first gas bubble in the images. In further examples, as will be described below, the phase envelope of the study fluid can be plotted, and/or the GOR can be measured.
Notably, in some examples of the methods described herein, after the slug(s) is/are loaded into the microfluidic channel, the slug(s) remains generally stationary within the microfluidic channel over the remainder of the method. That is, while the slug(s) may move somewhat within the microfluidic channel, the slug(s) generally do not pass entirely through and exit the microfluidic channel while the parameters are modified (e.g. while temperature and/or pressure are lowered), while equilibrium is reached, and while any real time steps of optical investigation are conducted. Instead, while the parameters are modified and equilibrium is reached, the microfluidic channel is generally closed to mass transfer of the study fluid, and the slug(s) generally remain in the microfluidic channel and bounded by the isolation fluid.
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In some examples, the microfluidic channel can include a nucleation site (not shown) to facilitate nucleation, so as to aid in preventing superheating of the study fluid.
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In the example shown, the study fluid inlet port 116 is in fluid communication with the microfluidic channel 108 via a study fluid inlet channel 122 that extends towards the microfluidic channel 108 from the study fluid inlet port 116, for loading study fluid (e.g. one or more slugs of study fluid or a continuous phase of study fluid) into the microfluidic channel 108. The study fluid inlet channel 122 has a length (also referred to herein as a “study fluid inlet channel length”), a width (also referred to herein as a “study fluid inlet channel width”), and a depth (also referred to herein as a “study fluid inlet channel depth). The study fluid inlet channel length can be, for example, between about 0.5 cm and about 20 cm (e.g. about 2 cm). The study fluid inlet channel width can be, for example, between about 2 microns and about 100 microns (e.g. about 5 microns). The study fluid inlet channel depth can be, for example between about 0.1 micron and about 5 microns (e.g. about 0.5 microns). In the example shown, the study fluid inlet channel 122 is shallower and narrower than the microfluidic channel 108. In alternative examples, the study fluid inlet channel 122 can be of the same width and depth as the microfluidic channel 108.
In the example shown, the isolation fluid inlet port 118 is in direct fluid communication with the first end 110 of the microfluidic channel 108, for loading an isolation fluid (e.g. one or more slugs of isolation fluid or a continuous phase of isolation fluid) into the microfluidic channel 108.
In the example shown, the outlet port 120 is in direct fluid communication with the second end 112 of the microfluidic channel 108, for allowing egress of fluids from the microfluidic channel 108, and for allowing a back pressure to be applied to the microfluidic channel 108 (as will be described below).
The study fluid inlet port 116, isolation fluid inlet port 118, outlet port 120, and study fluid inlet channel 122 can, for example, be etched and/or drilled into the base panel 104 (shown in
The terms “study fluid inlet port”, “isolation fluid inlet port”, “outlet port”, and “study fluid inlet channel” are used herein for simplicity, and are not intended to limit the use of these ports and channels. For example, while the “study fluid inlet port” may in many examples be used to load a study fluid into the microfluidic device 100, it may in other examples be used to load other materials (such as an isolation fluid), or may be used for egress of materials from the microfluidic device 100.
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In alternative examples, the pressure regulation sub-system and the isolation fluid injection sub-system can be integrated as a single sub-system.
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The microfluidic system 300 can further include an optical investigation sub-system (not shown), for optically accessing the microfluidic channel 108 (i.e. the entire microfluidic channel 108 or a portion thereof), and optionally other features of the microfluidic device 100. The optical investigation sub-system can include, for example, one or more microscopes having a viewing window in which all or a portion of the microfluidic channel 108 can sit, one or more laser analysis systems, one or more photodiode analysis systems, one or more video cameras, and/or one or more still image cameras. The optical investigation sub-system can be computerized and can further include image processing software and image analysis software. The image processing software can optionally automatically process images captured by the optical investigation sub-system, and the image analysis software can optionally automatically analyze images the processed images.
