The present application is related to co-owned U.S. Pat. No. 9,500,583 to Jiang et al., which is hereby incorporated by reference herein in its entirety.
The subject disclosure relates to the downhole monitoring of fluids in a formation. More particularly, the subject disclosure relates to apparatus and methods for measuring the refractive index of a formation fluid which may be useful during production of hydrocarbons from a formation, although the disclosure is not limited thereto.
In developing an oilfield, and during both injection and production, reservoir fluids are monitored. In enhanced oil recovery (EOR) processes, compositional measurements within fluids are useful for quantitative evaluation of displacement induced migration. Specifically, data on fluids characterization in different producing zones may be used to infer reservoir structure.
One commonly used approach in measuring fluid composition is to withdraw fluid samples from a reservoir in a formation using a formation testing probe (downhole tool) or packed-off intervals. Light beams and light sensors of the downhole tool are used to measure light transmission at infra-red (IR) wavelengths of the fluid sample which is pulled into a flowline. The spectral characteristics of the transmitted beam are indicative of various components within the fluid, each chemical component having its own absorption signature. In addition, transport properties of the fluid such as the density and viscosity may be obtained.
As disclosed in previously-incorporated U.S. Pat. No. 9,500,583 to Jiang et al., attenuated total reflection (ATR) measurements at mid-IR frequencies can be used to measure a dissolved component, e.g. CO2 in a liquid. Methods utilizing ATR measurements rely on the attenuation of a reflected wave due to a small penetration (usually to a depth of a fraction of a wavelength) of the incident beam's evanescent wave. The penetration depth is dependent on the refractive indices of the fluid and the material with which the fluid is in contact. In the absence of any information, a particular refractive index for the fluid is assumed. However, since the refractive index of the fluid may vary with the concentration of the dissolved components, as well as temperature and pressure, the assumption that the refractive index of fluids flowing through a flowline remains constant can result in certain inaccuracies in analyzing the fluid components, especially in EOR processes.
While the refractive index of formation fluids such as crude oil has been measured uphole using conventional refractometers, it is logistically difficult and expensive to routinely bring reconstituted representative samples to the laboratory for analysis. Moreover, the reservoir fluids being brought uphole may be contaminated by drilling-mud filtrate, and contaminants may be introduced or removed during the fluid transfer process from downhole to the lab, thereby introducing significant bias in the estimates of the refractive index of the downhole fluid. Another challenge arises due to the variability of the refractive index with temperature, fluid composition, and pressure. Yet a further challenge to measuring the refractive index of the formation fluid is posed by the dissolution of gases such as CO2 in the fluid hydrocarbon, the very concentration of which is often the interest in EOR monitoring.
This summary is provided to introduce a selection of concepts that are further described below in the detailed description. This summary is not intended to identify key or essential features of the claimed subject matter, nor is it intended to be used as an aid in limiting the scope of the claimed subject matter.
Illustrative embodiments of the present disclosure include a borehole tool employing a flow line, a light source, two non-alike crystals interfacing with the flow line, light detectors, and a processor, where the light source, crystals, and flow line are arranged for light to be transmitted through the crystals and to undergo attenuated total reflection, and the detected intensities (or absorbances) detected by the light detectors are used by the processor in determining the refractive index of the fluid flowing in the flow line. In one embodiment, the non-alike crystals are not alike in that they have different refractive indices, e.g., they are different materials. In one embodiment, the non-alike crystals are of the same material but are not alike in that they have different geometries. In one embodiment, the non-alike crystals differ in both their materials and their geometries.
Additional aspects, embodiments, objects and advantages of the disclosed apparatus and methods may be understood with reference to the following detailed description taken in conjunction with the provided drawings.
The particulars shown herein are by way of example and for purposes of illustrative discussion of the examples of the subject disclosure only and are presented in the cause of providing what is believed to be the most useful and readily understood description of the principles and conceptual aspects of the subject disclosure. In this regard, no attempt is made to show details in more detail than is necessary, the description taken with the drawings making apparent to those skilled in the art how the several forms of the subject disclosure may be embodied in practice. Furthermore, like reference numbers and designations in the various drawings indicate like elements.
Before discussing embodiments, it is useful to understand some of the underlying physics, and to provide certain definitions.