The microfluidic system 300 can further include a control sub-system (not shown) connected to the study fluid injection sub-system 304, the isolation fluid injection sub-system 322, the pressure regulation sub-system 330, the temperature regulation sub-system 346, and the optical investigation sub-system. The control sub-system can include one or more processors, which can receive, process, and/or store information received from the study fluid injection sub-system 304, the isolation fluid injection sub-system 322, the pressure regulation sub-system 330, the temperature regulation sub-system 346, and the optical investigation sub-system. For example, the control system can receive temperature information from the temperature transducers 356, 358, and 360, and pressure information from the pressure transducers 338, 340, 342, and 344. Furthermore, the control sub-system can send instructions to the study fluid injection sub-system 304, the isolation fluid injection sub-system 322, the pressure regulation sub-system 330, the temperature regulation sub-system 346, and/or the optical investigation sub-system. For example, the control system can instruct the temperature regulation sub-system 346 to increase and/or decrease the output of one or more of the heaters 348, 352, and 354. The control sub-system can optionally provide automatic control of the microfluidic system 300. For example, the control sub-system can be configured to automatically instruct the temperature regulation sub-system 346 to increase and/or decrease the output of one or more of the heaters 348, 352, and 354, based on the received temperature information. The control sub-system can provide similar instructions to the pressure regulation sub-system 330.
The microfluidic system can further include a vibrating element (not shown) or a high power laser to facilitate bubble nucleation in the study fluid inside a microfluidic channel.
Methods of assessing thermophysical properties of a study fluid, particularly an oil composition, will now be described. The methods will be described with reference to the microfluidic device 100 and the microfluidic system 300; however, the methods are not limited to the microfluidic device 100 and the microfluidic system 300, and the microfluidic device 100 and microfluidic system 300 are not limited to operation in accordance with the methods. Furthermore, for clarity, the methods with be described with reference to a certain sequence of steps (e.g. a given step may be described as “a first step” or “a second step”, or terms such as “then” or “next” may be used); however, unless expressly indicated as such in the claims, the methods are not limited to any particular sequence of steps.
In general, the methods can include isolating a first slug of a study fluid within an isolation fluid in a microfluidic channel. Then, while maintaining the first slug in the microfluidic channel and isolated within the isolation fluid, the pressure within the microfluidic channel and/or the temperature within the microfluidic channel can be modified. Before, during, and/or after modifying the pressure and/or temperature, an optical investigation of the first slug can be conducted, to assess one or more thermophysical properties of the study fluid (e.g. to assess the bubble point pressure of the study fluid, to plot a phase envelope for the study fluid, and/or to assess the gas to oil ratio of the study fluid).
More specifically, an example method 400 for assessing the bubble point pressure of an oil composition is shown in
At step 404, while continuing to maintain the microfluidic channel 108 at the test temperature, valves 328 and 336 can be opened and the second syringe pump 324 can be engaged, to fill the microfluidic channel 108 with the isolation fluid by flowing the isolation fluid from the second syringe pump 324 to the third syringe pump 332 via the microfluidic channel 108.
At step 406, valve 328 can be closed and the third syringe pump 332 can be engaged, to apply a back pressure to the microfluidic channel 108. The back pressure can be applied to pressurize the microfluidic channel 108 to a first pressure. The first pressure can be well above the saturation pressure of the oil composition, for example, between 1 bara and 1000 bara.
At step 408, while continuing to apply back pressure to maintain the microfluidic channel 108 at the first pressure, and while maintaining the microfluidic channel 108 filled with the isolation fluid, a first slug of oil composition can be loaded into the microfluidic channel 108. More specifically, valves 312 and 318 can be opened, and the first syringe pump 306 can be engaged, to force an aliquot of the oil composition from the study fluid cylinder 308 and into the study fluid inlet channel 122. As the aliquot enters the microfluidic channel 108 from the study fluid inlet channel 122, valves 312 and 318 can be closed and the first syringe pump 306 can be disengaged. Then, while continuing to apply back pressure, valve 328 can be opened and the second syringe pump 324 can be engaged, so that the flow of isolation fluid drives a slug of the oil composition into the microfluidic channel 108, and so that the slug is isolated in the isolation fluid.