The refractive index, η, is the reciprocal of the ratio of the phase velocity ν in the medium of interest to the speed of light in a vacuum (c) i.e.,
Light travels slower in a non-vacuum medium than it travels in vacuum because of electromagnetic field interactions with the charged particles of the medium. The speed of light in a particular medium and its refractive index are dependent both on temperature and pressure. Various relationships have been proposed to capture the dependence between refractive index and mass density. For example, in miscible systems, the Gladstone-Dale equation is
where is the mass density of the medium, ηMi is the molar refractivity of the ith component, wi is the mass fraction of the component i, and the summation is over all the N components. Another well-known relationship is the Lorentz-Lorenz equation
where α denotes the molecular polarizability of the medium, NA is the Avogadro's number, and M is the molecular weight of the medium. The polarizability is the coefficient of proportionality between the dipole moment and the electric field.
Measurements of refractive index can be combined with one or more of the aforementioned formulae to obtain physical properties of interest, including mass density, composition of crude oil, viscosity etc. within a restricted series of materials. These estimates are useful for reservoir modeling and in many other contexts.
ATR technology is based on measuring the change in the intensity of a totally internally reflected (infrared) beam when it passes through the interface of the sensor (crystal) and the sample. The change of intensity may be described in terms of the attenuation of the reflected beam intensity when compared to the incident beam.
In implementing technology utilizing attenuated total reflection, two necessary conditions for total internal reflection should be satisfied including that the refractive index of the crystal is greater than that of the sample, and that the incident angle of the beam is greater than the critical angle at the crystal-sample interface. As previously suggested, the amplitude of the internally reflected wave at the crystal-sample interface is affected because the evanescent wave formed while undergoing total internal reflection penetrates the sample adjacent to the interface, and exponentially decays with the distance from the crystal-sample interface. The penetration depth dp is the distance from the crystal-sample interface where the intensity of the evanescent wave decays to 1/e of its original value and is given by
where λ is the wavelength of infrared radiation, nf is the refractive index of the fluid, ηc is the refractive index of the ATR crystal, and Θ is the angle of incidence. In a strongly absorbing medium, the interaction between the probing light beam and the medium should be sufficiently small to ensure that measurements are not entirely attenuated. In this context, the extent of interaction is quantified by the depth of penetration. Since the penetration depth of the evanescent wave may be measured in the range of microns to a few millimeters, as set forth in previously incorporated U.S. Pat. No. 9,500,583 to Jiang et al., ATR can be a powerful technique for obtaining indications of CO2 dissolved in brine and crude oil downhole. It is also noted that if the ATR sensing apparatus is configured to have multiple reflections NR, the cumulative depth of penetration NRdp may be used to compute the effective optical path length of the sensor, l.
In one aspect, it may be assumed that the effective path length of mid-IR waves in a ATR crystal is proportional to dp as may be calculated from equation (4). In reality, the interactions are more complicated, as parallel and perpendicular polarized waves undergo differing attenuations, a complexity that is circumvented by the perturbation expansions considered hereinafter. Thus, as a starting point, the effective path length may be calculated according to
l=KNRdp, (5)
where NR is the number of reflections that is determined by the design of the crystal-fluid interface, and K is an oft-ignored proportionality variable that is likely to vary with ηf, ηc and Θ.
One purpose of making an ATR measurement is for a determination of the concentration C of a dissolved species that attenuates the incident IR-signal at one or more chosen wavelengths. The measurement is conducted by measuring the attenuation ratio, and assuming that ηf is known, l is calculated, and from which, the attenuation coefficient at the wavelength of interest is inferred. Since the attenuation coefficient is directly related to C at the sensitive wavelength λ, the concentration may be estimated. The issue is that the procedure assumes that either ηf is known, or that ηf is independent of C and that the solvent's ηf is known as a function of pressure and temperature. The latter dependence is sufficiently weak and may be accounted for through calibration. Also, traditionally the technique has worked well for dilute solutions. However, when the solution is not dilute in the solute, ηf varies with C, resulting in an error in estimated C.
The Beer-Lambert's law relates the absorbance A(λ), concentration C of a component in the downhole fluid that induces absorption at λ, and the optical path length l. At any wavelength
A(λ)=ε(λ)Cl=ε(λ)CKNRdp, (6)
where ε(λ) is the absorption coefficient of the component at wavelength λ. Knowing the intensity of the incident beam (e.g., by using a reference wavelength where no attenuation is expected to occur), and the intensity of the reflected beam, A(λ) is obtained from
where I0(λ) and I(λ) are the magnitudes of the incident intensity and reflected intensity respectively at wavelength λ. Thus, the measurements allow a determination of A(λ). Knowing A(λ) provides a determination of C (equation (6)) if dp is known (for a constant K). This in turn assumes that ηf of the fluid is known. However, in the oil-field, the solvent is unknown. Properties of the hydrocarbon vary from well to well or from zone to zone in a given well. In addition, for a given solvent, ηf may vary with C.
It will be appreciated by those of skill in the art that the intensity I0(λ) is an unknown unless a reference wavelength at which no attenuation takes place is available. Since the ratio of the intensities of the source beam is known at the two wavelengths (this drift is assumed to be negligible), the reference and the absorption values, I0(λ) is obtained from the reference response. The ratio of the incident intensity may be a function of temperature, but this is known a priori.
With the previously described underlying physics in mind, according to one aspect, the refractive index of a fluid is measured downhole as hereinafter described by using information obtained from two different attenuated total reflectance (ATR) sensors. Knowing the refractive index permits a calculation of the concentration of the species that attenuates the signal at the wavelength of interest. The present description focuses on the mid-infrared (m-IR) range; however, the technique is also extensible to a different range of wavelengths.
Turning now to
In at least one aspect, at least two testing chambers are placed in communication with the flow line 30 in a manner described hereinafter with respect to
In the regions of the infrared spectrum where the sample absorbs energy, the evanescent wave will be attenuated. The crystal 120 directs the reflected beam 130 (including the attenuated energy from each evanescent wave) for supply to an IR detector 132. Signal processing circuitry 134 (e.g. amplifier and filter circuitry, and A/D conversion circuitry) processes the output of the IR detector 132 to measure and process the output of the IR detector 132, thereby measuring the intensity of the detected light within the predetermined IR measurement bands as a function of time and generating digital data corresponding to such measurements. In one embodiment, one or more predetermined IR measurement bands include a predetermined absorption band centered around 4.27 microns (e.g., 4.27 microns ±75 nanometers), a predetermined reference band centered around 4 microns (e.g., 4 microns ±75 nanometers), and a reference band centered around 3 microns (e.g., 3 microns ±75 nanometers).
In one embodiment, the reflected beam (including the attenuated evanescent waves) is guided by a lens 136 through an optical filter 138 to the IR detector 132. The optical filter 138 provides bandpass optical filtering for the predetermined infrared measurement (and reference) bands. The IR detector 132 may include an array of IR detector elements corresponding to the predetermined infrared measurement bands. Alternatively, a single IR detector element can be used.
In one embodiment, additional supporting electronics can be supplied in conjunction with the IR light sources 124 and IR detectors 132. The supporting electronics may be provided for each light source and each detector or may be shared by the light sources and by the detectors. As seen in
In one aspect, the sensing crystal will be exposed to a high-pressure fluid, whereas the infrared source, detectors, and electronics may be isolated from the fluid. Arrangements for accomplishing the same are described in co-owned U.S. Pat. No. 9,500,583 which was previously incorporated by reference herein.
Turning now to
In
In other embodiments, the unalike crystals may have identical geometries (angles of incidence), but may be made from different materials; i.e., the crystals have different refractive indices. By way of example only, one crystal may be a sapphire crystal and the other crystal may be a diamond material.
In yet other embodiments, both the materials and the angles of incidence (geometry) of the unalike crystals may be different. The geometry of each material may be optimized in order to maximize sensitivity to ηf. Within an expected range of ηf, the configuration may be tailored so that the difference in the attenuation between the two crystals is maximized for the same wavelength λ and number of reflections NR.
With the unalike crystals, equation (4) can be rewritten with an index j which is used to refer to either
where ηcj denotes the refractive index of crystal j, j=1, 2, . . . and Θj is the angle of incidence designed for each j. With two crystals, using equation (8), a ratio of penetration depths can be expressed as
Using equations (5) and (6), and replacing dp yields
(since NR is expected to be the same for both crystals), where A1 and A2 are attenuations for j=1, 2. As a first approximation, it is assumed that K1=K2. With that assumption, equation (10) may be used to find the index of refraction for the fluid ηf, as the indices of refraction of the crystals ηc1 and ηc2 are known, the angles of incidence Θ1 and Θ2 are known, and the attenuations A1 and A2 are measured. However, in certain embodiments, and as described in more detail hereinafter, the index of refraction for the fluid may be determined without the K1=K2 approximation.