Once loading of the microfluidic channel 108 with the first slug 500 of the oil composition is complete, valve 328 can be closed and the second syringe pump 324 can be disengaged, while continuing to apply back pressure to maintain the microfluidic channel 108 at the first pressure. Then, at step 410, a first optical investigation can be conducted to assess one or more thermophysical properties of the oil composition. For example, the optical investigation can include obtaining images of the first slug 500, and analyzing the images to determine the volume of the first slug 500 at the test temperature and first pressure. Alternatively, the optical investigation can include using a laser analysis system or a photodiode analysis system to assess the thermophysical properties of the first slug 500. All or a portion of step 410 can be carried out in real time. For example, images can be captured in real time. Then, the analysis of the images can either be carried out in real time (e.g. while the first slug 500 is in the microfluidic channel), or can be carried out at a later time (e.g. based on still images or a video recording of the slug). Optionally, step 410 can be at least partially automated. For example, as mentioned above, the control system can include image processing and analysis software that can assess the volume of the first slug 500.
At step 412, while maintaining the microfluidic channel 108 at the test temperature, maintaining the first slug 500 isolated in the microfluidic channel 108, and maintaining the microfluidic channel 108 filled with the isolation fluid 502, the pressure in the microfluidic channel 108 can be lowered. More specifically, the second syringe pump 324 and/or third syringe pump 332 can be engaged (while opening the corresponding valves), to lower the pressure in the microfluidic channel 108 from the first pressure to a second pressure. The second pressure can be, for example, between about 1 bara and about 1000 bara (e.g. about 300 bara), or about 5 to 10 bar lower than the first pressure.
At step 414, once equilibrium has been reached, a second optical investigation can then be conducted, to re-assess the thermophysical properties of the oil composition at the test temperature and the second pressure. For example, images of the first slug 500 can be obtained and analyzed to re-assess the volume of the first slug 500 (i.e. to determine the volume of the first slug at the test temperature and second pressure), and to determine a change in volume as a result of the lowered pressure. Alternatively or in addition, an image of the first slug 500 can be inspected to determine whether a bubble has appeared. As described with respect to step 410, all or a portion of step 414 can be carried out in real time.
The steps of lowering the pressure in the microfluidic channel 108 and conducting an optical investigation at the lowered pressure (i.e. steps 412 and 414) can be repeated, optionally in a step-wise fashion, until the bubble point pressure of the oil composition is determined. For example, the steps can be repeated until a first bubble is visible in images of the first slug 500. Alternatively, the steps can be repeated until the slope of the pressure-volume curve changes sharply.
As noted above, in method 400, after the first slug 500 is loaded into the microfluidic channel 108 (i.e. after step 408), the first slug 500 remains generally stationary within the microfluidic channel 108 over the remainder of the method (i.e. during step 412 and any real time portions of steps 410 and 414). That is, while the first slug 500 may move somewhat within the microfluidic channel 108 during steps 410 to 414, it does not flow through and exit the microfluidic channel 108 as the pressure is lowered, while equilibrium is reached, and while any real time steps of the optical investigations are conducted. During these steps, the microfluidic channel 108 is generally closed to mass transfer of the oil composition, and the first slug 500 generally remains in the microfluidic channel 108 and surrounded by the isolation fluid 502, and remains available for optical investigation.
In alternative examples, the dew point pressure of the oil composition can be assessed. In such examples, the method can be similar to method 400 described above; however, the pressure can be increased over the course of the method (as opposed to decreased), until dew appears.