For K1≠K2, the ratio of K2 to K1 may be represented as
In order to construct the dependence of the function R on its arguments, it may be supposed that the true penetration depth is given by the average of the perpendicular and parallel polarized waves' effective path length (de). Explicit relationships for these are known and the mean value is used for unpolarized light. Therefore de/dp may be computed for various ηf, ηc, and Θ as long as conditions of ATR are met, i.e., a total reflection occurs assuming unpolarized light is used. Otherwise, for polarized light, the components of parallel and perpendicular fields may be considered so as to compute the effective path length appropriately.
Now the ratio of the effective path length and the penetration depth is denoted D, with D=de/dp, and a refractive index range restricted between 1.325 to 1.475 is assumed, with the minimum ηm=1.325 and the maximum ηM=1.475. This range by no means is restrictive, but is chosen based on commonly encountered values of aqueous fluids and oils. It is easily extended to encompass a larger range. An interesting computational result is that if one denotes as D0 for D at a ηf of 1.325, the ratio Dn=D/D0 is nearly independent of Θ for diamond and sapphire, commonly used in ATR measurements. This is true for 65°≤Θ≤75°. Based on this normalization,
or f is independent of Θ for the angles of interest.
In one aspect, the dependence of the ratio on the refractive index of the crystal may also be removed through another normalization. More particularly, a double normalized ratio is defined according to
where ηs is the refractive index of sapphire and ηc is the refractive index of the crystal (diamond or sapphire) through which the measurement is made. Equation (13) is consistent with the earlier statement that for sapphire, Dn is nearly independent of Θ. Equation (13) may be considered important because g is a function of ηf alone and shows little dependence on ηc.
Thus, given the known function g(ηf) through calibration, or less accurately through
Now, D0 is the depth of penetration at ηf=1.325, a value that is known for a given ηc and Θ, or D0 may be written according to D0=h(ηc,Θ). Thus, D is now known from Equation (14) as a function ηf.
The measurement of the refractive index of a formation fluid supposes that there are two crystals placed along the tubing or a pipe of a a borehole tool through which a fluid flows. The purpose of the instrumentation is to find the refractive index of the fluid from which other determinations may be made (e.g., inferring a dissolved component concentration), but the component could alter the refractive index determination by its very presence.
As previously suggested, two different ATR crystals (either different Θ, or ηc or both) are utilized, and an attenuation measurement is made on the same fluid so that A2/A1 is measured. On the right hand side of Equation (10) the unknowns are ηf and K2/K1.
In one embodiment, a premise is that D=de/dp≈l/dp=K. Thus (see Eq. 9 and 10) the ratio of the D values are the same as that of K. Therefore,
where ηs is the known refractive index of sapphire, and the right hand side is a function of ηf for given geometries of the crystal and its material. Therefore, from the ratio of A1 to A2, ηf is obtained by inverting Equation (15), since ηc and Θ are known for the crystals. Note that g(ηf) does not appear in the ratio.
Though the inferences are based on the assumption of l being approximately the same as de, this is by no means restrictive. It is possible to take several different solvents whose refractive indices are known and are within the range of interest, dissolve the component whose concentration is desired to a small value, and measure attenuation. This in turn allows knowledge of the path length or K. It is then a matter of constructing a suitable function h(ηc, Θ) and g(ηf) from the measured data. The purpose of knowing g(ηf) is to confirm that such a function is possible, although it is not used in the ratio evaluation. Note that for the case of K being a constant, Dn=1 and Dnn=1. The depth of penetration from an attenuation point of view is simply proportional to dp. Regardless, the calibration allows a determination of the characteristics of K.
Embodiments of methods utilizing the disclosed apparatus are understood with reference to
More particularly, and according to one aspect, a dissolved component concentration of a gas such as CO2 may be measured as follows. First, a calibration for dissolved CO2 is made with a solvent-solute mixture for which the refractive index is ηf1. Using the methodology already described, the fluid refractive index η2 for which the dissolved concentration is desired is obtained. The attenuation A2 is known, but in order to infer the concentration of the dissolved component, the calibration curve known for a fluid refractive index ηf1 is used. Then, the attenuation obtained with ηf2 is shifted to an attenuation that would have been obtained had the fluid been one of refractive index Rewriting Eq. 15 with a crystal of ηc2 and Θ2, but for fluids of refractive index and ηf2, the following is obtained:
Knowing A1 from the above equation from a measured A2 thus allows the use of the calibration curve corresponding to a fluid of calibration of ηf2.
In one aspect, some of the methods and processes described above, such as calculating the attenuation values and calculating the refractive index of the formation fluid are performed by a processor. The term “processor” should not be construed to limit the embodiments disclosed herein to any particular device type or system. The processor may include a computer system. The computer system may also include a computer processor (e.g., a microprocessor, microcontroller, digital signal processor, or general purpose computer) for executing any of the methods and processes described above. The computer system may further include a memory such as a semiconductor memory device (e.g., a RAM, ROM, PROM, EEPROM, or Flash-Programmable RAM), a magnetic memory device (e.g., a diskette or fixed disk), an optical memory device (e.g., a CD-ROM), a PC card (e.g., PCMCIA card), or other memory device.
Some of the methods and processes described above, can be implemented as computer program logic for use with the computer processor. The computer program logic may be embodied in various forms, including a source code form or a computer executable form. Source code may include a series of computer program instructions in a variety of programming languages (e.g., an object code, an assembly language, or a high-level language such as FORTRAN, C, C++, Python, or JAVA). Such computer instructions can be stored in a non-transitory computer readable medium (e.g., memory) and executed by the computer processor. The computer instructions may be distributed in any form as a removable storage medium with accompanying printed or electronic documentation (e.g., shrink wrapped software), preloaded with a computer system (e.g., on system ROM or fixed disk), or distributed from a server or electronic bulletin board over a communication system (e.g., the Internet or World Wide Web).
Alternatively or additionally, the processor may include discrete electronic components coupled to a printed circuit board, integrated circuitry (e.g., Application Specific Integrated Circuits (ASIC)), and/or programmable logic devices (e.g., a Field Programmable Gate Arrays (FPGA)). Any of the methods and processes described above can be implemented using such logic devices.
Although only a few examples have been described in detail above, those skilled in the art will readily appreciate that many modifications are possible in the examples without materially departing from this subject disclosure. Thus, by way of example only, and not by way of limitation, while various embodiments describe the use of two unalike crystals, more than two unalike crystals may be utilized. Also, while sapphire and diamond were described for use as crystals, it will be appreciated that other materials could be used. Accordingly, all such modifications are intended to be included within the scope of this disclosure as defined in the following claims. In the claims, means-plus-function clauses are intended to cover the structures described herein as performing the recited function and not only structural equivalents, but also equivalent structures. It is the express intention of the applicant not to invoke 35 U.S.C. § 112, paragraph 6 for any limitations of any of the claims herein, except for those in which the claim expressly uses the words ‘means for’ together with an associated function.