In further alternative examples, the bubble point or dew point temperature of the oil composition can be assessed. In such examples, the method can be similar to method 400 described above; however, the method can be carried out at a generally constant test pressure, and the volume of the first slug can be assessed at various temperatures (i.e. a first temperature, a second temperature, and so on).
In further alternative examples, the gas to oil ratio (GOR) of the oil composition can be assessed. In such examples, the method can be similar to method 400 described above; however, after initially filling the microfluidic channel 108 with the isolation fluid 502 and loading the first slug 500 into the microfluidic channel 108, the temperature in the microfluidic channel 108 can be lowered to a predetermined temperature (e.g. about 60 degrees F.), and then the pressure in the microfluidic channel 108 can be lowered to a predetermined pressure (e.g. about atmospheric pressure, or 1 bara). An optical investigation can then be carried out to assess a liquid volume of the first slug 500 and a gas volume of the first slug 500, to thereby assess a gas to oil ratio of the oil composition.
In further alternative examples, a phase envelope can be plotted for the oil composition. That is, in addition to the steps described above, the method can be repeated with additional slugs of oil composition in additional phase states, or with the same slug in another phase state, or with additional slugs of different volumes, or by performing dew point and bubble point pressure measurements at different test temperatures, or by performing dew point and bubble point temperature measurements at different test pressures. For example, the method can be carried out with the first slug 500 loaded into the microfluidic channel 108 in a liquid-only state, and with a second slug (not shown) that is in a liquid only state. For further example, the method can initially be carried out with a first slug 500 loaded into the microfluidic channel 108 in a liquid-only state, and the method can include reducing the pressure until the first slug 500 is in a gas+liquid phase state. For further example, the method can be carried out with a first slug 500 having a first volume, and also with a second slug (not shown) that has a second volume. In such examples, the first slug 500 and the second slug can optionally be in the microfluidic channel 108 concurrently, separated by isolation fluid, and the optical investigation of each slug can optionally be carried out concurrently. Alternatively, the method can initially be carried out with the first slug 500, and can then be repeated with the second slug.
In addition, quality lines inside the phase envelope can be plotted by assessing the pressure required to achieve a certain liquid or gas volume percentage. This can be carried out with a single slug or multiple slugs in the microfluidic channel 108.
In further alternative examples, the asphaltene onset pressure of the oil composition can be assessed. In such examples, the method can be similar to method 400 described above; however, the optical investigation can include assessing the pressure at which asphaltenes precipitate in the first slug 500 of the oil composition.
In further alternative examples, gas hydrate formation conditions of the oil composition can be assessed. In such examples, the method can be similar to method 400 described above; however, the study fluid can be a mixture of a gas (e.g. methane, argon, or nitrogen) and water, and the temperature and pressure can be modified (e.g. by decreasing the temperature and increasing the pressure in a stepwise fashion) until the optical investigation indicates that a gas hydrate has formed.
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In further examples, in order to further facilitate cavitation, a laser may be used to agitate the contents of the microfluidic channel.
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While the above description provides examples of one or more processes or apparatuses or compositions, it will be appreciated that other processes or apparatuses or compositions may be within the scope of the accompanying claims.
To the extent any amendments, characterizations, or other assertions previously made (in this or in any related patent applications or patents, including any parent, sibling, or child) with respect to any art, prior or otherwise, could be construed as a disclaimer of any subject matter supported by the present disclosure of this application, Applicant hereby rescinds and retracts such disclaimer. Applicant also respectfully submits that any prior art previously considered in any related patent applications or patents, including any parent, sibling, or child, may need to be re-visited.
This application claims the benefit of and/or priority to U.S. Provisional Patent Application No. 63/127,206 filed on Dec. 18, 2020, which is incorporated herein by reference in its entirety.
Filing Document | Filing Date | Country | Kind |
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PCT/CA2021/051797 | 12/14/2021 | WO |
Number | Date | Country | |
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63127206 | Dec 2020 | US |