Number | Name | Date | Kind |
---|---|---|---|
1968202 | Hansen | Jul 1934 | A |
5473161 | Nix et al. | Dec 1995 | A |
6218662 | Tchakarov et al. | Apr 2001 | B1 |
6627873 | Tchakarov et al. | Sep 2003 | B2 |
6662116 | Brown | Dec 2003 | B2 |
6969857 | Owen | Nov 2005 | B2 |
6995360 | Jones et al. | Feb 2006 | B2 |
7289690 | Li | Oct 2007 | B2 |
7812312 | Mantele et al. | Oct 2010 | B2 |
8099241 | Niu et al. | Jan 2012 | B2 |
9500583 | Jiang et al. | Nov 2016 | B2 |
20070108378 | Terabayashi et al. | May 2007 | A1 |
20070200065 | Arno | Aug 2007 | A1 |
20080078544 | Christian et al. | Apr 2008 | A1 |
20080309922 | Anders et al. | Dec 2008 | A1 |
20090302221 | Tavernier et al. | Dec 2009 | A1 |
20110051125 | Kim | Mar 2011 | A1 |
20120085144 | Krolak et al. | Apr 2012 | A1 |
20120290208 | Jiang et al. | Nov 2012 | A1 |
20130056626 | Shen et al. | Mar 2013 | A1 |
Number | Date | Country |
---|---|---|
1903329 | Mar 2008 | EP |
06341949 | Dec 1994 | JP |
2000035399 | Feb 2000 | JP |
0042416 | Jul 2000 | WO |
0062028 | Oct 2000 | WO |
Entry |
---|
Smits et al., “In-situ [sic] optical fluid analysis as an aid to wireline formation sampling”, SPE Formation Evaluation, 10(2):91-98, 1995. |
Crombie et al., “Innovations in wireline fluid sampling”, Schlumberger Oilfiedl Review, 10(3):26-41, 1998. |
Morris et al., “Using optical fluid analysis to evaluate downhole fluid sample contamination”, SPE 50603, In proc. Of European Petroleum Conference, Society of Petroleum Engineers, 1998, pp. 283-295. |
Paulter et al., “The effect of pressure on the index of refraction of paraffin oil and glycerine”, Phys. Rev., 41:366-367, 1932. |
Dubey et al., “Refractive index of ternary liquid systems of squalane(+hexane+benzene; +cyclohexane+ benzene and+ hexane+ cyclohexane)”, Indian J. of Pure and Applied Phys., 43(3):175-179, 2005. |
Khosrokhavar et al., “Visualization and investigation of natural convection flow of CO2 in aqueous and oleic systems”, Journal of Petroleum Science and Engineering, 122:230-239, 2014. |
Malacara, “Geometrical and Instrumental Optics”, Experimental Methods in the Physical Science, Academic Press, 1988. available at: https://books.google.com/books?id=M7VZrgEACAAJ. |
Shumate, “An interferometric measurement of index of refraction”, Master's thesis, California Institute of Technology, Pasadena, California, 3, 1964, 75 pages. |
Tilton and Taylor, “Refractive index measurement”, in: Walter G. Berl, editor, Physical Methods in Chemical Analysis, 2nd ed. vol. I, pp. 412-462, Academic Press, New York, 1960. |
Bauer and Fajans, “Refractormetry”, In: Arnold Weissberger, editor, Physical Methods of Organic Chemistry, 2nd ed. vol. II, pp. 1141-1240, Academic Press, New York, 1949. |
Hasell et al., “High-pressure carbon dioxide uptake for porous organic cages: comparison of spectroscopic and manometric measurement techniques”, Chemical Communications, 49(82):9410-9412, 2013. |
Cash et al., “Novel Online Sensor for Measuring Dissolved CO2 Using Attenuated Total Reflectance (ATR) Technology”, 2007 ASBC Annual Meeting, Jun. 16-20, 2007, Fairmont Empress, Victoria, British Columbia, Canada, Tehermal Fisher Scientific, 1 page. |
O'Leary et al., “Attenuated Total Reflection Spectroscopy method for measuring dissolved CO2 concentration in Beer”, Published Aug. 2006, 9 pages. |
“Spectral Calculator—Atmospheric Gas Spectra, Infrared Molecular Absorpotion Spectrum”, SpectralCalc.com, GATS, Inc., May 28, 2010, Web. May 25, 2016, 1 page. |
Carroll et al., “The Solubility of Carbon Dioxide in Water at Low Pressure”, Journal of Physical and Chemical Reference Data, 1991, vol. 20(6): pp. 1201-1209. |
Cotton and Wilkinson, “Advanced Inorganic Chemistry, A Comprehensive Text”, 4th Edition, John Wiley & Sons: New York, 1980: pp. 366-367. |
Duan and Sun, “An Improved Model Calculating CO2 Solubility in Pure Water and Aqueous NaCL Solutions From 273 to 533 K and From 0 to 2000 Bar”, Chemical Geology, 2003, vol. 193(3-4): pp. 257-271. |
Halloway et al., “Chapter 5: Carbon Dioxide Transport, Injection and Geological Storage”, 2006 IPCC Guidelines for National Greenhouse Gas Inventories, Eds.: Eggleston et al., Intergovernmental Panel on Climate Change, 2006: pp. 5.1 to 5.32. |
Hansen et al., “Global Warming in the Twenty-First Century: An Alternative Scenario”, PNAS, Aug. 2000, vol. 97(18): pp. 9875-9880. |
Number | Date | Country | |
---|---|---|---|
20190079007 A1 | Mar 2019 | US |